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US4590242A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of low-shrinkage nylon moldings

Assignee: BASF SE
•
Filing: 1983-07-14
•
Granted: 1986-05-20
•
Expires: 2003-07-14
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Abstract

Abstract Low-shrinkage nylon moldings are produced by activated alkaline lactam polymerization, preferably using the reactive injection molding technique, by a process wherein the polymerization is carried out in the presence of from 5 to 80% by weight of a polymer P which 1. is completely soluble in the lactam, 2. separates out in the course of polymerization at a conversion of from 1 to 50%, 3. is composed of one or more blocks which are compatible with polylactam and one or more blocks which are incompatible therewith, and preferably 4. possesses functional groups which are incorporated into the growing polylactam chain.

Inventors

  • 👤 Peter Horn
  • 👤 Hellmut Bunsch
  • 👤 Anton Hesse
  • 👤 Matthias Marx
  • 👤 Dietmar Nissen
  • 👤 Walter Heckmann

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 16:50
CPC Classifications
C; C08; C08G; C08G69/00; C08G69/02; C08G69/08; C08G69/14; C08G69/16; C08G69/18

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 66 words
A process for the production of a low-shrinkage nylon molding by activated alkaline polymerization of lactams, wherein the polymerization is carried out in the presence of from 5 to 80% by weight, based on the lactam, of a polymer P which 1. is completely soluble in the lactam, 2. separates out in the course of the polymerization at a conversion of from 1 to 50%, and
Claim 2
Dependent Claim 66 words
A process for the production of a low-shrinkage nylon molding by activated alkaline polymerization of lactams, wherein the polymerization is carried out in the presence of from 5 to 80% by weight, based on the lactam, of a polymer P which 1. is completely soluble in the lactam, 2. separates out in the course of the polymerization at a conversion of from 1 to 50%, and
Claim 3
Dependent Claim 144 words
is composed of two or more chemically different blocks, and wherein the polymer P is a graft polymer comprising (W) from 2 to 50% by weight of a polyether prepolymer having a number average molecular weight of from 1,000 to 100,000 and containing, on average, from 0.2 to 1.5 olefinic double bonds per prepolymer molecule, and (X) from 98 to 50% by weight of a monomer selected from the group consisting of styrene and methyl methacrylate, with or without (Y) from 0 to 10% by weight of monoolefinically unsaturated monomers selected from the group consisting of N-vinylpyrrolidone, N-vinylcaprolactam, acrylamide, methacrylamide and acryloylcaprolactam, and (Z) from 0 to 10% by weight of a polyunsaturated monomer selected from the group consisting of diolefins of 4 to 10 carbon atoms, esters of olefinically unsaturated carboxylic acids with polyhydric alcohols and vinyl or allyl ethers of polyhydric alcohols.
Claim 4
Dependent Claim 144 words
is composed of two or more chemically different blocks, and wherein the polymer P is a graft polymer comprising (W) from 2 to 50% by weight of a polyether prepolymer having a number average molecular weight of from 1,000 to 100,000 and containing, on average, from 0.2 to 1.5 olefinic double bonds per prepolymer molecule, and (X) from 98 to 50% by weight of a monomer selected from the group consisting of styrene and methyl methacrylate, with or without (Y) from 0 to 10% by weight of monoolefinically unsaturated monomers selected from the group consisting of N-vinylpyrrolidone, N-vinylcaprolactam, acrylamide, methacrylamide and acryloylcaprolactam, and (Z) from 0 to 10% by weight of a polyunsaturated monomer selected from the group consisting of diolefins of 4 to 10 carbon atoms, esters of olefinically unsaturated carboxylic acids with polyhydric alcohols and vinyl or allyl ethers of polyhydric alcohols.
Claim 5
Dependent Claim 60 words
A process as claimed in claim 1, wherein, in the alkaline lactam polymerization, a Component A, which contains the lactam and a catalyst, and a Component B, which contains the lactam and an activator, are mixed thoroughly at from 70° to 140° C., and the mixture is transported into a mold and polymerized therein at from 130° to 200° C.
Claim 6
Dependent Claim 19 words
A process as claimed in claim 1, wherein the polymerization is carried out by the reactive injection molding technique.
Claim 7
Dependent Claim 35 words
A process as claimed in claim 2, wherein, as a stabilizer, a cryptophenol, an amine or a mixture of CuI and KI in a molar ratio of 1:3 is added to the activator-containing component B.

References Cited (Backward Citations)

US3470139A Cited
US3539662A Cited
US3770689A Cited
US3793399A Cited
US4448956A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-05-19 1989-11-18 1990-05-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-05-19 1993-11-18 1994-05-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-05-19 1997-11-18 1998-05-20 $7700.00 Window Closed / Lapsed

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