US2430675A - Bleaching fatty acid compounds with chlorite and aldehyde - Google Patents
Bleaching fatty acid compounds with chlorite and aldehyde Download PDFInfo
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- US2430675A US2430675A US599753A US59975345A US2430675A US 2430675 A US2430675 A US 2430675A US 599753 A US599753 A US 599753A US 59975345 A US59975345 A US 59975345A US 2430675 A US2430675 A US 2430675A
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- chlorite
- aldehyde
- bleaching
- fatty acid
- solution
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C1/00—Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
- C11C1/08—Refining
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D215/00—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems
- C07D215/02—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom
- C07D215/16—Heterocyclic compounds containing quinoline or hydrogenated quinoline ring systems having no bond between the ring nitrogen atom and a non-ring member or having only hydrogen atoms or carbon atoms directly attached to the ring nitrogen atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
- C07D215/38—Nitrogen atoms
- C07D215/40—Nitrogen atoms attached in position 8
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/02—Refining fats or fatty oils by chemical reaction
- C11B3/08—Refining fats or fatty oils by chemical reaction with oxidising agents
Definitions
- This invention relates to an' improved process for effecting color improvement or bleachin f fatty acid compounds.
- fatty acid compounds are oils, fats, fatty acids, waxes and soaps.
- the material to be bleached is subjected to the simultaneous action of a chlorite and any aldehyde in the presence ,of water
- the material being treated is admixed in liquid form with the chlorite and aldehyde in aqueous solution,
- the pH of the solution during the bleaching operation is generally maintained at not less than about 7, though in some instances, as subsequently noted herein, mildly acid solutions maybe employed.
- fatty acid compounds can economically be bleached to an exceptionally high degree, without substantial degradation or danger of deleteriously affecting their desired characteristics, by subjecting them to the action of a chlorite in an alkaline, substantially neutral or only mildly acid aqueous solution, in the presence of an aldehyde as hereinafter more fully de- 2
- aldehydes may be used, including the aliphatic aldehydes, aromatic aldehydes, other carbocyclic aldehydes and heterocyclic aldehydes.
- Temperatures and concentrations are not usually critical and may be varied over a wide range. Increasing the temperature has generally been found to increase the rate of bleaching, Also, the ratio of chlorite to aldehyde may be widely varied. However. a molar ratio of chlorite to aldehyde of about 1:1 has been found generally useful.
- the temperature best suited for a particular operation will, to a considerable extent, depend upon the nature of the material being treated. Ordinary room temperature may frequently be employed with advantage but higher temperatures are usually desirable when treating fatty acid compounds normally solid where it is desired to effect the melting or solutionthereof. Temperatures at which the material being treated becomes unstable or at which the material is I deleteriously affected, are to be avoided.
- chlorites of the alkali and alkaline earth metals such as sodium chloaffected by strongly acid solutions and, where chlorine is introduced or liberated during the reaction, there is a tendency forthe chlorine to
- the hydrogen ion concentration of. my imrite, NaClQz, and calcium chlorite, Ca(Cl0a) fprovedtleaching solution may vary over a 'considerable range.
- a mildly acid condition may be used where desired, providing the fatty acid compound being bleached is of such a nature as not to be injured thereby, or where the compound has an acid reaction, for instance, a fatty acid.
- a buffer salt may, with advantage. be used to maintain the solution at the desired pH.
- Alkali metal phosphates such as the monosodium and di-sodium orthophosphates have been found to be particularly advantageous buffers for the purpose of the present invention, though other buffers may be used with advantage. I have found that, by builering the solution to a pH of about 7 by the presence of such phosphates, the consumption of chlorite in the bleaching operation is materially reduced. In some instances, a saving of 50% of chlorite has been effected by the use of these phosphates in conjunction with theother constituents of my bleaching solution previously noted.
- My invention is applicable to the treatment of either natural or synthetic fatty acid compounds, including saponiflable oils and waxes, such as beeswax, camauba wax, candelilla wax, corn oil, soybean oil and oleic acid, or commercial red oil. It is especially applicable to the bleaching of soaps and similar alkaline-reacting materials.
- saponiflable oils and waxes such as beeswax, camauba wax, candelilla wax, corn oil, soybean oil and oleic acid, or commercial red oil. It is especially applicable to the bleaching of soaps and similar alkaline-reacting materials.
- the bleaching of such fatty acid compounds is with advantage effected by treating the material while in a liquid condition, 1. e., either molten or in aqueous solution or suspension, depending upon the characteristics of the particular material treated.
- such materials either molten or in aqueous solution, may be admixed with the chlorite in the presence of water, and the aldehyde thereafter added, or'the material to be treated may be admixed with the aldehyde in the presence of water and the chlorite added to this mixture.
- the resultant mixture is maintained at a temperature usually ranging from ,room temperature to about 100 C. for a period of time sufficient to effect the desired bleaching and is thereafter cooled and separated,
- the soap may be melted by heating in water, the soap solution admixed with an aqueous chlorite solution and the desired amount of aldehyde thereafter added gradually or as a series of small portions, during agitation.
- the material In the treatment of wax or the like, which is solidat normal temperatures, the material is with advantage melted and an aqueous solution of the chlorite and the aldehyde admixed therewith or the chlorite and aldehyde may be added separately.
- Example I An aqueous solutio was prepared byfadmixing 50 c. c. of pH 7 sodium phosphate buffer 4 solution containing 10 grams of available chlorine and c. c. of a dilute aqueous formalin solution containing 2.2 grams of HCHO. 100 Brains of soybean oil was then admixed with the resultant solution and allowed to stand for 2 hours, at the end of which time much of the original yellow color of the oil had been removed and, upon separation from the solution. a superior product was obtained. During the admixing of the'oil with the solution and during the followingz hour period a pH of .about 7 and a temperature of about 25 C. were maintained.
- Example II Beeswax was not only bleached but the texture thereof was made smoother by the following treatment: To 50 grams of beeswax melted in a water bath there was added 50 c. c. of an aqueous pH 7 sodium phosphate buffer solution, 100 c. c. of an aqueous sodium chlorite solution containing 5 grams of available chlorine as chlorite and 1.9 c. c. of furfural. After admixing the solution and the melted beeswax, the admixture was permitted to stand for 1 hour at a temperature of 60 C. Thereafter, the wax was separated and allowed to solidify. The resultant product was found to have a much lighter color than the original wax.
- Example III cocoabutter was saponified by treatment with caustic soda and 200 grams of the resulting soap was melted with 200 grams of water. 1 gram of sodium chlorite dissolved in an equal weight of water was then added and admixed with the soap solution.- This was followed by the addition of 10 c. c. of aqueous formaldehyde solution I
- Example IV A further batch of the cocoabutter soap was bleached, as described in Example III, except that a reduced amount of formaldehyde was used. In this operation the formaldehyde solution was prepared by dissolving 0.4 gram of 30% formalin in 100 o. c. of water. The color of the bleached soap was found to be even superior to that resulting in Example III.
- Example V Example VI 200 grams of yellow laundry soap was melted with an equal weight of water containing 0.48 gram of 36% formalin. At 15 minute intervals.
- Example VIII To 50 parts of red oil (oleic acid), heated in a boiling water bath to a temperature of about 100 0., and agitated by the passage gf steam therethrough, there was added 0.5 part of available chlorine as sodium chlorite dissolved in 10 parts of water. A solution of 0.25 part of 36% formalin in 10 parts of water was prepared and 1 part of this solution was added at 5 minute intervals until the total had been added. A few the necessity of critical control of time, temperature and concentration heretofore required to avoid iniuring the material.
- aldehyde in accordance with my present invention, has the effect of materially acceleratlnlthe bleaching action of the chlorite, even in such acid environment, and is particularly desiravoided.
- the improvement which comprises admixing the material to be bleached with a water soluble chlorite in the presence .of water and an aldehyde at a pH not less than about 7.
- the improvement which comprises admixing the material to be bleached with a water soluble chlorite in the presence of water and an adlehyde, and maintaining the hydrogen ion concentration of themixture at a pH not less than about '7 by the presence of an alkali metal phosphate buffer.
- the improvement which comprises subjecting the fatty acid to be bleached to the action of and in admixture with an aqueous solution of a chlorite having a pH not less than about 7 in the presence of an aldehyde.
- non-acidic material comprising fatty acid compounds.
- the improvement which comprises subjecting the material to be bleached to the action of and in admixture with an aqueous solution of achlorite at a pH within the range of about 7 to about 11 in the presence of an aldehyde.
- the improvement which comprises subjecting the fatty acid to the action of and in admixture with an aqueous solution of a chlorite at a pH not less than about 7 in the presence of an aldehyde, the molar ratio of chlorite to aldehyde being about 1:1.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
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Description
Patented Nov. 11, I947 OFFICE BLEACHING FATTY ACID COMPOUNI DS WITH CHLORITE AND ALDEHYDE Y cussed A. Hampel, Harvey, 111., assignor to The Mathieson Alkali Works, lno., New York, N. Y a corporation of Virginia No Drawing. Application June 15, 1945, Serial No. 599,753
This invention relates to an' improved process for effecting color improvement or bleachin f fatty acid compounds. Such fatty acid compounds are oils, fats, fatty acids, waxes and soaps.
In accordance'with the process of my present 8 Claims. (Cl. 260-423) invention, the material to be bleached is subjected to the simultaneous action of a chlorite and any aldehyde in the presence ,of water, Advantageously, the material being treated is admixed in liquid form with the chlorite and aldehyde in aqueous solution, The pH of the solution during the bleaching operation is generally maintained at not less than about 7, though in some instances, as subsequently noted herein, mildly acid solutions maybe employed.
Various-methods have heretofore been proposed for the bleaching of fatty acid compounds.
Many of such methods have involved the use of acids and other strong chemicals which have a tendency to injure the material being bleached or require very careful, critical control to avoid such injury.
Many of these previously-proposed bleaching methods, especially those involving the use of strong acid solutions, tend to char or cause an undesirable reaction between the fatty acid compounds and the acid constituents of thesolution H :-are not applicable to the treatment of many materials ofthis type, particularly soaps and other alkaline reacting materials.
I-have discovered that fatty acid compounds can economically be bleached to an exceptionally high degree, without substantial degradation or danger of deleteriously affecting their desired characteristics, by subjecting them to the action of a chlorite in an alkaline, substantially neutral or only mildly acid aqueous solution, in the presence of an aldehyde as hereinafter more fully de- 2 Various aldehydes may be used, including the aliphatic aldehydes, aromatic aldehydes, other carbocyclic aldehydes and heterocyclic aldehydes.
For example. I have found formaldehyde, acetal- 'dehyde, paraformaldehyde, furfural, benzaldehyde, and 5 and 6 carbon atom aldose sugars and inverted sugars to beparticularly useful. All of these compounds are characterized by the CH0 group. In addition to those highly soluble in water, the relatively insoluble aldehydes have been found to function satisfactorily in most instances.
Temperatures and concentrations are not usually critical and may be varied over a wide range. Increasing the temperature has generally been found to increase the rate of bleaching, Also, the ratio of chlorite to aldehyde may be widely varied. However. a molar ratio of chlorite to aldehyde of about 1:1 has been found generally useful.
The optimum operating conditions, with respect to temperature, concentration and ratio of chlorite to aldehyde, are to a considerable extent interdependent and also will vary somewhat with the particular material'being bleached, the 'de-' gree of bleaching required, the length of the period of the treatment and, to some extent, with the particular chlorite and aldehyde employed.
The temperature best suited for a particular operation will, to a considerable extent, depend upon the nature of the material being treated. Ordinary room temperature may frequently be employed with advantage but higher temperatures are usually desirable when treating fatty acid compounds normally solid where it is desired to effect the melting or solutionthereof. Temperatures at which the material being treated becomes unstable or at which the material is I deleteriously affected, are to be avoided.
It has previously been proposed to bleach cellulosic materials, for instance, by treatment with a chlorite activated by an acid environment, or activated by the introduction of, chlorine gas, or a hypochlorite. Many fatty acid compounds, as
. previously noted, are destroyed or deleteriously ciently soluble in water to provide an adequate concentration to effect the desired -bleaching. when the bleaching requirement is relatively low,
less soluble chlorites may be used. However, for most purposes, I prefer the chlorites of the alkali and alkaline earth metals such as sodium chloaffected by strongly acid solutions and, where chlorine is introduced or liberated during the reaction, there is a tendency forthe chlorine to The hydrogen ion concentration of. my imrite, NaClQz, and calcium chlorite, Ca(Cl0a) fprovedtleaching solution may vary over a 'considerable range. A mildly acid condition may be used where desired, providing the fatty acid compound being bleached is of such a nature as not to be injured thereby, or where the compound has an acid reaction, for instance, a fatty acid. However, it is preferred to carry out the process at a pH within the rangeof about to about 11.
Generally satisfactory results are obtained in bleaching non-acidic fatty acid compounds where the pH is maintained at about 7 or higher, for instance within the range of about 7 to about 11. Solutions having a pH somewhat lower than 7 may be used in the treatment of acid materials,
' such as fatty acids. and various other fatty acid compounds not injured by the acid condition. A buffer salt may, with advantage. be used to maintain the solution at the desired pH.
Alkali metal phosphates such as the monosodium and di-sodium orthophosphates have been found to be particularly advantageous buffers for the purpose of the present invention, though other buffers may be used with advantage. I have found that, by builering the solution to a pH of about 7 by the presence of such phosphates, the consumption of chlorite in the bleaching operation is materially reduced. In some instances, a saving of 50% of chlorite has been effected by the use of these phosphates in conjunction with theother constituents of my bleaching solution previously noted.
My invention is applicable to the treatment of either natural or synthetic fatty acid compounds, including saponiflable oils and waxes, such as beeswax, camauba wax, candelilla wax, corn oil, soybean oil and oleic acid, or commercial red oil. It is especially applicable to the bleaching of soaps and similar alkaline-reacting materials.
The bleaching of such fatty acid compounds is with advantage effected by treating the material while in a liquid condition, 1. e., either molten or in aqueous solution or suspension, depending upon the characteristics of the particular material treated.
'For example, such materials either molten or in aqueous solution, may be admixed with the chlorite in the presence of water, and the aldehyde thereafter added, or'the material to be treated may be admixed with the aldehyde in the presence of water and the chlorite added to this mixture. The resultant mixture is maintained at a temperature usually ranging from ,room temperature to about 100 C. for a period of time sufficient to effect the desired bleaching and is thereafter cooled and separated,
In the bleaching of soap, for instance, the soap may be melted by heating in water, the soap solution admixed with an aqueous chlorite solution and the desired amount of aldehyde thereafter added gradually or as a series of small portions, during agitation.
In the treatment of wax or the like, which is solidat normal temperatures, the material is with advantage melted and an aqueous solution of the chlorite and the aldehyde admixed therewith or the chlorite and aldehyde may be added separately.
My invention and its application will be further illustrated by the following specific examples:
Example I An aqueous solutio was prepared byfadmixing 50 c. c. of pH 7 sodium phosphate buffer 4 solution containing 10 grams of available chlorine and c. c. of a dilute aqueous formalin solution containing 2.2 grams of HCHO. 100 Brains of soybean oil was then admixed with the resultant solution and allowed to stand for 2 hours, at the end of which time much of the original yellow color of the oil had been removed and, upon separation from the solution. a superior product was obtained. During the admixing of the'oil with the solution and during the followingz hour period a pH of .about 7 and a temperature of about 25 C. were maintained.
Example II Beeswax was not only bleached but the texture thereof was made smoother by the following treatment: To 50 grams of beeswax melted in a water bath there was added 50 c. c. of an aqueous pH 7 sodium phosphate buffer solution, 100 c. c. of an aqueous sodium chlorite solution containing 5 grams of available chlorine as chlorite and 1.9 c. c. of furfural. After admixing the solution and the melted beeswax, the admixture was permitted to stand for 1 hour at a temperature of 60 C. Thereafter, the wax was separated and allowed to solidify. The resultant product was found to have a much lighter color than the original wax.
Example III cocoabutter was saponified by treatment with caustic soda and 200 grams of the resulting soap was melted with 200 grams of water. 1 gram of sodium chlorite dissolved in an equal weight of water was then added and admixed with the soap solution.- This was followed by the addition of 10 c. c. of aqueous formaldehyde solution I Example IV A further batch of the cocoabutter soap was bleached, as described in Example III, except that a reduced amount of formaldehyde was used. In this operation the formaldehyde solution was prepared by dissolving 0.4 gram of 30% formalin in 100 o. c. of water. The color of the bleached soap was found to be even superior to that resulting in Example III.
Example V Example VI 200 grams of yellow laundry soap was melted with an equal weight of water containing 0.48 gram of 36% formalin. At 15 minute intervals.
10 c. c. portions of an aqueous solution of com mercial sodium chlorite, each containing 0.1 gram of chlorite, were added until a total of 100 c. c. of the chlorit solution had been added. During this period, the pH of the solution was about 9.3, no
The addition of 10 c. e.
after until all of the available chlorine had disappeared. by the e of steam through the solution. 'I'hereaftr, the soap was salted out and was found to be of a very good white color.
Example VII able where strongly acid solutions are to be For the purposes of illustrating the advantages derived from the use. of the aldehyde in my process, results of the following experiments are presented:
To 500 grams of the yellow laundry soap of about 100 0., there was added and admixed therewith 2.5 grams of sodium chlorite in 3 c. c. of water. After being maintained at this temperature for about 2 hours, the soap was only slightly Example VI. maintained at its melting point,-
its'melting point, there was added 2.5 grams of sodium chlorite and 0.932 gram of 36.6% formalin solution. After stirring the mixture for 20 minutes, all available chlorine had disappeared and the s apwas well bleached. After removing a 100 gram sample of the soap, an additional 1.25 grams of sodium chlorite and 0.466 gram of formalin was added. After 15 minutes of stirring, the available chlorine had disappeared and still further bleaching of the soap obtained. During these tests, the pH of the soap solution was about 9.3, no buffer being used.
Example VIII To 50 parts of red oil (oleic acid), heated in a boiling water bath to a temperature of about 100 0., and agitated by the passage gf steam therethrough, there was added 0.5 part of available chlorine as sodium chlorite dissolved in 10 parts of water. A solution of 0.25 part of 36% formalin in 10 parts of water was prepared and 1 part of this solution was added at 5 minute intervals until the total had been added. A few the necessity of critical control of time, temperature and concentration heretofore required to avoid iniuring the material.
Where the process is carried out under'acid conditions, as previously described, it is possible that the activation of the chlorite is. in part.
elected by the acid environment. However, the
use of aldehyde. in accordance with my present invention, has the effect of materially acceleratlnlthe bleaching action of the chlorite, even in such acid environment, and is particularly desiravoided.
The present application is in part a continuation of my co-pending application Serial No. 472,052, flied January 11, 1943.
I claim:
1. In the bleaching of material comprising fatty acid compounds, the improvement which comprises admixing the material to be bleached with a water soluble chlorite in the presence .of water and an aldehyde at a pH not less than about 7.
2. In the bleaching of material comprising fatty acid compounds, the improvement which comprises admixing the material to be bleached with a water soluble chlorite in the presence of water and an adlehyde, and maintaining the hydrogen ion concentration of themixture at a pH not less than about '7 by the presence of an alkali metal phosphate buffer.
3. In the bleaching of fatty acids, the improvement which comprises subjecting the fatty acid to be bleached to the action of and in admixture with an aqueous solution of a chlorite having a pH not less than about 7 in the presence of an aldehyde.
4. In the bleaching of soap, the improvement which comprises subjecting the soap to the action of and in admixture with an aqueous solution of a chlorite in the presence of an aldehyde.
5. In the bleaching of non-acidic material comprising fatty acid compounds. the improvement which comprises subjecting the material to be bleached to the action of and in admixture with an aqueous solution of achlorite at a pH within the range of about 7 to about 11 in the presence of an aldehyde.
6. In the bleaching of fatty acids, the improvement which comprises subjecting the fatty acid to the action of and in admixture with an aqueous solution of a chlorite at a pH not less than about 7 in the presence of an aldehyde, the molar ratio of chlorite to aldehyde being about 1:1.
7. In the bleaching of soap, the improvement which comprises subjecting the soap to the action of an aqueous solution of a chlorite at a pH within the range of about '1 to about 11 in the presence of an aldehyde.
8. In the bleaching of soap, the improvement which comprises subjecting the soap to the action of an aqueous solution of a chlorite at a pH not less than about 7 in the presence of an aldehyde, the molar ratio of chlorite to aldehyde being about 1:1.
CLIFFORD A. HAMPEL REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Number Name Date 1,788,848 Schumaker Jan. 18, 1981 2,269,687 Kauli'mann Jan. 18, 1942 OTHER REFERENCES Taylor t al., Ind. Eng.- Chemistry, Jul 1940, page 899.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US599753A US2430675A (en) | 1945-06-15 | 1945-06-15 | Bleaching fatty acid compounds with chlorite and aldehyde |
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US599753A US2430675A (en) | 1945-06-15 | 1945-06-15 | Bleaching fatty acid compounds with chlorite and aldehyde |
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US2430675A true US2430675A (en) | 1947-11-11 |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2810735A (en) * | 1954-02-16 | 1957-10-22 | Lever Brothers Ltd | Hypolchlorite-chlorite bleaching of soapstock |
US2846457A (en) * | 1953-09-28 | 1958-08-05 | Rayette Inc | Decolorized detergents and method of manufacture |
US3063782A (en) * | 1960-02-29 | 1962-11-13 | Olin Mathieson | Bleaching cellulosic materials |
US4157300A (en) * | 1976-12-17 | 1979-06-05 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler | Process for the purification of phenol and phenol formaldehyde containing waste water |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1788848A (en) * | 1928-06-26 | 1931-01-13 | Mathieson Alkali Works Inc | Process of bleaching soap |
US2269667A (en) * | 1940-01-27 | 1942-01-13 | Buffalo Electro Chem Co | Refining of oils, fats, and waxes |
-
1945
- 1945-06-15 US US599753A patent/US2430675A/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1788848A (en) * | 1928-06-26 | 1931-01-13 | Mathieson Alkali Works Inc | Process of bleaching soap |
US2269667A (en) * | 1940-01-27 | 1942-01-13 | Buffalo Electro Chem Co | Refining of oils, fats, and waxes |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2846457A (en) * | 1953-09-28 | 1958-08-05 | Rayette Inc | Decolorized detergents and method of manufacture |
US2810735A (en) * | 1954-02-16 | 1957-10-22 | Lever Brothers Ltd | Hypolchlorite-chlorite bleaching of soapstock |
US3063782A (en) * | 1960-02-29 | 1962-11-13 | Olin Mathieson | Bleaching cellulosic materials |
US3063783A (en) * | 1960-02-29 | 1962-11-13 | Olin Mathieson | Bleaching cellulosic materials |
US4157300A (en) * | 1976-12-17 | 1979-06-05 | Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler | Process for the purification of phenol and phenol formaldehyde containing waste water |
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