CN1305552A - Process for making paper - Google Patents
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- CN1305552A CN1305552A CN99807216A CN99807216A CN1305552A CN 1305552 A CN1305552 A CN 1305552A CN 99807216 A CN99807216 A CN 99807216A CN 99807216 A CN99807216 A CN 99807216A CN 1305552 A CN1305552 A CN 1305552A
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- starch
- fixative
- paper
- anionic
- amylopectin
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
- D21H21/20—Wet strength agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/76—Processes or apparatus for adding material to the pulp or to the paper characterised by choice of auxiliary compounds which are added separately from at least one other compound, e.g. to improve the incorporation of the latter or to obtain an enhanced combined effect
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- Paper (AREA)
- Making Paper Articles (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
The invention relates to a process for making paper wherein an anionic starch, which is based on a starch comprising at least 95 wt. %, based on dry substance of the starch, of amylopectin, or a derivative of said starch, is used in combination with a fixative as a strengthening agent.
Description
The present invention relates to the application in described method of a kind of papermaking process and starch.
In order to improve the intensity of paper, in the past 30 in the period of always widespread usage be to add cationic starch in the making beating stage of papermaking process (wet-end).The making beating of papermaking process is meant a stage of papermaking process, and in this stage, fiber is processed to paper pulp, and these fibers come from cellulosic substrates, as recycled writing paper, the paper of using, timber, cotton, perhaps other source.Term " making beating " originates from a large amount of water of use and processes paper pulp.
Over past ten years, several trend are arranged in papermaking process, promptly require to add than the more starch of practicable cationic starch in paper, perhaps make the application of cationic starch difficult more, wherein a kind of trend is the requirement of environment to recycled writing paper, when paper is reproduced, the paper fiber tends to shorten and die down, and the latter is owing to interfibrous interaction reduction causes, thus, in order to produce the paper of sufficient intensity, the amount that increases starch in the pulping process of papermaking process is very important.Have now found that paper is regenerated behind certain number of times,, cause paper intensity relatively poor because the loss of strength that regeneration causes can not compensate by adding cationic starch.
Another kind of trend be exactly people to producing the urgent need of cheap paper, this can realize by add a large amount of cheap filler in paper.Yet a large amount of fillers can cause the decline of paper intensity in the paper, has so also caused increase the requirement of amount of starch in pulping process.
Another trend is based on the consideration that the equipment that is used for papermaking process is changed.The sizing press that tradition is used is constantly measured sizing press in advance and is replaced.Use pre-metering sizing press to compare with using traditional sizing press, starch is more shallow to the infiltration of paper, therefore causes starch to provide less contribution to paper strength.In addition, using pre-metering sizing press to be used to dye will make the internal stress of paper reduce more.For this reason, need provide a kind of method that paper intensity is increased.
Publish such one piece of report on 87～91 pages in that Manchester PITA assembles in October, 1997: " anionic starch: a kind of be used to promote paper intensity and effective making beating notion ", reported that by J.Terpstra and R.C.Versluijs the use anionic starch replaces cationic starch as reinforcing agent in the pulping process of papermaking process, so that the paper of producing obtains bigger internal stress.Use the notion of anionic starch also to be described, see by P.Brouwer: Wochenblatt fur Papierfabrikation, 19 (1997), 928-937, WO-A-93/01353 and WO-A-96/05373 can be explained as follows:
The fiber and the filler grain that are used to produce paper have negative electrical charge.When using cationic starch as the reinforcing agent of paper, its reservation amount mainly is to be caused by reacting to each other between positively charged starch and electronegative fiber and the filler grain.For the cationic starch molecule is deadlocked on anion fiber and filler grain, use a kind of cationic fixative.Although some CATION paper auxiliary agent is better than some other CATION paper auxiliary agent result of use, say on the principle that any CATION paper auxiliary agent can both be used as the fixative of anionic starch.Because low price and be subjected to the influence of the water hardness hardly, the chlorination polymeric aluminum is considered to very tempting fixative.Fix other material of agent of recommended use has alum or cationic polymer, as chlorination poly dimethyl allyl ammonium and polyamine.
Have found that by being used in combination anionic starch with suitable fixative, the mixed volume of starch is compared independent use cationic starch to exceed 5 times as the amount of reinforcing agent be possible in paper, certainly, can produce more high-intensity paper like this.Meanwhile, when using anionic starch and fixative to replace cationic starch, the reservation amount of starch is also very high in papermaking process, this means, at the starch that the papermaking process making beating stage adds in paper pulp, seldom a part can be taken away by water.Furthermore,, find that the reservation amount of fines and filler significantly increases, might reduce correct grinding like this and handle, equally also observe the quickening of dewatering speed by being used in combination anionic starch with suitable fixative.
Use anionic starch to replace the disadvantage of cationic starch to be essential a kind of fixative that uses in the papermaking process making beating stage.Although recommend some fixatives of use more cheap relatively in the prior art, because used fixative, the production cost of paper also may significantly increase.Equally, because fixative is a kind of cationic compound, also join in the paper simultaneously with fixative inevitably with the anion of its balance.Equilibrium ion is chlorion normally, and chlorion is mordant.And then, use a kind of fixative may cause handling the sclerosis of water and the generation of salt, this can produce other paper making additive and disturb.
Surprisingly, the present use anionic starch of finding can alleviate by using a kind of anionic starch as the above-mentioned deficiency of the reinforcing agent of paper, and this anionic starch mainly is made up of amylopectin.
So far, the present invention relates to a kind of papermaking process, wherein a kind of anionic starch combines with fixative and is used as reinforcing agent, and this anionic starch is based on the derivative of a kind of starch or described starch, and this starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.Have found that, compare, use this special anionic starch just may realize using very small amount of fixative with using traditional anionic starch.Simultaneously, the anionic starch of sneaking in paper based on amylopectin can make paper have very high intensity.
Most of type starch are made up of the particle of two kinds of glucose polymers, and wherein a kind of is amylose (accounting for the 15-35% of dried starch weight), and another kind is amylopectin (accounting for the 65-85% of dried starch weight).Amylose is by non-branching or contains the molecular composition of a small amount of side chain, and the average degree of polymerization of this molecule is 1000 to 5000, dissimilar starch degree of polymerization differences; Amylopectin is that the average degree of polymerization of this molecule is 1,000, more than 000 by molecular composition very large, high branching.Business-like main flow starch type (cornstarch, farina, wheaten starch and tapioca) contains the amylose of 15% to 30% (weight).
To some cereals, as barley, cassava, barnyard grass, wheat, chinese sorghum, rice and Chinese sorghum almost all are made up of amylopectin the starch granules of some kinds, press the percetage by weight of dry and calculate, these starch granuless contain 95% or more and usually are amylopectin more than 98%.The content of amylose also just is less than 5% and usually be below 2% in these cereal starch particles.Above-mentioned cereal kind also often is classified as glutinous property cereal, and wherein the amylopectin particle is therefrom separated as glutinous property cereal starch.
Opposite with different cereal situations, the root that starch granules mainly is made up of amylopectin and the kind nature of stem tuber are still unknown.For example, isolated potato starch particle contains have an appointment 20% amylose and 80% amylopectin (accounting for the dry percetage by weight) usually in the potato tubers.But, in in the past 10 years, obtained successful result by plantation genetic modification potato plants, both the starch granules that forms contained amylopectin more than 95% (the accounting for dry weight) in potato tubers, What is more, it has been found that to produce the potato tubers of almost being made up of amylopectin entirely.
In the middle of the formation of starch granules, different enzymes have played catalytic action.Wherein particle participates in the generation of amylose in conjunction with starch synthase (GBSS).The activity of the gene of the described GBSS enzyme of encoding is depended in the existence of GBSS enzyme.The expression of eliminating or suppressing these specific genes will stop or limit the generation of GBSS enzyme.The elimination of these genes can realize by the genetic modification or the recessive mutation of potato plants.For example produce the no amylose mutant (amf) of potato, only contain amylopectin in its starch basically by the recessive mutation in the gbss gene.This mutating technology is referring to " separation of the no amylose mutant of potato (Solanum tuberosum L.) " that people such as J.H.M.Hovenkamp-Hermelink deliver, Theor.Appl.Gent., (1987), 75:217-221, not " will not the having the breeding that amylose mutant (amf) imports the potato Solanumtuberosum L. of plantation " of delivering with people such as E.Jacobsen, Euphytica, (1991), 53:247-253.
The expression of gbss gene in elimination or the inhibition of potato, the method that is referred to as Antisense Suppression by use also can realize.This potato genetic modification is described in the paper that people such as R G.F.Visser deliver, and sees: " by particle in the antisense construct inhibition of potato in conjunction with the starch synthase expression of gene ", Mol.Gen.Genet., (1991), 225:289-296.
Contain considerably less in the starch granules or do not contain the root and the stem tuber of amylose by using genetic modification to have been found that to plant and to cultivate, as potato, Chinese yam or cassava class (south african patent 97/4383).The alleged amylopectin-potato starch of this paper is an isolated potato starch particle from potato tubers, and the content of its amylopectin accounts for more than 95% of dry matter.
From manufacturing feasibility and properties, be amylopectin-potato starch on the one hand, be glutinous property cereal starch on the other hand, both are significantly different.This point is specially adapted to waxy corn starch-a kind of up to the present business-like most important glutinous property cereal starch.The glutinous corn plantation that is suitable for the production waxy corn starch is difficult for realizing commercialization in country cold or temperate climate, as Holland, Belgium, England, Germany, Poland, Sweden and Denmark, but these national environmental conditions are fit to the plantation potato on the contrary.The tapioca that from cassava, obtains be suitable for weather the country of heat produce, as in Southeast Asia and area, South Africa.
The composition of root and tuber starch such as amylopectin-potato starch and side chain tapioca and character are different with glutinous property cereal starch.Amylopectin-potato starch is compared with glutinous property cereal starch has much lower lipid and protein.Consider from bad smell and generation air bubble problem, owing to contain lipid and/or protein, when using glutinous property cereal starch products (natural with modification) this class problem just may take place, but just this problem can or not take place slightly when using corresponding amylopectin-potato starch products.Opposite with glutinous property cereal starch, amylopectin-potato starch contains the phosphate group of chemical bonding, and therefore, the amylopectin-potato starch products of dissolved state has the characteristics of tangible polyeletrolyte.
One aspect of the present invention relates to the application of the anionic starch that obtains from cereal and fruit, relate on the other hand from the application of the anionic starch in root and stem tuber source.In cereal starch, it is most suitable that waxy corn starch is proved to be.Certainly, root and tuber starch are more preferably usually.As previously mentioned, use the starch of grease with unusual low content and/or protein more favourable usually.Have found that, use anion amylopectin-potato starch and side chain tapioca can produce high-intensity paper as the reinforcing agent of paper.
The term anionic starch is meant a kind of starch, and the charge density that this starch has is at least 0.03 μ eq/mg starch, preferably is 0.15 μ eq/mg starch at least.Charge density described in the literary composition of the present invention is defined as a kind of cationic polymer (Propylene Glycol chitosan iodide, SIGMA M-3150) consumption, needed amount when being about to make it reach equivalent point in the dissolving starch that this polymer joins known quantity.Equivalent point is to measure as the electrophoresis zeta potential of the dispersion of the silica dioxide granule of indicator by measuring adding.As an example, zeta potential can be measured with Malvern Zetasizer 3.
Combining the anionic starch that is used as the paper reinforcing agent with fixative according to the present invention can be from a kind of starch or described starch derivatives with the known any way preparation of the conventional starch that comprises amylopectin and amylose, and described starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.A kind of description that may mode for preparing a kind of anionic starch can be with reference to the document of O.B.Wurzburg (Ed.): " modified starch: character and use ", CRC publishing company, Boca Eaton, Florida, 1986.
Obtain the example of anionic starch, as known oxidation treatment method in deriving by the introducing of any anion substituent or by starch.The corresponding example of anion substituent has phosphate, phosphonate ester, sulphonic acid ester, sulfuric ester, (alkyl) succinate, anionic grafting copolymer and their combination; The corresponding example of oxidation is the oxidation of hypochlorite.What preferably use is the carboxymethyl starch of phosphorylation.In the starch molecule in each glucose unit the mol ratio of substituted amount of hydroxyl groups and its glucose unit amount be called the substitution value of this starch, the scope of substitution value (DS) is between 0.005 and 0.5, be preferably between 0.01 and 0.2, most preferably be between 0.01 and 0.1.
The suitable starch derivatives that contains at least 95% amylopectin (accounting for the weight of dry) is more such starch, wherein, except anion substituent, also has one or more nonionics or cationic substituent to be introduced into.The corresponding example of nonionic or cationic substituent is to be introduced into by etherification or same esterification, as methylate, the inferior amidatioon (carba-imidation) of ethylization, hydroxyethylation, hydroxypropylation, alkyl glycidyl etherization (wherein from 1 to 20 carbon atom of alkyl chain length does not wait), acetylation, propylated, carbon, diethyllaminoethylization and/or trimethylammonium hydroxypropylation.Furthermore, starch can take place crosslinked by the known on any crosslinked action of starch derivativesization, and the example of corresponding crosslink agent comprises chloropropylene oxide, dichlorohydrin, trimethyl sodium phosphate, phosphorous oxychloride and adipic anhydride.Certainly, the total electrical charge that it should be noted that starch is negative.
As mentioned above, be used to pull an oar and when improving the intensity of paper, it is very important using fixative when anionic starch.According to the present invention, suitable fixative is the compound of positively charged, and this compound can adhere to anionic starch on anion paper fiber and the filler particles.Say that in principle those are recommended in any cationic compound that is used as the anionic starch fixative in the papermaking process making beating and can both be used.For example comprise alum, cationic starch or their derivative, poly-aluminium compound, cationic polymer such as chlorination poly dimethyl allyl ammonium, polyamine, polyvinylamine, polymine, dicyandiamide condensation polymer, or other high-molecular cationic polymer or copolymer one for example contain quaternised nitrogen-atoms or polyvinyl alcohol and their composition.These cationic polymers preferably should have at least about 10,000 weight average molecular weight, preferably at least about 50,000, and most preferably at least 100,000.In preferred embodiments, the weight average molecular weight range that cationic polymer has is from about 50,000 to about 2,000,000.
What preferably use is the fixative with high charge density.About this point, charge density is considered to high charge density greater than 1 μ eq/mg.The charge density of fixative is defined as a kind of anionic polymer (kayexalate, Aldrich cat.No.24, consumption 305-1) is about to (normally containing several milliliters of fixatives in the 500ml deionized water) needed amount when making it reach equivalent point in the fixative that this polymer joins known quantity.Equivalent point is to measure as the electrophoresis zeta potential of the dispersion of the silica dioxide granule of indicator by measuring adding.As an example, zeta potential can be measured with Malvem Zetasizer 3.Have found that the fixative that uses high charge density causes papermaking process that the sensitiveness of handling hardness of water and electrical conductivity is reduced.The fixative that preferably has high charge density is poly-aluminium compound such as the poly-aluminium of chlorination or the poly-aluminium of sulfuric acid, chlorination poly dimethyl allyl ammonium, polyamine and their composition.
In papermaking process, anionic starch and fixative are added in the making beating of method, and wherein anionic starch is based on the derivative of a kind of starch or described starch, and this starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.This means that they are added into the paper pulp that contains the fiber that obtains from recycled writing paper or timber and water.Usually add filling compound in paper pulp, according to the present invention, any filling compound commonly used can be used, as potter's clay, fine grinding CaCO
3, deposit C aCO
3, talcum or titanium dioxide.Preferably added filling compound before adding anionic starch and fixative, further, anionic starch preferably added before fixative adds.
The amount that is added into the anionic starch in the paper pulp will depend on required paper intensity.Generally speaking, use amount is 0.1% to 10%, and preferably 1% to 5%, this concentration is based on the solid formation in the paper pulp (fiber, filling compound, meticulous material or the like) weight.
The addition of fixative promptly depends on the character of fixative and the paper pulp that is used, and also depends on the amount of mixing anionic starch in paper.Usually, it is can obtain at least 60% that the fixative consumption is selected, preferably at least 80%, and most preferably at least 90% anionic starch adsorbs.It should be noted that between absorption and the reservation obviously different about this point.Keep to be meant that the final quilt that adds sneaks into the amount of the starch in paper in pulping process, and absorption is meant the amount of the starch that the paper fiber by in the making beating paper pulp that adds is adsorbed in pulping process.Those skilled in the art can join the amount of fixative in this environment according to the field condition adjustment.The typical amounts of organic fixative and inorganic fixative is different.Under normal circumstances use when containing the anionic starch of amylose, the weight ratio of fixative and anionic starch is about 1: 1 to inorganic fixative, is about 1: 4 to organic fixative.Under situation of the present invention, when using the anionic starch of amylopectin type, to organic fixative, consumption will reduce 8-10 doubly, and to inorganic fixative, consumption will reduce 4-6 doubly.
According to method of the present invention, the paper pulp that is used for papermaking can be any suspension that can be used as the cellulosic substrates fiber of papermaking.After anionic starch and fixative were added in the paper pulp, this paper pulp can be processed into paper in any known mode.
The present invention will further illustrate by following embodiment, but is not limited to these embodiment.
The embodiment I
The urea and the 31.1g phosphoric acid (85%) that in the water of 85ml, add 30g, with this solution with 50% the NaOH pH6.0 that neutralizes, this solution was mixed on the Hobar mixer 30 minutes with the amylopectin-potato starch (humidity is 20%) of 600g, mixture is placed on drying on the Retsch fluid bed dryer after reaching balance, drying is 30 minutes in the time of 60 ℃, drying is 30 minutes in the time of 90 ℃, and mixture is heated to 145 ℃ and kept 30 minutes in fluidized-bed reactor.Obtain product HK4017A at last, its charge density is 0.47 μ eq/mg.
The embodiment II
The urea and the 31.1g phosphoric acid (85%) that in the water of 85ml, add 30g, with this solution with 50% the NaOH pH6.0 that neutralizes, this solution was mixed on the Hobar mixer 30 minutes with the amylopectin-potato starch (humidity is 20%) of 600g, mixture is placed on drying on the Retsch fluid bed dryer after reaching balance, drying is 30 minutes in the time of 60 ℃, drying is 30 minutes in the time of 90 ℃, and mixture is heated to 140 ℃ and kept 30 minutes in fluidized-bed reactor.Obtain product HK4041B at last, its charge density is 0.34 μ eq/mg.
The embodiment III
The research that starch is adsorbed onto on the solid pulp compositions is as follows, in paper pulp (concentration is 1%), add anionic starch (concentration is 3%), paper pulp rotating speed with 800rpm in having the beaker of deflector is stirred, and adds a kind of fixative, filter paper pulp after 60 seconds after 60 seconds.The absorption of starch is determined by the amount of measuring the starch that is not adsorbed in the filtrate.
This paper pulp is the white birch wood pulp of sulfuric acid treatment, and using the Hollander beater is 2% to beat 35 ° of SR (measuring temperature is 21 ℃) with concentration in running water, and it is 1% that the paper pulp after the making beating is diluted to concentration with running water.
This paper pulp is divided into three parts, the electrical conductivity of a copy of it sodium sulphate (Na
2SO
410H
2O, Merck reinst) is modulated into 3.01mS/cm; Second part water hardness calcium chloride (CaCl
22H
2O, Merck reinst) be increased to ca.80 ° of GH from ca.11 ° of GH, the electrical conductivity of this part is 3.01mS/cm; The 3rd part with salt, and the electrical conductivity and the water hardness are respectively 0.51 mS/cm and ca.11 ° of GH.The electrical conductivity of paper pulp is measured with Radiometer CDM 80 conductivity meters.
The starch that uses is, anion farina PR9510A (trade names are AniofaxAP25) and two kinds of amylopectin-potato starch: HK4017A and HK4041B, and back two kinds of products prepare by the method in " embodiment I " and " embodiment II " respectively.Starch running water slurries vapours boiling with 10%, the starch solution after the boiling is diluted to 5% with the running water of heat.The viscosity of 5% starch solution is measured (seeing Table 1) with Brookfield LVTDV-II viscosimeter under the 60rpm condition.Excessive phosphoric acid was dialysed 48 hours with the hydrochloric acid of 0.05N, remove with deionized water dialysis 24 hours then, with the NaOH of the 0.01N pH7-8 that neutralizes, phosphoric acid substitution value in the starch is measured by hereinafter describing afterwards: J.Th.LB.Rameau and J.ten Have, Chemisch Weekblad, No.50 (1951).
Table 1: the characteristic of applying starch
| Starch | ???DSP [mol/mol] | Viscosity (50 ℃, 5%) [mPas] | ????pH |
| ?PR9510A(AZM) | 0.022 | ????391 | ????7.1 |
| ?HK4017A(AAZM) | 0.024 | ????680 | ????7.1 |
| ?HK4041B(AAZM) | 0.018 | ????252 | ????7.2 |
The fixative that uses is Sachtokar (obtaining from the Sachtleben Chemie GmbH of Germany), Retinal 1030 (obtaining from the Joud of France) and PD5-8159 (obtaining from the colloid company of alliance of Britain).
Before the use, 10 times of fixative Sachtokar and the dilutions of Retinal 1030 usefulness deionized waters; The PD5-8159 formulations prepared from solutions is as follows: dissolving 1g polymer in 4g acetone, stir adding 95g deionized water after 30 minutes.The part character of said fixing agent is listed in table 2.
Fixative charge density adopts the adding kayexalate to measure to the method in the fixative (normally containing several milliliters of fixatives in the 500ml deionized water) of known quantity.Necessary amount is exactly a charge density when reaching balance.Equivalent point is to adopt Malvern Zetasizer 3, measures as the electrophoresis zeta potential of the dispersion of the silica dioxide granule of indicator by the measurement adding.
Table 2: the characteristic of using fixative
| Fixative | Fixative pH | Viscosity (20 ℃, 60 rpm) [mPas] | Solid formation content [%] | Charge density [μ eq/mg] |
| Saehtoklar (=Paper-PAC-N) | ????2.3 | ????7.3 | ????23.2 | ????+2.0 |
| ?Retinal1030 | ????5.7 | ????950 | ????50.1 | ????+7.6 |
| ?PD5-8159 | ????6.6 | ????2240 | ????26.8 | ????+7.0 |
Amount of starch enzymatic assays in the filtrate.According to said method, starch is at first changed into glucose by α-Dian Fenmei and amyloglucosidase, uses hexokinase method of testing (Boehringerno. 716251) to measure the amount of glucose with spectrographic technique subsequently.Amount of starch is by using a correction factor to not changed into glucose fully from starch by enzyme to calculate from obtaining glucose amount.The employed enzymatic conversion coefficient of Aniofax AP25 is 0.78.Starch concentration in the filtrate that the absorption of starch can be measured according to enzyme process calculates, and its expression formula is as follows:
Wherein A is starch absorption, C
sBe starch concentration in the filtrate, V is the cumulative volume of water, and G is the amount that adds starch.The water cumulative volume is obtained by following formula:
V=V
p-ds
p+V
st-ds
st+V
fix-ds
fix????eq.B
V wherein
p, V
StAnd V
FixRepresent the volume of paper pulp, the volume of starch and the volume of fixative respectively, the cumulative volume solid formation content d that does
Sp, ds
StAnd ds
FixRevise (density of supposing dried solid formation is 1g/ml).
Starch absorption is studied by changing three parameters: the character of starch, fixative and paper pulp (electrical conductivity and hardness of water).The result will discuss by the consumption of the fixative of drying on fiber.
The summary of required fixative consumption under every kind of starch and every kind of experiment condition when table 3 provides at least 90% starch and is adsorbed.
Under the HK4017A situation, when the starch more than 90% was adsorbed, required fixed dosage was minimum.For PD5-8159, increase by 1.5 to 2.5 times under the amount ratio HK4017A situation of fixative, than increasing by 2.5 to 5 times under the PR9510A situation; For fixative Retinal1030, increase by 2 to 2.5 times for the HK4017A consumption, and be 5 times at least for PR9510A.
To PAC Sachtokar, amylopectin has also obtained best result equally.It is high 1.5 to 3.5 times that the consumption of PAC is compared to HK4017A for PR9510A.
The service efficiency of organic fixative PD5-8159 and Retinal 1030 under the different conditions that are the high water hardness that it should be noted that PR9510A and HK4017A.For HK4017A, all than higher, but for PR9510A, adsorptive value is identical or lower for these two kinds of fixatives for the starch adsorptive value under the condition of high rigidity.So, for anion AAZM, the high water hardness will cause high starch adsorptive value, and will be not only to PACs, also like this to underproof organic fixative.To another kind of anion AAZM, HK4041B can observe same water hardness impact effect with Retinal 1030, and PD5-8159 is not then had.
These results prove that it is more effective to the absorption amylose molecule for absorption amylopectin molecular proportion to use organic fixative.
Table 3: the data of different starch relatively
The consumption of listed fixative is the minimum amount at starch adsorptive value＞90% o'clock, and the ratio of fixative consumption is the ratio of the required fixed dosage of required fixed dosage of HK4041B or PR9510A and HK4017A.
| Sequence number | Fixative | Electrical conductivity (mS/cm) | Hardness | Starch | The fixative consumption | The starch adsorptive value | The ratio of fixative consumption |
| ?1 | ?Sachtoklar | ????0.51 | ????11 | ?HK4017A | ????0.46 | ????99.0 | ????- |
| ?2 | ?Sachtoklar | ????0.51 | ????11 | ?HK4041B | ????0.46 | ????92.6 | ????1 |
| ?3 | ?Sachtoklar | ????0.51 | ????11 | ?PR9510A | ????0.70 | ????98.6 | ???1.5 |
| ?4 | ?Sachtoklar | ????3.01 | ????11 | ?HK4017A | ????0.46 | ????93.4 | ????- |
| ?5 | ?Sachtoklar | ????3.01 | ????11 | ?HK4041B | ????0.70 | ????90.6 | ???1.5 |
| ?6 | ?Sachtoklar | ????3.01 | ????11 | ?PR9510A | ????1.62 | ????85.6 | ??＞3.5 |
| ?7 | ?Sachtoklar | ????2.98 | ????80 | ?HK4017A | ????0.23 | ????95.0 | ????- |
| ?8 | ?Sachtoklar | ????2.98 | ????80 | ?HK4041B | ????0.46 | ????96.9 | ????2 |
| ?9 | ?Sachtoklar | ????2.98 | ????80 | ?PR9510A | ????0.46 | ????92.6 | ????2 |
| ?10 | ?PD5-8159 | ????0.51 | ????11 | ?HK4017A | ????0.10 | ????94.5 | ????- |
| ?11 | ?PD5-8159 | ????0.51 | ????11 | ?HK4041B | ????0.15 | ????92.6 | ???1.5 |
| ?12 | ?PD5-8159 | ????0.51 | ????11 | ?PR9510A | ????0.25 | ????92.3 | ???2.5 |
| ?13 | ?PD5-8159 | ????3.01 | ????11 | ?HK4017A | ????0.25 | ????98.0 | ????- |
| ?14 | ?PD5-8159 | ????3.01 | ????11 | ?HK4041B | ????0.50 | ????91.9 | ????2 |
| ?15 | ?PD5-8159 | ????3.01 | ????11 | ?PR9510A | ????1.00 | ????91.3 | ????4 |
| ?16 | ?PD5-8159 | ????2.98 | ????80 | ?HK4017A | ????0.10 | ????97.0 | ????- |
| ?17 | ?PD5-8159 | ????2.98 | ????80 | ?HK4041B | ????0.25 | ????91.7 | ???2.5 |
| ?18 | ?PD5-8159 | ????2.98 | ????80 | ?PR9510A | ????0.50 | ????94.2 | ????5 |
| ?19 | ?Retinal?1030 | ????0.51 | ????11 | ?HK4017A | ????0.13 | ????95.2 | ????- |
| ?20 | ?Retinal?1030 | ????0.51 | ????11 | ?HK4041B | ????0.25 | ????97.2 | ????2 |
| ?21 | ?Retinal?1030 | ????0.51 | ????11 | ?PR9510A | ????0.25 | ????91.8 | ????2 |
| ?22 | ?Retinal?1030 | ????3.01 | ????11 | ?HK4017A | ????0.25 | ????92.0 | ????- |
| ?23 | ?Retinal?1030 | ????3.01 | ????11 | ?HK4041B | ????1.00 | ????94.6 | ????4 |
| ?24 ?25 | ?Retinal?1030 | ????3.01 | ????11 | ?PR9510A | ????1.00 ????2.00 | ????89.9 ????95.7 | ???＞4 ????8 |
| ?26 | ?Retinal?1030 | ????2.98 | ????80 | ?HK4017A | ????0.05 | ????90.0 | |
| ?27 | ?Retinal?1030 | ????2.98 | ????80 | ?HK4041B | ????0.13 | ????91.5 | ????2.5 |
| ?28 | ?Retinal1030 | ????2.98 | ????80 | ?PR9510A | ????0.25 | ????93.3 | ?????5 |
Claims (9)
1, a kind of papermaking process, wherein a kind of anionic starch combines with a kind of fixative and is used as reinforcing agent, this anionic starch is based on the derivative of a kind of starch or described starch, and this starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.
2, according to the process of claim 1 wherein that starch is root or tuber starch.
3, according to the method for claim 2, wherein starch is potato or tapioca.
4, according to any one method of claim 1 to 3, wherein the derivative of starch be by esterification or etherification reaction or they in conjunction with resulting.
5, according to the method for aforementioned any one claim, wherein fixative is a kind of cationic compound that charge density is at least 1 μ eq/mg.
6, according to any one sharp method that requires of aforementioned power, wherein fixative is selected from as next group, and described group comprises poly-aluminium compound, alum, cationic starch or derivatives thereof, chlorination poly dimethyl allyl ammonium, polyamine, polyvinylamine, polymine, dicyandiamide condensation polymer.
7, the paper that obtains according to the method for aforementioned any one claim.
8, a kind of anionic starch is as the application of the reinforcing agent of paper, and wherein anionic starch is based on the derivative of a kind of starch or described starch, and this starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.
9, the application in the amount of the fixative that in reducing papermaking process, uses of a kind of anionic starch, wherein this anionic starch in papermaking process as reinforcing agent, this anionic starch is based on the derivative of a kind of starch or described starch, and this starch comprises the amylopectin of the dry at least 95% (weight) based on this starch.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP98201943 | 1998-06-10 | ||
| EP98201943.2 | 1998-06-10 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1305552A true CN1305552A (en) | 2001-07-25 |
| CN1136360C CN1136360C (en) | 2004-01-28 |
Family
ID=8233797
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB998072168A Expired - Lifetime CN1136360C (en) | 1998-06-10 | 1999-06-04 | Process for making paper |
Country Status (12)
| Country | Link |
|---|---|
| US (1) | US20030145966A1 (en) |
| EP (1) | EP1086274B9 (en) |
| JP (1) | JP4475810B2 (en) |
| CN (1) | CN1136360C (en) |
| AT (1) | ATE226662T1 (en) |
| AU (1) | AU4293199A (en) |
| BR (1) | BR9910991B1 (en) |
| CA (1) | CA2334532C (en) |
| DE (1) | DE69903628T2 (en) |
| ID (1) | ID27649A (en) |
| MX (1) | MXPA00012086A (en) |
| WO (1) | WO1999064677A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111886381A (en) * | 2018-03-22 | 2020-11-03 | 凯米拉公司 | Dry strength composition, use thereof and process for making paper, board and the like |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6982327B2 (en) * | 1996-05-20 | 2006-01-03 | Cooperatieve Verkoop-En Productievereniging Van Aardeppelmeel En Derivaten Abebe, B.A. | Methods for producing and transforming cassava protoplasts |
| AU5070899A (en) * | 1998-07-23 | 2000-02-14 | Cooperatieve Verkoop- En Productievereniging Van Aardappelmeel En Derivaten Avebe B.A. | Adhesive composition |
| GB0014946D0 (en) * | 2000-06-20 | 2000-08-09 | Cerestar Holding Bv | Starch composition and the use thereof in the wet-end of paper preparation |
| US6824650B2 (en) † | 2001-12-18 | 2004-11-30 | Kimberly-Clark Worldwide, Inc. | Fibrous materials treated with a polyvinylamine polymer |
| FR2854898B1 (en) | 2003-05-12 | 2007-07-13 | Roquette Freres | PROCESS FOR CATIONIZATION OF AMIDONS FROM LEGUMES, CATIONIC STARCH SO OBTAINED AND THEIR APPLICATIONS |
| PL2192228T3 (en) * | 2006-04-24 | 2017-12-29 | Chemigate Oy | Use of cationic starch |
| US7758934B2 (en) * | 2007-07-13 | 2010-07-20 | Georgia-Pacific Consumer Products Lp | Dual mode ink jet paper |
| CL2008002019A1 (en) * | 2007-07-16 | 2009-01-16 | Akzo Nobel Chemicals Int Bv | A filler composition comprising a filler, a cationic inorganic compound, a cationic organic compound, and an anionic polysaccharide; method of preparing said composition; use as an additive for an aqueous cellulosic suspension; procedure for producing paper; and paper. |
| EP2199462A1 (en) * | 2008-12-18 | 2010-06-23 | Coöperatie Avebe U.A. | A process for making paper |
| US8980059B2 (en) * | 2009-08-12 | 2015-03-17 | Nanopaper, Llc | High strength paper |
| JP5933550B2 (en) * | 2010-08-25 | 2016-06-08 | ソレニス・テクノロジーズ・ケイマン・エル・ピー | A method to increase the benefits of starch in pulped cellulosic materials in the production of paper and paperboard |
| CN104693441B (en) * | 2015-02-13 | 2017-04-19 | 华南理工大学 | Method for preparing paper-making fixing agent and application thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3794558A (en) * | 1969-06-19 | 1974-02-26 | Crown Zellerbach Corp | Loading of paper furnishes with gelatinizable material |
| DE2924947C2 (en) * | 1979-06-21 | 1983-11-17 | Giulini Chemie Gmbh, 6700 Ludwigshafen | Process for the production of a surface sizing agent for paper, cardboard, paperboard and nonwovens |
| GB8531558D0 (en) * | 1985-12-21 | 1986-02-05 | Wiggins Teape Group Ltd | Loaded paper |
| US4964953A (en) * | 1986-08-13 | 1990-10-23 | National Starch And Chemical Investment Holding Corporation | Amphoteric starches and process for their preparation |
| FR2612213B1 (en) * | 1987-03-13 | 1989-06-30 | Roquette Freres | PAPERMAKING PROCESS |
| US5059282A (en) * | 1988-06-14 | 1991-10-22 | The Procter & Gamble Company | Soft tissue paper |
| SE461404C (en) * | 1988-06-22 | 1999-11-15 | Betzdearborn Inc | Gluing composition, process for making thereof, process for making glued paper, and glued paper |
| US5185062A (en) * | 1991-01-25 | 1993-02-09 | Nalco Chemical Company | Papermaking process with improved retention and drainage |
| EP0592572B1 (en) * | 1991-07-02 | 1998-01-14 | Eka Chemicals AB | A process for the manufacture of paper |
| ATE141357T1 (en) * | 1991-07-02 | 1996-08-15 | Eka Chemicals Ab | METHOD FOR PRODUCING PAPER |
| US5221435A (en) * | 1991-09-27 | 1993-06-22 | Nalco Chemical Company | Papermaking process |
| US5266164A (en) * | 1992-11-13 | 1993-11-30 | Nalco Chemical Company | Papermaking process with improved drainage and retention |
| EP0776397B1 (en) * | 1994-08-16 | 2000-10-25 | Chemisolv Limited | Process of improving paper strength |
| IT1271003B (en) * | 1994-09-08 | 1997-05-26 | Ausimont Spa | HIGH MECHANICAL RESISTANCE PAPER AND CARDBOARD PRODUCTION PROCESS |
| US5595630A (en) * | 1995-08-31 | 1997-01-21 | E. I. Du Pont De Nemours And Company | Process for the manufacture of paper |
| US5766366A (en) * | 1995-10-13 | 1998-06-16 | A. E. Staley Manufacturing Co. | Dry thinned starches, process for producing dry thinned starches, and products and compositions thereof |
-
1999
- 1999-06-04 WO PCT/NL1999/000351 patent/WO1999064677A1/en active IP Right Grant
- 1999-06-04 CA CA002334532A patent/CA2334532C/en not_active Expired - Fee Related
- 1999-06-04 DE DE69903628T patent/DE69903628T2/en not_active Expired - Lifetime
- 1999-06-04 ID IDW20010031A patent/ID27649A/en unknown
- 1999-06-04 MX MXPA00012086A patent/MXPA00012086A/en active IP Right Grant
- 1999-06-04 AU AU42931/99A patent/AU4293199A/en not_active Abandoned
- 1999-06-04 EP EP99955510A patent/EP1086274B9/en not_active Expired - Lifetime
- 1999-06-04 BR BRPI9910991-3A patent/BR9910991B1/en not_active IP Right Cessation
- 1999-06-04 AT AT99955510T patent/ATE226662T1/en active
- 1999-06-04 JP JP2000553661A patent/JP4475810B2/en not_active Expired - Fee Related
- 1999-06-04 CN CNB998072168A patent/CN1136360C/en not_active Expired - Lifetime
-
2002
- 2002-11-27 US US10/305,929 patent/US20030145966A1/en not_active Abandoned
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111886381A (en) * | 2018-03-22 | 2020-11-03 | 凯米拉公司 | Dry strength composition, use thereof and process for making paper, board and the like |
| CN111886381B (en) * | 2018-03-22 | 2022-11-25 | 凯米拉公司 | Dry strength composition, use thereof and process for making paper, board and the like |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1086274A1 (en) | 2001-03-28 |
| MXPA00012086A (en) | 2003-04-22 |
| AU4293199A (en) | 1999-12-30 |
| EP1086274B1 (en) | 2002-10-23 |
| ATE226662T1 (en) | 2002-11-15 |
| ID27649A (en) | 2001-04-19 |
| JP2002517637A (en) | 2002-06-18 |
| DE69903628D1 (en) | 2002-11-28 |
| BR9910991B1 (en) | 2009-01-13 |
| CA2334532C (en) | 2008-03-11 |
| EP1086274B9 (en) | 2005-01-19 |
| BR9910991A (en) | 2001-02-13 |
| WO1999064677A1 (en) | 1999-12-16 |
| CA2334532A1 (en) | 1999-12-16 |
| JP4475810B2 (en) | 2010-06-09 |
| DE69903628T2 (en) | 2003-07-03 |
| CN1136360C (en) | 2004-01-28 |
| US20030145966A1 (en) | 2003-08-07 |
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