WO2000059965A1 - Bifunctional polymers - Google Patents

Bifunctional polymers Download PDF

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Publication number
WO2000059965A1
WO2000059965A1 PCT/IB1999/002101 IB9902101W WO0059965A1 WO 2000059965 A1 WO2000059965 A1 WO 2000059965A1 IB 9902101 W IB9902101 W IB 9902101W WO 0059965 A1 WO0059965 A1 WO 0059965A1
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WO
WIPO (PCT)
Prior art keywords
composition
paper
substituent
substituents
starch
Prior art date
Application number
PCT/IB1999/002101
Other languages
English (en)
French (fr)
Inventor
Donald Kendall Drummond
Patrick Clinton Wernett
Original Assignee
Minerals Technologies Inc.
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
Priority claimed from US09/286,745 external-priority patent/US6287423B1/en
Priority claimed from US09/286,742 external-priority patent/US6090242A/en
Priority to CA002366474A priority Critical patent/CA2366474A1/en
Priority to AU24553/00A priority patent/AU2455300A/en
Priority to JP2000609471A priority patent/JP2002541276A/ja
Priority to AT99967997T priority patent/ATE248867T1/de
Application filed by Minerals Technologies Inc. filed Critical Minerals Technologies Inc.
Priority to BR9917249-6A priority patent/BR9917249A/pt
Priority to EP99967997A priority patent/EP1171492B1/en
Priority to DE69911073T priority patent/DE69911073T2/de
Publication of WO2000059965A1 publication Critical patent/WO2000059965A1/en
Priority to NO20014814A priority patent/NO20014814D0/no
Priority to HK02107083.1A priority patent/HK1045534B/zh

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/18Reinforcing agents

Definitions

  • the present invention relates to novel polymer compositions which contain amide, sulfonate and/or phosphonate groups and method of use, including, but not limited to, paper making methods, particularly as retention or strength aids.
  • filler levels in paper are limited, in part, by paper strength losses as filler levels increase. Minimum strength requirements prohibit the paper maker from adding more filler which is desirable because fillers are generally less expensive than the wood fiber that they replace. The ability to add more filler would allow the paper maker to reduce paper production costs by replacing the more expensive fiber.
  • the paper maker needs fillers, additives or processes which increase paper strength.
  • filler modification wet end additives and fiber modifications to achieve higher strength levels in paper.
  • Filler modifications have included changing filler type, changing filler particle size and surface treatments of fillers.
  • Wet end additives have included synthetic and natural polymers such as polyacrylamides and starches.
  • Fiber modifications have included changing fiber type and fiber processing.
  • An object of the present invention is to provide a polymer having varied substituent groups having varied functions or utilities.
  • One specific objective is to provide a polymer useful for binding mineral fillers, particularly to polysaccharide materials, such as paper pulps and the like.
  • Another object is to provide a polymer useful as a binder in non-paper applications, such as rubbers, sealants, plastics, modifiers, pharmaceuticals etc.
  • the present invention provides novel polymers having phosphonated and sulphonated substituent groups such that the polymer is multifunctional in its use.
  • Optional amide substituents are used to reduce electrostatic charge density or for increasing hydrogen bonding.
  • An advantage of the polymer is the flexibility of using it for multiple purposes. Other advantages will be discerned by those skilled in the art in familiarizing themselves with this specification.
  • One embodiment of the present invention is a polymer composition having a polymeric core, one or more phosphonated substituents effective for bonding with an inorganic material, and one or more sulphonated substituents effective for bonding with a polysaccharide material.
  • the polymeric core comprises one or more polymer units selected from polymerizable monomeric units, such as by condensation or free radical methods, preferably from allylic units, epoxidic units, and vinylic units.
  • the polymeric core can be composed of varying proportions or sequences of substituted or unsubstituted monomeric (or polymeric) units of allylic units, epoxidic units and vinylic units. Not all allylic unit, epoxidic units, or vinylic units need be the same as the other respective allylic units, epoxidic units, or vinylic units, but they can be. Such difference can result from hydrolysis reactions, among others, and whether intended or not.
  • Such allylic, epoxidic and vinylic units can have one or more of the phosphonated or sulphonated substituents attached before or after polymerization.
  • Such units of the core can be repeating in a predictable sequence or repeat randomly.
  • a preferred allylic unit is a polyacrylamide unit.
  • the epoxidic unit can be one derived from a compound with the moiety of
  • a preferred vinylic unit is vinylphosphonate. Any one or more of the hydrogen atoms may be substituted before, during or after polymerization.
  • the proportions of allylic units, epoxidic units, and vinylic units can vary widely, or a polymer can be composed of only one type of unit alone or various combinations thereof. Whether a polymer is made of only allylic units, only epoxidic units, only vinylic units or a combination of these types of units, the units of each type may be the same or different because of substitution.
  • the amount or proportion of the polyacrylamide units or the epoxidic units to the balance of the polymer composition is effective for reducing the electrostatic charge density of the polymer composition or for increasing the hydrogen bonding to the polysaccharide material or, more preferably, both.
  • Polysaccharide materials include cellulose, starch and other similar natural and synthetic glycosidic-linked saccharides.
  • Preferred polysaccharides are cellulose, more preferably wood fiber and bagasse; even more preferably, cellulosic fibers for paper production.
  • the present invention is a polymer composition comprising a various mixture of linking monomeric units, amide or epoxide monomeric units, phosphonated monomeric units and sulphonated monomeric units.
  • the preferred linking monomeric unit can be represented by the formula - CH-CH(R 1 ) -, wherein R ! is hydrogen, a halogen or a lower alkyl.
  • C is carbon; “O” is oxygen; “N” is nitrogen; "A” is an unsubstituted or substituted (C C 6 ) alkylene or a hydrogen, wherein the substituents are independently selected from (C ⁇ C-,) alkyls and halogens, "B” is hydrogen, hydroxyl, or ether; preferably hydrogen.
  • the nitrogen, N can also be a quaternary nitrogen, including, but not limited to, combinations of the groups above; and "R ' and “R 2 " are each independently hydrogen, halogen or a (C 1 -C 3 ) alkyl.
  • A if not hydrogen, is an (C,-C 6 ) alkylene, e.g., methylene, ethylene, propylene, butylene, pentylene or hexylene.
  • alkylenes can have a (C,-C 3 ) alkyl substituent, e.g., methyl, ethyl or propyl.
  • the halogen which can be a substituent on an alkyl or alkylene chain herein is selected from bromine, chlorine and fluorine atoms.
  • the (C ⁇ Cs) alkyls are methyl, ethyl and n- propyl.
  • the preferred epoxide monomeric unit can be represented by the formula -CHR-0-CH 2 , wherein R is hydrogen or lower alkyl or alkylene, e.g. alkylene having one to six carbon atoms.
  • the preferred phosphonated monomeric unit can be represented by the formula
  • P is phosphorus; "O” is oxygen; and "A” is selected from an unsubstituted or substituted (C 0 -C 6 ) alkylene, wherein the substituent is independently selected from (C 1 -C 3 ) alkyls and halogens, or from carbonyl (-CO-), carbonylaminos (-CO-NE-, where "E” hydrogen, hydroxyl, or ether), alkylenecarbonylaminos (e.g. -(CH 2 ) X -CO-NE-, where x is an integer), carbonylaminoalkylenes (e.g.
  • alkylenecarbonylamino-alkylenes e.g. - (CH 2 ) X - CO- NE- (CH 2 ) X -
  • "D" is a hydrogen proton or a salt moiety selected from aluminum, calcium, iron, lithium, magnesium, potassium, sodium, titanium and zinc ions. When in a salt moiety, the substituents are such that results in an electronic balance for the substituent group.
  • the "A” is an (C 0 -C 6 ) alkylene, e.g., nothing, methylene, ethylene, propylene, butylene, pentylene or, hexylene.
  • such preferred alkylenes can have one or more (C,-C 3 ) alkyl substituent(s), e.g.. methyl, ethyl, or propyl.
  • the halogen which can be a substituent on an alkyl chain herein is selected from bromine, chlorine, and fluorine atoms. Such halogens can be substituents on the alkylene chain also.
  • the nitrogen, N can also be a quaternary nitrogen, including, but not limited to, combinations of the groups above.
  • "D” may also represent a pairing of hydrogen and salt moiety, e.g. -(PO 3 ) H +1 Na +1 .
  • the inorganic material is preferably a mineral containing material such as that which can be used for a filler in paper or non-paper products as hereinafter described. Although such is contemplated in the present invention, the invention is not necessarily limited to such inorganic materials.
  • the inorganic material is a filler or other additive for paper compositions.
  • the inorganic material is a filler or other additive for non-paper compositions, such as plastics.
  • a preferred inorganic material is one derived from or made with calcium containing matter, such as some clays or natural calcium carbonate. Another preferred inorganic material is precipitated calcium carbonate.
  • S is sulfur, “O” is oxygen; and "A” is selected from an unsubstituted or substituted (C 0 -C 6 ) alkylene, wherein the substituent is independently selected from (C ⁇ Ca) alkyls and halogens, or from a carbonyl (-CO-), carbonylaminos (-CO-NE-, where "E” hydrogen, hydroxyl, or ether), alkylenecarbonylaminos (e.g. -(CH 2 ) X -CO-NE-, where x is an integer), carbonylaminoalkylenes (e.g. -CO-NE-(CH 2 ) x -), or alkylenecarbonylaminoalkylenes (e.g.
  • the "A” is an (C 0 -C 6 ) alkylene, e.g., nothing, methylene, ethylene, propylene, butylene, pentylene or, hexylene.
  • alkylenes can have a (C r C 3 ) alkyl substituent, e.g., methyl, ethyl, or propyl.
  • the halogen which can be a substituent on an alkyl chain herein is selected from bromine, chlorine, and fluorine atoms. Such halogens can be substituents on the alkylene chain also.
  • E is hydrogen, hydroxyl, or ether; preferably hydrogen.
  • the nitrogen, N can also be a quaternary nitrogen, including, but not limited to, combinations of the groups above.
  • D is sodium
  • - S0 3 - D can be represented as - S0 3 " Na + .
  • - S0 3 - D can be represented as - SO 3 CH 3 .
  • Non-limiting examples of the substituent groups are:
  • the molecular weight of the composition having the above core and substituents ranges from about 100,000 to about 20,000,000.
  • the more preferred molecular weight ranges from about 500,000 to about 5,000,000.
  • the more preferred molecular weight is about 500,000 to about 5,000,000.
  • composition of the present invention can be produced with varying proportions or ratios of the molar units of the phosphonated substituents, the sulfonated substituents, and the optional cationic or neutrally charged amide substituents.
  • the molar unit ratio of phosphonated substituents to sulfonated substituents can range from about 99/1 to about 1/99, but is preferably from about 45/55 to about 1/99, more preferably from about 10/90 to about 1/99.
  • substituents are preferably predominate in proportion to the other substituents, preferably in a ratio of about 1/1 , more preferable about 10/1 or higher relative to the phosphonated substituent.
  • the ratio of the other two substituents to each other can remain as stated hereinabove.
  • a preferred molar unit ratio of (cationic or neutrally charged amide substituents) to (sulphonated substituents) to (phosphonated units) is (from about 70 [preferably about 85] to about 90) molar units of cationic or neutrally charged amide substituents to (from about 0 [preferably about 10] to about 30) molar units of sulphonated substituents to (from about 0 [preferably about 5] to about 10) molar units phosphonated units.
  • molar unit ratios of cationic or neutrally charged amide substituents/sulphonated units/phosphonated units of 85/10/5, 89/10/1 and 90/9/1. Other exact ratios are also preferred when in the stated ranges.
  • the sequencing of the units may vary according to the intended use, there is no general requirement or preference and the invention is not to be limited to any particular sequence illustrated herein. Additionally, the terminal units of the polymer , as well as other units and substituents, can be other than the units or substituents described as long as the presence of such does not interfere with the benefits of the present invention. Similarly, some degree of cross-linking may occur, but preferably is substantially absent.
  • the phosphonated substituent can be described as having the chemical structure of - PO 3 H; the sulphonated substituent as having the chemical structure of -C(O)NHC(CH 3 ) 2 CH 2 SO 3 H; and the cationic or neutrally charged amide substituent as having the chemical structure of -C(O)NH 2 .
  • Such polymer can be synthesized by the polymerization of varying proportions of vinylphosphonic acid monomers; 2 -acrylamido- 2 -methylpropanesulfonic acid monomers; and acrylamide monomers.
  • Table 1 is a non-limiting illustration of the polymers and molecular weights possible. (Molecular weights can be determined by an intrinsic viscosity method, such as one using Mark-Houwink-Sakurada constants.)
  • AMPS 2-acrylamido - 2-methylpropanesulfonic acid monomers
  • VPA vinylphosphonic acid monomers
  • PAM polyacrylamide monomers
  • a non-limiting example of one of the polymers of the present invention can be exemplified by the following polymer segment structure:
  • the phosphonated substituents are effective for bonding with a mineral filler.
  • mineral fillers can be those typically used in paper making applications.
  • Non-limiting examples of such fillers are clays, calcium carbonates (such as ground carbonates or precipitated calcium carbonates), and talcs.
  • the phosphonated substituent(s) used and its(their) effectiveness will vary according to the type of paper making materials (e.g. pulps and/or fillers) and manufacturing conditions (e.g. temperatures, pressures, other chemicals) applied.
  • “Bonding” as used herein may include either or both of an acid-base interaction and ionic bonding to create a useful amount of affixation or affinity between the polymer and the mineral filler for the intended utility. Accordingly, bonding can be, but need not be, indicated by secondary measurements, such as retention or strength measurements in paper applications.
  • the sulphonated substituents are effective for bonding with a polysaccharide material.
  • polysaccharide material can be those typically used in paper making applications, such as starches, fibers, thickening agents and the like.
  • fiber materials are wood, bamboo, bagasse or other cellulosic biomass.
  • Starch examples are cationic or neutral waxy maize, potato, tapioca, converted or chemically modified starch, synthetic starch, and the like.
  • Thickening agents are the carboxymethyl family of thickeners and the like.
  • the present invention is a polymer wherein the phosphonated substituents are effective for bonding with a mineral filler used for non-paper applications, in such application, the mineral filler is used in a composition which also contains material bonding with the sulphonated substituent of the polymer.
  • non-paper applications can include, but are not necessarily limited to, applications involving natural and synthetic rubbers, sealants, plastics, paints (e.g. latex and emulsified), rheology modifiers, pharmaceutical tablets, etc.
  • Such materials can include casted or extruded non-paper materials containing cellular or polymeric or polysaccharide material suitable for effective bonding with the sulphonated substituent, such as fillers useful for bulk or strength purposes.
  • the selection and amount of the optional cationic or neutrally charged amide substituent for reducing the electrostatic charge density and for hydrogen bonding will vary according to the selection of the phosphonated and sulphonated substituents.
  • the present invention is a polymeric composition
  • polymeric composition comprising the novel polymers described hereinabove, which polymeric composition can have wide and varying characteristics relating to average molecular weights, molecular weight distributions, charge density, and type of monomeric units. Depending on the application, these characteristics can be adjusted. For instance, in a desired application the average molecular weight might be 1 ,000,000 with 85% of the polymers having a molecular weight of 1 ,000,000 ⁇ 15%. As a further example, in another application, 85% of the polymers might have a molecular weight of 1 ,000,000 ⁇ 50%.
  • Polymers can be classified as straight polymers and cross-linking polymers. Using known methods of analysis, such as Nuclear Magnetic Resonance Spectrocopy (NMR), the degree of cross-linking polymers (as a weight percent of the total composition) can be ascertained.
  • NMR Nuclear Magnetic Resonance Spectrocopy
  • the polymer composition of the present invention has a low degree of cross-linking and contains less than about 15 weight percent; more preferably, less than about 5 weight percent; and even more preferably, less than about 1 weight percent of cross-linking polymers.
  • the composition of the present invention has in lieu thereof a substituent comprising a derivative of a condensed phosphate, such as of a polyphosphate, pyrophosphate, or polyphospho c acid (e.g. such as pyrophosphoric acid, metaphospho c acid, superphosphoric acid or orthophosphoric acid).
  • a substituent comprising a derivative of a condensed phosphate, such as of a polyphosphate, pyrophosphate, or polyphospho c acid (e.g. such as pyrophosphoric acid, metaphospho c acid, superphosphoric acid or orthophosphoric acid).
  • an embodiment of the present invention is a method for improving the strength in paper comprising the addition of certain polymers compositions of the above polymer to a paper furnish optionally containing fillers.
  • the preferred polymers are copolymers comprising acrylamide monomers and phosphonated monomers or sulphonated monomers or are terpolymers comprising acrylamide monomers, phosphonated monomers and sulphonated monomers.
  • the addition of the polymer composition can be prior to the headbox of a paper machine in either the thick or thin stock. Split or multiple addition points and other strategies can be used. The amount added will vary according to the nature of the papermaking furnish and the intended use of the paper produced, but should be typically in the range of from about one pound to about five pounds of polymer composition per ton of furnish.
  • the polymer of the present invention in admixture with starch provides a synergistic increase in the strength of the paper produced.
  • the synergistic effect is signified by the fact that no amount of either additional polymer or starch, when used alone, can provide an equivalent result to the combination of polymer and starch.
  • the starch useable are those typically useable for papermaking.
  • Such starch can be synthetic, such as ethylated or oxidized forms; or organic, such as potato based, preferably cationic potato starch, or corn based, such as cationic waxy maize.
  • the polymer is preferably added to the thick stock and preferably before the addition of the starch. Split addition of each can be performed. Use of such polymers alone and in combination with starch improves the strength of paper formed with the polymers. Such strength improvement can conveniently be measured using known methods, such as breaking length, mullen burst and Scott bond methods.
  • one embodiment of the present invention is a process for the production of paper comprising the admixing of starch and a polymer composition comprising one or more polymers of the group consisting of acrylamide polymers, acrylamide polymers co-polymerized with a monomer containing a pendent sulfonic acid group or a phosphonic acid a group, and terpolymers of acrylamide co-polymerized with both a monomer containing a pendant sulfonic acid group and a monomer containing pendant phosphonic acid group.
  • Such admixing occurs prior to or during the preparation of the furnish before providing the furnish to the paper machine.
  • the sequence of the admixing can be before, during or after the addition of the starch and polymer compositions to the furnish, preferably before.
  • the starch and polymer composition is added to the furnish separately, the preferred order is to add the starch first.
  • the polymer compositions are those described hereinabove.
  • the preferred process comprises effectively admixing the starch and polymer compositions to produce a paper sheet having a strength unexpectedly significantly greater than when either the starch or polymer composition is used alone, preferably at least about
  • an embodiment of the present invention is a process comprising effectively admixing the starch and polymer composition to produce a paper sheet having an unexpected synergistic increase in strength over the strength when either starch or polymer composition is used alone.
  • Such "Synergistic Increase” is measured by comparing the strength attained by the combination of starch and polymer composition over the absence of both starch and polymer composition in comparison to the additive sums of the separate increases in strength of each of the starch and polymer composition alone over the absence of both starch and polymer compositions in the formed paper. Stated in the form of an equation:
  • SI [(SC - SA)/(SA)] - [(SS-SA)/(SA) + (SP-SA)/(SA)] , wherein SI is the synergistic increase, SC is the strength of the paper with the combination of starch and polymer composition, SA is the strength of the paper in the absence of either starch or polymer composition, and SS and SP are the respective strengths of paper with starch and polymer composition alone.
  • SI is the synergistic increase
  • SC the strength of the paper with the combination of starch and polymer composition
  • SA is the strength of the paper in the absence of either starch or polymer composition
  • SS and SP are the respective strengths of paper with starch and polymer composition alone.
  • the synergistic increase is one such that no amount of additional polymer or starch alone when singularly present will provide the equivalent strength provided by the inventive combination of polymer and starch for a given weight percent of inorganic (e.g., filler) material.
  • the amount of starch useable will vary in accordance with the particular furnish and paper being produced. Such amounts can typically range from about five to about fifty pounds per ton of paper. Similarly, the amount of the polymer composition can typically range from about one to about ten pounds per ton of paper.
  • a second potassium persulfate solution (0.333 grams of potassium persulfate and 83.3 milliliters of distilled water) is added. 3-4 minutes later, a sodium metabisulfite solution (0.167 grams of sodium metabisulfite and 83.3 milliliters of distilled water) is added.
  • the flask temperature is held at 80°C while distilled water (of a 4167 milliliter amount) is added in amounts to avoid thickness.
  • the flask is held at 80°C with water addition for about an hour, at which time a sampling is checked for residual monomer presence. If residual monomer presence is too much, continue holding at 80°C until monomer amount is acceptable. Then add remaining water (of 4167 ml.) and mix well. Cool and recover.
  • the flask temperature is held at 80°C while distilled water (of a 4167 milliliter amount) is added in amounts to avoid thickness.
  • the flask is held at 80°C with water addition for about an hour, at which time a sampling is checked for residual monomer presence. If residual monomer presence is too much, continue holding at 80°C until monomer amount is acceptable. Then add remaining water (of 3747 ml), and additional water (up to 500 ml) if needed, and mix well. Cool and recover.
  • a flask is charged with 145.0 milliliters of distilled water, 21.75 grams of acrylamide and 4.0 grams of sodium 2-acrylamido-2-methylpropanesulfonic acid monomer (50%) and heated under nitrogen to 70°C. Add approximately 1 gram solid sodium hydroxide to adjust pH to about 7. Then 0.005 grams of potassium persulfate in 5 milliliters distilled water is added and the temperature permitted to rise to 80°C. As mix thickens, add 5 milliliters distilled water.
  • Handsheets were made using a 75% hardwood / 25% softwood blend of bleached northern Kraft pulps, co-refined at 1.6% consistency to an endpoint of 400 Canadian Standard
  • the refined pulp was diluted to 0.3125% consistency for papermaking.
  • Hercon 75 cationic alkyl ketene dimer emulsion was added to the furnish at the rate of 0.25%.
  • Polymer consisting of either unfunctionalized polyacrylamide, copolymer of acrylamide and 2- acrylamido-2-methylpropanesuifonic acid (AMPS) or a terpolymer of the PAM, AMPS and vinylphosphonic acid (VPA) was added to the furnish at the rate of 0.25% when specified.
  • Albacar ® HO precipitated calcium carbonate was added to the furnish batch for each set of handsheets in amounts adjusted to achieve filler levels of approximately 14, 21 , and 28%.
  • Stalok 400 cationic potato starch was added to the furnish at 0.75% when specified. Reten 1523 anionic polyacrylamide retention aid was added to the furnish at the rate of 0.025%. Each furnish batch was then divided into four aliquots to produce 2.5 gram handsheets (60.6 g/m 2 ). After each handsheet was formed on the Formax (Noble & Wood type) sheet former, it was pressed between a stainless steel roll and a rubber roll at 20 psi, while sandwiched between pieces of paper machine "wet felt” material. These handsheets were dried on a 115°C drum dryer, then conditioned and tested under TAPPI standard conditions of 23°C and 50% relative humidity. The results of the testing are shown in Figures 1 and 2.
  • VPA weight percent vinylphosphonic acid

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polyamides (AREA)
PCT/IB1999/002101 1999-04-06 1999-12-22 Bifunctional polymers WO2000059965A1 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
DE69911073T DE69911073T2 (de) 1999-04-06 1999-12-22 Bifunktionelle polymere
EP99967997A EP1171492B1 (en) 1999-04-06 1999-12-22 Bifunctional polymers
AU24553/00A AU2455300A (en) 1999-04-06 1999-12-22 Bifunctional polymers
JP2000609471A JP2002541276A (ja) 1999-04-06 1999-12-22 二官能性ポリマー
AT99967997T ATE248867T1 (de) 1999-04-06 1999-12-22 Bifunktionelle polymere
CA002366474A CA2366474A1 (en) 1999-04-06 1999-12-22 Bifunctional polymers
BR9917249-6A BR9917249A (pt) 1999-04-06 1999-12-22 Composição polimérica, processo para a fabricação de papel, e, composição de papel
NO20014814A NO20014814D0 (no) 1999-04-06 2001-10-03 Bifunksjonelle polymerer
HK02107083.1A HK1045534B (zh) 1999-04-06 2002-09-26 雙官能團聚合物

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US09/286,745 US6287423B1 (en) 1999-04-06 1999-04-06 Paper composition for improved sheet properties
US09/286,742 1999-04-06
US09/286,742 US6090242A (en) 1999-04-06 1999-04-06 Method of improvement strength of papers
US09/286,745 1999-04-06

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WO2000059965A1 true WO2000059965A1 (en) 2000-10-12

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EP (1) EP1171492B1 (no)
JP (1) JP2002541276A (no)
CN (1) CN1149238C (no)
AT (1) ATE248867T1 (no)
AU (1) AU2455300A (no)
BR (1) BR9917249A (no)
CA (1) CA2366474A1 (no)
DE (1) DE69911073T2 (no)
HK (1) HK1045534B (no)
NO (1) NO20014814D0 (no)
PT (1) PT1171492E (no)
WO (1) WO2000059965A1 (no)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005012637A1 (de) * 2003-07-25 2005-02-10 Basf Aktiengesellschaft Wässrige zusammensetzung und deren verwendung zur papierherstellung
US8747617B2 (en) 2007-09-12 2014-06-10 Nalco Company Controllable filler prefloculation using a dual polymer system
US8778140B2 (en) 2007-09-12 2014-07-15 Nalco Company Preflocculation of fillers used in papermaking
WO2014114870A1 (fr) 2013-01-22 2014-07-31 Emin Leydier Matériaux fibreux en feuille à propriétés de résistance mécanique améliorées, procédé, utilisation et compositions aqueuses associés
US9487916B2 (en) 2007-09-12 2016-11-08 Nalco Company Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking
US9752283B2 (en) 2007-09-12 2017-09-05 Ecolab Usa Inc. Anionic preflocculation of fillers used in papermaking

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US8097126B2 (en) 2003-07-25 2012-01-17 Basf Se Aqueous composition and use thereof for paper production
US8747617B2 (en) 2007-09-12 2014-06-10 Nalco Company Controllable filler prefloculation using a dual polymer system
US8778140B2 (en) 2007-09-12 2014-07-15 Nalco Company Preflocculation of fillers used in papermaking
US9487916B2 (en) 2007-09-12 2016-11-08 Nalco Company Method of improving dewatering efficiency, increasing sheet wet web strength, increasing sheet wet strength and enhancing filler retention in papermaking
US9752283B2 (en) 2007-09-12 2017-09-05 Ecolab Usa Inc. Anionic preflocculation of fillers used in papermaking
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WO2014114870A1 (fr) 2013-01-22 2014-07-31 Emin Leydier Matériaux fibreux en feuille à propriétés de résistance mécanique améliorées, procédé, utilisation et compositions aqueuses associés

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EP1171492A1 (en) 2002-01-16
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PT1171492E (pt) 2004-01-30
ATE248867T1 (de) 2003-09-15
AU2455300A (en) 2000-10-23
CA2366474A1 (en) 2000-10-12
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CN1149238C (zh) 2004-05-12
HK1045534B (zh) 2005-02-18

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