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US3925329A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of polymers in powdered form which contain carboxylic acid or carboxylic anhydride groups

Assignee: BASF SE
•
Filing: 1973-12-28
•
Granted: 1975-12-09
•
Expires: 1993-12-28
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Abstract

Abstract A process for the production in powdered form of a polymer containing carboxylic acid or carboxylic anhydride groups in which the monomers are polymerized with agitation in the presence of an auxiliary liquid in such a way that the surface of the mixture is increased by a multiple with respect to the stagnant mixture and then the auxiliary liquid is distilled off. The powdered polymer is particularly suitable as a surface sizing agent for paper.

Inventors

  • 👤 Bernhard Heinrich
  • 👤 Herbert Naarmann
  • 👤 Peter Thoma

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 09:14
CPC Classifications
D; D21; D21H; D21H17/00; D21H17/20; D21H17/33; D21H17/34; D21H17/41; D21H17/42; D21H17/43; C; C08; C08F; C08F22/00; C08F22/04; C08F220/00; C08F220/02; C08F220/04; C08F220/06

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 199 words
A PROCESS FOR THE PRODUCTION IN POWDERED FORM OF A POLYMER CONTAINING CARBOXYLIC ACID OR CARBOXYLIC ANHYDRIDE GROUPS WHICH COMPRISES POLYMERIZING ACRYLIC ACID, METHACRYLIC ACID OR MALEIC ANHYDRIDE WITH ONE OR MORE THAN ONE OTHER MONOMERS SELECTED FROM THE GROUP CONSISTING OF STYRENE AND ESTERS OF ACRYLIC ACID AND METHACRYLIC ACID WITH ALCOHOLS OF THE STRUCTURE HO-CH2-R WHEREIN R IS HYDROGEN, ALKYL OF FROM ONE TO FIVE CARBONS, BENZYL, CH2-NR2 OR CH2-CH2NR2, IN SUCH AMOUNTS THAT THE RESULTING COPOLYMERS CONTAIN FROM 5 TO 40% BY WEIGHT OF THE MONOMERS CONTAINING CARBOXYLIC ACID GROUPS OR FROM 10 TO 50% BY WEIGHT OF MALEIC ANHYDRIDE, SAID POLYMERIZATION BEING CONDUCTED AT A TEMPERATURE OF FROM 70* TO 150*C AND IN THE PRESENCE OF AN ALCOHOL OR HYDROCARBON AUXILIARY LIQUID HAVING A BOILING OF FROM 70* TO 150*C, WHEREIN THE RATIO BY WEIGHT OF MONOMERS TO AUXILIARY LIQUID IS FROM 0.5:1 TO 1.5:1, AND WHEREIN THE SURFACE AREA OF THE MIXTURE IN THE REACTION ZONE IS INCREASED BY MECHANICAL STIRRING TO AT LEAST TWENTY TIMES THAT OF THE UNSTIRRED MIXTURE AND DISTILLING OFF THE AUXILLIARY LIQUID WHILE STIRRING AFTER THE MIXTURE HAS REACHED A VISCOSITY OF AT LEAST 20,000 CENTIPOISES MEASURED AT 20*C.
Claim 2
Dependent Claim 199 words
A PROCESS FOR THE PRODUCTION IN POWDERED FORM OF A POLYMER CONTAINING CARBOXYLIC ACID OR CARBOXYLIC ANHYDRIDE GROUPS WHICH COMPRISES POLYMERIZING ACRYLIC ACID, METHACRYLIC ACID OR MALEIC ANHYDRIDE WITH ONE OR MORE THAN ONE OTHER MONOMERS SELECTED FROM THE GROUP CONSISTING OF STYRENE AND ESTERS OF ACRYLIC ACID AND METHACRYLIC ACID WITH ALCOHOLS OF THE STRUCTURE HO-CH2-R WHEREIN R IS HYDROGEN, ALKYL OF FROM ONE TO FIVE CARBONS, BENZYL, CH2-NR2 OR CH2-CH2NR2, IN SUCH AMOUNTS THAT THE RESULTING COPOLYMERS CONTAIN FROM 5 TO 40% BY WEIGHT OF THE MONOMERS CONTAINING CARBOXYLIC ACID GROUPS OR FROM 10 TO 50% BY WEIGHT OF MALEIC ANHYDRIDE, SAID POLYMERIZATION BEING CONDUCTED AT A TEMPERATURE OF FROM 70* TO 150*C AND IN THE PRESENCE OF AN ALCOHOL OR HYDROCARBON AUXILIARY LIQUID HAVING A BOILING OF FROM 70* TO 150*C, WHEREIN THE RATIO BY WEIGHT OF MONOMERS TO AUXILIARY LIQUID IS FROM 0.5:1 TO 1.5:1, AND WHEREIN THE SURFACE AREA OF THE MIXTURE IN THE REACTION ZONE IS INCREASED BY MECHANICAL STIRRING TO AT LEAST TWENTY TIMES THAT OF THE UNSTIRRED MIXTURE AND DISTILLING OFF THE AUXILLIARY LIQUID WHILE STIRRING AFTER THE MIXTURE HAS REACHED A VISCOSITY OF AT LEAST 20,000 CENTIPOISES MEASURED AT 20*C.
Claim 3
Dependent Claim 78 words
A process as set forth in claim 1 wherein in a first stage the mixture is kept at a temperature of from 70* to 90*C and after a viscosity of 500 centipoises measured at 20*C has been reached is kept in a second stage at a temperature of from 90* to 130*C until a viscosity of 20,000 centipoises at 20*C has been reached and then the auxiliary liquid is distilled off at a temperature of less than 130*C.
Claim 4
Dependent Claim 29 words
A process as set forth in claim 1 wherein said auxiliary liquid is selected from the group consisting of benzene, toluene, xylene, cyclohexane, octane, nonane, propanol, isopropanol and butanol.
Claim 5
Dependent Claim 14 words
A process as set forth in claim 1 wherein said other monomer is styrene.
Claim 6
Dependent Claim 24 words
A process as set forth in claim 1 wherein said mixture of monomers and auxiliary liquid contains from 40 to 60% of the monomers.
Claim 7
Dependent Claim 24 words
A process as set forth in claim 1 wherein said auxiliary liquid is distilled off at a pressure of from 10 to 500 mm.
Claim 8
Dependent Claim 67 words
A process as set forth in claim 1 wherein said copolymer contains from 20 to 35% by weight of monomers containing carboxylic acid groups, styrene, and up to 10% by weight of monomers selected from the group consisting of esters of acrylic acid and methacrylic acid with alcohols of the structure HO-CH2-R wherein R is hydrogen, alkyl of from one to five carbons, benzyl, CH2-NR2 or CH2-CH2-NR2.
Claim 9
Dependent Claim 34 words
A Process as set forth in claim 1 wherein the surface area of the mixture in the reaction zone is increased by mechanical stirring to at least fifty times that of the unstirred mixture.

References Cited (Backward Citations)

US3035033A Cited
US3178395A Cited
US3388106A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-12-08 1979-06-09 1979-12-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-12-08 1983-06-09 1983-12-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-12-08 1987-06-09 1987-12-09 $7700.00 Window Closed / Lapsed

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