EP0349935A2 - Solutions aqueuses de resines polyamide-amine-epichlorhydrine, leur procédé de préparation et leur utilisation - Google Patents

Solutions aqueuses de resines polyamide-amine-epichlorhydrine, leur procédé de préparation et leur utilisation Download PDF

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Publication number
EP0349935A2
EP0349935A2 EP89112049A EP89112049A EP0349935A2 EP 0349935 A2 EP0349935 A2 EP 0349935A2 EP 89112049 A EP89112049 A EP 89112049A EP 89112049 A EP89112049 A EP 89112049A EP 0349935 A2 EP0349935 A2 EP 0349935A2
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EP
European Patent Office
Prior art keywords
resin
acid
epichlorohydrin
polyamidoamine
resin solution
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
EP89112049A
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German (de)
English (en)
Other versions
EP0349935A3 (fr
EP0349935B1 (fr
Inventor
Manfred Marten
Walter Dr. Kamutzki
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Hoechst AG
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Hoechst AG
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Publication date
Application filed by Hoechst AG filed Critical Hoechst AG
Priority to AT89112049T priority Critical patent/ATE90405T1/de
Publication of EP0349935A2 publication Critical patent/EP0349935A2/fr
Publication of EP0349935A3 publication Critical patent/EP0349935A3/fr
Application granted granted Critical
Publication of EP0349935B1 publication Critical patent/EP0349935B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/54Synthetic 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
    • D21H17/55Polyamides; Polyaminoamides; Polyester-amides
    • 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
    • D21H21/20Wet strength agents

Definitions

  • US Pat. No. 3,352,833 describes, inter alia, an alkaline aftertreatment of polyamidoamine-epichlorohydrin resins for reactivating the wet strength activity.
  • the acidified resin solutions are then reacted with 0.25 to 2.5 equivalents of base per equivalent of acid in aqueous solution.
  • the base is added before using the resin for papermaking, and the resin solution is left to age for four hours and then used immediately.
  • the reworking of the alkaline aftertreatment specified in this US patent shows that this does not result in resin solutions which are sufficiently stable in storage and / or low in chlorine (cf. the further comparative experiments below).
  • the present invention now relates to a storage-stable, aqueous resin solution with a pH of at most 7, containing as resin a water-dilutable, preferably water-soluble polyamidoamine-epichlorohydrin resin (A) obtained by converting a water-dilutable, preferably water-soluble, basic polyamidoamine (B) , consisting of an acid component (B1) and an amine component (B2), with epichlorohydrin (C), the content of organically bound chlorine in the resin (A) being at most 4% by weight and the component (B2) - if the acid component (B1) is an aliphatic or aromatic carboxylic acid or its functional derivatives, optionally in admixture with an amino carboxylic acid or its lactams - consists of a mixture of polyamines and alkanol monoamines.
  • A water-dilutable, preferably water-soluble polyamidoamine-epichlorohydrin resin
  • A water-dilutable
  • the invention relates to a process for the preparation of these resin solutions and their use.
  • stable in storage is intended here to mean that no noticeable gelation or precipitation occurs during storage for at least three months at room temperature (or for at least 10 days at 50 ° C.).
  • solution is also intended to include a colloidal solution.
  • the pH of the resin solution according to the invention is preferably between 1.5 and 5.
  • the viscosity of a 12.5% solution at 25 ° C. is generally about 10 to 200, preferably 15 to 80 mPa.s.
  • the content of resin (A) in the solution according to the invention is generally between 8 and 25% by weight, preferably 10 and 15% by weight, based on the solution.
  • this resin solution contains small amounts of inorganic substances (from the base treatment and the subsequent neutralization) and optionally up to 0.5% by weight, preferably 0.05 to 0.2% by weight, of antifungal agents, such as sorbic acid or Potassium sorbate and optionally other additives, such as, for example Defoaming agent.
  • antifungal agents such as sorbic acid or Potassium sorbate
  • other additives such as, for example Defoaming agent.
  • the resin (A) generally has an average molecular weight M n of at least 500, preferably of at least 1000 and in particular of 1000 to 500,000.
  • the content of organically bound chlorine is generally between 0.1 and 4, preferably between 1 and 4 and in particular between 1 and 3% by weight. In a 12.5% resin solution, this chlorine content does not exceed 0.5% by weight and is generally between 0.0125 and 0.5, preferably between 0.125 and 0.5 and in particular between 0.125 to 0.375% by weight, based on the solution.
  • the amount of units in (A) derived from the epichlorohydrin is generally 20 to 50% by weight, preferably 30 to 40% by weight, based on (A).
  • the process according to the invention for the preparation of the resin solutions described above is characterized in that water-soluble, basic polyamidoamines (B) are reacted with epichlorohydrin (C) in a ratio of 0.6 to 2 moles per mole of basic amino groups of the polyamidoamine (B) in an aqueous system brings, and then, optionally after prior acidification of the reaction system, with as much a base (D), generally 0.1 to 1.0 mol, preferably 0.1 to 0.6 mol per mol of epichlorohydrin used, at 25 to 95 ° C converts that the pH is greater than 8, then adjusts the pH to at most 7 by adding acid.
  • a base generally 0.1 to 1.0 mol, preferably 0.1 to 0.6 mol per mol of epichlorohydrin used, at 25 to 95 ° C converts that the pH is greater than 8, then adjusts the pH to at most 7 by adding acid.
  • the water-soluble polyamidoamine (B) generally has an average molecular weight M n (determined via the carboxyl end groups) of at least 500, preferably at least 1000 and in particular 2000 to 20,000; the amine number is usually between 200 and 400, preferably between 250 and 350 mg KOH / g and the acid number between 0 and 50, preferably 10 and 30 mg KOH / g.
  • Polyamidoamines (B) which meet the conditions according to the invention are, for example, in DE-AS 1,777,824, GB-PS 865,727, US-PS 4,075,177 and 4,336,835, DE-OS 3,323,732 and EP -OS 31 899 described, to which reference is made here.
  • the corresponding products according to DE-OS 3,323,732 are preferred insofar as they come under the present framework.
  • Polyamidoamines (B) of this type are generally obtained by reacting the acid component (B1), such as dicarboxylic acids or their functional derivatives, and ⁇ -aminocarboxylic acids or their lactams with the amine component (B2), such as polyamines, these being present in a mixture with alkanolmonoamines if ( B1) meets the conditions mentioned above.
  • These polyamines contain at least two primary amino groups and preferably at least one secondary and / or tertiary amino group.
  • the quantity ratio of the components is to be chosen so that in the resulting polyamidoamine (B) there is still a sufficient number of basic (ie reactive with epichlorohydrin (C)) amino groups, no gelation occurs during the reaction and the molecular weight of (A) in the specified range.
  • Reaction products of type 1) using diethylene triamine, triethylene tetramine and tetraethylene pentamine as the polyamine and 2-aminoethanol as the alkanol monoamine are particularly preferred.
  • Examples of polyamines b1) and c1) are those of the formula (I) considered in the p is zero or an integer from 1 to 6, preferably 1 to 4,
  • R1 is a divalent, preferably non-aromatic hydrocarbon radical having 2 to 18 carbon atoms, preferably a branched or unbranched alkylene radical having 2 to 10 carbon atoms, in particular having 2 to 6 carbon atoms, or a cycloalykylene radical having 5 to 12 carbon atoms, preferably 6 to 10 carbon atoms, or an aralkylene radical having 7 to 12 carbon atoms, preferably 8 to 10 carbon atoms and R2, R 2 ' independently of one another for H or one of the two radicals for stand in which R1 has the same meaning as above and R3, R4 are either independently of one another H, (C1-C20) alkyl, preferably (C1-C6) alkyl, where these alkyl radicals can also carry hydroxyl groups.
  • polyamines b1) are called methyl bis (3-aminopropyl) amine, ethyl bis (3-aminopropyl) amine, N- (3-aminopropyl) tetramethylene diamine, N, N'-bis (3-aminopropyl) tetramethylene diamine, Polyalkylene polyamines such as di-propylene- (1,2) -triamine, bis- (3-aminopropyl) -amine, tripropylene- (1,2) -tetramine and especially diethylene triamine, triethylene tetramine and tetraethylene pentamine.
  • Polyamines c1) are, for example: ethylenediamine, propylenediamine, 1-amino-3-methylamino-propane, 2-methylpentamethylene diamine, pentanethylene diamine, hexamethylene diamine, trimethyl hexamethylene diamine, neopentyl diamine, octamethylene diamine, dioxadodecane diamine, cyclialiphatic diamines such as 1,2-, 1,3- or 1,4-cyclohexane diamine; 4,4'-methylene-bis-cyclohexylamine, isophoronediamine, menthandiamine, 4,4'-diamino-3,3'-dimethyl-di-cyclohexylmethane, 3-aminomethyl-1- (3-aminopropyl-1-methyl) -4 -methylcyclohexane, N-methylethylenediamine, N-aminoethylpiperazine, 1,3-bis-amin
  • alkanol monoamines are those of the formula H2N-R1-OH (II) suitable in which R1 has the above meaning, such as 2-aminoethanol, 1-amino-2-propanol, 3-amino-1-propanol, 2-amino-1-butanol, 4-amino-1-butanol, 5-amino -1-pentanol, 6-amino-1-hexanol and their isomers, the hydrocarbon radical of which is branched or which carry the amino group and / or the hydroxyl group on a primary or secondary carbon atom; furthermore those which are derived from cyclic hydrocarbon radicals, preferably having 5-7 carbon atoms.
  • the molar amount of dicarboxylic acid or its functional derivatives to polyamine / alkanol monoamine is such that the ratio of carboxyl groups to the sum of primary NH2 groups 1: (0.8-1.4), preferably 1: (0, 95-1.1).
  • the ratio of their molar amounts is 0.6: 0.4 to 0.99: 0.01, preferably 0.8: 0.2 to 0.95: 0.05.
  • the polyamidoamines (B) can be prepared in the customary manner, for example by heating the for several hours corresponding components with the exclusion of oxygen at temperatures of 125 to 250 ° C, preferably from 140 to 180 ° C, first under ordinary pressure and then under reduced pressure, with a small amount of hydrazine hydrate or hydrazides can be added to avoid the darkening of the polyamides.
  • the reaction time depends on the temperatures and pressures used and is generally between 4 and 10 hours.
  • dichlorohydrin (1,3-dichloro-2-hydroxypropane) can optionally also be used.
  • Bases (D) which can be used include: alkali metal hydroxides, preferably sodium and potassium hydroxide, carbonates, bicarbonates, alkaline earth metal hydroxides, such as calcium hydroxide, furthermore benzyltrimethylammonium hydroxide, tetramethylammonium hydroxide, tetraethylammonium hydroxide or corresponding mixtures.
  • the reaction products can be prepared by the process according to the invention in such a way that the polyamidoamines (B) and epichlorohydrin (C) are in a first reaction step at a concentration of the reactants of about 25 to 50%, preferably 35 to 45% and at one Temperature between 25 and 95 ° C, preferably 40 to 70 ° C, until it can react until the viscosity of a 40% solution (determined at 25 ° C) is about 100 to 600, preferably 200 to 400 mPa.s.
  • This solution is then set in a second reaction step with an aqueous solution of a base (D) which is used in an amount of generally 0.1 to 1.0, preferably 0.1 to 0.6, mol per mol of epichlorohydrin (C) is contained, at a concentration of the reactants of 10 to 40%, preferably 15 to 25%, and a temperature between 25 to 95 ° C, preferably 40 to 70 ° C, until the viscosity a 12.5% solution (determined at 25 ° C.) is 10-200 mPa.s, preferably 15 to 80 mPa.s.
  • the pH in this second reaction step is greater than 8, preferably between 9 and 12.
  • the mixture is expediently added to the mixture in order to terminate the action and to stabilize the self-crosslinking reaction products, so much acid or acid derivatives that the pH the aqueous solution is 1 to 7, preferably between 1.5 and 5, and adjusts the solids content of the reaction solution to 8 to 25% by weight by dilution with water.
  • acid can be added to the solution during or after the reaction of polyamidoamine (B) and epichlorohydrin (C) and the pH can be adjusted to less than 7, preferably 1.5 and 5.
  • Sufficient base (D) is then added to this acidic reaction mixture such that the pH is greater than 8, preferably between 9 and 12, and this system is then used for a period of 0.5 to 8 hours, preferably 1 to 4 hours at a temperature of 25 to 95 ° C, preferably 40 to 70 ° C.
  • Halogen-free acids such as sulfuric, phosphoric or acetic acid are particularly suitable as acids and corresponding anhydrides or acidic salts as acid derivatives.
  • the amount of epichlorohydrin (C) is generally 0.6 to 2 mol, preferably 1.0 to 1.4 mol, per mol of basic amino groups (primary, secondary or tertiary) in the polyamidoamine (B) and the amount of base (D) 0.1 to 1.0 mol, preferably 0.1 to 0.6 mol, per mol of epichlorohydrin used.
  • the resins or resin solutions according to the invention have a considerably lower level than the previously known reaction products of polyamidoamine and epichlorohydrin organically bound chlorine content and are therefore ideally suited to significantly reduce the organic chlorine content of wastewater, including paper mills.
  • the reaction products which have hitherto been used to improve the wet strength effectiveness of paper do not possess this valuable property to the same extent. Due to the high storage stability of the resin solutions according to the invention, their wet strength effectiveness remains constant even after months of storage.
  • the wet strength of paper - including paper made from unbleached cellulose - can be outstandingly improved. In some cases, depending on the type of paper or as desired, it is also possible to increase the absorbency. It is noteworthy that the reaction products practically do not affect the whiteness of paper made from bleached pulp. It should also be mentioned that the speed at which the reaction products to be used according to the invention crosslink on the paper or in the pulp is high and that the reaction products are also used as retention aids for fillers used in papermaking, drainage aids to improve the papermaking speed and flocculants to remove fine particles Particles from dirty water, for example industrial waste water, can be used.
  • the resins in question in the form of aqueous solutions to the aqueous suspension of the paper raw material before processing into paper.
  • the amounts of resin required to achieve the desired wet strength can be determined by Determine preliminary tests without difficulty.
  • the polyamidoamine was diluted with 570 g of water.
  • the solution had a solids content of 59.8% (1 g, 1 hour, 125 ° C.) and a viscosity at 25 ° C. of 1174 mPa.s.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
  • Polyamides (AREA)
EP89112049A 1988-07-02 1989-07-01 Solutions aqueuses de resines polyamide-amine-epichlorhydrine, leur procédé de préparation et leur utilisation Expired - Lifetime EP0349935B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89112049T ATE90405T1 (de) 1988-07-02 1989-07-01 Waessrige loesungen von polyamidoamin-epichlorhyrin-harzen, verfahren zu ihrer herstellung und ihre verwendung.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3822490 1988-07-02
DE3822490A DE3822490A1 (de) 1988-07-02 1988-07-02 Waessrige loesungen von polyamidoamin-epichlorhyrin-harzen, verfahren zu ihrer herstellung und ihre verwendung

Publications (3)

Publication Number Publication Date
EP0349935A2 true EP0349935A2 (fr) 1990-01-10
EP0349935A3 EP0349935A3 (fr) 1991-05-08
EP0349935B1 EP0349935B1 (fr) 1993-06-09

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EP89112049A Expired - Lifetime EP0349935B1 (fr) 1988-07-02 1989-07-01 Solutions aqueuses de resines polyamide-amine-epichlorhydrine, leur procédé de préparation et leur utilisation

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Country Link
US (1) US5019606A (fr)
EP (1) EP0349935B1 (fr)
AT (1) ATE90405T1 (fr)
DE (2) DE3822490A1 (fr)
ES (1) ES2058408T3 (fr)

Cited By (20)

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EP0512423A2 (fr) * 1991-05-06 1992-11-11 Hoechst Aktiengesellschaft Solutions aqueuses de résines polyamidoamine cationiques
US5171795A (en) * 1990-08-01 1992-12-15 Hercules Incorporated Process for the production of improved polyaminopolyamide epichlorohydrin resins
WO1992022601A1 (fr) * 1991-06-19 1992-12-23 Akzo N.V. Resines a base d'epihalohydrine a teneur reduite en halogene
WO1993003222A1 (fr) * 1991-08-05 1993-02-18 Henkel Corporation Composition de resine de resistance a l'etat humide et procede de preparation
US5470742A (en) * 1991-04-24 1995-11-28 Hercules Incorporated Dehalogenation of organohalogen-containing compounds
EP0703265A1 (fr) 1994-07-22 1996-03-27 Hoechst Aktiengesellschaft Hydrogels hydrophiles à capacité de gonflement élevée
WO1999009252A1 (fr) * 1997-08-13 1999-02-25 Fort James Corporation Formulations de resines thermodurcissables resistant au mouille et polymeres de polyaminamide appropries pour l'emploi dans la fabrication de produits en papier
US5972691A (en) * 1995-06-07 1999-10-26 Hercules Incorporated Dehalogenation of polyamine, neutral curing wet strength resins
US6107432A (en) * 1997-05-28 2000-08-22 Basf Ag Water-swellable, hydrophilic polymer compositions
US6429267B1 (en) 1997-12-31 2002-08-06 Hercules Incorporated Process to reduce the AOX level of wet strength resins by treatment with base
US6472478B1 (en) 1998-02-21 2002-10-29 Basf Aktiengesellschaft Process for crosslinking hydrogels with bis- and poly-2- oxazolidinones
US6503979B1 (en) 1998-02-26 2003-01-07 Basf Aktiengesellschaft Method for cross-linking hydrogels with bis- and poly-2-oxazolidinones
US6559239B1 (en) 1998-11-26 2003-05-06 Basf Aktiengesellschaft Method for the secondary cross-linking of hydrogels with N-acyl-2-oxazolidinones
US6657015B1 (en) 1998-11-26 2003-12-02 Basf Aktiengesellschaft Method for the secondary cross-linking of hydrogels with 2-oxotetrahydro-1,3-oxazines
US7175740B2 (en) 1999-06-11 2007-02-13 Hercules Incorporated Reduced by product polyamine-epihalohydrin resins
US7183360B2 (en) 2001-10-05 2007-02-27 Basf Aktiengesellschaft Method for crosslinking hydrogels with morpholine-2,3-diones
US7303652B2 (en) 2000-12-09 2007-12-04 Hercules Incorporated Reduced byproduct high solids polyamine-epihalohydrin compositions
WO2008036241A1 (fr) 2006-09-18 2008-03-27 Hercules Incorporated Procédé de séparation par membrane pour retirer des résidus provenant de résines polyamine-épihalohydrine
US7655733B2 (en) 2004-08-04 2010-02-02 Basf Aktiengesellschaft Postcrosslinking of water absorbing polymers with cyclic carbamates and/or cyclic ureas
US7947771B2 (en) 2004-11-30 2011-05-24 Basf Aktiengesellschaft Insoluble metal sulfates in water absorbing polymeric particles

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US5567798A (en) * 1994-09-12 1996-10-22 Georgia-Pacific Resins, Inc. Repulpable wet strength resins for paper and paperboard
US5614597A (en) 1994-12-14 1997-03-25 Hercules Incorporated Wet strength resins having reduced levels of organic halogen by-products
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US5773507A (en) * 1995-08-25 1998-06-30 Henkel Corporation Anti-static composition and process for making same
US5786429A (en) * 1996-04-18 1998-07-28 Hercules Incorporated Highly branched polyamidoamines and their preparation
DE19728789A1 (de) 1997-07-05 1999-01-07 Bayer Ag Naßfestmittel mit niedrigem DCP-Gehalt
US6294645B1 (en) * 1997-07-25 2001-09-25 Hercules Incorporated Dry-strength system
US5942085A (en) * 1997-12-22 1999-08-24 The Procter & Gamble Company Process for producing creped paper products
US6291023B1 (en) * 1998-04-22 2001-09-18 Sri International Method and composition for textile printing
US20030070783A1 (en) * 2000-12-09 2003-04-17 Riehle Richard James Reduced byproduct high solids polyamine-epihalohydrin compositions
US7081512B2 (en) * 2003-05-21 2006-07-25 Hercules Incorporated Treatment of resins to lower levels of CPD-producing species and improve gelation stability
US20060142432A1 (en) * 2004-12-29 2006-06-29 Harrington John C Retention and drainage in the manufacture of paper
US7589153B2 (en) * 2005-05-25 2009-09-15 Georgia-Pacific Chemicals Llc Glyoxalated inter-copolymers with high and adjustable charge density
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MY150700A (en) * 2006-08-24 2014-02-28 Hercules Inc Adhesive composition of low molecular weight polyaminopolyamide-epichlorohydrin (pae) resin and protein
US20080292886A1 (en) * 2007-03-23 2008-11-27 Hercules Inc. Adhesive formulations containing urea additives, methods of forming plywood therewith, and plywood products made thereby
US7868071B2 (en) * 2007-07-30 2011-01-11 Georgia-Pacific Chemicals Llc Method of stabilizing aqueous cationic polymers
CA2701918C (fr) * 2007-10-09 2014-08-05 Hercules Incorporated Compositions adhesives contenant un reticulant
EP2148003A1 (fr) * 2008-07-22 2010-01-27 Mühle Rüningen GmbH & Co. KG Procédé pour la production d'un produit contenant de l'amidon modifié, produit contenant de l'amidon modifié obtenu par ce procédé et son utilisation dans la fabrication de papier
EP2456828A1 (fr) 2009-07-20 2012-05-30 Akzo Nobel Coatings International B.V. Système adhésif et procédé de production d un produit à base de bois
EP2456835A1 (fr) 2009-07-20 2012-05-30 Akzo Nobel Coatings International B.V. Système adhésif et procédé de production d un produit à base de bois
EP2649145B1 (fr) 2010-12-10 2014-11-26 Akzo Nobel Coatings International B.V. Composition adhésive aqueuse contenant un polymère synthétique et proteine de lupin
US20120247697A1 (en) 2011-03-29 2012-10-04 Kemira Oyj Polyamine Polyamidoamine Epihaloohydrin Compositions and Processes for Preparing and Using the Same
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WO2013046060A1 (fr) 2011-09-30 2013-04-04 Kemira Oyj Papier et procédés de fabrication du papier
US9777434B2 (en) 2011-12-22 2017-10-03 Kemira Dyj Compositions and methods of making paper products
CA2886043A1 (fr) 2012-09-26 2014-04-03 Kemira Oyj Materiaux absorbants, produits les contenant, compositions et procedes de fabrication de ces materiaux absorbants
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US9562326B2 (en) 2013-03-14 2017-02-07 Kemira Oyj Compositions and methods of making paper products
ES2718044T3 (es) 2014-08-13 2019-06-27 Solenis Tech Lp Proceso para mejorar el rendimiento de resinas de resistencia en húmedo mediante la activación con base
CN105348524A (zh) * 2015-12-14 2016-02-24 广东省造纸研究所 一种环境友好型pae造纸湿强剂的制备方法
CN106589420A (zh) * 2015-12-15 2017-04-26 广东省造纸研究所 一种低氯丙醇pae造纸湿强剂的制备方法
WO2020181092A1 (fr) * 2019-03-05 2020-09-10 Kemira Oyj Compositions et méthodes comprenant des résines de renforcement à l'état humide
CN111203197A (zh) * 2020-01-14 2020-05-29 吉首大学 基于环氧和氨基交联的吸附材料及其制备方法

Citations (3)

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US5171795A (en) * 1990-08-01 1992-12-15 Hercules Incorporated Process for the production of improved polyaminopolyamide epichlorohydrin resins
US5470742A (en) * 1991-04-24 1995-11-28 Hercules Incorporated Dehalogenation of organohalogen-containing compounds
US5843763A (en) * 1991-04-24 1998-12-01 Hercules Incorporated Dehalogenation of organohalogen-containing compounds
US5871616A (en) * 1991-04-24 1999-02-16 Hercules Incorporated Dehalogenation of organohalogen-containing compounds
EP0512423A2 (fr) * 1991-05-06 1992-11-11 Hoechst Aktiengesellschaft Solutions aqueuses de résines polyamidoamine cationiques
EP0512423A3 (en) * 1991-05-06 1993-11-10 Hoechst Ag Aqueous solutions of cationic polyamidoamine resins
WO1992022601A1 (fr) * 1991-06-19 1992-12-23 Akzo N.V. Resines a base d'epihalohydrine a teneur reduite en halogene
EP0776923A2 (fr) * 1991-06-19 1997-06-04 Akzo Nobel N.V. Résines à base d'épihalohydrines à teneur réduite en halogène
EP0776923A3 (fr) * 1991-06-19 1997-08-06 Akzo Nobel Nv Résines à base d'épihalohydrines à teneur réduite en halogène
WO1993003222A1 (fr) * 1991-08-05 1993-02-18 Henkel Corporation Composition de resine de resistance a l'etat humide et procede de preparation
EP0703265A1 (fr) 1994-07-22 1996-03-27 Hoechst Aktiengesellschaft Hydrogels hydrophiles à capacité de gonflement élevée
US5972691A (en) * 1995-06-07 1999-10-26 Hercules Incorporated Dehalogenation of polyamine, neutral curing wet strength resins
US6107432A (en) * 1997-05-28 2000-08-22 Basf Ag Water-swellable, hydrophilic polymer compositions
WO1999009252A1 (fr) * 1997-08-13 1999-02-25 Fort James Corporation Formulations de resines thermodurcissables resistant au mouille et polymeres de polyaminamide appropries pour l'emploi dans la fabrication de produits en papier
US6222006B1 (en) 1997-08-13 2001-04-24 Fort James Corporation Wet strength thermosetting resin formulations and polyaminamide polymers suitable for use in the manufacture of paper products
US6429267B1 (en) 1997-12-31 2002-08-06 Hercules Incorporated Process to reduce the AOX level of wet strength resins by treatment with base
US6472478B1 (en) 1998-02-21 2002-10-29 Basf Aktiengesellschaft Process for crosslinking hydrogels with bis- and poly-2- oxazolidinones
US6503979B1 (en) 1998-02-26 2003-01-07 Basf Aktiengesellschaft Method for cross-linking hydrogels with bis- and poly-2-oxazolidinones
US6559239B1 (en) 1998-11-26 2003-05-06 Basf Aktiengesellschaft Method for the secondary cross-linking of hydrogels with N-acyl-2-oxazolidinones
US6657015B1 (en) 1998-11-26 2003-12-02 Basf Aktiengesellschaft Method for the secondary cross-linking of hydrogels with 2-oxotetrahydro-1,3-oxazines
US7175740B2 (en) 1999-06-11 2007-02-13 Hercules Incorporated Reduced by product polyamine-epihalohydrin resins
US7303652B2 (en) 2000-12-09 2007-12-04 Hercules Incorporated Reduced byproduct high solids polyamine-epihalohydrin compositions
US7183360B2 (en) 2001-10-05 2007-02-27 Basf Aktiengesellschaft Method for crosslinking hydrogels with morpholine-2,3-diones
US7655733B2 (en) 2004-08-04 2010-02-02 Basf Aktiengesellschaft Postcrosslinking of water absorbing polymers with cyclic carbamates and/or cyclic ureas
US7947771B2 (en) 2004-11-30 2011-05-24 Basf Aktiengesellschaft Insoluble metal sulfates in water absorbing polymeric particles
WO2008036241A1 (fr) 2006-09-18 2008-03-27 Hercules Incorporated Procédé de séparation par membrane pour retirer des résidus provenant de résines polyamine-épihalohydrine

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EP0349935A3 (fr) 1991-05-08
ES2058408T3 (es) 1994-11-01
DE3822490A1 (de) 1990-01-04
ATE90405T1 (de) 1993-06-15
US5019606A (en) 1991-05-28
DE58904602D1 (de) 1993-07-15
EP0349935B1 (fr) 1993-06-09

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