CA1186550A - Stabilized amorphous calcium carbonate - Google Patents
Stabilized amorphous calcium carbonateInfo
- Publication number
- CA1186550A CA1186550A CA000364108A CA364108A CA1186550A CA 1186550 A CA1186550 A CA 1186550A CA 000364108 A CA000364108 A CA 000364108A CA 364108 A CA364108 A CA 364108A CA 1186550 A CA1186550 A CA 1186550A
- Authority
- CA
- Canada
- Prior art keywords
- solution
- calcium carbonate
- amorphous calcium
- water
- stabilized amorphous
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Medicinal Preparation (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
STABILIZED AMORPHOUS CALCIUM CARBONATE
Stabilized amorphous calcium carbonate which is useful as a carbonate factor in effervescent compo sitions. Process for preparing stabilized amorphous calcium carbonate and compositiors containing stabil-ized amorphous calcium carbonate.
STABILIZED AMORPHOUS CALCIUM CARBONATE
Stabilized amorphous calcium carbonate which is useful as a carbonate factor in effervescent compo sitions. Process for preparing stabilized amorphous calcium carbonate and compositiors containing stabil-ized amorphous calcium carbonate.
Description
STABILIZED AMORPHOUS CALCIUM CARBONATE
This invention relates to calcium carbonate which is useful as a carbonating agent, to processes therefor and effer-vescent compositions containing same.
The reaction of acidic compositions, hereinafter re-ferred to as the "acid factor", with bicarbonate or carbonate-containing compositions, hereinafter referred to as the "carbon-ate factor", in an aqueous environment, such as a solution, to produce or release carbon dioxide is well known in the art and will hereinafter be referred to as the "effervescent reaction".
The effervescent reaction has heretofore been utilized in many fields, such as the food and medicament industries, where a rapid release of carbon dioxide at a controlled point in time is desirable.
Products that undergo the efervescent reaction upon use normally comprise a dry, solid mixture of an acid factor and a carbonate factor, said mixture being hereinafter referred to as an "effervescent composition". The acid factor and the carbonate factor in the effervescènt compositions are normally dry solids and are water soluble, at least in the presence of each other. Additionally, the acid and carbonate factors uti lized must be compatible with their intended use, i.e., if to be consumed, they must be physiologically acceptable.
Many such effervescent compositions have been pro-vided commercially. For instance, it is known that an efferves-cent composition of citric acid, sodium bicarbonate (in less than the stoichiometric equivalent of citric acid) and a flavor will provide a carbonated beverage upon adding the composition to the proper amount of water. Other examples of effervescent compositions are the well-known effervescent medicament tab-lets, baking sodas and the like. The major advantage of theseproducts is, of course, that the effervescent composition may be easily and economically stored as a dry solid and may then ~,.B~t~
be used, as desired, by merely contacting it with water to pro-duce a carbonated beverage, i.e., the release of carbon diox-ide.
The food industry has long sought commercially feas-ible products to provide a carbonated beverage from an efferves-cent composition. Such a beverage must be highly palatable and, as a practical matter, must afford a rapid rate of prepara-tion by the consumer. Normally, the consumer expects to be able to prepare the beverage in a short time, i.e., within about one to three minutes at the most. It is essential, there-fore that the effervescent composition rapidly undergo the effervescent reaction upon contact with water providing a car-bonated beverage that is highly palatable to the consumer.
Although many acid factors are available, such as citric acid, fumaric acid, adipic acid, malic acid, tartaric acid, etc., the primary carbonate factor heretoEore utilized in effervescent compositions has been sodium bicarbonate. Sodium bicarbonate is highly reactive with acid factors in aqueous solutions, rapidly releasing carbon dioxide, and has become the standard carbonate factor utilized by industry in effervescent compositions. Other carbonate factors, such as calcium carbon-ate and magnesium carbonate have been suggested as possible alternatives, but to date only sodium bicarbonate has been able to provide the desired rate of carbon dioxide release. Sodium bicarbonate does, however, have a major drawback, particularly in the food and medicament industries, in that it gives a dis-tinctly disagreeable saline or soapy taste to the solutions con-taining it, which is known to be due to the presence of the sodium ion. Accordingly, many attempts have been made to sub-stitute a more agreeable tasting cation in the carbonate fac-tors utilized in effervescent compositions.
A cation that provides excellent taste characteris-tics in aqueous solutions or compositions containing it is the calcium ion. Although calcium carbonate and compositions con-taining it have been heretofore suggested as carbonate factors `' --`1 ' for effervescent compositions, they have not been utilized in commercial products due primarily to the slow rate of carbon dioxide release they display in the effervescent reaction. For instance, it takes the calcite state of calcium carbonate from about ten to about fifteen times the length of time required for an equivalent amount of sodium bicarbonate to release the total available carbon dioxide in a given acidic aqueous solu-tion. Although several crystalline states of calcium carbonate are known such as the heretofore-mentioned calcite and others such as aragonite and vaterite, none have been known-to possess the requisite rate of carbon dioxide release for commercially feasible use in effervescent compositions. It is obvious, therefore, that a carbonate factor that contains calcium carbon-ate and that will rapidly undergo the effervescent reaction would be most welcome by those skilled in the art. Prior work-ers in this field have been unable to provide such a carbonate factor.
It is an object of the present invention to provide such a carbonate factor.
It is also an object of the present invention to pro-vide a process for producing calcium carbonate that can be read-ily utilized as a carbonate factor in effervescent composi-tions.
Furthermore, it is an object of the present invention to provide effervescent compositions that contain such a carbon-ate factor.
These and other objects and advantages will be appar-ent from a consideration of the following description of the inventlon .
Accordingly, this invention provides stabilized amor-~hous calcium carbonate.
In accordance with one embodiment of the present invention, there is provided a process for preparing stabilized amorphous calcium carbonate which comprises (l) forming an alka-line aqueous solution of calcium ions and a hydrogen-bonding ma-terial, (2) contacting the solution with carbon dioxide while maintaining the solution at a temperature below 15C to form a precipitate containing chemically-bound water and continuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while retaining hydrogen--bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amorphous calcium carbonate having a reactivity such that the time taken for a 0.18 g sam-ple to react completely when added to a stirred solution pre-pared by mixing 5 ml of O.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5~ when a 2 g sample of the stabilized amorphous calcium carbon-ate is stored in a sealed 29.6 ml glass bottle at 20-25C for one month~
In accordance with another embodiment of the present invention, there is provided a stabilized amcrphous calcium car-bonate that is the product of the above process.
In accordance with a further embodiment of the pre-sent invention, there is provided a dry concentrate for prepar-ing a carbonated beverage by admixture of the concentrate with water, said concentrate comprising an acid factor and a carbon-ate factor in less than the stoichiometric equivalent of the acid factor, characterized in that the carbonate factor com-prises the above stabilized amorphous calcium carbonate.
In accordance with a still further embodiment of the present invention, there is provided a composition comprising a dry carbonated beverage concentrate for preparing a carbonated beverage by admixture with water, said concentrate comprising:
36~5~
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in ex-cess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament.
Yet another embodiment of the present invention pro-vides a process for preparing a dry concentrate for use in pre-paring a carbonated beverage by admixture of the concentrate with water, comprising ~1) forming an alkaline aqueous solution of calcium ions and a hydrogen-bonding material,
This invention relates to calcium carbonate which is useful as a carbonating agent, to processes therefor and effer-vescent compositions containing same.
The reaction of acidic compositions, hereinafter re-ferred to as the "acid factor", with bicarbonate or carbonate-containing compositions, hereinafter referred to as the "carbon-ate factor", in an aqueous environment, such as a solution, to produce or release carbon dioxide is well known in the art and will hereinafter be referred to as the "effervescent reaction".
The effervescent reaction has heretofore been utilized in many fields, such as the food and medicament industries, where a rapid release of carbon dioxide at a controlled point in time is desirable.
Products that undergo the efervescent reaction upon use normally comprise a dry, solid mixture of an acid factor and a carbonate factor, said mixture being hereinafter referred to as an "effervescent composition". The acid factor and the carbonate factor in the effervescènt compositions are normally dry solids and are water soluble, at least in the presence of each other. Additionally, the acid and carbonate factors uti lized must be compatible with their intended use, i.e., if to be consumed, they must be physiologically acceptable.
Many such effervescent compositions have been pro-vided commercially. For instance, it is known that an efferves-cent composition of citric acid, sodium bicarbonate (in less than the stoichiometric equivalent of citric acid) and a flavor will provide a carbonated beverage upon adding the composition to the proper amount of water. Other examples of effervescent compositions are the well-known effervescent medicament tab-lets, baking sodas and the like. The major advantage of theseproducts is, of course, that the effervescent composition may be easily and economically stored as a dry solid and may then ~,.B~t~
be used, as desired, by merely contacting it with water to pro-duce a carbonated beverage, i.e., the release of carbon diox-ide.
The food industry has long sought commercially feas-ible products to provide a carbonated beverage from an efferves-cent composition. Such a beverage must be highly palatable and, as a practical matter, must afford a rapid rate of prepara-tion by the consumer. Normally, the consumer expects to be able to prepare the beverage in a short time, i.e., within about one to three minutes at the most. It is essential, there-fore that the effervescent composition rapidly undergo the effervescent reaction upon contact with water providing a car-bonated beverage that is highly palatable to the consumer.
Although many acid factors are available, such as citric acid, fumaric acid, adipic acid, malic acid, tartaric acid, etc., the primary carbonate factor heretoEore utilized in effervescent compositions has been sodium bicarbonate. Sodium bicarbonate is highly reactive with acid factors in aqueous solutions, rapidly releasing carbon dioxide, and has become the standard carbonate factor utilized by industry in effervescent compositions. Other carbonate factors, such as calcium carbon-ate and magnesium carbonate have been suggested as possible alternatives, but to date only sodium bicarbonate has been able to provide the desired rate of carbon dioxide release. Sodium bicarbonate does, however, have a major drawback, particularly in the food and medicament industries, in that it gives a dis-tinctly disagreeable saline or soapy taste to the solutions con-taining it, which is known to be due to the presence of the sodium ion. Accordingly, many attempts have been made to sub-stitute a more agreeable tasting cation in the carbonate fac-tors utilized in effervescent compositions.
A cation that provides excellent taste characteris-tics in aqueous solutions or compositions containing it is the calcium ion. Although calcium carbonate and compositions con-taining it have been heretofore suggested as carbonate factors `' --`1 ' for effervescent compositions, they have not been utilized in commercial products due primarily to the slow rate of carbon dioxide release they display in the effervescent reaction. For instance, it takes the calcite state of calcium carbonate from about ten to about fifteen times the length of time required for an equivalent amount of sodium bicarbonate to release the total available carbon dioxide in a given acidic aqueous solu-tion. Although several crystalline states of calcium carbonate are known such as the heretofore-mentioned calcite and others such as aragonite and vaterite, none have been known-to possess the requisite rate of carbon dioxide release for commercially feasible use in effervescent compositions. It is obvious, therefore, that a carbonate factor that contains calcium carbon-ate and that will rapidly undergo the effervescent reaction would be most welcome by those skilled in the art. Prior work-ers in this field have been unable to provide such a carbonate factor.
It is an object of the present invention to provide such a carbonate factor.
It is also an object of the present invention to pro-vide a process for producing calcium carbonate that can be read-ily utilized as a carbonate factor in effervescent composi-tions.
Furthermore, it is an object of the present invention to provide effervescent compositions that contain such a carbon-ate factor.
These and other objects and advantages will be appar-ent from a consideration of the following description of the inventlon .
Accordingly, this invention provides stabilized amor-~hous calcium carbonate.
In accordance with one embodiment of the present invention, there is provided a process for preparing stabilized amorphous calcium carbonate which comprises (l) forming an alka-line aqueous solution of calcium ions and a hydrogen-bonding ma-terial, (2) contacting the solution with carbon dioxide while maintaining the solution at a temperature below 15C to form a precipitate containing chemically-bound water and continuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while retaining hydrogen--bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amorphous calcium carbonate having a reactivity such that the time taken for a 0.18 g sam-ple to react completely when added to a stirred solution pre-pared by mixing 5 ml of O.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5~ when a 2 g sample of the stabilized amorphous calcium carbon-ate is stored in a sealed 29.6 ml glass bottle at 20-25C for one month~
In accordance with another embodiment of the present invention, there is provided a stabilized amcrphous calcium car-bonate that is the product of the above process.
In accordance with a further embodiment of the pre-sent invention, there is provided a dry concentrate for prepar-ing a carbonated beverage by admixture of the concentrate with water, said concentrate comprising an acid factor and a carbon-ate factor in less than the stoichiometric equivalent of the acid factor, characterized in that the carbonate factor com-prises the above stabilized amorphous calcium carbonate.
In accordance with a still further embodiment of the present invention, there is provided a composition comprising a dry carbonated beverage concentrate for preparing a carbonated beverage by admixture with water, said concentrate comprising:
36~5~
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in ex-cess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament.
Yet another embodiment of the present invention pro-vides a process for preparing a dry concentrate for use in pre-paring a carbonated beverage by admixture of the concentrate with water, comprising ~1) forming an alkaline aqueous solution of calcium ions and a hydrogen-bonding material,
(2) contacting the solution with carbon dioxicle while maintaining the solution at a temperature below 15C to form a precipitate containing chemically-bound water and con-tinuing said contacting until no more carbon dioxide is taken up, and
(3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while re-taining hydrogen-bonding material in the product and while main-taining the resulting product in an environment that is essen-tially free of unbound water, the said stabilized amorphous calcium carbonate hav-ing a reactivity such that the time taken for a 0.18 g sample to react completely when added to a stirred solution prepared by mixing 5 ml of O.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time ~or complete reaction does not increase by more than 5~ when a 2 g sample of the stabilized amorphous calcium carbonate is stored in a sealed 29.6 ml glass bottle at 20-25C for one month;
(4) and admixing said stabilized amorphous calcium carbonate with an acid factor.
- ~8 86~i5g~
Still another embodiment of the present invention pro-vides a process for preparing a dry, effervescent medicament composition which comprises admixing:
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in excess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament.
STABILI ZED AMORPHOUS CALCIUM CARBONATE
For purposes of this discussion the term "amorphous"
shall mean that morphological state of a material that does not show a crystalline state upon analysis by the known means of in-vestigating a material's morphological state. For instance, a material is considered to be amorphous if it does not show any X-ray pattern upon X-ray analysis and shows only one refractive index upon subjecting the material to refractive index analy-sis .
For purposes of this discussion the term "stabilized"
means that the amorphous material under consideration will re-main essentially in the amorphous state for significant periods of time, i.e., for at least one month and longer when stored in a closed container.
Amorphous calcium carbonate has been reported in sev-eral sources [Louisfert, J. et al., Compt. rend. 235, 287 (1952) and Gillott, J.E., J. Appl. Chem. 17 185 tl967)].
Gillott states that carbonate of Ca~OH)2 may result in the ormation of synthetic amorphous calcium carbonate which cry-stallizes to calcite in the presence of moisture at room temper-atu~e. Our experience with amorphous calcium carbonate agrees with Gillott's findings. We have found, however, that stabi-lized amorphous calcium carbonate is more resistant to calcite crystal formation than previously known amorphous calcium car-bonate.
It has been found that stabilized amorphous calcium carbonate has an infra-red spectrum quite similar to that ob-tained with the known crystalline states of calcium carbonate but distinguishable in that stabilized amorphous calcium carbon-ate gives a spectrum wherein the peaks obtained are significant-ly broader than those obtained with the known crystalline states of calcium carbonate.
Furthermore, examination under the electron micro-scope reveals a significant difference between stabilized amor-phous calcium carbonate and the known crystalline states of cal-cium carbonate (calcite/ aragonite and vaterite). Calcite cry-stals appear as well formed cubes unifcrm in size. Crystals of vaterite occur as spheres of different size while those of aragonite form fairly uniform neeales. In contrast, particles of stabilized amorphous calcium carbonate have no distinct size or shape at the same magnification. Further magnification reveals that stabilized amorphous calcium carbonate has a rough surface and non-uniform size suggesting an agglomerate of smal-ler particles. Still further magnification shows extremely small, substantially spherical particles with an average parti-cle size of from about 10 A to about 340 A at the edge oflarger, irregularly-shaped agglomerates. Upon subjecting stabi-lized amorphous calcium carbonate to X-ray analysis no X-ray pattern is obtained. These results indicate that, in fact, stabilized amorphous calcium carbonate is "amorphousl'.
The amorphous state of stabilized amorphous calcium carbonate was further confirmed by refractive index determina-tions. It was found that not only is stabilized amorphous cal-cium carbonate clearly isotropic but that it gives refractive indices that are distinctly different from the refractive indices found with other amorphous calcium carbonate and the known crystalline states of calcium carbonate.
Stabilized amorphous calcium carbonate is useful wher-ever small particle calcium carbonate has heretofore been found useful. Furthermore, stabilized amorphous calcium carbonate is ~' .~
i55~
extremely useful as a carbonate factor in effervescent composi-tions. Therefore, this invention also provides excellent effer-vescent compositions comprising an acid factor and stabili~ed amorphous calcium carbonate.
The term "hydrogen-bonding material" as utilized here-in means a material or combination of two or more materials that form hydrogen bonds in aqueous solutions. The hydrogen-bonding material is preferably an organic material whose mole-cule contains at least one oxygen or nitrogen atom that is cap-able of bonding hydrogen in another part of the same moleculeor in some other molecule. ~urthermore, the hydrogen-bonding material is preferably water-soluble at the temperatures contem-plated for the precipitate-forming step of the process of the present invention. It may occur that the hydrogen-bonding material is not completely water-soluble per se in the forma-tion of the aqueous solution but will go into solution as the precipitate-forming step proceeds; these materials are also within the scope of the present invention. Examples of hydroyen-bonding materials include all the mono-, di-, tri- and oligo- saccharides which are water-soluble such as sucrose, glu-cose, fructose and mannose, or saccharide derivatives of the hydrocolloid-type such as gum arabic, guar gum, propylene gly-col, alginate, carrageen; the alcohols and polyhydric materials which are water-soluble such as methanol, ethanol, propanol, sorbitol and glycerine, the amino acids which are water-soluble, including optically active and inactive materials and polymeric amino acids (peptides), such as glycine and lysine, aspartic acid, phenylalanine and the dipeptide esters thereof such as the methyl ester of L-aspartyl-L-phenylalanine; the car-boxylic and hydroxycarboxylic acids such as glycolic, acetic,tartaric and lactic acid. The preferred hydrogen-bonding materials are the saccharides due to their ready availability and usefulness in products to be consumed.
,.. . .
The concentration of the hydroyen-bonding material in the aqueous solution to be utilized in the present invention can generally be in the range of from about 2~ up to about 95%
by weight of the total solution. Although it is possible to carry out the process at lower and higher levels of hydrogen-bonding materials, it has been found that the range of from about 10% up to about 45% by weight is the most practical from a commercial operation point of view. However, it should be understood that, depending on the particular hydrogen-bonding materials selected, the concentration can be varied widely to obtain the desired results. For instance, excellent results have been obtained with a glycine concentration as low as about 10% whereas, with methanol, a concentration of about 90% has been found to give excellent results.
In determining the proper amount of hydrogen-bonding material to be utilized the physical effects of the hydrogen-bonding material in the a~ueous solution should be considered.
For instance, the aqueous solution should not contain so high a concentration o hydrogen-bonding material so as to form a solu-tion that is so viscous as to present problems such as poorheat transfer, poor mixing~ etc. The preferred amount of hydrogen-bonding material in the aqueous solution is in the range of from about 10% to about 30% by weight of the total solution. It has been found that when sucrose is utilized with-in this range excellent results have been obtained with the pro-cess of this invention.
The first step of the process of this invention com-prises the formation of an aqueous solution of calcium ions and the hydrogen-bonding material. The concentration of calcium ions in the solution should be in the range of from about 0.01%
to about 23~ by weight of the solution and preferably from about 1% to about 10%. Although, as a practical matter, this latter range is preferred, the process can in fact be carried out at lower levels of calcium ion concentration, dependent only on the payload desired, whereas the higher levels are ~8~5~
dependent on the amount of calcium ion that can be placed in solution which is, in turn, somewhat dependent upon the hydrogen-bonding material utilized and the tempera-ture at which the aqueous solution is formed.
Although there are a number of different ways to form the aqueous solution containing calcium ions and hydrogen-bonding material, this is not a critical aspect of the present invention and many different methods may be utilized to form this solution. For instance, the aqueous solution may be formed by dissolving such calcium-containing materials as cal-cium oxide, calcium hydroxide, calcium hydride, calcium per-oxide or other water-soluble calcium salts such as calcium chloride, etc. in either (a) water, and thereafter dispersing the hydrogen-bonding material therein, or in (b) an aqueous solution already containing the hydrogen-bonding material. It is also possible to utilize calcium metal to provide the cal-cium ions in the aqueous solution by contacting it with water, although this is somewhat impractical.
It is, of course, also possible to form the aqueous solution by admixing an aqueous solution of the calcium-containing material with an aqueous solution of the hydrogen-bonding material or any other such modifications thereof as long as the resulting aqueous solution has the proper concentra-tion of calcium ions and hydrogen-bonding material.
The water used for forming the aqueous solution can be either distilled water or tap water as long as an undue amount of hardness is avoided.
The temperature at which the solution is formed is not critical to the process of this invention, but it is prefer-ably below about 70C., so as to avoid any adverse conversionof the hydrogen-bonding material, such as, for instance, the inversion of sucrose. In particular, it has been found that excellent results can be obtained by forming the solution at ambient temperatures. Moreover, it has been found that when the hydrogen-bonding material is sucrose, the lower the tempera-ture of the aqueous solution, the higher the level of calcium ion concentration that can be provided in the solution which is, of course, particularly advantageous to the process of the present invention due to superior payloads per unit weight of aqueous solution.
Although insoluble impurities sometimes found in the aqueous solution of calcium ions and hydrogen-bonding material do not significantly affect the process of this invention, they can end up in the resulting prodwct as an impurity and result in a decreased reactivity of the stabilized amorphous calcium carbonate when it is utilized as a carbonate factor in an effer-vescent composition. It is prefçrred, therefore, that the solu-tion be filtered, centrifuged or otherwise treated so as to remove most, if not all, of the insoluble impurities found in the solution. Furthermore, it is preferred to form a solution in the first step of the process of this invention that is "clear", i.e., transparent, as opposed to an opaque solution.
This results in products that are substantially supe~ior in their functionality in the effervescent reaction.
In regard to the removal of insoluble impurities, there is a lower limitation on the temperature of the solution when removing the insoluble impurities because it has been found that the lower the temperature of the solution the slower the rate of removal, such as by filtration, and therefore the longer the time required for removing the insolubles. Because it has been found that the calcium ion concentration in the solution can be increased at lower temperatures with some hydrogen-bonding agents, this lower limit on the temperature at which removal of insolubles should take place will have to be balanced against the desirability of improving or increasing the calcium ion concentration. In general, it is preferred to remove most of the insoluble impurities from the solution at lower temperatures; that is, at as low a temperature as is pos-s;ble wherein the insoluble impurities will be at a minimum, s~
due to the higher solubillty of calcium-containing materials ak lower temperatures, without requiring an undue amount of time for removal. The insoluble impurities mentioned hereinabove may be excess calcium oxide, other calcium-containing materials such as calcium hydroxide, calcium carbonate and many of the other insoluble salts that are found normal:Ly as an impurity in calcium-containing materials.
Once the aqueous solution of calcium ions and hydro-gen-bonding material has been formed, the second step, which will herein be referred to as the "precipitate-forming step", consists of contacting~the resulting solution with carbon diox-ide in order to form a precipitate.
In general, it has been found that if the precipi-tate-forming step is carried out at lower temperatures, the stabilized amorphous calcium carbonate obtained has faster rates of reactivity in effervescent reactions.
Therefore, it should be noted here that the tempera-ture oE the aqueous solution during the precipitate-forming step should, in general, be maintained below about 15C. down to as low as about the freezing point of the aqueous solution in order to obtain the more reactive products of this inven-tion. Furthermore, it has been found that the temperature main-tained in the aqueous solution during the precipitate-forming step affects-the reproducibility of the desired products of this invention. Although the reasons for such an effect are not known, it has been found that the reproducibility of such products is greatly improved at the lower temperatures. Accord-ingly, it is preferred that the temperature of the aqueous solu-tion in this precipitate-forming step be below about 10C., and further preferred that the temperature be from about -5C.
'o about +5C. and still further preferred that the tempera-ture of the solution be from about -3C. to about 0C.
In regard to the temperature of the aqueous solution while the precipitate-forming step is being carried out, it has been observed that the presence of ice in the aqueous solution will assist in the maintaining of the proper temperature of the aqueous solution and also appears to assist in the formation of an excellent procluct. Although a good prodllct is obtained with-out the presence of ice, it should be noted that the presence of ice in the aqueous solution will improve the product ob-tained from the process of this invention.
The aqueous solution containing the hydrogen-bonding material and calcium ions is brought to the proper temperature and maintained at that temperature while contacting it with car-bon dioxide. The carbon dioxide may be in the form of a gas ora solid or may be introduced on the surface of the solution, sub-surface, or even contacted in a counter-current fashion.
The preferred method of contacting is subsurface to provide both intimate contact and good agitation. Carbon dioxide may also be introduced in conjunction with other gases, such as a converter gas, as long as the other gases are inert.
Sufficient agitation of the aqueous solution should be provided so that the temperature of the solution at any par-ticular location in the aqueous solution does not rise above about 15C. (i.e., to prevent localized "hot spots").
In carrying out the precipitate-forming step, the aqueous solution must, at the outset, be in a basic or alkaline state to form a precipitate. The pH will decrease as the preci-pitation takes place. It has been found that this alkaline pH
condition is necessary to obtain stabilized amorphous calcium carbonate. This alkaline state can ordinarily be obtained by utilizing those forms of calcium that will form basic or alka-line solutions upon contact with water but it can also be ob-tained by incorporating alkaline materials in the aqueous solu-tion.
The carbon dioxide should be introduced into theaqueous solution until no further carbon dioxide is taken up.
(The carbon dioxide can continue to be introduced but it has no further effect on the aqueous solution.) If the aqueous solu-tion evolves carbon dioxide (other than the normal carbon diox-ide evolving from a carbon dioxide saturated aqueous solution) then the aqueous solution should be allowed to equilibrate un-til substantially all of the carbon dioxide has evolved.
The precipitate formed in the precipitate-forming step is a form of calcium carbonate that contains a large pro-portion by weight, based on the weight of the precipitate, of chemically-bound water and also contains a hydrogen-bonding material.
This precipitate must then be treated to reduce the amount of chemically-bound water contained in the resulting pre-cipitate to below about 15%, or in other words, to cause a "dehydration" of the precipitate. It is critical that -the dehy-dration be carried out in a manner such that the resulting com-position is maintained in an environment that is essentially free of unbound water. By this statement it is meant that r to provide the products of the present invention by proper dehydra-tion, means must be provided to substantially avoid contacting the resulting composition with water that is in a free state;
either water from the aqueous solution or water that has been released from the precipitate. It has been found that the novel products of this invention can only be provided in this manner.
Several methods have been developed to carry out the dehydration. One of these methods comprises isolating the pre-cipitate from the aqueous solution by recovering the precipi-tate from the solution and washing it with a volatile organic solvent and subsequently dehydrating the precipitate in an environment that facilitates a substantially instantaneous removal of a portion of the chemically-bound water from the remaining composition once the water has been released from its chemically-bound form in the precipitate. This method is des-cribed in greater detail as follows.
i5i~3 Once the precipitate-forming step of the process of this invention has been completed, the precipitate can be recov-ered from the aqueous solution. Recovery can be carried out by any of the usual means of recovering a solid from a li~uid con-taining it, such as, by filtration, centrifugation or sedimenta-tion, etc., resulting in a cake of the precipitate with some of the aqueous solution adhering to it.
The recovered cake can then be washed free of the aqueous solution by solvent displacement with a water-miscible organic solvent so as to remove the last traces of any remain-ing aqueous solution that may be adhering to the particles of the precipitate. The preferred water-miscible organic solvents to be utilized in washing the cake are the lower alkyl alco-hols, such as methanol, ethanol or isopropanol; or the ketones, such as acetone that can be readily removed from the precipi-tate by drying at low temperatures. This results in a material that is free of any of the aqueous solution from which it was ormed.
It has been ~ound that some organic solvents will not only remove the aqueous solution adhering to the precipitate cake but will also cause some portion of the chemically-bound water to be removed. This is not only not detrimental but is desirable as it requires less dehydration of the resulting iso-lated precipitate without adversely affecting the resulting end product.
During recovery and washing it is preferred to main-tain the precipitate at low temperatures until the cake i5 sub-stantially free of the aqueous solution. It is preferred to conduct the isolation, including the solvent displacement or washing portion, at temperatures below about 15C. and prefer-ably at temperatures below about 10C. and particularly pre-ferred at temperatures of from about -5C. to about +5C.
This provides excellent products of this invention.
The temperatures utilized in removing the water-miscible solvent from the precipitate may vary somewhat depend-ing on the particular organic solvent utilized for washing the Stj~
precipitate without adverse effects in the resulting products.
For instance it has been found that, when utilizing me-thanol, a temperature up to about 40C. can be used whereas with acetone and ethanol a temperature higher than about 5C. can cause adverse effects in the resulting produc-ts.
After washing with the organic so]vent, it has been found that the water now remaini~g in the precipitate is chemi-cally-bound rather than merely adhering to the precipitate par-ticles and is a large part by weight of the precipitate.
The precipitate must then be treated to reduce the amount of chemically-bound water contained therein to below about 15~ so as to provide stabilized amorphous calcium carbon-ate. The reduction of the amount of chemically-bound water in the resulting precipitate is accomplished by treating the preci-pitate in a particular manner for removal of the chemically-bound water and should be clearly distinguished from the isola-tion of recovery of the precipitate from the aqueous solution as previously described. In particular, the precipitate as isolated above must now be treated in an environment that faci-litates the substantially instantaneous removal of a portion of the chemically-bound water from the remaining composition once the water has been released from its chemically-bound form in the precipitate. In other words, there is a two-fold effect required that co~prises (a) causing a portion of the chemically-bound water to be released from the combination in which it is bound, while (b) substantially instantaneously removing the water so released from the resulting composition.
The dehydration can be carried out by va~ious means and in many types of equipment. For instance, it has been found that excellent dehydration results are obtained by treat-ing the solvent washed and dried precipitate in vacuum ovens, fluid bed dryers, and, although the length of time required is increased, even dehydration ~y air drying in low humidity condi-tions. In each of these procedures the solvent washed and . ~
, dried precipitate is treated so as to cause a portion of the chemically-bound water to be released while substantially instantaneously removing the water from the surrounding composi-tion as it is released. Dehydration should be continued until the amount of chemically-bound water remaining in the resulting composition is less than 15~ by weight. While the chemically-bound water content can be reduced to as low as about 0.1% of the resulting composition the dehydration is preferably stopped when the chemically-bound water content is from about 2~ to about 5~ by weight of the composition.
The undehydrated precipitate, after isolation from the solution in which it was formed and whether solvent washed or not, is a soft, friable semi-solid. When properly dehy-drated it retains this friable condition but becomes harder and more solid.~ If not properly dehydrated, i.e., the water is not removed rapidly enough, the soft, friable semi-solid loses its shape and becomes a slurry. Drying the slurry results in a hard, brittle, chalk-like solid which is apparently the calcite crystalline state of calcium carbonate which does not have the desired rate of reactivity in the effervescent reaction. This undesirable effect will be hereinafter referred to as ~Idecompo-sition".
In another illustrative embodiment of the dehydration portion of the process of the present invention, it has been found that dehydration can be carried out in the following man-ner. This embodiment consists of forming a cold aqueous slurry of the precipitate formed in the precipitate-forming step of the process of this invention and spray drying the slurry.
One way of preparing the cold aqueous slurry is by separating the major portion of the aqueous solution, in which the precipitate was formed, by such means as filtration, centri-fugation, sedimentation, etc., leaving a wet cake which has adhering to it a small amount of aqueous solution and subse-quently slurrying the wet cake in cold water.
- ~8 86~i5g~
Still another embodiment of the present invention pro-vides a process for preparing a dry, effervescent medicament composition which comprises admixing:
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in excess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament.
STABILI ZED AMORPHOUS CALCIUM CARBONATE
For purposes of this discussion the term "amorphous"
shall mean that morphological state of a material that does not show a crystalline state upon analysis by the known means of in-vestigating a material's morphological state. For instance, a material is considered to be amorphous if it does not show any X-ray pattern upon X-ray analysis and shows only one refractive index upon subjecting the material to refractive index analy-sis .
For purposes of this discussion the term "stabilized"
means that the amorphous material under consideration will re-main essentially in the amorphous state for significant periods of time, i.e., for at least one month and longer when stored in a closed container.
Amorphous calcium carbonate has been reported in sev-eral sources [Louisfert, J. et al., Compt. rend. 235, 287 (1952) and Gillott, J.E., J. Appl. Chem. 17 185 tl967)].
Gillott states that carbonate of Ca~OH)2 may result in the ormation of synthetic amorphous calcium carbonate which cry-stallizes to calcite in the presence of moisture at room temper-atu~e. Our experience with amorphous calcium carbonate agrees with Gillott's findings. We have found, however, that stabi-lized amorphous calcium carbonate is more resistant to calcite crystal formation than previously known amorphous calcium car-bonate.
It has been found that stabilized amorphous calcium carbonate has an infra-red spectrum quite similar to that ob-tained with the known crystalline states of calcium carbonate but distinguishable in that stabilized amorphous calcium carbon-ate gives a spectrum wherein the peaks obtained are significant-ly broader than those obtained with the known crystalline states of calcium carbonate.
Furthermore, examination under the electron micro-scope reveals a significant difference between stabilized amor-phous calcium carbonate and the known crystalline states of cal-cium carbonate (calcite/ aragonite and vaterite). Calcite cry-stals appear as well formed cubes unifcrm in size. Crystals of vaterite occur as spheres of different size while those of aragonite form fairly uniform neeales. In contrast, particles of stabilized amorphous calcium carbonate have no distinct size or shape at the same magnification. Further magnification reveals that stabilized amorphous calcium carbonate has a rough surface and non-uniform size suggesting an agglomerate of smal-ler particles. Still further magnification shows extremely small, substantially spherical particles with an average parti-cle size of from about 10 A to about 340 A at the edge oflarger, irregularly-shaped agglomerates. Upon subjecting stabi-lized amorphous calcium carbonate to X-ray analysis no X-ray pattern is obtained. These results indicate that, in fact, stabilized amorphous calcium carbonate is "amorphousl'.
The amorphous state of stabilized amorphous calcium carbonate was further confirmed by refractive index determina-tions. It was found that not only is stabilized amorphous cal-cium carbonate clearly isotropic but that it gives refractive indices that are distinctly different from the refractive indices found with other amorphous calcium carbonate and the known crystalline states of calcium carbonate.
Stabilized amorphous calcium carbonate is useful wher-ever small particle calcium carbonate has heretofore been found useful. Furthermore, stabilized amorphous calcium carbonate is ~' .~
i55~
extremely useful as a carbonate factor in effervescent composi-tions. Therefore, this invention also provides excellent effer-vescent compositions comprising an acid factor and stabili~ed amorphous calcium carbonate.
The term "hydrogen-bonding material" as utilized here-in means a material or combination of two or more materials that form hydrogen bonds in aqueous solutions. The hydrogen-bonding material is preferably an organic material whose mole-cule contains at least one oxygen or nitrogen atom that is cap-able of bonding hydrogen in another part of the same moleculeor in some other molecule. ~urthermore, the hydrogen-bonding material is preferably water-soluble at the temperatures contem-plated for the precipitate-forming step of the process of the present invention. It may occur that the hydrogen-bonding material is not completely water-soluble per se in the forma-tion of the aqueous solution but will go into solution as the precipitate-forming step proceeds; these materials are also within the scope of the present invention. Examples of hydroyen-bonding materials include all the mono-, di-, tri- and oligo- saccharides which are water-soluble such as sucrose, glu-cose, fructose and mannose, or saccharide derivatives of the hydrocolloid-type such as gum arabic, guar gum, propylene gly-col, alginate, carrageen; the alcohols and polyhydric materials which are water-soluble such as methanol, ethanol, propanol, sorbitol and glycerine, the amino acids which are water-soluble, including optically active and inactive materials and polymeric amino acids (peptides), such as glycine and lysine, aspartic acid, phenylalanine and the dipeptide esters thereof such as the methyl ester of L-aspartyl-L-phenylalanine; the car-boxylic and hydroxycarboxylic acids such as glycolic, acetic,tartaric and lactic acid. The preferred hydrogen-bonding materials are the saccharides due to their ready availability and usefulness in products to be consumed.
,.. . .
The concentration of the hydroyen-bonding material in the aqueous solution to be utilized in the present invention can generally be in the range of from about 2~ up to about 95%
by weight of the total solution. Although it is possible to carry out the process at lower and higher levels of hydrogen-bonding materials, it has been found that the range of from about 10% up to about 45% by weight is the most practical from a commercial operation point of view. However, it should be understood that, depending on the particular hydrogen-bonding materials selected, the concentration can be varied widely to obtain the desired results. For instance, excellent results have been obtained with a glycine concentration as low as about 10% whereas, with methanol, a concentration of about 90% has been found to give excellent results.
In determining the proper amount of hydrogen-bonding material to be utilized the physical effects of the hydrogen-bonding material in the a~ueous solution should be considered.
For instance, the aqueous solution should not contain so high a concentration o hydrogen-bonding material so as to form a solu-tion that is so viscous as to present problems such as poorheat transfer, poor mixing~ etc. The preferred amount of hydrogen-bonding material in the aqueous solution is in the range of from about 10% to about 30% by weight of the total solution. It has been found that when sucrose is utilized with-in this range excellent results have been obtained with the pro-cess of this invention.
The first step of the process of this invention com-prises the formation of an aqueous solution of calcium ions and the hydrogen-bonding material. The concentration of calcium ions in the solution should be in the range of from about 0.01%
to about 23~ by weight of the solution and preferably from about 1% to about 10%. Although, as a practical matter, this latter range is preferred, the process can in fact be carried out at lower levels of calcium ion concentration, dependent only on the payload desired, whereas the higher levels are ~8~5~
dependent on the amount of calcium ion that can be placed in solution which is, in turn, somewhat dependent upon the hydrogen-bonding material utilized and the tempera-ture at which the aqueous solution is formed.
Although there are a number of different ways to form the aqueous solution containing calcium ions and hydrogen-bonding material, this is not a critical aspect of the present invention and many different methods may be utilized to form this solution. For instance, the aqueous solution may be formed by dissolving such calcium-containing materials as cal-cium oxide, calcium hydroxide, calcium hydride, calcium per-oxide or other water-soluble calcium salts such as calcium chloride, etc. in either (a) water, and thereafter dispersing the hydrogen-bonding material therein, or in (b) an aqueous solution already containing the hydrogen-bonding material. It is also possible to utilize calcium metal to provide the cal-cium ions in the aqueous solution by contacting it with water, although this is somewhat impractical.
It is, of course, also possible to form the aqueous solution by admixing an aqueous solution of the calcium-containing material with an aqueous solution of the hydrogen-bonding material or any other such modifications thereof as long as the resulting aqueous solution has the proper concentra-tion of calcium ions and hydrogen-bonding material.
The water used for forming the aqueous solution can be either distilled water or tap water as long as an undue amount of hardness is avoided.
The temperature at which the solution is formed is not critical to the process of this invention, but it is prefer-ably below about 70C., so as to avoid any adverse conversionof the hydrogen-bonding material, such as, for instance, the inversion of sucrose. In particular, it has been found that excellent results can be obtained by forming the solution at ambient temperatures. Moreover, it has been found that when the hydrogen-bonding material is sucrose, the lower the tempera-ture of the aqueous solution, the higher the level of calcium ion concentration that can be provided in the solution which is, of course, particularly advantageous to the process of the present invention due to superior payloads per unit weight of aqueous solution.
Although insoluble impurities sometimes found in the aqueous solution of calcium ions and hydrogen-bonding material do not significantly affect the process of this invention, they can end up in the resulting prodwct as an impurity and result in a decreased reactivity of the stabilized amorphous calcium carbonate when it is utilized as a carbonate factor in an effer-vescent composition. It is prefçrred, therefore, that the solu-tion be filtered, centrifuged or otherwise treated so as to remove most, if not all, of the insoluble impurities found in the solution. Furthermore, it is preferred to form a solution in the first step of the process of this invention that is "clear", i.e., transparent, as opposed to an opaque solution.
This results in products that are substantially supe~ior in their functionality in the effervescent reaction.
In regard to the removal of insoluble impurities, there is a lower limitation on the temperature of the solution when removing the insoluble impurities because it has been found that the lower the temperature of the solution the slower the rate of removal, such as by filtration, and therefore the longer the time required for removing the insolubles. Because it has been found that the calcium ion concentration in the solution can be increased at lower temperatures with some hydrogen-bonding agents, this lower limit on the temperature at which removal of insolubles should take place will have to be balanced against the desirability of improving or increasing the calcium ion concentration. In general, it is preferred to remove most of the insoluble impurities from the solution at lower temperatures; that is, at as low a temperature as is pos-s;ble wherein the insoluble impurities will be at a minimum, s~
due to the higher solubillty of calcium-containing materials ak lower temperatures, without requiring an undue amount of time for removal. The insoluble impurities mentioned hereinabove may be excess calcium oxide, other calcium-containing materials such as calcium hydroxide, calcium carbonate and many of the other insoluble salts that are found normal:Ly as an impurity in calcium-containing materials.
Once the aqueous solution of calcium ions and hydro-gen-bonding material has been formed, the second step, which will herein be referred to as the "precipitate-forming step", consists of contacting~the resulting solution with carbon diox-ide in order to form a precipitate.
In general, it has been found that if the precipi-tate-forming step is carried out at lower temperatures, the stabilized amorphous calcium carbonate obtained has faster rates of reactivity in effervescent reactions.
Therefore, it should be noted here that the tempera-ture oE the aqueous solution during the precipitate-forming step should, in general, be maintained below about 15C. down to as low as about the freezing point of the aqueous solution in order to obtain the more reactive products of this inven-tion. Furthermore, it has been found that the temperature main-tained in the aqueous solution during the precipitate-forming step affects-the reproducibility of the desired products of this invention. Although the reasons for such an effect are not known, it has been found that the reproducibility of such products is greatly improved at the lower temperatures. Accord-ingly, it is preferred that the temperature of the aqueous solu-tion in this precipitate-forming step be below about 10C., and further preferred that the temperature be from about -5C.
'o about +5C. and still further preferred that the tempera-ture of the solution be from about -3C. to about 0C.
In regard to the temperature of the aqueous solution while the precipitate-forming step is being carried out, it has been observed that the presence of ice in the aqueous solution will assist in the maintaining of the proper temperature of the aqueous solution and also appears to assist in the formation of an excellent procluct. Although a good prodllct is obtained with-out the presence of ice, it should be noted that the presence of ice in the aqueous solution will improve the product ob-tained from the process of this invention.
The aqueous solution containing the hydrogen-bonding material and calcium ions is brought to the proper temperature and maintained at that temperature while contacting it with car-bon dioxide. The carbon dioxide may be in the form of a gas ora solid or may be introduced on the surface of the solution, sub-surface, or even contacted in a counter-current fashion.
The preferred method of contacting is subsurface to provide both intimate contact and good agitation. Carbon dioxide may also be introduced in conjunction with other gases, such as a converter gas, as long as the other gases are inert.
Sufficient agitation of the aqueous solution should be provided so that the temperature of the solution at any par-ticular location in the aqueous solution does not rise above about 15C. (i.e., to prevent localized "hot spots").
In carrying out the precipitate-forming step, the aqueous solution must, at the outset, be in a basic or alkaline state to form a precipitate. The pH will decrease as the preci-pitation takes place. It has been found that this alkaline pH
condition is necessary to obtain stabilized amorphous calcium carbonate. This alkaline state can ordinarily be obtained by utilizing those forms of calcium that will form basic or alka-line solutions upon contact with water but it can also be ob-tained by incorporating alkaline materials in the aqueous solu-tion.
The carbon dioxide should be introduced into theaqueous solution until no further carbon dioxide is taken up.
(The carbon dioxide can continue to be introduced but it has no further effect on the aqueous solution.) If the aqueous solu-tion evolves carbon dioxide (other than the normal carbon diox-ide evolving from a carbon dioxide saturated aqueous solution) then the aqueous solution should be allowed to equilibrate un-til substantially all of the carbon dioxide has evolved.
The precipitate formed in the precipitate-forming step is a form of calcium carbonate that contains a large pro-portion by weight, based on the weight of the precipitate, of chemically-bound water and also contains a hydrogen-bonding material.
This precipitate must then be treated to reduce the amount of chemically-bound water contained in the resulting pre-cipitate to below about 15%, or in other words, to cause a "dehydration" of the precipitate. It is critical that -the dehy-dration be carried out in a manner such that the resulting com-position is maintained in an environment that is essentially free of unbound water. By this statement it is meant that r to provide the products of the present invention by proper dehydra-tion, means must be provided to substantially avoid contacting the resulting composition with water that is in a free state;
either water from the aqueous solution or water that has been released from the precipitate. It has been found that the novel products of this invention can only be provided in this manner.
Several methods have been developed to carry out the dehydration. One of these methods comprises isolating the pre-cipitate from the aqueous solution by recovering the precipi-tate from the solution and washing it with a volatile organic solvent and subsequently dehydrating the precipitate in an environment that facilitates a substantially instantaneous removal of a portion of the chemically-bound water from the remaining composition once the water has been released from its chemically-bound form in the precipitate. This method is des-cribed in greater detail as follows.
i5i~3 Once the precipitate-forming step of the process of this invention has been completed, the precipitate can be recov-ered from the aqueous solution. Recovery can be carried out by any of the usual means of recovering a solid from a li~uid con-taining it, such as, by filtration, centrifugation or sedimenta-tion, etc., resulting in a cake of the precipitate with some of the aqueous solution adhering to it.
The recovered cake can then be washed free of the aqueous solution by solvent displacement with a water-miscible organic solvent so as to remove the last traces of any remain-ing aqueous solution that may be adhering to the particles of the precipitate. The preferred water-miscible organic solvents to be utilized in washing the cake are the lower alkyl alco-hols, such as methanol, ethanol or isopropanol; or the ketones, such as acetone that can be readily removed from the precipi-tate by drying at low temperatures. This results in a material that is free of any of the aqueous solution from which it was ormed.
It has been ~ound that some organic solvents will not only remove the aqueous solution adhering to the precipitate cake but will also cause some portion of the chemically-bound water to be removed. This is not only not detrimental but is desirable as it requires less dehydration of the resulting iso-lated precipitate without adversely affecting the resulting end product.
During recovery and washing it is preferred to main-tain the precipitate at low temperatures until the cake i5 sub-stantially free of the aqueous solution. It is preferred to conduct the isolation, including the solvent displacement or washing portion, at temperatures below about 15C. and prefer-ably at temperatures below about 10C. and particularly pre-ferred at temperatures of from about -5C. to about +5C.
This provides excellent products of this invention.
The temperatures utilized in removing the water-miscible solvent from the precipitate may vary somewhat depend-ing on the particular organic solvent utilized for washing the Stj~
precipitate without adverse effects in the resulting products.
For instance it has been found that, when utilizing me-thanol, a temperature up to about 40C. can be used whereas with acetone and ethanol a temperature higher than about 5C. can cause adverse effects in the resulting produc-ts.
After washing with the organic so]vent, it has been found that the water now remaini~g in the precipitate is chemi-cally-bound rather than merely adhering to the precipitate par-ticles and is a large part by weight of the precipitate.
The precipitate must then be treated to reduce the amount of chemically-bound water contained therein to below about 15~ so as to provide stabilized amorphous calcium carbon-ate. The reduction of the amount of chemically-bound water in the resulting precipitate is accomplished by treating the preci-pitate in a particular manner for removal of the chemically-bound water and should be clearly distinguished from the isola-tion of recovery of the precipitate from the aqueous solution as previously described. In particular, the precipitate as isolated above must now be treated in an environment that faci-litates the substantially instantaneous removal of a portion of the chemically-bound water from the remaining composition once the water has been released from its chemically-bound form in the precipitate. In other words, there is a two-fold effect required that co~prises (a) causing a portion of the chemically-bound water to be released from the combination in which it is bound, while (b) substantially instantaneously removing the water so released from the resulting composition.
The dehydration can be carried out by va~ious means and in many types of equipment. For instance, it has been found that excellent dehydration results are obtained by treat-ing the solvent washed and dried precipitate in vacuum ovens, fluid bed dryers, and, although the length of time required is increased, even dehydration ~y air drying in low humidity condi-tions. In each of these procedures the solvent washed and . ~
, dried precipitate is treated so as to cause a portion of the chemically-bound water to be released while substantially instantaneously removing the water from the surrounding composi-tion as it is released. Dehydration should be continued until the amount of chemically-bound water remaining in the resulting composition is less than 15~ by weight. While the chemically-bound water content can be reduced to as low as about 0.1% of the resulting composition the dehydration is preferably stopped when the chemically-bound water content is from about 2~ to about 5~ by weight of the composition.
The undehydrated precipitate, after isolation from the solution in which it was formed and whether solvent washed or not, is a soft, friable semi-solid. When properly dehy-drated it retains this friable condition but becomes harder and more solid.~ If not properly dehydrated, i.e., the water is not removed rapidly enough, the soft, friable semi-solid loses its shape and becomes a slurry. Drying the slurry results in a hard, brittle, chalk-like solid which is apparently the calcite crystalline state of calcium carbonate which does not have the desired rate of reactivity in the effervescent reaction. This undesirable effect will be hereinafter referred to as ~Idecompo-sition".
In another illustrative embodiment of the dehydration portion of the process of the present invention, it has been found that dehydration can be carried out in the following man-ner. This embodiment consists of forming a cold aqueous slurry of the precipitate formed in the precipitate-forming step of the process of this invention and spray drying the slurry.
One way of preparing the cold aqueous slurry is by separating the major portion of the aqueous solution, in which the precipitate was formed, by such means as filtration, centri-fugation, sedimentation, etc., leaving a wet cake which has adhering to it a small amount of aqueous solution and subse-quently slurrying the wet cake in cold water.
5'i~
Alternatively~ less of the aqueous solution can be separated from the precipitate leaving a cold aqueous slurry of the precipitate in the aqueous solution. The degree of separa-tion of the aqueous solution from the precipitate will depend on the desirability of recycling the aqueous solution back through the first step of the process of this invention so as to avoid undue use of the hydrogen-bonding material balanced against the economics of providing cold make-up water to reslur-ry the cake. The cold aqueous slurry formed may even be a com-promise between the two above illustrations wherein the aqueous solution is not separated enough to form a cake of the precipi- ;
tate but cold water is added, nevertheless, to provide the slur-ry desired. In any case, the resulting slurry should be main-tained at all times during formation and until drying below about 15C. so as to avoid adverse effects on the resulting product.
The cold aqueous slurry is then spray dried while maintaining the spray dryer at conditions sufficient to rapidly dry and dehydrate the slurry and precipitate that is being introduced into the spray dryer at below about 15C.
It has been found that this embodiment of the process of the present invention will result in a combination of com-pleting the isolation of the precipitate from the aqueous solu-tion in which it was formed and at the same time causing the release of chemically-bound water while substantially instan-taneously removing the water so released. This portion of the process of this invention is thereby simplified and improved resulting in less preparation time. Furthermore, this proce-dure eliminates the necessity of washing the precipitate with a 30 water-miscible solvent.
It is to be noted that the effect on the precipitate using spray drying is essentially the same as previously dis-closed. That is, the action of the spra~ dryer removes the remaining aqueous solution from the precipitate which, in essence, completes the isolation as previously described and~
, 5~
concurrently, the spray drying causes a release of most of the chemically-bound water from the precipitate while causing the substantially instantaneous removal of the water so freed from the surrounding composition. It has been found that the result-ing chemically~bound water in the product is within the pre-ferred range of chemically-bound water content.
It should be understood that the products of this invention while having the desirable characteristics previously described can also have some of the undesirable properties of materials of the prior art due to partial decomposition appar-entiy due to conditions maintained during the dehydration step.
A test was developed to measure the reactivity of various calcium carbonates which is as follows: 200 milli-liters of distilled water is mixed with 5.0 milliliters of 1.0 normal citric acid solution to form a solution that contains 5 milli-equivalents of citric acid. The pH of this citric acid solution is 2.6 as measured on a Leeds and Northrup pH meter with expandable scale (the full scale deflection is 2 pH
units). The pH meter is connected to a Leeds and Northrup recorder with a 6.5 inch width chart and a speed equivalent to 8 inches per minute and adjusted so that full scale deflection is 2 pH units. The electrodes of the pH meter are immersed in the citric acid solution and the beaker containing the solution is placed on a magnetic stirrer. The stirrer is adjusted to approximately 125 rpm. The pH meter is ad~usted to 0 deflec-tion (the recorder is therefore also at 0 deflection). The recorder chart is activated. A 0.18 gram sample of the calcium carbonate to be tested is then added to the beaker. The pH of the solution, as recorded on the recorder, will increase until all of the calcium carbonate has reacted and the reaction is considered to be complete when the pH of the solution no longer increases. By determining the point at which the pH no longer increases, the length of time required for a particular sample of calcium carbonate to react can be observed.
~;
S~ f Utili~ing this reactivity test, the "reactivity" of various calcium carbonates can be determined. It has been found that those calcium carbonates that have a reactivity time of less than one minute, when measured by the above test, will provide carbonate factors for effervescent compositions that are extremely useful in that they are capable of supporting extremely rapid effervescent reactions upon use. The process of the present invention will provide such calcium carbonates.
During the investigations which resulted in the lCf present invention it was found that some calcium carbonates prepared, although initially possessing this desirable characteristic of rapid reactivity, would lose their rapid reactivity after periods of storage. It was found that, in contact with saturated air, many such rapidly reactive calcium carbonates quickly lose their rapid reactivity. A lower degree of saturation or relative humidity resulted in a slower loss in the rapid reactivity. Those samples that were stored under low humidity conditions retained their rapid reactivity for longer periods of time.
2Q It was found that the most severe conditions of storage for such calcium carbonates is storage in a small sealed container (i.e. with very little air space~. This is apparently due to the fact that the sample has only to give up a very small amount of water to saturate the air in the container. (Saturated air at 22.2C. contains 0.0002 grams water vapor/cc.) s~
In order to determine the "storability" of various rapidly reactive calcium carbonates including those of the pre-sent invention the following test was developed. Weiyh 2.0 g.
of a sample into a 1 oz. glass bottle and seal with a cap.
Store the bottle and contents at room temperature (20-25C.).
At the end of one month storage measure reactivity by the above-described test. If the "reactivity" increases more than 5% in this test the sample tested does not have an acceptable storability.
In generall we have found that a chemically-bound water content in stabilized amorphous calcium carbonate of below about 5% is desired for good storability. However~ it has been found that the storability of the materials of this invention is not solely dependent on the chemically-bound water content. Materials have been prepared containing as much as 15~ chemically-bound water which have been found storable for greater than 3 months and other materials containing only 2 water were found to be nonstorable in less than one month.
It is preferred, however, that stabilized amorphous calcium carbonate have a water content of no more than about 5 to have a reasonably predictable and acceptable storability.
The process of the present invention will be more rea-dily understood by reference to the following examples, of which Example 1 is a general procedure, which are understood not to limit the present invention, but to be construed broadly 5~
and be restricted solely by the appended claims. In these exam-ples the water content of the dehydrated precipitate refers to chemically-bound water content. Unless otherwise noted in these examples, analyses of the products resulting from the following procedures show the presence therein of the hydrogen-bonding material utilized.
In a suitable vessel, an aqueous solution of calcium ions and sucrose is prepared. The preferred amount of sucrose in the aqueous solution is from about 10% to about 30% by weight of the solution. The concentration of calcium ions in the solution can be from about .~1~ to about 23% by weight calcium per weight of the total solution. This solution may be formed by dispersing such calcium-containing materials as a calcium oxide, calcium hydroxide, calcium hydride, calcium peroxide or other water soluble salts such as calcium chlorides, etc., in either water and subsequently adding sucrose, or in an aqueous sucrose solution. It is preferred to add the calcium-containing material before the sucrose, and it has been found tha~ the calcium ion solubility is increased as the sucrose concentration in the aqueous solution is increased.
It is preferred to form the calcium ions and sucrose aqueous solution by adding calcium oxide to water to form a slaked lime slurry adding sucrose to the resulting slurry. For illustrative purposes calcium oxide will be utrilized in this example. The purity of the sucrose material is not critical as long as excessive amounts of impurities are avoided.
The purity of the calcium oxide utilized is also not critical, but it is undesirable to have much more than a trace amount of magnesium ions associated with the aqueous solution~
It is also particularly helpful in forming the solution to . ~
~ i 5S~3 select the materials that have uniformly small particle sizes so as to afford a fairly rapid rate of dissolving the material.
It is preferred to obtain an aqueous solution that has both sucrose and calcium at the higher levels oE the above-noted ranges due to superior yields in product per unit weight of solution.
The temperature utilized in forming the solution is not critical to the process of this invent:ion, but it is preferably below about 70C. so as to avoid any adverse conversion of the sucrose such as by inversion. Furthermore, it has been found that the lower the temperature of the sucrose-containing aqueous solution when adding the calcium oxide thereto, the higher the concentration of calcium ions that can be placed in the solution. It is preferred to remove any insolubles remaining in the solution.
The resulting aqueous solution of sucrose and calcium ions is then contacted with carbon dioxide. The solution is at a temperature preferably of from about -3C. to about -~3C., and maintained at that temperature while contacting it with carbon dioxide. The carbon dioxide is in the form of a gas and is introduced into the solution subsurface. This provides both ; intimate contact and good agitation. A precipitate begins to form after about 1.4 to about 1.5 moles carbon dioxide/moles calcium in the solution has been consumed and continues to form until about 1.7 to about 2.2 moles of carbon dioxide per mole of calcium has been consumed; the formation of a precipitate in this phase is exothermic. At this point, it is preferred to stop the feeding of the carbon dioxide to the solution, although the processs of this invention can be carried out by continuing to feed carbon dioxide into the solution.
it~
When the exothermic phase of the precipitate-forming step has been concluded, the solution begins to evolve carbon dioxide in an endothermic phase. If the carbon dioxide feed stream is continuously being fed to the aqueous solution, it can be observed that the amount being released from the solution is greater than the amount being added thereto. If the carbon dioxide feed stream to the aqueous solution has been stopped at the end of the exothermic phase as above-described the solution containing the precipitate will evolve carbon dioxide. In either case, this endothermic carbon dioxide-releasing phase continues until the mole ratio of consumed carbon dioxide to calcium in the solution is about 1.0 moles of carbon dioxide per mole of calcium. It is critical in the formation of the precipitate that the phases as described above be completed and, further, that the second phase be continued until the point where carbon dioxide release has essentially ceased.
The precipitate is then isolated from the solution, such as by centrifugation, followed by washing with water-miscible solvent and evaporating the solvent. This procedure results in a washed precipitate that is free of any of the solution from which it was formed. Any water remaining in the precipitate is chemically-bound rather than merely adhering to the precipitate particles. The amount of this chemically-bound water must be reduced below about 15% so as to provide stabilized amorphous calcium carbonate.
The washed precipitate is then dehydrated. For instance, this can be carried out most readily in a vacuum oven at high vacuum that continuously removes the water as it is released from its chemically-bound condition.
The resulting products are finely divided white powders that, upon subjection to the above described reactivity ~.~
test, react within one minute and maintain this reactivity for at least one month storage.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water ~as stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. of sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of the product marketed under the trade mark "Dicalite Speed-Plus" (filter-aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 1000 g. of ice was added, resulting in a mixture containing 2.0% calcium and 1~.1% sucrose. To this mixture was added 40 liters of C02, fed into the mixture subsurface with rapid stirring with a precipi-tate being formed.
The resulting mixture was stirred for one hour at -2 &., then warmed to ~2C. and the precipitate was removed in a basket centrifuge. The precipitate cake was slurred in 700 ml. of 0C. water (13% solids) and the slurry was spray dried at 500 F. inlet temperature (outlet temperature 300F.).
Ninety grams of product were recovered. Analysis indicated the presence of 4.9% H20. The reactivity of the product was 45 sec. and remained so over extended periods of storage In a suitable vessel, a mixture of 1300 g. of water, 300 g. of sucrose and 30 g. of calcium oxicle was stirred for one hour at ambient temperature, then cooled to 5C. Twenty grams of Dicalite Speed-Plus was added and the mixture was vacuum filtered through 20g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 300 g. of crushed ice was added resulting in a mixture containing 1.1~ calcium and 15.5%
sucrose and 0.85 cu. ft. of C02 was fed into this mixture subsurface with rapid stirring with a precipitate being formed.
The resulting mixture was stirred at -2C. for one hour and then warmed to +1C. The precip~jtate was removed by centrifugation and slurried 4 times with 550 ml. quantities of 5C. acetone. After each wash the solvent was removed by vacuum filtration. The washed precipitate was dehydrated for 18 hours at 44C. in a vacuum oven (0.45 mm). The product obtained contained 9.1~ H20, had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
~,_~,1 5S~
EXAMPLE ~
Following the procedure of Example 2 a precipitate was prepared and centrifuged. The resulting cake (250 g.) was washed 4 times with 475 ml. quantities of 2C. acetone. The acetone was removed after each wash by vacuum filtration. The washed precipitate was dried in a fluid bed dryer at 40C.
with 5-5.5 ft.3/min. air flow for 60 minutes. The resulting product contained 7.5% H20, had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
A precipitate is prepared by the following procedure.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225 . O g. of water was stirred at ambient temperature for 15 minutes to- form a slaked lime slurry. A solution of 337.5 g.
of sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at am~ient temperature and then cooled to 5C~ Twenty grams oE
Dicalite Speed-Plus (filter aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 750 g. of ice was added resulting in a mixture containing 2.2% calcium and 14.5% sucrose. Forty liters of C02 was fed subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -2C., then warmed to +2C. and the precipitate was removed in a basket centrifuge. Samples of the precipitate cake prepared by the above procedure were dried and/or dehydrated as follows:
A. The precipitate cake is dried "as is" --(without solvent wash).
;cj~
~28-~1) Ten grams of cake dried in vacuum oven tNational Appliance Co., inside dimensions 12"x8"x8") at 25~C. and less than 1.0 mm. for 4 hours followed by drying at 67C.
and less than 1.0 mm. for 18 hours.
Water Content - 4.6~
Reactivity - 45 seconds Storability - excellent (2) Forty grams of cake dried in vacuum oven 0 at 25C. and less than 1.0 mm. for 2 hours followed by drying at 84C and less than 1.00 mm. for 18 hour~
Water content - 0.8 Reactivity - 102 seconds (3) Twenty-five grams of cake dried in a forced draft oven IBlue M Electric Co., Blue Island, Illinois) at 45C. for 20 hours.
Wa-ter content = 1.0~
Reactivity - 102 seconds 0 (4) Twenty-five grams of cake dried in oven (National Appliance Co.) at 70C. for 20 hours.
Water content - 0.8%
Reactivity - 150 seconds (5) Twenty-five grams of cake allowed to dry on bench at 30% relative humidity and 24C. for 20 hours.
Water content - 1.1%
Reactivity - 120 seconds 5~
-2~-
Alternatively~ less of the aqueous solution can be separated from the precipitate leaving a cold aqueous slurry of the precipitate in the aqueous solution. The degree of separa-tion of the aqueous solution from the precipitate will depend on the desirability of recycling the aqueous solution back through the first step of the process of this invention so as to avoid undue use of the hydrogen-bonding material balanced against the economics of providing cold make-up water to reslur-ry the cake. The cold aqueous slurry formed may even be a com-promise between the two above illustrations wherein the aqueous solution is not separated enough to form a cake of the precipi- ;
tate but cold water is added, nevertheless, to provide the slur-ry desired. In any case, the resulting slurry should be main-tained at all times during formation and until drying below about 15C. so as to avoid adverse effects on the resulting product.
The cold aqueous slurry is then spray dried while maintaining the spray dryer at conditions sufficient to rapidly dry and dehydrate the slurry and precipitate that is being introduced into the spray dryer at below about 15C.
It has been found that this embodiment of the process of the present invention will result in a combination of com-pleting the isolation of the precipitate from the aqueous solu-tion in which it was formed and at the same time causing the release of chemically-bound water while substantially instan-taneously removing the water so released. This portion of the process of this invention is thereby simplified and improved resulting in less preparation time. Furthermore, this proce-dure eliminates the necessity of washing the precipitate with a 30 water-miscible solvent.
It is to be noted that the effect on the precipitate using spray drying is essentially the same as previously dis-closed. That is, the action of the spra~ dryer removes the remaining aqueous solution from the precipitate which, in essence, completes the isolation as previously described and~
, 5~
concurrently, the spray drying causes a release of most of the chemically-bound water from the precipitate while causing the substantially instantaneous removal of the water so freed from the surrounding composition. It has been found that the result-ing chemically~bound water in the product is within the pre-ferred range of chemically-bound water content.
It should be understood that the products of this invention while having the desirable characteristics previously described can also have some of the undesirable properties of materials of the prior art due to partial decomposition appar-entiy due to conditions maintained during the dehydration step.
A test was developed to measure the reactivity of various calcium carbonates which is as follows: 200 milli-liters of distilled water is mixed with 5.0 milliliters of 1.0 normal citric acid solution to form a solution that contains 5 milli-equivalents of citric acid. The pH of this citric acid solution is 2.6 as measured on a Leeds and Northrup pH meter with expandable scale (the full scale deflection is 2 pH
units). The pH meter is connected to a Leeds and Northrup recorder with a 6.5 inch width chart and a speed equivalent to 8 inches per minute and adjusted so that full scale deflection is 2 pH units. The electrodes of the pH meter are immersed in the citric acid solution and the beaker containing the solution is placed on a magnetic stirrer. The stirrer is adjusted to approximately 125 rpm. The pH meter is ad~usted to 0 deflec-tion (the recorder is therefore also at 0 deflection). The recorder chart is activated. A 0.18 gram sample of the calcium carbonate to be tested is then added to the beaker. The pH of the solution, as recorded on the recorder, will increase until all of the calcium carbonate has reacted and the reaction is considered to be complete when the pH of the solution no longer increases. By determining the point at which the pH no longer increases, the length of time required for a particular sample of calcium carbonate to react can be observed.
~;
S~ f Utili~ing this reactivity test, the "reactivity" of various calcium carbonates can be determined. It has been found that those calcium carbonates that have a reactivity time of less than one minute, when measured by the above test, will provide carbonate factors for effervescent compositions that are extremely useful in that they are capable of supporting extremely rapid effervescent reactions upon use. The process of the present invention will provide such calcium carbonates.
During the investigations which resulted in the lCf present invention it was found that some calcium carbonates prepared, although initially possessing this desirable characteristic of rapid reactivity, would lose their rapid reactivity after periods of storage. It was found that, in contact with saturated air, many such rapidly reactive calcium carbonates quickly lose their rapid reactivity. A lower degree of saturation or relative humidity resulted in a slower loss in the rapid reactivity. Those samples that were stored under low humidity conditions retained their rapid reactivity for longer periods of time.
2Q It was found that the most severe conditions of storage for such calcium carbonates is storage in a small sealed container (i.e. with very little air space~. This is apparently due to the fact that the sample has only to give up a very small amount of water to saturate the air in the container. (Saturated air at 22.2C. contains 0.0002 grams water vapor/cc.) s~
In order to determine the "storability" of various rapidly reactive calcium carbonates including those of the pre-sent invention the following test was developed. Weiyh 2.0 g.
of a sample into a 1 oz. glass bottle and seal with a cap.
Store the bottle and contents at room temperature (20-25C.).
At the end of one month storage measure reactivity by the above-described test. If the "reactivity" increases more than 5% in this test the sample tested does not have an acceptable storability.
In generall we have found that a chemically-bound water content in stabilized amorphous calcium carbonate of below about 5% is desired for good storability. However~ it has been found that the storability of the materials of this invention is not solely dependent on the chemically-bound water content. Materials have been prepared containing as much as 15~ chemically-bound water which have been found storable for greater than 3 months and other materials containing only 2 water were found to be nonstorable in less than one month.
It is preferred, however, that stabilized amorphous calcium carbonate have a water content of no more than about 5 to have a reasonably predictable and acceptable storability.
The process of the present invention will be more rea-dily understood by reference to the following examples, of which Example 1 is a general procedure, which are understood not to limit the present invention, but to be construed broadly 5~
and be restricted solely by the appended claims. In these exam-ples the water content of the dehydrated precipitate refers to chemically-bound water content. Unless otherwise noted in these examples, analyses of the products resulting from the following procedures show the presence therein of the hydrogen-bonding material utilized.
In a suitable vessel, an aqueous solution of calcium ions and sucrose is prepared. The preferred amount of sucrose in the aqueous solution is from about 10% to about 30% by weight of the solution. The concentration of calcium ions in the solution can be from about .~1~ to about 23% by weight calcium per weight of the total solution. This solution may be formed by dispersing such calcium-containing materials as a calcium oxide, calcium hydroxide, calcium hydride, calcium peroxide or other water soluble salts such as calcium chlorides, etc., in either water and subsequently adding sucrose, or in an aqueous sucrose solution. It is preferred to add the calcium-containing material before the sucrose, and it has been found tha~ the calcium ion solubility is increased as the sucrose concentration in the aqueous solution is increased.
It is preferred to form the calcium ions and sucrose aqueous solution by adding calcium oxide to water to form a slaked lime slurry adding sucrose to the resulting slurry. For illustrative purposes calcium oxide will be utrilized in this example. The purity of the sucrose material is not critical as long as excessive amounts of impurities are avoided.
The purity of the calcium oxide utilized is also not critical, but it is undesirable to have much more than a trace amount of magnesium ions associated with the aqueous solution~
It is also particularly helpful in forming the solution to . ~
~ i 5S~3 select the materials that have uniformly small particle sizes so as to afford a fairly rapid rate of dissolving the material.
It is preferred to obtain an aqueous solution that has both sucrose and calcium at the higher levels oE the above-noted ranges due to superior yields in product per unit weight of solution.
The temperature utilized in forming the solution is not critical to the process of this invent:ion, but it is preferably below about 70C. so as to avoid any adverse conversion of the sucrose such as by inversion. Furthermore, it has been found that the lower the temperature of the sucrose-containing aqueous solution when adding the calcium oxide thereto, the higher the concentration of calcium ions that can be placed in the solution. It is preferred to remove any insolubles remaining in the solution.
The resulting aqueous solution of sucrose and calcium ions is then contacted with carbon dioxide. The solution is at a temperature preferably of from about -3C. to about -~3C., and maintained at that temperature while contacting it with carbon dioxide. The carbon dioxide is in the form of a gas and is introduced into the solution subsurface. This provides both ; intimate contact and good agitation. A precipitate begins to form after about 1.4 to about 1.5 moles carbon dioxide/moles calcium in the solution has been consumed and continues to form until about 1.7 to about 2.2 moles of carbon dioxide per mole of calcium has been consumed; the formation of a precipitate in this phase is exothermic. At this point, it is preferred to stop the feeding of the carbon dioxide to the solution, although the processs of this invention can be carried out by continuing to feed carbon dioxide into the solution.
it~
When the exothermic phase of the precipitate-forming step has been concluded, the solution begins to evolve carbon dioxide in an endothermic phase. If the carbon dioxide feed stream is continuously being fed to the aqueous solution, it can be observed that the amount being released from the solution is greater than the amount being added thereto. If the carbon dioxide feed stream to the aqueous solution has been stopped at the end of the exothermic phase as above-described the solution containing the precipitate will evolve carbon dioxide. In either case, this endothermic carbon dioxide-releasing phase continues until the mole ratio of consumed carbon dioxide to calcium in the solution is about 1.0 moles of carbon dioxide per mole of calcium. It is critical in the formation of the precipitate that the phases as described above be completed and, further, that the second phase be continued until the point where carbon dioxide release has essentially ceased.
The precipitate is then isolated from the solution, such as by centrifugation, followed by washing with water-miscible solvent and evaporating the solvent. This procedure results in a washed precipitate that is free of any of the solution from which it was formed. Any water remaining in the precipitate is chemically-bound rather than merely adhering to the precipitate particles. The amount of this chemically-bound water must be reduced below about 15% so as to provide stabilized amorphous calcium carbonate.
The washed precipitate is then dehydrated. For instance, this can be carried out most readily in a vacuum oven at high vacuum that continuously removes the water as it is released from its chemically-bound condition.
The resulting products are finely divided white powders that, upon subjection to the above described reactivity ~.~
test, react within one minute and maintain this reactivity for at least one month storage.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water ~as stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. of sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of the product marketed under the trade mark "Dicalite Speed-Plus" (filter-aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 1000 g. of ice was added, resulting in a mixture containing 2.0% calcium and 1~.1% sucrose. To this mixture was added 40 liters of C02, fed into the mixture subsurface with rapid stirring with a precipi-tate being formed.
The resulting mixture was stirred for one hour at -2 &., then warmed to ~2C. and the precipitate was removed in a basket centrifuge. The precipitate cake was slurred in 700 ml. of 0C. water (13% solids) and the slurry was spray dried at 500 F. inlet temperature (outlet temperature 300F.).
Ninety grams of product were recovered. Analysis indicated the presence of 4.9% H20. The reactivity of the product was 45 sec. and remained so over extended periods of storage In a suitable vessel, a mixture of 1300 g. of water, 300 g. of sucrose and 30 g. of calcium oxicle was stirred for one hour at ambient temperature, then cooled to 5C. Twenty grams of Dicalite Speed-Plus was added and the mixture was vacuum filtered through 20g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 300 g. of crushed ice was added resulting in a mixture containing 1.1~ calcium and 15.5%
sucrose and 0.85 cu. ft. of C02 was fed into this mixture subsurface with rapid stirring with a precipitate being formed.
The resulting mixture was stirred at -2C. for one hour and then warmed to +1C. The precip~jtate was removed by centrifugation and slurried 4 times with 550 ml. quantities of 5C. acetone. After each wash the solvent was removed by vacuum filtration. The washed precipitate was dehydrated for 18 hours at 44C. in a vacuum oven (0.45 mm). The product obtained contained 9.1~ H20, had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
~,_~,1 5S~
EXAMPLE ~
Following the procedure of Example 2 a precipitate was prepared and centrifuged. The resulting cake (250 g.) was washed 4 times with 475 ml. quantities of 2C. acetone. The acetone was removed after each wash by vacuum filtration. The washed precipitate was dried in a fluid bed dryer at 40C.
with 5-5.5 ft.3/min. air flow for 60 minutes. The resulting product contained 7.5% H20, had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
A precipitate is prepared by the following procedure.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225 . O g. of water was stirred at ambient temperature for 15 minutes to- form a slaked lime slurry. A solution of 337.5 g.
of sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at am~ient temperature and then cooled to 5C~ Twenty grams oE
Dicalite Speed-Plus (filter aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 750 g. of ice was added resulting in a mixture containing 2.2% calcium and 14.5% sucrose. Forty liters of C02 was fed subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -2C., then warmed to +2C. and the precipitate was removed in a basket centrifuge. Samples of the precipitate cake prepared by the above procedure were dried and/or dehydrated as follows:
A. The precipitate cake is dried "as is" --(without solvent wash).
;cj~
~28-~1) Ten grams of cake dried in vacuum oven tNational Appliance Co., inside dimensions 12"x8"x8") at 25~C. and less than 1.0 mm. for 4 hours followed by drying at 67C.
and less than 1.0 mm. for 18 hours.
Water Content - 4.6~
Reactivity - 45 seconds Storability - excellent (2) Forty grams of cake dried in vacuum oven 0 at 25C. and less than 1.0 mm. for 2 hours followed by drying at 84C and less than 1.00 mm. for 18 hour~
Water content - 0.8 Reactivity - 102 seconds (3) Twenty-five grams of cake dried in a forced draft oven IBlue M Electric Co., Blue Island, Illinois) at 45C. for 20 hours.
Wa-ter content = 1.0~
Reactivity - 102 seconds 0 (4) Twenty-five grams of cake dried in oven (National Appliance Co.) at 70C. for 20 hours.
Water content - 0.8%
Reactivity - 150 seconds (5) Twenty-five grams of cake allowed to dry on bench at 30% relative humidity and 24C. for 20 hours.
Water content - 1.1%
Reactivity - 120 seconds 5~
-2~-
(6) Forty grams of cake dried in oven ~National Appliance Co.) at 200C. for 18 hours.
Water content - 0.2~
Reactivity - 165 seconds The dehydration carried out in A. (2) through (6) illustrates the decomposition of the precipitate due to improper dehydration as compared to the proper dehydration carried out in A. (1). In A. (1) a small amount of precipitate was dehydrated in a high vacuum and the resultant material had excellent reactivity and storability. In A. (2) through (6) the precipitate formed a slurry during the dehydration and resulted in a hard, brittle chalk-like solid that had a low water content and poor reactivity apparently due to not removlng the free water from the precipitate being dried rapidly enough.
B. The precipitate cake (250-300 g.) is washed twice with 353 g. quantities of 0-5C.
anhydrous acetone. Acetone removed after each wash by suction filtration. The washed 20 precipitate was dehydrated as Eollows:
(1) Two hundred grams of cake dried in vacuum oven at 25C. and less than 1 mm. for 4 hours followed by drying at 86C. and less than 1 mm. for 18 hours.
Water content - 8.3~
Reactivity - 45 seconds Storability - excellent (2) Two hundred grams of cake dried in vacuum oven at 25C. and 10 mm. for 4 hours ~ollowed by drying at 74C. and 10-15 mm.
for 18 hours.
~, .
5S~
~30-Water Content - 0.5%
Reactivity - 135 seconds ~3) Twenty-five grams of cake dried in a forced draft oven at 47C. for 20 hours.
Water content 2.15~
Reactivity - 150 seconds (4) Twenty-five grams of cake dried in oven at 72 DC . for 20 hours.
Water content 1~0%
Reactivity - 150 seconds (5) Twenty-five grams of cake dried on bench at relative humidity and 24C.
Water content - 1.0%
Reactivity - 150 seconds.
As in Part A. the samples dehydrated in B. l2) through ~5) are examples of improper dehydration causing decomposition of the precipitate In B. (2) through (5) a slurry was formed during the dehydration step and a hard, brittle, chalk-like material resulted which had low water content and poor reactiyity. On the other hand, B. (1) illustrates the proper manner of carrying out the dehydration step as no decomposition occurred and the product resulting therefrom was excellent.
~, C. The precipita-te cake is washed twice wikh a 5:1 ratio (ml. solvent: g. cake) oE 25C.
methanol. The solvent was removed after each wash by vacuum filtration. The washed preci-pitate was dehydrated as follows:
(1) Two hundred grams of cake dried in a vacuum oven at 25C. and c2 mm. for 4 hours followed by drying at 76C. and ~2 mm. for 18 hours.
Water content - 3.9%
Reactivity - 45 seconds Storability - excellent (2) Two hundred grams of cake dried in a vacuum oven at 25C. and 7.8 mm. for 4 hours and at 63C. and 7.8 mm. for 18 hours.
Water content - 16.1%
Reactivity - 45 seconds Storability - poor (3) Twenty-five grams of cake dried in a forced draft oven at 48C. for 20 hours Water content - 12,7~
Reactivity - 45 seconds Storability - poor (4) Twenty-five grams of cake dried in an oven at 40C. for 20 hours.
Water content - 2.7~
Reactivity - 45 seconds Storability - excellent s~
(5) Fifteen grams sample of cake dried on the bench at 39~ relat:ive humidity and 24C. for 20 hours.
Water content - 15.0%
Reactivity - 45 seconds Storability - excel:lent The samples dehydrated in Part C. (2) and (3) are illustrative of a manner of carrying out the dehydration step under the proper conditions but not for a sufficient length of time, thereby resulting in products that have excellent reactivity initially but that have poor storabilit~. C. (1), (4) and (5) are illustrative of the proper manner of carrying out the de~hydration step and the product resulting therefrom.
In a suitable vessel, a mixture of 20.0 g. of calcium o~ide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry~ A solution of 90.0 g. of sucrose and 250.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then coole'd 5C. Ten grams of Dicalite Speed-Plus was added and the mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 240 g of ice was added resulting in a mixture containing 2.1~ calcium and 13.6 sucrose and 24 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate. The resulting mixture was stirred for one hour at -2C., then warmed to +0.5C. and the precipitate recovered b~ vacuum filtration. The resulting cake was slurried twice with 400 g. quantities of 25C.
, I
5~i~
water. The water was removed by vacuum filtration and the cake was then washed with 400 ml. of 25C. methanol. The washed precipitate was allowed to air dry at a relative humidity of 45% and a temperature of about 24C. for 18 hours.
The resulting white solid powder had an unacceptable reactivity of 79 seconds. The product apparently changed during the water washing step and upon analysis it was determined that no sucrose was present in the precipitate.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature Eor 15 minutes to form a slaked lime slurry. A solution of 90.0 g. of sucrose and 490.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 12C. Ten grams of Dicalite Speed-Plus was added and the mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate containing 2.1% calcium and 13.6~ sucrose was then cooled to 13C. and 27 1. of C02 was fed subsurface with rapid stirring to Eorm a precipitate. During this time the temperature rose to 17C. The resulting mixture was stirred for an hour at about 15C. and the precipitate recovered by vacuum filtration. The resulting cake was slurried twice with 400 ml. quantities of 25C. methanol. The methanol was removed by vacuum filtration and the washed precipitate was air-dried at a relative humidity of 43% and a temperature of about 24C. for 18 hours.
The resulting fine, white powder had a reactivity of 45 seconds and retained this reactivity during storage.
i5'~`9~
In a suitable vessel, a mixture of 10.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry.
A solution of 50.0 g. of glucose and 300.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred and cooled to 5C. The mixture was filtered through 10 g. of "Dicalite Speed-Plus". I'he filtrate was then cooled to 0C and 200 g. of ice was added resulting in a mixture containing 1.1~ calcium and 8.5% glucose. Ten liters of C02 was fed subsur-face into the mixture with rapid stirring to foxm a precipitate. The resulting mixture was stirred for 45 minutes at - 2C, then warmed to ~2C., and the precipitate recovered by vacuum filtration. The resulting cake was slurred twice with 150 ml. quantities of 25C.
methanol. The methanol was removed by vacuum iltration and the washed precipitate was air dried for 24 hours at a relative humidity of 20% and a temperature of 24C.
The resulting fine white powder contained about 15.0% water, had a reactivity of 30 seconds and retained this reactivity for extended periods of storage.
In a suitable vessel, a mixture of 1162.5 g. of water, 337.5 g. of glucose and 75.0 g. of calcium oxide was stirred for 1 hour at ambient temperature and then cooled to 5C. Twenty grams of the product marketed under the trade mark "Hyflo Supercel" tfilter-aid) was added and the resulting mixture was vacuum filtered through 20 g. of "Hyflo Supercel".
The filtrate was then cooled to 0C., 900 g. of crushed ice was added resulting in a mixture containing 2.1~ calcium and 13.6% glucose and 40 liters of C02 was fed subsurface into the mixture with rapid stirring :~, ~ "i s~
to form a precipitate. The resulting mixture was stirred at -l~C. for one hour, then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 700 ml. of 0C. water (13 wt. % solids) and the slurry was spray dried at 500F. inlet temperature ~300F.
outlet temperature). The resulting fine white powder contained 4.7% water, had a reactivity of 30 seconds and had excellent storability over extended periods of storage.
'10 In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 90.0 g. sorbitol and 250.0 g. of water was added to the slaked lime slurry and the resulting mixtùre was stirred and cooled to 3C. The mixture was filtered through lO g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 240 g.
of ice was added resulting in a mixture containing 2.1~ calcium and i3.1% sorbitol and 27 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate~
The resulting mixture was stirred for 70 minutes at -2C, then warmed to +1C. and the precipitate recovered by vacuum filtration. The precipitate cake was slurried twice with 400 ml. quantities of 25C. methanol and twice with 400 ml.
quantities of acetone. The solvents were removed by vacuum filtration and the washed precipitate was air dried 24 hours at a relative humidity of 40~ and a temperature of 25C.
The water content of the resulting product was about 17.6~ and its reactivity was 45 seconds. However, the product 3~ did not retain this reactivity during storage.
~,~
5~
In a suitable vessel, a mixture of ~0 g. of calcium oxide and 180 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 270 g. of sorbitol and 750 g. of water was added to the slaked lime slurry and the resulting mixture was stirrled 15 minutes at ambient temperature and then cooled to 5C. Twenty grarns of Hyflo Supercel ~filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was cooled to ODC., 720 g. of ice was charged resulting in a mixture containing 2.1% calcium and 13.6~ sorbitol and 41 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate. The resulting mixture was stirred for one hour at -1C., then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 700 ml. of 0C. water (11 solids) and the slurry was spray dried at 500F. inlet temperature, 300F. outlet temperature.
The resulting product contained 4.4% water, had a reactivity of 50 seconds and retained its reactivity for extended periods of storage.
In suitable vessel, a mixture of lO.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. 500.0 g. of methanol was added to the slaked lime slurry and the resulting mixture containing 92.5% methanol and 1.3~ calcium was then cooled to -12C. 24 liters of C02 were fed into the mixture subsurface with rapid stirring during which the temperature rose to -5.5C. and then decreased again to -12C. with a precipitate being formed. The precipitate was recovered by filtration and washed twice with 250 ml. of cold methanol. The methanol was removed by vacuum Eiltration.
The washed precipitate was air dried for 72 hours at a relative humidity of 15% and a temperature of 24C.
The resulting product contained 11.7% water, had a reactivity of 60 seconds and was unable to retain this reactivity upon storage.
In a suitable vessel, a mixture of 10.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature 1~ for 15 minutes to form a slaked lime slurry. A mixture of 250.0 g. of methanol and 250.0 g. of water was added to the slaked lime slurry and the resulting mixture containing 46.3%
methanol and 1.3% calcium was then cooled to -12.5C. 52 liters of C02 was fed into the mixture subsurface with rapid stirring during whi~h the temperature rose to -8C. and dropped again to -12.5C. with a precipitate being formed.
The precipitate was recovered by vacuum filtration and washed twice with 150 ml. of cold methanol. The methanol was removed by vacuum filtration and the washed precipitate was air dried 2~ for 72 hours at a relative humidity of 4~ and a temperature of 24C.
The resulting product contained 2.7% water, had a reactivity of 50 seconds and retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 90.0 g. of glycerine and 25n.0 g. of water was added to the slaked lime slurry. The resulting mixture was stirred ~and cooled to 5C. and was then filtered through t~
-38~
10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 240 g. of ice was added resulting in a mixture containing 2.3% calcium and 15.0~ glycerine and 17 liters of C2 was fed into the mixture subsurEace with rapid stirring at -4C. with a precipita-te being formed. The resulting mixture was warmed to 1C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with 250 ml. quantities of 25C. methanol and the methanol was removed by vacuum filtration. The washed precipitate was air-dried for 24 hours at a relative humiclity of 25% and a temperature of 24C.
The resulting fine white powder contained 1.3% water and had a reac~ivity of 45 seconds. The product retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a s`laked lime slurry. A solution of 45 g. glycine and 250.0 g. of water was added to -the s:Laked lime slurry and the resulting mixture was stirred and cooled to 5C. The mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0 and 240 g. of ice was added resulting in a mixture containing 1.9% calcium and 7.3~ glycine and 52 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The mixture was then stirred for 30 minutes at -2C., then warmed to +1C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with 450 ml. quantities of 25C. methanol. The methanol was ~0 removed by vacuum filtration and the washed precipitate was air dried for 24 hours at a relative ~r~
.
5~
humidity of 35% and a temperature of 24C.
The resulting product contains 1707% water and has a reactivity of 55 seconds but did not retain this reactivity during storage.
In a suitable vessel, a mixture of 60 g. of calcium oxide and 1~0 g. of water was stirred at ambient te~perature for 15 minutes to form a slaked lime slurry. A solution of 67.5 g. of glycine and 750 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Hyflo Supercel ~filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was then cooled to 0C., 720 g of ice was added resulting in a mixture containing 1.0% calcium and 3.8% glycine and 35 liters f C2 was fed into the mixture subsurface with rapid stirring with precipitate being formed. The resulting mixture was stirred for one hour at -1C., then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 500 ml. of 0C. water and the slurry was spray dried at 50QF inlet, 300F outlet temperature.
The resulting product contained 3.7~ water had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
In a suitable vessel, a mixture of 10 g. CaO and 30 g. water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 25 g. lysine and 250 g. water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature ~ . , s~ ~
and then cooled to 5C. Ten grams of filter-aid was added to the mixture which was then filtered through 10 g. of filter-aid. The filtrate was then cooled to 0C., 240 g. of ice was added resulting in a mixture containing 0.6% calcium and 4.5% lysine and 22.5 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -1.5C., warmed to 0C. and the precipitate was recovered by . vacuum filtration. The precipitate cake was slurried twice with 200 ml. of 25C. methanol and then twice with 200 ml. of 25C. acetone. The precipitate was removed from the solvents each time by vacuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 35~ and a temperature of 24C.
The resulting product contained 11.7~ water and had a reactivity of 33 seconds but did not retain this reactivity during storage.
In a suitable vessel, a mixture of 70 g. of calcium oxide and 210 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 175 g. of lysine and 1750 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Hyflo Supercel (filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was then cooled to 0C., 1680 g. of ice was added resulting in a mixture containing 0.6~ calcium and 4.5% lysine and P5~3 37 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -1C., then warmed to +1C and the precipitate was recovered in a basket centrifuge.
The resulting cake was slurried in 700 ml. of 0C. water (12%
solids) and the slurry was spray dried at 500F. inlet temperature, 300F. outlet.
The resulting product contained 4.5% water, had a reactivity of 55 seconds and retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 75.0 g~ of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. oE sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Dicalite Speed-Plus (filter-aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate containing 3.2% calcium and 21.4% sucrose was then cooled to -2C. and, with external cooling, 40 liters of C02 was fed into the mixture subsurface with rapid stirring at such a rate that the temperature did not exceed 0C. with a precipi~ate being formed. The resulting mixture was stirred for one hour at 0C. and the precipitate was recovered in a basket centrifuge. The cake was slurried twice with 1000 ml.
quantities of methanol. The solvent was removed aEter each wash by vacuum filtration. The washed precipitate was air dried for 18 hours at a relative humidity of 15% and a temperature of 24C.
:~ 18~i5~i~
-~2-The resulting product contained about 15.0~ water and had a reactivity of 55 seconds which it retained for extended periods of storage.
In a suitable vessel, a mixture of 382 g. of water, 9.6 g. of CaO and 39.2 g. of sucrose was stirred at 25C. for 45 minutes, then with ice bath cooling until the temperature of the mixture was 5C. Five grams of Hyflo Supercel (filter-aid) was added and the mixture was stirred for an additional 5 minutes. The mixture was suction filtered through a filter precoated with Hyflo Supercel. The filtrate was then cooled with stirring at 0C., 100 g. of ice was added resulting in a mixture containing 1.2% calcium and 7.3% sucrose and 5.5 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred at -1C. for one hour, then warmed to +1C.. The precipitate was recovered by vacuum iltration and slurried 2 times with 50 g. quantities of 2C
acetone. The solvent was removed after each wash by vacuum filtration; The washed precipitate was dried in a vacuum oven at less than one mm. for 2 hours at 25C and for 18 hours at 70C.
The resulting product contained 7.5% water and had a reactivity of 50 seconds which it retained during extended periods ~f storage.
EXA~PLE 21 In a suitable vessel, a mixture of 20 g. CaO and 60 g. water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 22.5 g. glycine and 250 g. water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5~. Ten grams of fiIter-aid was added , . . .
1, cj~
to the mixture which was then filtered through 10 g.
filter-aid. The filtrate was then cooled to 0C., 240 g. of ice were added resulting in a mixture containing 1.0% calcium and 3.8% glycine and 36 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for half an hour at -1.5C., warmed to 0C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with methanol (5 ml./g.) and twice with acetone (5 ml./g.).
The precipitate was removed from the solvents each time by vacuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 40~ and a temperature of 24C.
The resulting product contained 15.3% water and had a reactivity of 33 seconds but did not retain this reactivity in storage.
EXAMPLE_22 In a suitable vessel, a solution of 34 g. CaC12, 90 g. sucrose and 310 g~ water was cooled to 0C. and 240 g. of ice was added resulting in a mixture containing 0.18% calcium and 13.4% sucrose. The mixture was stirred rapidly while C02 was fed subsurface. The pH of the mixture was 7.0 at the beginning of the introduction of C02 and decreased to 3.5 during the C02 addition.
No precipitate resulted after 25 minutes of feeding CO2 .
In a suitable vessel, a solution of 34 g. CaC12, 90 g. sucrose, 210 g. water and 100 g. lN NaOH was cooled to 0C.
and 240 g. of ice was added. The resulting mixture containing 0.18% calcium and 13.4% sucrose was stirred rapidly while C02 was fed subsurface which caused a precipitate to form. The resulting mixture was stirred for one hour at ~8~
-1.5C., warmed to 0C. and the precipitate was recovered by vacuum filtration. The precipitate cake was washed twice with methanol ( 5 ml.g.) and twice with acetone (5 ml./g.) The precipitate was removed from the solvents each time by ~acuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 49%
and a temperature oE 24C.
The resulting product contained 15.5% water and had a reactivity of 33 seconds but did not retain this reactivity durin~g storage.
In a suitable vessel, a mixture of 7.5gO of CaO and 225 g. of water was slurried for 15 minutes at ambient temperature, 1275 g. of water was added and the mixture was cooled to 0C. To this cold mixture was added 900 ~. of ice resulting in a mixture containing 2.2~ calcium. With vigorous stirring C02 was fed into the mixture subsurface until no`
more was absorbed causing the formation of precipitate. The resulting mixture was stirred for one hour at 0C. then warmed to ~1C. The precipitate was recovered by centrifugation.
The cake was slurried with 500 ml. of 0C. water and the slurry was spray dried at 500F. inlet and 300F. outlet.
The reactivity time of the product was 180 seconds and the product contained 5.6% H20.
This example illustrates the need for the presence of a hydrogen-bonding material in the precipitated calcium carbonate.
In a suitable vessel, a mixture of 75.0 g. of 3 calcium oxide and 225.0 g. of water was stirred at ambient b~ ~
temperature for 15 minutes to form a slaked lime slurry. A
solution of 337.5 g. of sucrose and 1937.5 g. H20 was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 6C.
Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0% calcium and 13.2~ sucrose was then cooled to 2C. and C2 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C02 addition was 2-8C. The resulting mixture was stirred for one hour at 1C. and the precipitate was recovered in a basket centrifuge. Much of the precipitate was lost through the filter paper. 100 g. of wet precipitate cake was slurried with about 300 ml. of ice water and spray dried.
The resulting product contained 1.99% water and had a reactivity of 112 seconds.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to Eorm a slaked lime slurry. A solution of 337.5 g. of sucrose and 1937.5 g. H20 was added to the slaked `'ime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 11C. Twenty grams of filter-aid was added and the mixture was filtered through 20 g.
of filter-aid. The filtrate containing 2.0% calcium and 13.2%
sucrose was then cooled to 8C and C02 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C02 addition was 8-12C. The resulting mixture was stirred for one hour at
Water content - 0.2~
Reactivity - 165 seconds The dehydration carried out in A. (2) through (6) illustrates the decomposition of the precipitate due to improper dehydration as compared to the proper dehydration carried out in A. (1). In A. (1) a small amount of precipitate was dehydrated in a high vacuum and the resultant material had excellent reactivity and storability. In A. (2) through (6) the precipitate formed a slurry during the dehydration and resulted in a hard, brittle chalk-like solid that had a low water content and poor reactivity apparently due to not removlng the free water from the precipitate being dried rapidly enough.
B. The precipitate cake (250-300 g.) is washed twice with 353 g. quantities of 0-5C.
anhydrous acetone. Acetone removed after each wash by suction filtration. The washed 20 precipitate was dehydrated as Eollows:
(1) Two hundred grams of cake dried in vacuum oven at 25C. and less than 1 mm. for 4 hours followed by drying at 86C. and less than 1 mm. for 18 hours.
Water content - 8.3~
Reactivity - 45 seconds Storability - excellent (2) Two hundred grams of cake dried in vacuum oven at 25C. and 10 mm. for 4 hours ~ollowed by drying at 74C. and 10-15 mm.
for 18 hours.
~, .
5S~
~30-Water Content - 0.5%
Reactivity - 135 seconds ~3) Twenty-five grams of cake dried in a forced draft oven at 47C. for 20 hours.
Water content 2.15~
Reactivity - 150 seconds (4) Twenty-five grams of cake dried in oven at 72 DC . for 20 hours.
Water content 1~0%
Reactivity - 150 seconds (5) Twenty-five grams of cake dried on bench at relative humidity and 24C.
Water content - 1.0%
Reactivity - 150 seconds.
As in Part A. the samples dehydrated in B. l2) through ~5) are examples of improper dehydration causing decomposition of the precipitate In B. (2) through (5) a slurry was formed during the dehydration step and a hard, brittle, chalk-like material resulted which had low water content and poor reactiyity. On the other hand, B. (1) illustrates the proper manner of carrying out the dehydration step as no decomposition occurred and the product resulting therefrom was excellent.
~, C. The precipita-te cake is washed twice wikh a 5:1 ratio (ml. solvent: g. cake) oE 25C.
methanol. The solvent was removed after each wash by vacuum filtration. The washed preci-pitate was dehydrated as follows:
(1) Two hundred grams of cake dried in a vacuum oven at 25C. and c2 mm. for 4 hours followed by drying at 76C. and ~2 mm. for 18 hours.
Water content - 3.9%
Reactivity - 45 seconds Storability - excellent (2) Two hundred grams of cake dried in a vacuum oven at 25C. and 7.8 mm. for 4 hours and at 63C. and 7.8 mm. for 18 hours.
Water content - 16.1%
Reactivity - 45 seconds Storability - poor (3) Twenty-five grams of cake dried in a forced draft oven at 48C. for 20 hours Water content - 12,7~
Reactivity - 45 seconds Storability - poor (4) Twenty-five grams of cake dried in an oven at 40C. for 20 hours.
Water content - 2.7~
Reactivity - 45 seconds Storability - excellent s~
(5) Fifteen grams sample of cake dried on the bench at 39~ relat:ive humidity and 24C. for 20 hours.
Water content - 15.0%
Reactivity - 45 seconds Storability - excel:lent The samples dehydrated in Part C. (2) and (3) are illustrative of a manner of carrying out the dehydration step under the proper conditions but not for a sufficient length of time, thereby resulting in products that have excellent reactivity initially but that have poor storabilit~. C. (1), (4) and (5) are illustrative of the proper manner of carrying out the de~hydration step and the product resulting therefrom.
In a suitable vessel, a mixture of 20.0 g. of calcium o~ide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry~ A solution of 90.0 g. of sucrose and 250.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then coole'd 5C. Ten grams of Dicalite Speed-Plus was added and the mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C., 240 g of ice was added resulting in a mixture containing 2.1~ calcium and 13.6 sucrose and 24 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate. The resulting mixture was stirred for one hour at -2C., then warmed to +0.5C. and the precipitate recovered b~ vacuum filtration. The resulting cake was slurried twice with 400 g. quantities of 25C.
, I
5~i~
water. The water was removed by vacuum filtration and the cake was then washed with 400 ml. of 25C. methanol. The washed precipitate was allowed to air dry at a relative humidity of 45% and a temperature of about 24C. for 18 hours.
The resulting white solid powder had an unacceptable reactivity of 79 seconds. The product apparently changed during the water washing step and upon analysis it was determined that no sucrose was present in the precipitate.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature Eor 15 minutes to form a slaked lime slurry. A solution of 90.0 g. of sucrose and 490.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 12C. Ten grams of Dicalite Speed-Plus was added and the mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate containing 2.1% calcium and 13.6~ sucrose was then cooled to 13C. and 27 1. of C02 was fed subsurface with rapid stirring to Eorm a precipitate. During this time the temperature rose to 17C. The resulting mixture was stirred for an hour at about 15C. and the precipitate recovered by vacuum filtration. The resulting cake was slurried twice with 400 ml. quantities of 25C. methanol. The methanol was removed by vacuum filtration and the washed precipitate was air-dried at a relative humidity of 43% and a temperature of about 24C. for 18 hours.
The resulting fine, white powder had a reactivity of 45 seconds and retained this reactivity during storage.
i5'~`9~
In a suitable vessel, a mixture of 10.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry.
A solution of 50.0 g. of glucose and 300.0 g. of water was added to the slaked lime slurry and the resulting mixture was stirred and cooled to 5C. The mixture was filtered through 10 g. of "Dicalite Speed-Plus". I'he filtrate was then cooled to 0C and 200 g. of ice was added resulting in a mixture containing 1.1~ calcium and 8.5% glucose. Ten liters of C02 was fed subsur-face into the mixture with rapid stirring to foxm a precipitate. The resulting mixture was stirred for 45 minutes at - 2C, then warmed to ~2C., and the precipitate recovered by vacuum filtration. The resulting cake was slurred twice with 150 ml. quantities of 25C.
methanol. The methanol was removed by vacuum iltration and the washed precipitate was air dried for 24 hours at a relative humidity of 20% and a temperature of 24C.
The resulting fine white powder contained about 15.0% water, had a reactivity of 30 seconds and retained this reactivity for extended periods of storage.
In a suitable vessel, a mixture of 1162.5 g. of water, 337.5 g. of glucose and 75.0 g. of calcium oxide was stirred for 1 hour at ambient temperature and then cooled to 5C. Twenty grams of the product marketed under the trade mark "Hyflo Supercel" tfilter-aid) was added and the resulting mixture was vacuum filtered through 20 g. of "Hyflo Supercel".
The filtrate was then cooled to 0C., 900 g. of crushed ice was added resulting in a mixture containing 2.1~ calcium and 13.6% glucose and 40 liters of C02 was fed subsurface into the mixture with rapid stirring :~, ~ "i s~
to form a precipitate. The resulting mixture was stirred at -l~C. for one hour, then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 700 ml. of 0C. water (13 wt. % solids) and the slurry was spray dried at 500F. inlet temperature ~300F.
outlet temperature). The resulting fine white powder contained 4.7% water, had a reactivity of 30 seconds and had excellent storability over extended periods of storage.
'10 In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 90.0 g. sorbitol and 250.0 g. of water was added to the slaked lime slurry and the resulting mixtùre was stirred and cooled to 3C. The mixture was filtered through lO g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 240 g.
of ice was added resulting in a mixture containing 2.1~ calcium and i3.1% sorbitol and 27 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate~
The resulting mixture was stirred for 70 minutes at -2C, then warmed to +1C. and the precipitate recovered by vacuum filtration. The precipitate cake was slurried twice with 400 ml. quantities of 25C. methanol and twice with 400 ml.
quantities of acetone. The solvents were removed by vacuum filtration and the washed precipitate was air dried 24 hours at a relative humidity of 40~ and a temperature of 25C.
The water content of the resulting product was about 17.6~ and its reactivity was 45 seconds. However, the product 3~ did not retain this reactivity during storage.
~,~
5~
In a suitable vessel, a mixture of ~0 g. of calcium oxide and 180 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 270 g. of sorbitol and 750 g. of water was added to the slaked lime slurry and the resulting mixture was stirrled 15 minutes at ambient temperature and then cooled to 5C. Twenty grarns of Hyflo Supercel ~filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was cooled to ODC., 720 g. of ice was charged resulting in a mixture containing 2.1% calcium and 13.6~ sorbitol and 41 liters of C02 was fed into the mixture subsurface with rapid stirring to form a precipitate. The resulting mixture was stirred for one hour at -1C., then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 700 ml. of 0C. water (11 solids) and the slurry was spray dried at 500F. inlet temperature, 300F. outlet temperature.
The resulting product contained 4.4% water, had a reactivity of 50 seconds and retained its reactivity for extended periods of storage.
In suitable vessel, a mixture of lO.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. 500.0 g. of methanol was added to the slaked lime slurry and the resulting mixture containing 92.5% methanol and 1.3~ calcium was then cooled to -12C. 24 liters of C02 were fed into the mixture subsurface with rapid stirring during which the temperature rose to -5.5C. and then decreased again to -12C. with a precipitate being formed. The precipitate was recovered by filtration and washed twice with 250 ml. of cold methanol. The methanol was removed by vacuum Eiltration.
The washed precipitate was air dried for 72 hours at a relative humidity of 15% and a temperature of 24C.
The resulting product contained 11.7% water, had a reactivity of 60 seconds and was unable to retain this reactivity upon storage.
In a suitable vessel, a mixture of 10.0 g. of calcium oxide and 30.0 g. of water was stirred at ambient temperature 1~ for 15 minutes to form a slaked lime slurry. A mixture of 250.0 g. of methanol and 250.0 g. of water was added to the slaked lime slurry and the resulting mixture containing 46.3%
methanol and 1.3% calcium was then cooled to -12.5C. 52 liters of C02 was fed into the mixture subsurface with rapid stirring during whi~h the temperature rose to -8C. and dropped again to -12.5C. with a precipitate being formed.
The precipitate was recovered by vacuum filtration and washed twice with 150 ml. of cold methanol. The methanol was removed by vacuum filtration and the washed precipitate was air dried 2~ for 72 hours at a relative humidity of 4~ and a temperature of 24C.
The resulting product contained 2.7% water, had a reactivity of 50 seconds and retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 90.0 g. of glycerine and 25n.0 g. of water was added to the slaked lime slurry. The resulting mixture was stirred ~and cooled to 5C. and was then filtered through t~
-38~
10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0C. and 240 g. of ice was added resulting in a mixture containing 2.3% calcium and 15.0~ glycerine and 17 liters of C2 was fed into the mixture subsurEace with rapid stirring at -4C. with a precipita-te being formed. The resulting mixture was warmed to 1C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with 250 ml. quantities of 25C. methanol and the methanol was removed by vacuum filtration. The washed precipitate was air-dried for 24 hours at a relative humiclity of 25% and a temperature of 24C.
The resulting fine white powder contained 1.3% water and had a reac~ivity of 45 seconds. The product retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 20.0 g. of calcium oxide and 60.0 g. of water was stirred at ambient temperature for 15 minutes to form a s`laked lime slurry. A solution of 45 g. glycine and 250.0 g. of water was added to -the s:Laked lime slurry and the resulting mixture was stirred and cooled to 5C. The mixture was filtered through 10 g. of Dicalite Speed-Plus. The filtrate was then cooled to 0 and 240 g. of ice was added resulting in a mixture containing 1.9% calcium and 7.3~ glycine and 52 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The mixture was then stirred for 30 minutes at -2C., then warmed to +1C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with 450 ml. quantities of 25C. methanol. The methanol was ~0 removed by vacuum filtration and the washed precipitate was air dried for 24 hours at a relative ~r~
.
5~
humidity of 35% and a temperature of 24C.
The resulting product contains 1707% water and has a reactivity of 55 seconds but did not retain this reactivity during storage.
In a suitable vessel, a mixture of 60 g. of calcium oxide and 1~0 g. of water was stirred at ambient te~perature for 15 minutes to form a slaked lime slurry. A solution of 67.5 g. of glycine and 750 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Hyflo Supercel ~filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was then cooled to 0C., 720 g of ice was added resulting in a mixture containing 1.0% calcium and 3.8% glycine and 35 liters f C2 was fed into the mixture subsurface with rapid stirring with precipitate being formed. The resulting mixture was stirred for one hour at -1C., then warmed to +1C. and the precipitate was recovered in a basket centrifuge. The resulting cake was slurried in 500 ml. of 0C. water and the slurry was spray dried at 50QF inlet, 300F outlet temperature.
The resulting product contained 3.7~ water had a reactivity of 45 seconds and retained this reactivity for extended periods of storage.
In a suitable vessel, a mixture of 10 g. CaO and 30 g. water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 25 g. lysine and 250 g. water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature ~ . , s~ ~
and then cooled to 5C. Ten grams of filter-aid was added to the mixture which was then filtered through 10 g. of filter-aid. The filtrate was then cooled to 0C., 240 g. of ice was added resulting in a mixture containing 0.6% calcium and 4.5% lysine and 22.5 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -1.5C., warmed to 0C. and the precipitate was recovered by . vacuum filtration. The precipitate cake was slurried twice with 200 ml. of 25C. methanol and then twice with 200 ml. of 25C. acetone. The precipitate was removed from the solvents each time by vacuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 35~ and a temperature of 24C.
The resulting product contained 11.7~ water and had a reactivity of 33 seconds but did not retain this reactivity during storage.
In a suitable vessel, a mixture of 70 g. of calcium oxide and 210 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 175 g. of lysine and 1750 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Hyflo Supercel (filter-aid) was added and the mixture was filtered through 20 g. of Hyflo Supercel. The filtrate was then cooled to 0C., 1680 g. of ice was added resulting in a mixture containing 0.6~ calcium and 4.5% lysine and P5~3 37 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for one hour at -1C., then warmed to +1C and the precipitate was recovered in a basket centrifuge.
The resulting cake was slurried in 700 ml. of 0C. water (12%
solids) and the slurry was spray dried at 500F. inlet temperature, 300F. outlet.
The resulting product contained 4.5% water, had a reactivity of 55 seconds and retained this reactivity during extended periods of storage.
In a suitable vessel, a mixture of 75.0 g~ of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. oE sucrose and 937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5C. Twenty grams of Dicalite Speed-Plus (filter-aid) was added and the mixture was filtered through 20 g. of Dicalite Speed-Plus. The filtrate containing 3.2% calcium and 21.4% sucrose was then cooled to -2C. and, with external cooling, 40 liters of C02 was fed into the mixture subsurface with rapid stirring at such a rate that the temperature did not exceed 0C. with a precipi~ate being formed. The resulting mixture was stirred for one hour at 0C. and the precipitate was recovered in a basket centrifuge. The cake was slurried twice with 1000 ml.
quantities of methanol. The solvent was removed aEter each wash by vacuum filtration. The washed precipitate was air dried for 18 hours at a relative humidity of 15% and a temperature of 24C.
:~ 18~i5~i~
-~2-The resulting product contained about 15.0~ water and had a reactivity of 55 seconds which it retained for extended periods of storage.
In a suitable vessel, a mixture of 382 g. of water, 9.6 g. of CaO and 39.2 g. of sucrose was stirred at 25C. for 45 minutes, then with ice bath cooling until the temperature of the mixture was 5C. Five grams of Hyflo Supercel (filter-aid) was added and the mixture was stirred for an additional 5 minutes. The mixture was suction filtered through a filter precoated with Hyflo Supercel. The filtrate was then cooled with stirring at 0C., 100 g. of ice was added resulting in a mixture containing 1.2% calcium and 7.3% sucrose and 5.5 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred at -1C. for one hour, then warmed to +1C.. The precipitate was recovered by vacuum iltration and slurried 2 times with 50 g. quantities of 2C
acetone. The solvent was removed after each wash by vacuum filtration; The washed precipitate was dried in a vacuum oven at less than one mm. for 2 hours at 25C and for 18 hours at 70C.
The resulting product contained 7.5% water and had a reactivity of 50 seconds which it retained during extended periods ~f storage.
EXA~PLE 21 In a suitable vessel, a mixture of 20 g. CaO and 60 g. water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 22.5 g. glycine and 250 g. water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 5~. Ten grams of fiIter-aid was added , . . .
1, cj~
to the mixture which was then filtered through 10 g.
filter-aid. The filtrate was then cooled to 0C., 240 g. of ice were added resulting in a mixture containing 1.0% calcium and 3.8% glycine and 36 liters of C02 was fed into the mixture subsurface with rapid stirring with a precipitate being formed. The resulting mixture was stirred for half an hour at -1.5C., warmed to 0C. and the precipitate was recovered by vacuum filtration. The precipitate cake was slurried twice with methanol (5 ml./g.) and twice with acetone (5 ml./g.).
The precipitate was removed from the solvents each time by vacuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 40~ and a temperature of 24C.
The resulting product contained 15.3% water and had a reactivity of 33 seconds but did not retain this reactivity in storage.
EXAMPLE_22 In a suitable vessel, a solution of 34 g. CaC12, 90 g. sucrose and 310 g~ water was cooled to 0C. and 240 g. of ice was added resulting in a mixture containing 0.18% calcium and 13.4% sucrose. The mixture was stirred rapidly while C02 was fed subsurface. The pH of the mixture was 7.0 at the beginning of the introduction of C02 and decreased to 3.5 during the C02 addition.
No precipitate resulted after 25 minutes of feeding CO2 .
In a suitable vessel, a solution of 34 g. CaC12, 90 g. sucrose, 210 g. water and 100 g. lN NaOH was cooled to 0C.
and 240 g. of ice was added. The resulting mixture containing 0.18% calcium and 13.4% sucrose was stirred rapidly while C02 was fed subsurface which caused a precipitate to form. The resulting mixture was stirred for one hour at ~8~
-1.5C., warmed to 0C. and the precipitate was recovered by vacuum filtration. The precipitate cake was washed twice with methanol ( 5 ml.g.) and twice with acetone (5 ml./g.) The precipitate was removed from the solvents each time by ~acuum filtration. The washed precipitate was allowed to air dry on the laboratory bench for 18 hours at a relative humidity of 49%
and a temperature oE 24C.
The resulting product contained 15.5% water and had a reactivity of 33 seconds but did not retain this reactivity durin~g storage.
In a suitable vessel, a mixture of 7.5gO of CaO and 225 g. of water was slurried for 15 minutes at ambient temperature, 1275 g. of water was added and the mixture was cooled to 0C. To this cold mixture was added 900 ~. of ice resulting in a mixture containing 2.2~ calcium. With vigorous stirring C02 was fed into the mixture subsurface until no`
more was absorbed causing the formation of precipitate. The resulting mixture was stirred for one hour at 0C. then warmed to ~1C. The precipitate was recovered by centrifugation.
The cake was slurried with 500 ml. of 0C. water and the slurry was spray dried at 500F. inlet and 300F. outlet.
The reactivity time of the product was 180 seconds and the product contained 5.6% H20.
This example illustrates the need for the presence of a hydrogen-bonding material in the precipitated calcium carbonate.
In a suitable vessel, a mixture of 75.0 g. of 3 calcium oxide and 225.0 g. of water was stirred at ambient b~ ~
temperature for 15 minutes to form a slaked lime slurry. A
solution of 337.5 g. of sucrose and 1937.5 g. H20 was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 6C.
Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0% calcium and 13.2~ sucrose was then cooled to 2C. and C2 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C02 addition was 2-8C. The resulting mixture was stirred for one hour at 1C. and the precipitate was recovered in a basket centrifuge. Much of the precipitate was lost through the filter paper. 100 g. of wet precipitate cake was slurried with about 300 ml. of ice water and spray dried.
The resulting product contained 1.99% water and had a reactivity of 112 seconds.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to Eorm a slaked lime slurry. A solution of 337.5 g. of sucrose and 1937.5 g. H20 was added to the slaked `'ime slurry and the resulting mixture was stirred 15 minutes at ambient temperature and then cooled to 11C. Twenty grams of filter-aid was added and the mixture was filtered through 20 g.
of filter-aid. The filtrate containing 2.0% calcium and 13.2%
sucrose was then cooled to 8C and C02 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C02 addition was 8-12C. The resulting mixture was stirred for one hour at
7-9C. and ~.86~
-~6-the precipitate was recovered in a basket centriEuge. 150 g.
of wet precipitate cake was slurried with 300 ml. o ice water and spray aried.
The resulting product contained 1.7~ water and had a reactivity of 112 seconds.
In a suitable vessel, a mixture of 75.0 g. o calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. of sucrose and 1937.5 g. of water'was added to the slaked lime slurry and the resulting mixture was stlrred 15 minutes at ambient temperature and then cooled to 15C.
Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0~ calcium and 13.2~ sucrose was then cooled to 12C. and C2 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C2 addition was 12-17C. The resulting mixture was stirred for one hour at 14-16C. and the precipitate was recovered in a basket centrifuge. The 140 g. of wet precipitate cake was slurried with 300 ml. of ice water and then spray dried.
The resulting product contained 1.7% water and had a reactivity of 78.5 seconds.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 3375 g. of sucrose and 1937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature. Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0% calcium and s~
13.2% sucrose was then cooled to 18C. and C02 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature during C02 addition was 18-23DC. The resulting mixture was stirred for one hour at 21-23C. and the precipitate was recoverecl by vacuum filtration. 140 g. of wet precipitate cake was slurried with 200 ml. of ice water and spray dried.
The resulting product contained U.89% water and had a reactivity of 90 seconds.
lQ Examples 25-28 illustrate the generally lower reactivities obtained with precipitates formed at increasingly higher temperatures~
Heretofore, amorphous calcium carbonate has been obtained by some investigators. However, the heretofore obtained amorphous calcium carbonate has rapidly changed ~rom the amorphous state to a crystalline state. In other words, no prior investigator has been able to obtain amorphous calcium carbonate that will remain stable in the amorphous state for significant periods oE time (i.e., for periods exceeding about one month). It has now been Eound that the calcium carbonate provided by this invention is amorphous calcium carbonate that is stabilized in the amorphous state.
It has been found that the stabilized amorphous calcium carbonate prepared by the above described process comprises stabilized amorphous calcium carbonate that contains from about 0.1~ to 15% by weight chemically-bound water and a hydrogen-bonding material. Stabilized amorphous calcium carbonate is a fine, white powder. Analyses show that stabilized amorphous calcium carbonate consists of agglomerates of extremely small particles of calcium carbonate that 5~
are substantia]ly amorphous. Comparative analysis of stabilized amorphous calcium carbonate show that the particles of calcium carbonate are apparently stabilized in this amorphous state by the presence therein of the proper amount of chemically-bound water and a hydrogen-bonding material.
The analyses of stabilized amorphous calcium carbonate that will be described for illustrative purposes is that material prepared by the procedure of Example 2. For purposes of brevity and for this description this material will be hereinafter referred to as "stabilized amorphous calcium carbonate-2. n Stabilized amorphous calcium carbonate-2 was examined under the electron microscope and was studied by X-ray and infrared analyses.
Examination under the electron microscope reveals the significant difference between stabilized amorphous calcium carbonate-2 and the known crystalline states of calcium carbonate (calcite, aragonite and vaterite). Calcite crystals appear as well-formed cubes uniform in size at a magnification of 4000X. Crystals oE vaterite seem to occur as spheres of differing size, while those of aragonite form fairly uniform needles. In contrast, particles of stabilized amorphous calcium carbonate-2 have no distinct size or shape at a magnification of 4000X. ~agnified by 20,000X, stabilized amorphous calcium carbonate-2 appears to have a rough surface and non-uniform size suggesting an agglomerate of smaller particles. Photomicrographs were taken at magnifications of 57,000X and 147,000X that show spherical particles with an average particle size of from about lOA to about ~40A at the edge of larger, irrregularly-shaped agglomerates.
After determining that the particles of stabilized amor~hous calcium carbonate-2 appear different from the known s~
crystalline states of calcium carbonate under an electron microscope, further examination was made by X-ray analysis.
Unlike the known crystalline states of calcium carbonate, stabilized amorphous calcium carbonate-2 gives no X-ray pattern at all, that is, stabilized amorphous calc:ium carbonate-2 is "amorphous" to X-ray analysis. Being "amorphous 1l -to X-ray analysis is due to one of two reasons: either (1) stabilized amorphous calcium carbonate-2 is not a simple carbonate, but a polymeric or hydrogen-bonaed species whose repeating units are irregular or too long to be measured by the X-ray analysis, or (2) the particles of stabilized amorphous calcium carbonate-2 are too small to be detected by X-ray analysis.
Infrared analysis supports the second reason for stabilized amorphous calcium carbonate-2 being X-ray amorphous.
Infrared spectra were run on two samples of stabilized amorphous calcium carbonate-2 using the ~sI pellet technique giving spectra from 4000 cm 1 to 200 cm 1. One of these samples was combined with an e~tra 10~ ground sucrose so as to intensify the peaks caused by sucrose. Upon comparison of these two spectra the peaks due to sucrose become evident allowing the peaks due to the carbonate group to be isolated.
Table I shows the result of this comparison.
That the remaining isolated peaks are due to the carbonate group is confirmed by comparison of those remaining peaks to the spectra obtained using the Nujol mull technique with calcium carbonate prepared without a hydrogen-bonding agent by the procedure of Example 24. Table II shows the results of this comparison.
The remaining isolated peaks were compared to spectra for calcite, aragonite and vaterite obtained in our laboratory on the same instrument. This comparison is shown in Table III
which clearly shows that stabilized amorphous calcium carbonate-2 does, in fact, contain a carbonate group but that it does not resemble any one particular morphological state.
The basic difference in the spectra of stabilized amorphous calcium carbonate-2 and the other known calcium carbonates is that the peaks of stabilized amorphous calcium carbonate-2 are much broader than those obtained with the other crystalline states of calcium carbonate. Additionally, these spectra show that stabilized amorphous calcium carbonate-2 does, in fact, contain sucrose.
This conclusion as to a carbonate group is further confirmed by comparison of the peaks obtained with stabilized amorphous calcium carbonate-2 with the values for calcium carbonate shown in the literature. These comparisons are shown in Table IV with calcite, Table V with vaterite and Table VI
with aragonite.
., .
~`
TABLE I
Stabilized ~morphous Stab.ilized Amorphous Calcium Carbonate-2 Calcium Carbonate-2 (0% Extra Sugar) (10% Extra Suqar) (CsI Pellet) (CsI Pellet) Wave Numbers (cm ) Wave Numbers (cm ***3440 ***- 3440 *2940 *- 2940 2510 (weak) 2510 1770 (shoulder)1770 (shoulder) **1650 (shoulder)**1650 (shoulder) **1285 *1245 *1210 *1165 (shoulder) *1130 *~1130 *1070 *`1070 * 995 *. 995 * 942 * 925 * 920 * 910 3 ~split peak)~ (split Deak) * 700 ~broad) *'700 (broad) * 570 (broad) *'570 (broad) * sucrose, ** water, *** sucrose and water, ~ bands with increased intensity 1070 Cm 1 and 700 cm 1 bands are due to both sucrose and the carbonate group.
. ~ ... .
....
TABLE II
Stabilized Amorphous CalciumCalcium Carbonate carbonate-2of Example 24 (CsI Pellet)_1(Nujol mull) Wave Numbers (cm )Wave Numbers (cm ***3440 ***3400 *2940 2510 (weak) 1770 (shoulder) **165 (shoulder) *1130 *1070 1070 * 995 * 925
-~6-the precipitate was recovered in a basket centriEuge. 150 g.
of wet precipitate cake was slurried with 300 ml. o ice water and spray aried.
The resulting product contained 1.7~ water and had a reactivity of 112 seconds.
In a suitable vessel, a mixture of 75.0 g. o calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 337.5 g. of sucrose and 1937.5 g. of water'was added to the slaked lime slurry and the resulting mixture was stlrred 15 minutes at ambient temperature and then cooled to 15C.
Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0~ calcium and 13.2~ sucrose was then cooled to 12C. and C2 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature range during C2 addition was 12-17C. The resulting mixture was stirred for one hour at 14-16C. and the precipitate was recovered in a basket centrifuge. The 140 g. of wet precipitate cake was slurried with 300 ml. of ice water and then spray dried.
The resulting product contained 1.7% water and had a reactivity of 78.5 seconds.
In a suitable vessel, a mixture of 75.0 g. of calcium oxide and 225.0 g. of water was stirred at ambient temperature for 15 minutes to form a slaked lime slurry. A solution of 3375 g. of sucrose and 1937.5 g. of water was added to the slaked lime slurry and the resulting mixture was stirred 15 minutes at ambient temperature. Twenty grams of filter-aid was added and the mixture was filtered through 20 g. of filter-aid. The filtrate containing 2.0% calcium and s~
13.2% sucrose was then cooled to 18C. and C02 was fed into the mixture subsurface with rapid stirring causing a precipitate to form. The temperature during C02 addition was 18-23DC. The resulting mixture was stirred for one hour at 21-23C. and the precipitate was recoverecl by vacuum filtration. 140 g. of wet precipitate cake was slurried with 200 ml. of ice water and spray dried.
The resulting product contained U.89% water and had a reactivity of 90 seconds.
lQ Examples 25-28 illustrate the generally lower reactivities obtained with precipitates formed at increasingly higher temperatures~
Heretofore, amorphous calcium carbonate has been obtained by some investigators. However, the heretofore obtained amorphous calcium carbonate has rapidly changed ~rom the amorphous state to a crystalline state. In other words, no prior investigator has been able to obtain amorphous calcium carbonate that will remain stable in the amorphous state for significant periods oE time (i.e., for periods exceeding about one month). It has now been Eound that the calcium carbonate provided by this invention is amorphous calcium carbonate that is stabilized in the amorphous state.
It has been found that the stabilized amorphous calcium carbonate prepared by the above described process comprises stabilized amorphous calcium carbonate that contains from about 0.1~ to 15% by weight chemically-bound water and a hydrogen-bonding material. Stabilized amorphous calcium carbonate is a fine, white powder. Analyses show that stabilized amorphous calcium carbonate consists of agglomerates of extremely small particles of calcium carbonate that 5~
are substantia]ly amorphous. Comparative analysis of stabilized amorphous calcium carbonate show that the particles of calcium carbonate are apparently stabilized in this amorphous state by the presence therein of the proper amount of chemically-bound water and a hydrogen-bonding material.
The analyses of stabilized amorphous calcium carbonate that will be described for illustrative purposes is that material prepared by the procedure of Example 2. For purposes of brevity and for this description this material will be hereinafter referred to as "stabilized amorphous calcium carbonate-2. n Stabilized amorphous calcium carbonate-2 was examined under the electron microscope and was studied by X-ray and infrared analyses.
Examination under the electron microscope reveals the significant difference between stabilized amorphous calcium carbonate-2 and the known crystalline states of calcium carbonate (calcite, aragonite and vaterite). Calcite crystals appear as well-formed cubes uniform in size at a magnification of 4000X. Crystals oE vaterite seem to occur as spheres of differing size, while those of aragonite form fairly uniform needles. In contrast, particles of stabilized amorphous calcium carbonate-2 have no distinct size or shape at a magnification of 4000X. ~agnified by 20,000X, stabilized amorphous calcium carbonate-2 appears to have a rough surface and non-uniform size suggesting an agglomerate of smaller particles. Photomicrographs were taken at magnifications of 57,000X and 147,000X that show spherical particles with an average particle size of from about lOA to about ~40A at the edge of larger, irrregularly-shaped agglomerates.
After determining that the particles of stabilized amor~hous calcium carbonate-2 appear different from the known s~
crystalline states of calcium carbonate under an electron microscope, further examination was made by X-ray analysis.
Unlike the known crystalline states of calcium carbonate, stabilized amorphous calcium carbonate-2 gives no X-ray pattern at all, that is, stabilized amorphous calc:ium carbonate-2 is "amorphous" to X-ray analysis. Being "amorphous 1l -to X-ray analysis is due to one of two reasons: either (1) stabilized amorphous calcium carbonate-2 is not a simple carbonate, but a polymeric or hydrogen-bonaed species whose repeating units are irregular or too long to be measured by the X-ray analysis, or (2) the particles of stabilized amorphous calcium carbonate-2 are too small to be detected by X-ray analysis.
Infrared analysis supports the second reason for stabilized amorphous calcium carbonate-2 being X-ray amorphous.
Infrared spectra were run on two samples of stabilized amorphous calcium carbonate-2 using the ~sI pellet technique giving spectra from 4000 cm 1 to 200 cm 1. One of these samples was combined with an e~tra 10~ ground sucrose so as to intensify the peaks caused by sucrose. Upon comparison of these two spectra the peaks due to sucrose become evident allowing the peaks due to the carbonate group to be isolated.
Table I shows the result of this comparison.
That the remaining isolated peaks are due to the carbonate group is confirmed by comparison of those remaining peaks to the spectra obtained using the Nujol mull technique with calcium carbonate prepared without a hydrogen-bonding agent by the procedure of Example 24. Table II shows the results of this comparison.
The remaining isolated peaks were compared to spectra for calcite, aragonite and vaterite obtained in our laboratory on the same instrument. This comparison is shown in Table III
which clearly shows that stabilized amorphous calcium carbonate-2 does, in fact, contain a carbonate group but that it does not resemble any one particular morphological state.
The basic difference in the spectra of stabilized amorphous calcium carbonate-2 and the other known calcium carbonates is that the peaks of stabilized amorphous calcium carbonate-2 are much broader than those obtained with the other crystalline states of calcium carbonate. Additionally, these spectra show that stabilized amorphous calcium carbonate-2 does, in fact, contain sucrose.
This conclusion as to a carbonate group is further confirmed by comparison of the peaks obtained with stabilized amorphous calcium carbonate-2 with the values for calcium carbonate shown in the literature. These comparisons are shown in Table IV with calcite, Table V with vaterite and Table VI
with aragonite.
., .
~`
TABLE I
Stabilized ~morphous Stab.ilized Amorphous Calcium Carbonate-2 Calcium Carbonate-2 (0% Extra Sugar) (10% Extra Suqar) (CsI Pellet) (CsI Pellet) Wave Numbers (cm ) Wave Numbers (cm ***3440 ***- 3440 *2940 *- 2940 2510 (weak) 2510 1770 (shoulder)1770 (shoulder) **1650 (shoulder)**1650 (shoulder) **1285 *1245 *1210 *1165 (shoulder) *1130 *~1130 *1070 *`1070 * 995 *. 995 * 942 * 925 * 920 * 910 3 ~split peak)~ (split Deak) * 700 ~broad) *'700 (broad) * 570 (broad) *'570 (broad) * sucrose, ** water, *** sucrose and water, ~ bands with increased intensity 1070 Cm 1 and 700 cm 1 bands are due to both sucrose and the carbonate group.
. ~ ... .
....
TABLE II
Stabilized Amorphous CalciumCalcium Carbonate carbonate-2of Example 24 (CsI Pellet)_1(Nujol mull) Wave Numbers (cm )Wave Numbers (cm ***3440 ***3400 *2940 2510 (weak) 1770 (shoulder) **165 (shoulder) *1130 *1070 1070 * 995 * 925
8 ~
\(split peak) 867 8~_/
* 700 (broad) * 570 (broad) TABLE III
tabilized Amorphous ! _ ~Calcium Carbonate-2 Calcite ¦Aragonite__ ~ rite (CsI Pellet)(CsI Pellet)l(Nujol Mull),(CsI Pellet) ~ave Numbers (cm )Wave Numbers (cm ***3440 *2940 2520 1 1 2510 (weak) 2500 2510 ~ 1775 1770 (shoulder) **1650 (shoulder) *1130 . 1090 *107905 .
* 925 . 878 (split peak~ 875 877 * 700 (broad) 700 TABLE IV
Stabili~ed Amorphous ¦
Calcium Carbonate-2 ¦ Calcite _ _ ~CsI Pellet) 1 ~ (2) ¦(3) ¦ (4) ¦(5)1 (6) Wave Numbers (cm ) ! Wave Num ers (cm ?
***3440 l l *2940 I i 2510 (weak) ¦
1770 (shoulder) **1650 (shoulder) ~1130 ~144~ I ~ 1 432 r 107 0 I ~ I
* 999255 87~(split) 874 873 (peak ) 847 847 * 700 (broad) * 570 (broad) 320 (broad) 315 shoulder) (1) Miller, F.A. and Wilkins, C.H.,228 (shouldert Anal. Chem. 22(12), 1253 (1950)190 (should~r) (2) Louisfert, J. and Pobeguin, T.,106 (shoulaer Compt. rend. 235, 287 (1952) (3) Angino, E.E., Am. Mineral~ 52, 137-48 (1967) (4) Weir, C.E. and Lippincot~, E.R., Journal of Research of the National Bureau of Standards A Physics and Chemistry,-Vol. 65A,No.3,May-June 1961,p.173.
(5) Angino,E.E.,Am. Mineral.52,137-48(1967) (6) Bertin, E.P.,Penland,R.B.,Mizushima,S.,Curran C., and Quagliano, J.V., JACS 81,3818 (1959) .
~ r TABLE V
.
Stabilized Amorphous Calcium Carbonate-2 Va-terite (CsI Pellet) -1 (1) (2) 1 (3) _1 (4) Wave Numbers (cm ) Wave Numbers (Cm . _ _ .
***3440 *2940 2510 (weak) 1770 (shoulder) **1650 (shoulder) 1761 . 1450 1450 i 14417 *1130 1 1090 l 1088 1089 *1070 1070 * 999255 (split) 874 !
~peak) ~ 88756 747 l 850 !
*700 (broad) i *570 (broad) 320 (broad) (1) Louisfert, J. and Poberguin, T., Compt. rend. 235,287 (1952) (2) Baron,G. and Pesneau, M., Compt. rend. 243, 1217 (1956) (3) Weir, C.E. and Lippincott,E.R.,Journal of Research of the the National Bureau of Standards A Physics and Chemistry, Vol. 65A, No. 3 May-June 1961,p.173.
(4) Sterzel, W. and Charinsky, E., Spectrochim. Acta 24A.
353 (1967).
TABLE VI
Stabilized Amorphous Calclum Carbonate-2 Aragonite (CsI Pellet) -1 (1) (2) 1 ~3) ~ (5) Wave Numbers (cm ) Wave Numbersl(cm ) j 1, **3440 *2940 2510 (weak) 1774 1770 (shoulder) **1650 (shoulder) 1475~1489 *1130 1087 '1083 *19795 * 925 (split) 866 /(peak) l i 865l 858 857 1857 'I 713 713 715 1713 * 700 (broad) ! 710 703 ¦
* 570 (broad) I
320 (broad) j. ¦
L i I 1 ;
(1) Murphy, C.B.,Anal. Chem. 38¦5), 443R-45IR (1966).
(2) Louisfert, J. and Pobeguin, T., Compt. rend.235,287(1952).
(3) Baron, G. and Pesneau, M. Compt. rend. 243, 1217 (1956).
(4) Weir, C.E. and Lippincott, E.R., Journal of Research of the National Bureau of Standards A Physics and Chemistry, Vol.
65A, No. 3, May-June 1961, p. 173.
(5) Sterzel, W. and Charinsky, E., Spectrochim. Acta 24A, 353 (1967).
~ ' 55~3 Examination by these different analytical methods indicates that stabilized amorphous calcium carbonate-2 comprises extremely smal] particles of amorphous calcium carbonate. In this sense, stabilized amorphous calcium carbonate is "amorphous" in that it has no crystal lattice that can be identified by available analytical means.
The amorphous state of stabilized amorphous calcium carbonate was further confirmed by refractive index determinations utilizing a Light-Two-Beam, '~Mach-~ellnde~
(Trade Name~ Interference Microscope for transmitted light (Manuf.: Ernt~ Leitz, Wetzlar, W. Germany). This instrument enables one to determine the refractive indices of solids by the interferometer method.
With this instrument it was found that not only was stabilized amorphous calcium carbonate clearly isotropic but it gave refractive indices that are distinctly different from the refractive indices found with heretofore known amorphous calcium carbonate and known crystalline states of calcium carbonate. For comparative purposes Table VII gives refractive indices for calcium carbonate materials found in the literature together with the -refractive indices found with products made by the procedures of Examples 2, 11 and 16 (mounted in Dow 710 silicone oil with a refractive index of 1.52~5).
s~
TABLE VII
Literature Material Refractive Indices Reference -n~ n ~ n~
calcite 1.648~ 1.4820 --- (1) aragonite 1.5296 1.6804 1.6849 (2) vaterite 1.5460 1.6470 --- (3) calcium carbonate hexahydrate 1~460 1.535 1.545 (4) calcium carbonate monohydrate 1.590 1.543 --- (5) prior art amorphous calcium carbonate 1.51-1.53 --- --- (6) Ex. 2 1.5791 --- ---Ex. 2 (replicate) 1.5806 --- ---Ex. 11 1.5850 --- ---Ex. lG 1.5830 --- ---(1) Bailly, Am. Mineralogist, 33,519 (1948).
(2) Yamaguchi, J. Geol. Soc. Tokyo ~, 159 (1927 (3) Yoshimura, J. Geol. Soc. Tokyo 36, 7 t1929).
Gibson, Wyckoff, Merwin, Am. J. of Sci. (5)10, 325 (1925) ~4) J. Johnsto~, H.E. Merwin, E.D. Williamson, Am. J. Sci.
(4) 41,473 (1916) (5) Lippmann, Naturwiss. 46,553 (1959).
(6) Johnston, Merwin, Williamson, Am.J. Sci.~4)41,491(1916) From Table VII it can be concluded that no significant difference can be attributed to the products prepared with the hydrogen-bonding materials sorbitol, sucrose or glycine.
As noted before, amorphous calcium carbonate has been reported in several sources ~Louisfert, J. et al, Compt. rend.
235 287 (1952) and Gillott, J.E., J. Appl. Chem. 17, 185 (1967)]. Gillott states that carbonation of Ca(OH)2 may result in the formation of snythetic amorphous calcium carbonate which crystallizes to calcite in the presence of moisture at room temperature. Our experience with amorphous .....
s~
calcium carbonate agrees with Gillott's findings. We have found, however, that stabilized amorphous calcium carbonate is more resistant to calcite crystal formation than previously known amorphous calcium carbonate.
Utilizing stabi7ized amorphous calcium carbonate as a carbonate factor enables one to prepare effervescent compositions that will rapidly undergo the effervescent reaction upon contact with water and will provide a carbonated beverage that is highly palatable to the consumer. For instance, a typical dry beverage base effervescent composition may comprise a flavor, a sweetener, a color, an acid factor, such as citric acid, and a carbonate factor (in less than the stoichiometric equivalent of the acid factor). When stabilized amorphous calcium carbonate is utilized as the carbonate factor, excellent carbonated beverages result.
Typical effervescent compositions are the well-known effervescent medicament compositions which comprise an acid factor, such as citric acid, medicaments and a carbonate factor. Utilizing stabilized amorphous calcium carbonate as a carbonate factor in the proper proportions, i.e., sufficient to provide the desired C02 release, in such a composition will provide medicated beverages with improved taste.
Other effervescent compositions illustrating the use of stabilized amorphous calcium carbonate as the carbonate factor (termed "SACC") are shown in Table VIII. Table VIII
also shows the volumes of C02 developed with these effervescent compositions upon contacting them with 178 ml. of water at 40F.
~`
J ,,~.~
5~
_BLE VII
Ingredient Co osition (wt. grams) (1) (2) ~3) (4) Flavor 0.08 0.08 - -Color Sweetener(Synthetic) 0.09 0.09 Acid Factor (Citric) 2.60 2.70 1.74 3.30 10 SACC 1.70 1.45 1.30 2.40 Sodium bicarbonate 0.15 b. 28 Vol. CO2 developed 2.3 2.3 2.4 3.0 It has been Eound that excellent sweetened carbonated beverages can be obtained with effervescent compositions containing stabilized amorphous calcium carbonate and the synthetic sweeteners such as, for instance, saccharin, cyclamates, perilla-adehyde-aldoxin, dihydrochalcone derivatives, dulcin, steriosid, 5-t3-hydroxyphenyl)-lH-tetrazole and the newly discovered dipeptides as exemplified in U.S. Patent 3, 492rl31, Belgian Patent 739 r543 and West German Patent lr936,159 and the like.
While the invention has been described herein with regard to certain specific embodiments r it is not so limited.
It is to be unde~stood that variations and modifications thereof may be made by those skilled in the art without departing from the spirit and scope of the invention.
, ~ . .
\(split peak) 867 8~_/
* 700 (broad) * 570 (broad) TABLE III
tabilized Amorphous ! _ ~Calcium Carbonate-2 Calcite ¦Aragonite__ ~ rite (CsI Pellet)(CsI Pellet)l(Nujol Mull),(CsI Pellet) ~ave Numbers (cm )Wave Numbers (cm ***3440 *2940 2520 1 1 2510 (weak) 2500 2510 ~ 1775 1770 (shoulder) **1650 (shoulder) *1130 . 1090 *107905 .
* 925 . 878 (split peak~ 875 877 * 700 (broad) 700 TABLE IV
Stabili~ed Amorphous ¦
Calcium Carbonate-2 ¦ Calcite _ _ ~CsI Pellet) 1 ~ (2) ¦(3) ¦ (4) ¦(5)1 (6) Wave Numbers (cm ) ! Wave Num ers (cm ?
***3440 l l *2940 I i 2510 (weak) ¦
1770 (shoulder) **1650 (shoulder) ~1130 ~144~ I ~ 1 432 r 107 0 I ~ I
* 999255 87~(split) 874 873 (peak ) 847 847 * 700 (broad) * 570 (broad) 320 (broad) 315 shoulder) (1) Miller, F.A. and Wilkins, C.H.,228 (shouldert Anal. Chem. 22(12), 1253 (1950)190 (should~r) (2) Louisfert, J. and Pobeguin, T.,106 (shoulaer Compt. rend. 235, 287 (1952) (3) Angino, E.E., Am. Mineral~ 52, 137-48 (1967) (4) Weir, C.E. and Lippincot~, E.R., Journal of Research of the National Bureau of Standards A Physics and Chemistry,-Vol. 65A,No.3,May-June 1961,p.173.
(5) Angino,E.E.,Am. Mineral.52,137-48(1967) (6) Bertin, E.P.,Penland,R.B.,Mizushima,S.,Curran C., and Quagliano, J.V., JACS 81,3818 (1959) .
~ r TABLE V
.
Stabilized Amorphous Calcium Carbonate-2 Va-terite (CsI Pellet) -1 (1) (2) 1 (3) _1 (4) Wave Numbers (cm ) Wave Numbers (Cm . _ _ .
***3440 *2940 2510 (weak) 1770 (shoulder) **1650 (shoulder) 1761 . 1450 1450 i 14417 *1130 1 1090 l 1088 1089 *1070 1070 * 999255 (split) 874 !
~peak) ~ 88756 747 l 850 !
*700 (broad) i *570 (broad) 320 (broad) (1) Louisfert, J. and Poberguin, T., Compt. rend. 235,287 (1952) (2) Baron,G. and Pesneau, M., Compt. rend. 243, 1217 (1956) (3) Weir, C.E. and Lippincott,E.R.,Journal of Research of the the National Bureau of Standards A Physics and Chemistry, Vol. 65A, No. 3 May-June 1961,p.173.
(4) Sterzel, W. and Charinsky, E., Spectrochim. Acta 24A.
353 (1967).
TABLE VI
Stabilized Amorphous Calclum Carbonate-2 Aragonite (CsI Pellet) -1 (1) (2) 1 ~3) ~ (5) Wave Numbers (cm ) Wave Numbersl(cm ) j 1, **3440 *2940 2510 (weak) 1774 1770 (shoulder) **1650 (shoulder) 1475~1489 *1130 1087 '1083 *19795 * 925 (split) 866 /(peak) l i 865l 858 857 1857 'I 713 713 715 1713 * 700 (broad) ! 710 703 ¦
* 570 (broad) I
320 (broad) j. ¦
L i I 1 ;
(1) Murphy, C.B.,Anal. Chem. 38¦5), 443R-45IR (1966).
(2) Louisfert, J. and Pobeguin, T., Compt. rend.235,287(1952).
(3) Baron, G. and Pesneau, M. Compt. rend. 243, 1217 (1956).
(4) Weir, C.E. and Lippincott, E.R., Journal of Research of the National Bureau of Standards A Physics and Chemistry, Vol.
65A, No. 3, May-June 1961, p. 173.
(5) Sterzel, W. and Charinsky, E., Spectrochim. Acta 24A, 353 (1967).
~ ' 55~3 Examination by these different analytical methods indicates that stabilized amorphous calcium carbonate-2 comprises extremely smal] particles of amorphous calcium carbonate. In this sense, stabilized amorphous calcium carbonate is "amorphous" in that it has no crystal lattice that can be identified by available analytical means.
The amorphous state of stabilized amorphous calcium carbonate was further confirmed by refractive index determinations utilizing a Light-Two-Beam, '~Mach-~ellnde~
(Trade Name~ Interference Microscope for transmitted light (Manuf.: Ernt~ Leitz, Wetzlar, W. Germany). This instrument enables one to determine the refractive indices of solids by the interferometer method.
With this instrument it was found that not only was stabilized amorphous calcium carbonate clearly isotropic but it gave refractive indices that are distinctly different from the refractive indices found with heretofore known amorphous calcium carbonate and known crystalline states of calcium carbonate. For comparative purposes Table VII gives refractive indices for calcium carbonate materials found in the literature together with the -refractive indices found with products made by the procedures of Examples 2, 11 and 16 (mounted in Dow 710 silicone oil with a refractive index of 1.52~5).
s~
TABLE VII
Literature Material Refractive Indices Reference -n~ n ~ n~
calcite 1.648~ 1.4820 --- (1) aragonite 1.5296 1.6804 1.6849 (2) vaterite 1.5460 1.6470 --- (3) calcium carbonate hexahydrate 1~460 1.535 1.545 (4) calcium carbonate monohydrate 1.590 1.543 --- (5) prior art amorphous calcium carbonate 1.51-1.53 --- --- (6) Ex. 2 1.5791 --- ---Ex. 2 (replicate) 1.5806 --- ---Ex. 11 1.5850 --- ---Ex. lG 1.5830 --- ---(1) Bailly, Am. Mineralogist, 33,519 (1948).
(2) Yamaguchi, J. Geol. Soc. Tokyo ~, 159 (1927 (3) Yoshimura, J. Geol. Soc. Tokyo 36, 7 t1929).
Gibson, Wyckoff, Merwin, Am. J. of Sci. (5)10, 325 (1925) ~4) J. Johnsto~, H.E. Merwin, E.D. Williamson, Am. J. Sci.
(4) 41,473 (1916) (5) Lippmann, Naturwiss. 46,553 (1959).
(6) Johnston, Merwin, Williamson, Am.J. Sci.~4)41,491(1916) From Table VII it can be concluded that no significant difference can be attributed to the products prepared with the hydrogen-bonding materials sorbitol, sucrose or glycine.
As noted before, amorphous calcium carbonate has been reported in several sources ~Louisfert, J. et al, Compt. rend.
235 287 (1952) and Gillott, J.E., J. Appl. Chem. 17, 185 (1967)]. Gillott states that carbonation of Ca(OH)2 may result in the formation of snythetic amorphous calcium carbonate which crystallizes to calcite in the presence of moisture at room temperature. Our experience with amorphous .....
s~
calcium carbonate agrees with Gillott's findings. We have found, however, that stabilized amorphous calcium carbonate is more resistant to calcite crystal formation than previously known amorphous calcium carbonate.
Utilizing stabi7ized amorphous calcium carbonate as a carbonate factor enables one to prepare effervescent compositions that will rapidly undergo the effervescent reaction upon contact with water and will provide a carbonated beverage that is highly palatable to the consumer. For instance, a typical dry beverage base effervescent composition may comprise a flavor, a sweetener, a color, an acid factor, such as citric acid, and a carbonate factor (in less than the stoichiometric equivalent of the acid factor). When stabilized amorphous calcium carbonate is utilized as the carbonate factor, excellent carbonated beverages result.
Typical effervescent compositions are the well-known effervescent medicament compositions which comprise an acid factor, such as citric acid, medicaments and a carbonate factor. Utilizing stabilized amorphous calcium carbonate as a carbonate factor in the proper proportions, i.e., sufficient to provide the desired C02 release, in such a composition will provide medicated beverages with improved taste.
Other effervescent compositions illustrating the use of stabilized amorphous calcium carbonate as the carbonate factor (termed "SACC") are shown in Table VIII. Table VIII
also shows the volumes of C02 developed with these effervescent compositions upon contacting them with 178 ml. of water at 40F.
~`
J ,,~.~
5~
_BLE VII
Ingredient Co osition (wt. grams) (1) (2) ~3) (4) Flavor 0.08 0.08 - -Color Sweetener(Synthetic) 0.09 0.09 Acid Factor (Citric) 2.60 2.70 1.74 3.30 10 SACC 1.70 1.45 1.30 2.40 Sodium bicarbonate 0.15 b. 28 Vol. CO2 developed 2.3 2.3 2.4 3.0 It has been Eound that excellent sweetened carbonated beverages can be obtained with effervescent compositions containing stabilized amorphous calcium carbonate and the synthetic sweeteners such as, for instance, saccharin, cyclamates, perilla-adehyde-aldoxin, dihydrochalcone derivatives, dulcin, steriosid, 5-t3-hydroxyphenyl)-lH-tetrazole and the newly discovered dipeptides as exemplified in U.S. Patent 3, 492rl31, Belgian Patent 739 r543 and West German Patent lr936,159 and the like.
While the invention has been described herein with regard to certain specific embodiments r it is not so limited.
It is to be unde~stood that variations and modifications thereof may be made by those skilled in the art without departing from the spirit and scope of the invention.
, ~ . .
Claims (58)
- The embodiments of the invention in which an exclu-sive property or privilege is claimed are defined as follows:
l. A stabilized amorphous calcium carbonate that is the product of a process which comprises (l) forming an alkaline aqueous solution of calcium ions and a hydrogen-bonding mater-ial, (2) contacting the solution with carbon dioxide while main-taining the solution at a temperature below 15°C to form a precipitate containing chemically-bound water and continuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while retaining hydrogen -bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amorphous calcium càrbonate having a reactivity such that the time taken for a 0.18 g sam-ple to react completely when added to a stirred solution pre-pared by mixing 5 ml of 0.1N citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5% when a 2 g sample of the stabilized amorphous calcium carbon-ate is stored in a sealed 29.6 ml glass bottle at 20-25°C for one month. - 2. A stabilized amorphous calcium carbonate according to claim l wherein said hydrogen-bonding material is selected from the group consisting of water-soluble mono-, di-, tri- and oligo-saccharides; saccharide derivatives of a hydrocolloid-type; water-soluble alcohols and polyhydric materials; water-soluble amino acids and polymeric amino acids; and carboxylic and hydroxcarboxylic acids.
- 3. A stabilized amorphous calcium carbonate according to claim 1 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about 2% to about 95% by weight of the total solution.
- 4. A stabilized amorphous calcium carbonate according to claim 1 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about l0% to about 45% by weight of the total solution.
- 5. A stabilized amorphous calcium carbonate according to claim 1 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about l0% to about 30% by weight of the total solution.
- 6. A stabilized amorphous calcium carbonate according to claim 1 wherein the concentration of calcium ions in the solu-tion is in the range of from about 0.01% to about 23% by weight of the solution.
- 7. A stabilized amorphous calcium carbonate according to claim 1 wherein the concentration of calcium ions in the solu-tion is in the range of from about 1% to about 10% by weight of the solution.
- 8. A process for preparing stabilized amorphous calcium carbonate which comprises (l) forming an alkaline aqueous solu-tion of calcium ions and a hydrogen-bonding material, (2) con-tacting the solution with carbon dioxide while maintaining the solution at a temperature below 15°C to form a precipitate con-taining chemically-bound water and continuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while retaining hydrogen-bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amorphous calcium carbonate having a reactivity such that the time taken for a 0.18 g sample to react completely when added to a stirred solution prepared by mixing 5 ml of O.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5% when a 2 g sample of the stabilized amorphous calcium carbonate is stored in a sealed 29.6 ml glass bottle at 20-25°C for one month.
- 9. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about 2% to about 95% by weight of the total solution.
- 10. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about 10% to about 45% by weight of the total solution.
- 11. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the concentration of said hydrogen-bonding material in the aqueous solution is in the range of from about 10% to about 30% by weight of the total solution.
- 12. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the concentration of cal-cium ions in the solution is in the range of from about 0.01 to about 23% by weight of the solution.
- 13. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the concentration of cal-cium ions in the solution is in the range of from about 1% to about 10% by weight of the solution.
- 14. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the solution is formed at a temperature of below about 70°C.
- 15. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the solution is treated to remove most of the insoluble impurities in the solution.
- 16. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the step of contacting the solution with carbon dioxide is carried out while maintain-ing the solution at a temperature below about 10°C.
- 17. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the step of contacting the solution with carbon dioxide is carried out while maintain-ing the solution at a temperature of from about -5°C. to about 5°C.
- 18. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the step of contacting the solution with carbon dioxide is carried out while maintain-ing the solution at a temperature of from about -3°C. to about 0°C.
- 19. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein said contacting step is carried out on the subsurface of said solution.
- 20. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the amount of chemically--bound water contained in the precipitate is reduced by causing a portion of the chemically-bound water to be released, while substantially instantaneously removing the water so released.
- 21. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the chemically-bound water content is reduced to about 0.1% by weight.
- 22. A process for preparing stabilized amorphous calcium carbonate according to claim 8 wherein the chemically-bound water content is reduced to about from 2% to about 5% by weight.
- 23. A dry concentrate for preparing a carbonated beverage by admixture of the concentrate with water, said concentrate comprising an acid factor and a carbonate factor in less than the stoichiometric equivalent of the acid factor, characterized in that the carbonate factor comprises a stabilized amorphous calcium carbonate that is the product of a process which com-prises (1) forming an alkaline aqueous solution of calcium ions and a hydrogen-bonding material, (2) contacting the solution with carbon dioxide while maintaining the solution at a tempera-ture below 15°C to form a precipitate containing chemically-bound water and continuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while retaining hydrogen-bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amor-phous calcium carbonate having a reactivity such that the time taken for a 0.18 g sample to react completely when added to a stirred solution prepared by mixing 5 ml of O.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5% when a 2 g sample of the stabi-lized amorphous calcium carbonate is stored in a sealed 29.6 ml glass bottle at 20-25°C for one month.
- 24. A concentrate according to claim 23 wherein the car-bonate factor includes a carbonation-producing source supplemen-tal to the stabilized amorphous calcium carbonate in an amount sufficient to bring the carbonation to a level greater than 1.0 volume of carbon dioxide gas per volume of final beverage.
- 25. A concentrate according to claim 24 wherein said supplemental carbonation-producing source is sodium bicarbonate.
- 26. A concentrate according to claim 24 wherein said sup-plemental carbonation source is present in an amount sufficient to bring the carbonation to a level of 2.3 volumes of carbon dioxide gas per volume of final beverage.
- 27. A concentrate according to claim 26 wherein said sup-plemental carbonation-producing source is sodium bicarbonate.
- 28. A concentrate according to claim 23, 24 or 25 wherein said acid factor is citric acid.
- 29. A concentrate according to claim 26 or 27 wherein said acid factor is citric acid.
- 30. A concentrate according to claim 23, 24 or 25 which further comprises a flavorant and/or a synthetic sweetener.
- 31. A concentrate according to claim 26 or 27 which further comprises a flavorant and/or a synthetic sweetener.
- 32. A concentrate according to claim 23, 24 or 25 wherein said acid factor is citric acid and which further comprises a flavorant and/or a synthetic sweetener.
- 33. A concentrate according to claim 26 or 27 whèrein said acid factor is citric acid and which further comprises a flavorant and/or a synthetic sweetener.
- 34. A concentrate according to claim 23, 24 or 25 which further comprises a flavorant and/or a synthetic sweetener com-prising saccharin, a dipeptide or a mixture thereof.
- 35. A concentrate according to claim 26 or 27 which fur-ther comprises a flavorant and/or a synthetic sweetener com-prising saccharin, a dipeptide or a mixture thereof.
- 36. A concentrate according to claim 23, 24 or 25 wherein said acid factor is citric acid and which further comprises a flavorant and/or a synthetic sweetener comprising saccharin, a dipeptide or a mixture thereof.
- 37. A concentrate according to claim 26 or 27 wherein said acid factor is citric acid and which further comprises a flavorant and/or a synthetic sweetener comprising saccharin, a dipeptide or a mixture thereof.
- 38. A composition comprising a dry carbonated beverage concentrate for preparing a carbonated beverage by admixture with water, said concentrate comprising:
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in excess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament. - 39. A composition according to claim 38 wherein said con-centrate further includes a flavorant.
- 40. A composition according to claim 38 wherein said con-centrate further comprises a sweetener.
- 41. A composition according to claim 38 wherein said con-centrate further includes a supplemental carbonation producing source in an amount sufficient to bring the carbonation to a level greater than 1.0 volume of carbon dioxide gas per volume of final beverage.
- 42. A composition according to claim 41 wherein said sup-plemental carbonation producing source is sodium bicarbonate.
- 43. A composition according to claim 42 wherein said sup-plemental carbonation source is in an amount sufficient to bring the carbonation to a level of 2.3 volumes of carbon dioxide gas per volume of final beverage.
- 44. A composition according to claim 38, 39 or 40, where-in said acid factor is citric acid.
- 45. A composition according to claim 41, 42 or 43 wherein said acid factor is citric acid.
- 46. A composition according to claim 38, 39 or 40, where-in said concentrate further comprises a flavorant and/or a syn-thetic sweetener.
- 47. A composition according to claim 41, 42 or 43, where-in said concentrate further comprises a flavorant and/or a syn-thetic sweetener.
- 48. A composition according to claim 38, 39 or 40, where-in said concentrate further comprises a flavorant and/or a syn-thetic sweetener comprising saccharin, a dipeptide or a mixture thereof.
- 49. A composition according to claim 41, 42, or 43 wherein said concentrate further comprises a flavorant and/or a synthetic sweetener comprising saccharin, a dipeptide or a mixture thereof.
- 50. A composition according to claim 38, 39 or 40, where-in said acid factor is citric acid and wherein said concentrate further comprises a flavorant and/or a synthetic sweetener com-prising saccharin, a dipeptide or a mixture thereof.
- 51. A composition according to claim 41, 42 or 43, where-in said acid factor is citric acid and wherein said concentrate further comprises a flavorant and/or a synthetic sweetener com-prising saccharin, a dipeptide or a mixture thereof.
- 52. A process for preparing a dry concentrate for use in preparing a carbonated beverage by admixture of the concentrate with water, comprising (1) forming an alkaline aqueous solution of calcium ions and a hydrogen-bonding material, (2) contacting the solution with carbon dioxide while maintaining the solution at a temperature below 15°C to form a precipitate containing chemically-bound water and con-tinuing said contacting until no more carbon dioxide is taken up, and (3) reducing the amount of chemically-bound water contained in the precipitate to below 15% by weight while re-taining hydrogen-bonding material in the product and while maintaining the resulting product in an environment that is essentially free of unbound water, the said stabilized amorphous calcium carbonate having a reactivity such that the time taken for a 0.18 g sam-ple to react completely when added to a stirred solution pre-pared by mixing 5 ml of 0.lN citric acid with 200 ml of water is less than one minute, and having a stability such that the said time for complete reaction does not increase by more than 5% when a 2 g sample of the stabilized amorphous calcium car-bonate is stored in a sealed 29.6 ml glass bottle at 20-25°C
for one month;
(4) and admixing said stabilized amorphous calcium carbonate with an acid factor. - 53. A process for preparing a carbonated beverage which comprising dissolving a dry beverage concentrate as defined in claim 23 or 38 in water.
- 54. A process for preparing a dry, effervescent medicament composition which comprises admixing:
a. stabilized amorphous calcium carbonate, substan-tially devoid of calcium hydroxide, and b. an anhydrous, nontoxic acid in an amount in excess of the amount theoretically required to completely evolve the carbon dioxide from the amorphous calcium carbonate, and c. a medicament. - 55. A dry concentrate according to claim 23 wherein the concentration of calcium ions in the solution is in the range of from about 0.01% to about 23% by weight of the solution.
- 56. A dry concentrate according to claim 23 wherein the concentration of calcium ions in the solution is in the range of from about 1% to about 10% by weight of the solution.
- 57. A composition according to claim 38 wherein the concentration of calcium ions in the solution is in the range of from about 0.01% to about 23% by weight of the solution.
- 58. A composition according to claim 38 wherein the concentration of calcium ions in the solution is in the range of from about 1% to about 10% by weight of the solution.
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12437680A | 1980-02-25 | 1980-02-25 | |
US12437780A | 1980-02-25 | 1980-02-25 | |
US124,377 | 1980-02-25 | ||
US124,376 | 1980-02-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1186550A true CA1186550A (en) | 1985-05-07 |
Family
ID=26822507
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA000364108A Expired CA1186550A (en) | 1980-02-25 | 1980-11-06 | Stabilized amorphous calcium carbonate |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA1186550A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3275838A1 (en) | 2016-07-25 | 2018-01-31 | Omya International AG | Production of amorphous calcium carbonate |
-
1980
- 1980-11-06 CA CA000364108A patent/CA1186550A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3275838A1 (en) | 2016-07-25 | 2018-01-31 | Omya International AG | Production of amorphous calcium carbonate |
WO2018019701A1 (en) | 2016-07-25 | 2018-02-01 | Omya International Ag | Production of amorphous calcium carbonate |
US10745288B2 (en) | 2016-07-25 | 2020-08-18 | Omya International Ag | Production of amorphous calcium carbonate |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4237147A (en) | Stabilized amorphous calcium carbonate | |
US4539195A (en) | Basic magnesium aluminum hydroxycarbonate | |
US4824654A (en) | Process of producing needle-shaped calcium carbonate particles | |
US5250279A (en) | Method for the manufacture of hydrotalcite | |
CA1186550A (en) | Stabilized amorphous calcium carbonate | |
Sato et al. | Hydrothermal synthesis of fine perovskite PbTiO 3 powders with a simple mode of size distribution | |
EP0052677B1 (en) | Concentrates for the preparation of carbonated beverages | |
JPH0255371B2 (en) | ||
EP1075797B1 (en) | Novel sweetener compositions | |
EP0255092A2 (en) | Process for producing alpha-l-aspartyl-l-phenylalanine methyl ester having an improved solubility | |
US5993772A (en) | Method for coproducing calcium carbonate and sodium hydroxide | |
EP1075796A1 (en) | Sweetener compositions | |
JPH0352409B2 (en) | ||
CA2075589C (en) | Crystalline lactulose trihydrate and a method for its manufacture | |
CA1319787C (en) | Process for producing -l-aspartyl-l-phenylalanine methyl ester having an improved solubility | |
US5120762A (en) | Method for production of stabilized sodium ascorbate powder | |
JPS6125037B2 (en) | ||
US4835303A (en) | Process for producing dry α-L-aspartyl-L-phenylalanine methyl ester | |
US2211796A (en) | Manufacture of alkali earth carbonates | |
JPH054342B2 (en) | ||
FI80210C (en) | Means for raising the pH of dental plaque and the process for preparing it | |
JPS605021A (en) | Preparation of basic magnesium aluminum carbonate hydrate | |
EP0351775B1 (en) | Manufacturing process of magnetic strontiumhexaferrite powder | |
EP1062878B1 (en) | Mixed crystals comprising aspartame and aspartame derivative and process for producing the same | |
JP2802421B2 (en) | Method for producing high purity and high crystallinity calcium chloride |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MKEX | Expiry | ||
MKEX | Expiry |
Effective date: 20020507 |