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EP0700473A1 - Process for producing paper - Google Patents

Process for producing paper

Info

Publication number
EP0700473A1
EP0700473A1 EP93902274A EP93902274A EP0700473A1 EP 0700473 A1 EP0700473 A1 EP 0700473A1 EP 93902274 A EP93902274 A EP 93902274A EP 93902274 A EP93902274 A EP 93902274A EP 0700473 A1 EP0700473 A1 EP 0700473A1
Authority
EP
European Patent Office
Prior art keywords
cationic
added
aluminum
fiber suspension
process according
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.)
Granted
Application number
EP93902274A
Other languages
German (de)
French (fr)
Other versions
EP0700473B2 (en
EP0700473B1 (en
Inventor
Lars Harald Petander
Tore Anders Johan DUVNÄS
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kemira Oyj
Original Assignee
Kemira Oyj
Priority date (The priority date 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 date listed.)
Filing date
Publication date
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Application filed by Kemira Oyj filed Critical Kemira Oyj
Publication of EP0700473A1 publication Critical patent/EP0700473A1/en
Application granted granted Critical
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Publication of EP0700473B2 publication Critical patent/EP0700473B2/en
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Links

Classifications

    • 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
    • D21H21/06—Paper forming aids
    • D21H21/10—Retention agents or drainage improvers
    • 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
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
    • D21H17/375—Poly(meth)acrylamide
    • 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
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
    • D21H17/44—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups cationic
    • D21H17/45—Nitrogen-containing groups
    • D21H17/455—Nitrogen-containing groups comprising tertiary amine or being at least partially quaternised
    • 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
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/55—Polyamides; Polyaminoamides; Polyester-amides
    • 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
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
    • D21H17/56—Polyamines; Polyimines; Polyester-imides
    • 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
    • D21H17/63—Inorganic compounds
    • D21H17/66—Salts, e.g. alums
    • 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
    • D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/04—Addition to the pulp; After-treatment of added substances in the pulp
    • D21H23/06—Controlling the addition
    • D21H23/14—Controlling the addition by selecting point of addition or time of contact between components

Definitions

  • the present invention relates to a process for producing pape by adding to an aqueous fiber suspension, which possibly con ⁇ tains a filler, auxiliary agents to improve retention and/or .* dewatering, the auxiliaries being a cationic long-chain poly ⁇ acrylamide and an aluminum salt, and by dewatering the fiber suspension during the sheet-forming stage.
  • the invention thus relates to improving retention and dewater ⁇ ing in connection with the production of paper.
  • retention agents dispersed or emulsified substances present i the pulp, such as fillers, resin dispersions, fines, etc., are flocculated, whereby they are caused to adhere to the paper web.
  • the agents used for improving retention also improve dewatering in the wire section of the paper-making machine.
  • High dewatering and high retention are indeed often achieved simultaneously.
  • Dewatering can further be divided into free dewatering and dewatering produced by means of reduced pres ⁇ sure. These may be contradictory, and therefore a precise bal ⁇ ance is required between these properties.
  • the aim in selecting the retention agent is to obtain a maximally dry paper web bot after the wire section and after the press section.
  • the object of the present invention is to provide a paper production process wherein paper or board is made from an aqueous suspension containing cellulose fiber and possibly an inorganic filler by using a chemical combination and batching method which improve retention and dewatering.
  • the other objects are a clean machine and good compressibility. Furthermore, the quality properties of the paper must be good.
  • the invention is based on the fact that by using a long-chain polyacrylamide and an aluminum salt, a synergistic effect is achieved by adding to an aqueous fiber suspension, which pos ⁇ sibly contains a filler, first a cationic long-chain polyacryl ⁇ amide and then, directly before sheet formation, a polyaluminum salt or a combination which comprises an aluminum salt and a base or an acid which form in situ aluminum hydroxide particles having anionic surface charges, in which case the pH before sheet formation should be within the range 7-9 in order to produce the anionic surface charges of the aluminum hydroxide.
  • the present invention provides a number of advantages over the commercial systems and inventions mentioned above.
  • the process is not tied to polysaccharides, for example starch, which need to be used in large amounts. Therefore there is the danger that, when passin into the cycled waters, they cause problems, since they in ⁇ crease the consumption of oxygen in the water and load the waste water treatment plant. Furthermore, they deteriorate dewatering in certain conditions.
  • Polysaccharides often also contain anionic substituents, even though they are cationized. For this reason there may arise interaction with many differen pulp components. At the same time the pH dependency also in ⁇ creases.
  • the known system based on a colloidal silica sol is in general very expensive compared with the system according to the inven tion.
  • the known system made up of a polymer and bentonite involves certain disadvantages. It has been noted that bentonite in ⁇ creases the linting and porosity of paper. Its handling re ⁇ quires precise and rather expensive equipment. Controlling the constancy, i.e. the formation, of paper with such a system is problematic, and variations in basis weight may be great. According to the invention, it is also possible to add to the fiber suspension cationic auxiliary chemicals, which may also be polymeric, before the adding of the cationic polyacrylamide.
  • the cationic long-chain p ⁇ lyacryl- amide is first added to the stock, which is thereafter sub ⁇ jected to shear forces.
  • the aluminum salt is added according to the invention after the shearing stage.
  • the cationic long-chain polyacrylamide in amounts which are much larger than when batching the retention agents in the conventional manner, just before web forming. Overdosage leads in the latter case even to a situation in which retention is no longer improved or to a situation in which strong flocculation deteriorates paper for ⁇ mation.
  • the amount depends, for example, on the filler content of the pulp and on the cationic matter con ⁇ tained in the pulp.
  • the amount of long-chain polyacrylamide is preferably about 0.01-0.2 % of the dry weight of the pulp. Normally the amount is over 0.02 %.
  • the cationic auxiliary chemical added to the fiber suspension before the cationic polyacrylamide may be, for example, a dry- strength agent, such as a cationic or amphoteric starch or gua gum or a cationic or amphoteric short-chain polyacrylamide. It may also be a wet-strength agent, such as a polyamidamine- epichlorohydrine resin or polyamine-epichlorohydrine resin. It may also consist of cationic substances, so-called fixer chemi ⁇ cals, which neutralize and/or bind anionic interfering sub ⁇ stances, such as polyethylene-imines, quaternary polyamines or alum, or polyaluminum chloride.
  • a dry- strength agent such as a cationic or amphoteric starch or gua gum or a cationic or amphoteric short-chain polyacrylamide. It may also be a wet-strength agent, such as a polyamidamine-
  • cationic chemicals enhance the action of the cationic long-chain polyacrylamide, since they reduce the anionic quali ⁇ ty of the pulp suspension and prevent interfering substances from consuming the cationic long-chain polyacrylamide intended for the flocculation of the fiber suspension.
  • the said cationic chemicals ensure that the shearing of the floes in, for example, the pressure sieve or the feeding pump will result in stable microflocs in the headbox, since they contain a suf ⁇ ficient amount of cationic polyacrylamide and the surface charge of the microflocs is sufficiently cationic in order that they react with aluminum hydroxide particles having anionic charges.
  • the amount of these cationic chemicals is preferably approx. 0.01 - 1 % of the dry weight of the pulp.
  • Examples of the cationic long-chain polyacrylamides used in the invention include the following. Especially advantageous are the copolymers of acrylamide and one or two cationic un- saturated monomers. Suitable cationic monomers include dialkyl- amino(met)acrylates or -(met)acrylamides, in the form of acid salts or quaternary ammonium salts. The alkyl groups may each contain 1-4 carbon atoms, and the amino alkyl group may contain 1-8 carbon atoms. Dialkylaminoethyl(met)acrylates, dialkyl- aminomethyl(met)acrylamides and N,N-dialkylamino-propyl(met)- acrylamides and their quaternary salts are preferred monomers.
  • Suitable cationic monomers include diallyldialkylammoniu chlorides.
  • the polymer may be either linear or cross-linked or partly cross-linked.
  • cationic polyacrylamides also include the homopolymers of cationic acrylic monomers and the mixed polymers of two or more cationic monomers, at least one of the monomers being acrylic-based.
  • a base is added to form aluminum hydroxide having anionic surface charges.
  • the base used may be, for example, sodium or potassium hydroxide, sodium or potassium carbonate, sodium or potassium metasilicate, sodium or potassium waterglasses, sodium or potassium phosphate or borate, or sodium or potassium alumi- nate, or mixtures of these.
  • Aluminate compounds such as sodium aluminate or potassium alum- inate can also be used as the water-soluble aluminum salts.
  • acid is added in order to form, within the pH range 7-9, an aluminum hydroxide having anionic surface charges.
  • the acid used may be mineral acids such as sulfuric acid, hydro ⁇ chloric acid, nitric acid or phosphoric acid, or organic acids such as oxalic acid, citric acid or tartaric acid.
  • the acid used may also be acid aluminum salts such as aluminum sulfate, aluminum chloride, aluminum nitrate, or various water-soluble aluminum hydrophosphates.
  • polyaluminu salts so-called basic aluminum salts, which are also called polyaluminu hydroxy salts or aluminum hydroxy salts.
  • basic aluminum salts which are also called polyaluminu hydroxy salts or aluminum hydroxy salts.
  • polyaluminum salts for example poly aluminum sulfate, polyaluminum chloride and polyaluminum chlor ide sulfate.
  • the polyaluminum salt may, in addition t ⁇ the chloride and/or sulfate ion, also contain other anions, e.g. phosphate, polyphosphate, silicate, citrate, oxalate, or several of these.
  • polymeric aluminum salts of this type include PAC (polyaluminum chloride), PAS (polyaluminum sul ⁇ fate), UPAX 6 (silicate-containing polyaluminum chloride), and PASS (polyaluminum sulfate silicate).
  • the net formula of the water-soluble polyaluminum salt may be, for example
  • alkalinity may vary so that the m-value ranges from 1 to 5 (alkalinity is respectively 16 - 83 % according to the formula (m:6) x 100).
  • the ratio Al/OH is 2:1 - 1:2.5.
  • n is 2 or higher.
  • the said base or acid which forms in situ an aluminum hydroxid with the aluminum salt may be added to the fiber suspension, for example before the adding of the cationic long-chain poly ⁇ acrylamide, or just before the aluminum salt, or after it, or simultaneously with it.
  • the aluminum hydroxide may also be formed before the moment of adding, for example in the adding tube, or in advance in sol form.
  • the amount of the aluminum salt, calculated as AI2O3, is pref ⁇ erably approx. 0.01-1.0 % of the dry weight of the pulp.
  • the paper pulp used may be bleached or unbleached sulfate or sulfite pulp, semichemical pulp, refiner mechanical pulp, groundwood pulp, or mixtures of these. If a filler is present, it is preferably ground or precipitated calcium carbonate, but also other fillers such as kaolin, talc or titanium oxide are possible.
  • the pH is approx. 8-8.5, normally approx. 8 when a polyaluminum salt + CaC ⁇ 3 or alum + a base are used (the Al:OH ratio being appro . 4.5).
  • Pulp was added as in I, but a base had been added to it for controlling the Al/OH molar ratio approx. 30 min before the pulp was placed in the tester. After the polymer addition, the rotation speed was increased to 1500 rpm for a period of 20 s, whereafter it was returned to 1000 rpm, and alum A1 2 (S0 4 ) 3 x I4H2O was added. After 5 s, a filtration was performed as in System I.
  • the polyacrylamides A and B in the examples are copolymers of acrylamide and methyl-chloride quaternized dimethylaminoethyl acrylate. Their charge densities and molecular weights are (A) 1 mequiv./g:7"10 and (B) 1.5 mequiv./g:6 «10 .
  • This example shows that the process according to the invention improves retention in a paper pulp which contains a cationic pulp starch.
  • the pulp composition is in other respects similar to that in the previous example.
  • the test series was performed in a Britt Dynamic Drainage Jar.
  • the batching methods comply with the methods described in Example 1.
  • the degree of sub ⁇ stitution of the cationic starch was 0.035.
  • the starch was added 15 min before the polyacrylamide, and the NaOH for pre ⁇ liminary alkalization 5 min before the polyacrylamide.
  • the same polyacrylamides A and B were used as in Example 1.
  • the aluminum salt used was aluminum sulfate or a poly ⁇ aluminum chloride product.
  • the chemical formula of polyaluminum chloride (PAC) is Al n (OH) ra Cl ( 3 n _ m - ) . It is made up of a number of aluminum nuclei. The pulp was similar to that in the pre ⁇ vious examples.
  • the polyaluminum chloride was batched in a man- ner similar to that of aluminum sulfate. The difference was that the pre-alkalization was omitted.
  • the ratio 0H:A1 in the following table indicates, in addition to the degree of pre- alkalization, also the alkalinity of the polyaluminum product.
  • the polyacrylamide used was the same polyacrylamide A as in Example 1.
  • the batching methods were as in Example 1.
  • polyacrylamide can be enhanced by batching before it another polymer for binding interfering substances.
  • a short-chain cationic polymer QPOL
  • QPOL short-chain cationic polymer
  • the product concerned had a par ⁇ ticularly high charge density. It was added 10 min before the polyacrylamide, by stirring slowly.
  • the polyacrylamide was the same as in Example 2.
  • the batching methods were as in Example 1.
  • the process according to the invention works also when poly ⁇ aluminum chloride (PAC) is used as the fixing agent before the polyacrylamide.
  • PAC poly ⁇ aluminum chloride
  • the. test conditions are similar to those in Example 4, except that, instead of a quaternary poly ⁇ mer (QPOL) , the polyaluminum chloride product used in Example 3 was batched.
  • the batching method was according to Example 3.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Paper (AREA)
  • Making Paper Articles (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)
  • Electronic Switches (AREA)
  • Vending Machines For Individual Products (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)
  • Polishing Bodies And Polishing Tools (AREA)

Abstract

The invention relates to a process for the production of paper by adding to an aqueous fiber suspension, which possibly contains a filler, auxiliary agents for improving retention and/or dewatering, the auxiliary agents being a cationic long-chain polyacrylamide and an aluminum salt, and by dewatering the obtained fiber suspension during the sheet-forming stage. According to the invention, the said aqueous fiber suspension, possibly containing a filler, to which the cationic long-chain polyacrylamide has first been added, is subjected to shearing forces, whereafter there is added to it, directly before sheet forming, a polymeric aluminum salt or an aluminum salt, in which case a base or an acid is added, when necessary, to the said fiber suspension so that the pH be within the range 7-9 before the sheet forming, in which case aluminum hydroxy particles having anionic surface charges will be formed in situ.

Description

Process for producing paper
The present invention relates to a process for producing pape by adding to an aqueous fiber suspension, which possibly con¬ tains a filler, auxiliary agents to improve retention and/or .* dewatering, the auxiliaries being a cationic long-chain poly¬ acrylamide and an aluminum salt, and by dewatering the fiber suspension during the sheet-forming stage.
The invention thus relates to improving retention and dewater¬ ing in connection with the production of paper. By means of retention agents, dispersed or emulsified substances present i the pulp, such as fillers, resin dispersions, fines, etc., are flocculated, whereby they are caused to adhere to the paper web. Owing to the high water content of the pulp it is impor¬ tant that the agents used for improving retention also improve dewatering in the wire section of the paper-making machine. High dewatering and high retention are indeed often achieved simultaneously. Dewatering can further be divided into free dewatering and dewatering produced by means of reduced pres¬ sure. These may be contradictory, and therefore a precise bal¬ ance is required between these properties. Since the dewaterin of the paper web is most expensive in the drying section of th paper-making machine, maximal dewatering at as early a stage o the process as possible is advantageous. The aim in selecting the retention agent is to obtain a maximally dry paper web bot after the wire section and after the press section.
It is known that many advantages can be gained by combining, i a suitable manner, polymeric organic and inorganic components when forming a paper web. Advantage is taken of this commer¬ cially by combining a cationic starch and a silica sol in a system called Compozil. According to the Hydrocol combination, a cationic polymer and an anionic swelling bentonite are added to the pulp. In patent application SE-8700058-4, a cationic long-chain polysaccharide, mainly starch, is first added to an alkalized pulp and then an aluminum source, whereupon polymeric aluminum compounds are formed. It is stated that a synergistic effect is produced in this manner.
In patent application SE-8501652-5 it is claimed that, by adding to the pulp first a cationic polyacrylamide instead of a cationic starch or guar gum and subsequently an anionic silica sol, a clearly improved synergistic effect is achieved, espe¬ cially in a pulp which contains large amounts of interfering substances.
The object of the present invention is to provide a paper production process wherein paper or board is made from an aqueous suspension containing cellulose fiber and possibly an inorganic filler by using a chemical combination and batching method which improve retention and dewatering.
It is also an object of the invention to provide economical and well-controlled web formation by the process according to the invention, in particular in a neutral and alkaline paper pro¬ duction process. The other objects are a clean machine and good compressibility. Furthermore, the quality properties of the paper must be good.
These objects have been achieved by the process according to the invention, the principal characteristics of which are given in the accompanying patent claims.
The invention is based on the fact that by using a long-chain polyacrylamide and an aluminum salt, a synergistic effect is achieved by adding to an aqueous fiber suspension, which pos¬ sibly contains a filler, first a cationic long-chain polyacryl¬ amide and then, directly before sheet formation, a polyaluminum salt or a combination which comprises an aluminum salt and a base or an acid which form in situ aluminum hydroxide particles having anionic surface charges, in which case the pH before sheet formation should be within the range 7-9 in order to produce the anionic surface charges of the aluminum hydroxide.
According to the invention, it has been observed that* a syner¬ gistic effect is produced by a suitable dosage.
The present invention provides a number of advantages over the commercial systems and inventions mentioned above. By using a long-chain cationic polyacrylamide, the process is not tied to polysaccharides, for example starch, which need to be used in large amounts. Therefore there is the danger that, when passin into the cycled waters, they cause problems, since they in¬ crease the consumption of oxygen in the water and load the waste water treatment plant. Furthermore, they deteriorate dewatering in certain conditions. Polysaccharides often also contain anionic substituents, even though they are cationized. For this reason there may arise interaction with many differen pulp components. At the same time the pH dependency also in¬ creases. Also, it is not possible to control sufficiently well the constancy of the quality of the polysaccharides, since the are derived from vegetable raw materials. In a cationic poly¬ acrylamide, it is possible to produce, within very wide limits the desired chain length and charge density.
The known system based on a colloidal silica sol is in general very expensive compared with the system according to the inven tion.
The known system made up of a polymer and bentonite involves certain disadvantages. It has been noted that bentonite in¬ creases the linting and porosity of paper. Its handling re¬ quires precise and rather expensive equipment. Controlling the constancy, i.e. the formation, of paper with such a system is problematic, and variations in basis weight may be great. According to the invention, it is also possible to add to the fiber suspension cationic auxiliary chemicals, which may also be polymeric, before the adding of the cationic polyacrylamide.
According to the invention, the cationic long-chain pσlyacryl- amide is first added to the stock, which is thereafter sub¬ jected to shear forces. The aluminum salt is added according to the invention after the shearing stage.
According to the invention, very good retention and dewatering are achieved without the formation suffering to the same extent as when conventional retention agents are used. This is due to the fact that the cationic floes formed by the cationic long- chain polyacrylamide are comminuted by shearing forces into "microfIocs", which are then, before web-forming, bound to¬ gether with the help of aluminum hydroxide particles which have anionic surface charges. Although these bonds will open in the headbox, they are largely re-formed on the wire, whereupon the "microfIocs" of the web provide good formation, and the small even-sized pores of the web, which are not clogged owing to the good retention of fines, provide good dewatering, especially in the press section and the drying section, and often also im¬ proved dewatering at the suction boxes of the wire.
In the invention it is possible to use the cationic long-chain polyacrylamide in amounts which are much larger than when batching the retention agents in the conventional manner, just before web forming. Overdosage leads in the latter case even to a situation in which retention is no longer improved or to a situation in which strong flocculation deteriorates paper for¬ mation. According to the invention it is possible to use a 1- to 10-fold excess of cationic long-chain polyacrylamide as compared with normal use. The amount depends, for example, on the filler content of the pulp and on the cationic matter con¬ tained in the pulp. The amount of long-chain polyacrylamide is preferably about 0.01-0.2 % of the dry weight of the pulp. Normally the amount is over 0.02 %.
The cationic auxiliary chemical added to the fiber suspension before the cationic polyacrylamide may be, for example, a dry- strength agent, such as a cationic or amphoteric starch or gua gum or a cationic or amphoteric short-chain polyacrylamide. It may also be a wet-strength agent, such as a polyamidamine- epichlorohydrine resin or polyamine-epichlorohydrine resin. It may also consist of cationic substances, so-called fixer chemi¬ cals, which neutralize and/or bind anionic interfering sub¬ stances, such as polyethylene-imines, quaternary polyamines or alum, or polyaluminum chloride.
These cationic chemicals enhance the action of the cationic long-chain polyacrylamide, since they reduce the anionic quali¬ ty of the pulp suspension and prevent interfering substances from consuming the cationic long-chain polyacrylamide intended for the flocculation of the fiber suspension. Thus the said cationic chemicals ensure that the shearing of the floes in, for example, the pressure sieve or the feeding pump will result in stable microflocs in the headbox, since they contain a suf¬ ficient amount of cationic polyacrylamide and the surface charge of the microflocs is sufficiently cationic in order that they react with aluminum hydroxide particles having anionic charges.
The amount of these cationic chemicals is preferably approx. 0.01 - 1 % of the dry weight of the pulp.
Examples of the cationic long-chain polyacrylamides used in the invention include the following. Especially advantageous are the copolymers of acrylamide and one or two cationic un- saturated monomers. Suitable cationic monomers include dialkyl- amino(met)acrylates or -(met)acrylamides, in the form of acid salts or quaternary ammonium salts. The alkyl groups may each contain 1-4 carbon atoms, and the amino alkyl group may contain 1-8 carbon atoms. Dialkylaminoethyl(met)acrylates, dialkyl- aminomethyl(met)acrylamides and N,N-dialkylamino-propyl(met)- acrylamides and their quaternary salts are preferred monomers. Other suitable cationic monomers include diallyldialkylammoniu chlorides. The polymer may be either linear or cross-linked or partly cross-linked. In this context, cationic polyacrylamides also include the homopolymers of cationic acrylic monomers and the mixed polymers of two or more cationic monomers, at least one of the monomers being acrylic-based.
The aluminum salts used in the invention are water-soluble, and they may be aluminum sulfate, aluminum chloride, aluminum nitrate, or acid aluminum hydrophosphates in which P:A1 = 1.1:1 - 3:1.
When these aluminum salts or their mixtures are used, a base is added to form aluminum hydroxide having anionic surface charges. The base used may be, for example, sodium or potassium hydroxide, sodium or potassium carbonate, sodium or potassium metasilicate, sodium or potassium waterglasses, sodium or potassium phosphate or borate, or sodium or potassium alumi- nate, or mixtures of these.
Aluminate compounds such as sodium aluminate or potassium alum- inate can also be used as the water-soluble aluminum salts. In this case, acid is added in order to form, within the pH range 7-9, an aluminum hydroxide having anionic surface charges. The acid used may be mineral acids such as sulfuric acid, hydro¬ chloric acid, nitric acid or phosphoric acid, or organic acids such as oxalic acid, citric acid or tartaric acid. The acid used may also be acid aluminum salts such as aluminum sulfate, aluminum chloride, aluminum nitrate, or various water-soluble aluminum hydrophosphates.
According to the invention it is also possible to use water- soluble polymeric aluminum salts, i.e. polyaluminu salts, so- called basic aluminum salts, which are also called polyaluminu hydroxy salts or aluminum hydroxy salts. According to the in¬ vention it is possible to use as these salts, for example poly aluminum sulfate, polyaluminum chloride and polyaluminum chlor ide sulfate. The polyaluminum salt may, in addition tσ the chloride and/or sulfate ion, also contain other anions, e.g. phosphate, polyphosphate, silicate, citrate, oxalate, or several of these.
Commercially available polymeric aluminum salts of this type include PAC (polyaluminum chloride), PAS (polyaluminum sul¬ fate), UPAX 6 (silicate-containing polyaluminum chloride), and PASS (polyaluminum sulfate silicate).
The net formula of the water-soluble polyaluminum salt may be, for example
n[Al2(OH)m/Cl)6_m3
and its alkalinity may vary so that the m-value ranges from 1 to 5 (alkalinity is respectively 16 - 83 % according to the formula (m:6) x 100). In this case the ratio Al/OH is 2:1 - 1:2.5. n is 2 or higher.
When a polyaluminum compound is used, it is also possible to add a base in order to optimize the Al/OH ratio, even if all o the polyaluminum compounds in accordance with the invention do work as such.
The said base or acid which forms in situ an aluminum hydroxid with the aluminum salt may be added to the fiber suspension, for example before the adding of the cationic long-chain poly¬ acrylamide, or just before the aluminum salt, or after it, or simultaneously with it.
The aluminum hydroxide may also be formed before the moment of adding, for example in the adding tube, or in advance in sol form.
The amount of the aluminum salt, calculated as AI2O3, is pref¬ erably approx. 0.01-1.0 % of the dry weight of the pulp.
The paper pulp used may be bleached or unbleached sulfate or sulfite pulp, semichemical pulp, refiner mechanical pulp, groundwood pulp, or mixtures of these. If a filler is present, it is preferably ground or precipitated calcium carbonate, but also other fillers such as kaolin, talc or titanium oxide are possible.
The invention is described below in greater detail with the help of examples.
In the tests described, the pH is approx. 8-8.5, normally approx. 8 when a polyaluminum salt + CaCθ3 or alum + a base are used (the Al:OH ratio being appro . 4.5).
Example 1
Using a Britt Dynamic Jar as the tester, tests were carried out on a neutral pulp which was made up of bleached birch pulp and bleached pine pulp at a ratio of 60:40. The pulp components had been ground to SR values of 20 and 25. The filler was calcium carbonate, DX-40, 20 % of the dry weight of the pulp. The pH of the pulp was approx. 8. In the tester the pulp was of a typical headbox consistency, i.e. approx. 0.8 %. After the adding of the retention agent, the pulp was filtered for 30 s, and the ash content was determined.
Tests were performed in this example by using the following systems:
System (I) :
500 ml of a dilute pulp was placed in the tester, at 1000 rpm. After 10 s, polyacrylamide A was added for 5 s. After 10 s, 100 ml of filtrate was filtered for approx. 30 min.
System (II) :
Pulp was added as in I, but a base had been added to it for controlling the Al/OH molar ratio approx. 30 min before the pulp was placed in the tester. After the polymer addition, the rotation speed was increased to 1500 rpm for a period of 20 s, whereafter it was returned to 1000 rpm, and alum A12(S04)3 x I4H2O was added. After 5 s, a filtration was performed as in System I.
System (III):
As System II, but without the addition of a base.
System (IV):
As System II, but without the additions of a base and alum.
System (V) :
Was performed in accordance with System II, but without the addition of a base. Instead of the polyacrylamide, a cationic starch, Raisamyl 135, having a degree of substitution of 0.035, was added and was mixed in the same manner as the polymer in System II. Silica sol BMA (Eka Nobel) was used instead of alum.
System (VI):
Was performed as System II, but without the addition of a base to the pulp. Alkali-treated bentonite was added instead of alu (Hydrocol method) .
The polyacrylamides A and B in the examples are copolymers of acrylamide and methyl-chloride quaternized dimethylaminoethyl acrylate. Their charge densities and molecular weights are (A) 1 mequiv./g:7"10 and (B) 1.5 mequiv./g:6«10 .
Systems I-VI are compared in Table 1. 10
3 49
1:3 63
1:4.5 61
10 1:3 68
10 1:4.5 81
10 1:6 58
5 1:0 56 10 1:0 64 10 1:3 70
10 1:4.5 83
10 1:6 64
10 1:0 66
58
52
48
59
50
57
This example shows that the process according to the invention improves retention in a paper pulp which contains a cationic pulp starch. The pulp composition is in other respects similar to that in the previous example. The test series was performed in a Britt Dynamic Drainage Jar. The batching methods comply with the methods described in Example 1. The degree of sub¬ stitution of the cationic starch was 0.035. The starch was added 15 min before the polyacrylamide, and the NaOH for pre¬ liminary alkalization 5 min before the polyacrylamide. In this example, the same polyacrylamides A and B were used as in Example 1.
Example 3
Further retention tests were performed as in the above ex¬ amples. The aluminum salt used was aluminum sulfate or a poly¬ aluminum chloride product. The chemical formula of polyaluminum chloride (PAC) is Aln(OH)raCl(3n_m-) . It is made up of a number of aluminum nuclei. The pulp was similar to that in the pre¬ vious examples. The polyaluminum chloride was batched in a man- ner similar to that of aluminum sulfate. The difference was that the pre-alkalization was omitted. The ratio 0H:A1 in the following table indicates, in addition to the degree of pre- alkalization, also the alkalinity of the polyaluminum product.
The polyacrylamide used was the same polyacrylamide A as in Example 1. The batching methods were as in Example 1.
Test Polymer/ Aluminum source 0H:A1 Ash re- Batching
No. batch 1:A1 sulfate tention method kg/t 2:PAC % kg/t
This example shows that the action of polyacrylamide can be enhanced by batching before it another polymer for binding interfering substances. In this case a short-chain cationic polymer (QPOL) was added as a so-called fixing agent before th long-chain polyacrylamide. The product concerned had a par¬ ticularly high charge density. It was added 10 min before the polyacrylamide, by stirring slowly. The polyacrylamide was the same as in Example 2. The batching methods were as in Example 1.
Example 5
The process according to the invention works also when poly¬ aluminum chloride (PAC) is used as the fixing agent before the polyacrylamide. In this case the. test conditions are similar to those in Example 4, except that, instead of a quaternary poly¬ mer (QPOL) , the polyaluminum chloride product used in Example 3 was batched. The batching method was according to Example 3.
Test Polymer/ Aluminum OH.-A1 PAC Ash re- Batching No. batch sulfate kg/t tention method kg/t kg/t
1/1.0 10 4.5 52 II (accord¬ ing to invention)
1/1.0 10 4.5 2.5 63 II (accord¬ ing to invention)
Example 6
By the process according to the invention, good dewatering properties are achieved with wood-free fine-paper pulp. The pulps and batching methods were in accordance with Example 1. The dewatering rate was measured by means of a cylindrical tube. At the other end of the tube there was a wire through which the dewatering took place. Before filtration, this tube was used for adding the chemicals to the pulp in the manner described in the previous example, by using a Britt Jar Tester, Thereafter the pulp was poured into a dewatering cylinder and was filtered. The removed filtrate was measured as a function of the time. The pulp was of a type similar to that in the previous examples. In the filtrations, 500 ml of pulp per test ing point was used.
Batching Dewater- method ing time • s/250 m
aa)C+A+l (1)10 4.5
bb)D+A/l+l (2)10 4.5
7 A/1.0 (2)5.1 2
8 D+A/l+1 (2)5.1 2
9 C/10
10 E/1.0
a) silica sol, a commercial product b) alkali-treated bentonite, a commercial product aa) starch added 10 min before the polyacrylamide bb) quaternary polymer added 10 min before the polyacrylamide Polymer A: Polyacrylamide A, see Example 1
C: Cationic potato starch D.S. 0.035
D: Quaternary polyamine
B: Hydrocol 862 Example 7
It is shown that the process according to the invention works also when certain other aluminum salts are used. In this example, polyaluminum salts were used which contained-silica groups in addition to chloride, or sulfate instead of chloride. The fiber composition in the pulp was similar to that in Example 2. The calcium carbonate concentration was 30 %. A cationic polyacrylamide was added to the pulp in a Britt Jar
Tester, and it was mixed for 20 s at 1500 min . Thereafte ;rr ithe aluminum salt was added and was mixed for 10 s at 1000 min-1 In the filtering stage the rotation speed was 750 rpm. The ash retention was calculated on the basis of the ash contents of the pulp and the filtrate. The molecular weight of the cationic polyacrylamide was approx. 7 million g/mol and its charge density 1 mequiv./g. Compound A is a silicate-containing poly¬ aluminum chloride and B is polyaluminum sulfate.
Test Polymer/ Aluminum Compound Ash retention No. batch salt % g/t kg/t

Claims

Claims
1. A process for producing paper by adding to an aqueous fiber suspension, which possibly contains a filler, auxiliary agents for improving retention and/or dewatering, the auxiliar agents being a cationic long-chain polyacrylamide and -an alum¬ inum salt, and by dewatering the obtained fiber suspension during the sheet-forming stage, characterized in that the said aqueous fiber suspension, possibly containing a filler, to which there has first been added a cationic long-chain poly¬ acrylamide, is subjected to shearing forces, whereafter there is added to it, directly before sheet forming, a polymeric aluminum salt or an aluminum salt, in which case a base or an acid is added, when necessary, to the said fiber suspension in order that the pH be within the range 7-9 before sheet forma¬ tion, whereupon aluminum hydroxy particles having anionic surface charges will be formed in situ.
2. A process according to Claim 1, characterized in that the said fiber suspension may additionally contain one or sev¬ eral cationic auxiliary agents, which may be dry-strength agents, such as cationic starch, wet-strength agents, such as polyamidamine-epichlorohydrine resin, and/or agents, such as polyethylene imine or quaternary polyamines or alum, which neutralize and/or bind interfering substances.
3. A process according to Claim 2, characterized in that the said cationic additive or the said cationic additives are added to the said fiber suspension before the adding of the cationic long-chain polyacrylamide.
4. A process according to any of the above claims, charac¬ terized in that the aluminum salt used is aluminum sulfate, aluminum chloride or aluminum nitrate, in which case a base is added to the fiber suspension in order to form in situ an aluminum hydroxide having anionic surface charges.
5. A process according to Claim 4, characterized in that the base is added in such an amount that the Al/OH molar ratio will be within a range of approx. 1:2-1:5, preferably approx. 1:3.
6. A process according to any of the above claims, charac¬ terized in that the polymeric aluminum salt used is a water- soluble polyaluminum hydroxy complex with sulfate and/or chloride.
7. A process according to any of the above claims, charac¬ terized in that the polymeric aluminum salt used is a water- soluble aluminum hydroxy complex with sulfate and/or chloride, which complex contains in addition to a sulfate and/or chloride anion also other anions, such as phosphate, silicate, oxalate or citrate.
8. A process according to any of the above claims, charac¬ terized in that to the fiber suspension there is added the said cationic long-chain polyacrylamide in an amount of approx. 0.01-0.2 % of the dry weight of the pulp.
9. A process according to any of the above claims, charac¬ terized in that to the fiber suspension there is added the said polymeric aluminum salt or the said aluminum salt, calculated as AI2O3, in an amount of approx. 0.01-1.0 % of the dry weight of the pulp.
EP93902274A 1992-01-20 1993-01-20 Process for producing paper Expired - Lifetime EP0700473B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FI920246 1992-01-20
FI920246A FI920246A0 (en) 1992-01-20 1992-01-20 FOERFARANDE FOER TILLVERKNING AV PAPPER.
PCT/FI1993/000019 WO1993014263A1 (en) 1992-01-20 1993-01-20 Process for producing paper

Publications (3)

Publication Number Publication Date
EP0700473A1 true EP0700473A1 (en) 1996-03-13
EP0700473B1 EP0700473B1 (en) 2000-04-05
EP0700473B2 EP0700473B2 (en) 2003-01-22

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ID=8534094

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JP (1) JP3138475B2 (en)
AT (1) ATE191524T1 (en)
AU (1) AU660066B2 (en)
CA (1) CA2127992A1 (en)
DE (1) DE69328311T3 (en)
ES (1) ES2146609T5 (en)
FI (2) FI920246A0 (en)
PT (1) PT700473E (en)
WO (1) WO1993014263A1 (en)

Cited By (3)

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WO2008076071A1 (en) 2006-12-21 2008-06-26 Akzo Nobel N.V. Process for the production of cellulosic product
US10458067B2 (en) 2017-01-31 2019-10-29 Kimberly-Clark Worldwide, Inc. High bulk tissue comprising cross-linked fibers
US11970819B2 (en) 2020-01-30 2024-04-30 Kimberly-Clark Worldwide, Inc. Tissue products comprising crosslinked fibers

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US5707494A (en) * 1994-03-14 1998-01-13 E. I. Du Pont De Nemours And Company Process for preparing water soluble polyaluminosilicates
JP2000352386A (en) 1999-06-08 2000-12-19 Mitsubishi Heavy Ind Ltd Scroll compressor
DE102004063005A1 (en) 2004-12-22 2006-07-13 Basf Ag Process for the production of paper, cardboard and cardboard
JP4626374B2 (en) * 2005-04-20 2011-02-09 栗田工業株式会社 Papermaking method and papermaking additive

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JPS5512868A (en) † 1978-07-12 1980-01-29 Mitsubishi Paper Mills Ltd Production of neutral paper
JPH0611956B2 (en) † 1985-11-21 1994-02-16 星光化学工業株式会社 How to improve the yield of fillers
GB8602121D0 (en) * 1986-01-29 1986-03-05 Allied Colloids Ltd Paper & paper board
SE8701252D0 (en) † 1987-03-03 1987-03-25 Eka Nobel Ab SET FOR PAPER MAKING
US4927498A (en) † 1988-01-13 1990-05-22 E. I. Du Pont De Nemours And Company Retention and drainage aid for papermaking
SE8903752D0 (en) * 1989-11-09 1989-11-09 Eka Nobel Ab PROCEDURES FOR PREPARING PAPER

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008076071A1 (en) 2006-12-21 2008-06-26 Akzo Nobel N.V. Process for the production of cellulosic product
US10458067B2 (en) 2017-01-31 2019-10-29 Kimberly-Clark Worldwide, Inc. High bulk tissue comprising cross-linked fibers
US11970819B2 (en) 2020-01-30 2024-04-30 Kimberly-Clark Worldwide, Inc. Tissue products comprising crosslinked fibers

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FI920246A0 (en) 1992-01-20
FI943425A0 (en) 1994-07-19
CA2127992A1 (en) 1993-07-22
ES2146609T3 (en) 2000-08-16
EP0700473B2 (en) 2003-01-22
FI943425A (en) 1994-07-19
WO1993014263A1 (en) 1993-07-22
DE69328311T2 (en) 2000-08-10
JP3138475B2 (en) 2001-02-26
EP0700473B1 (en) 2000-04-05
AU660066B2 (en) 1995-06-08
PT700473E (en) 2000-07-31
DE69328311D1 (en) 2000-05-11
ATE191524T1 (en) 2000-04-15
AU3354193A (en) 1993-08-03
JPH07502791A (en) 1995-03-23
DE69328311T3 (en) 2003-07-31
ES2146609T5 (en) 2003-07-01

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