Thermoplastic composite material reinforced with synthetic fibers and manufacturing process

Patent metadata

Field	Value
Publication number	US-10000662-B2
Application number	US-201214353849-A
Country	US
Kind code	B2
Filing date	Oct 23, 2012
Priority date	Oct 25, 2011
Publication date	Jun 19, 2018
Grant date	Jun 19, 2018

Abstract

A method for producing a composite material, including an assembly of one or a plurality of synthetic reinforcement fibers, impregnated with at least one thermoplastic polymer having a vitreous transition temperature Tg greater than or equal to 80° C. including: i) a step of impregnating said assembly with a precursor composition in the molten state and including: a) at least one prepolymer P(X)n of said thermoplastic polymer, including a molecular chain P having, at the ends n thereof, identical reactive functions X, said prepolymer having a semiaromatic and/or semi-cycloaliphatic structure, b) at least one chain extender including two identical functions Y, which are reactive with at least one of said functions X; ii) a step of polymerization by mass (poly)addition, in the molten state, of said prepolymer with said chain extender, with said thermoplastic polymer of the thermoplastic matrix being the result of said polymerization by mass polyaddition.

First claim

The invention claimed is:

1. A process for the manufacture of a composite material, the composite material comprising an assemblage of one or more synthetic reinforcing fibers, which is impregnated with at least one thermoplastic polymer having a glass transition temperature Tg of greater than or equal to 80° C., said process comprising:
i) a stage of impregnation of said assemblage with a precursor composition in the molten state, the impregnation being carried out at a temperature such that the viscosity of said precursor composition in the molten state does not exceed 100 Pa·s, with said precursor composition comprising:
a) at least one prepolymer of said thermoplastic polymer, comprising a molecular chain having, at its ends, n identical reactive functional groups X, said prepolymer being of semiaromatic and/or semicycloaliphatic structure, with X being a reactive functional group from: OH, NH 2 or COOH, with n ranging from 1 to 3,
b) at least one chain extender, which can be represented by Y-A-Y, comprising two identical Y functional groups which react with at least one of said X functional groups, wherein A is a carbon-based spacer or radical carrying the two Y groups,

ii) a stage of bulk polymerization by (poly)addition in the molten state of said prepolymer with said chain extender,
with said thermoplastic polymer being the result of said bulk polymerization by polyaddition.

2. The process as claimed in claim 1 , wherein the process comprises a stage iii) of final processing of said composite material.

3. The process as claimed in claim 1 , wherein the polymerization stage ii) is carried out at a temperature ranging from 150 to 340° C.

4. The process as claimed in claim 1 , wherein said thermoplastic polymer is chosen from: a polyamide, a polyester, their copolymers, including polyamide-polyether, or their mixtures.

5. The process as claimed in claim 1 , wherein said chain extender is nonpolymeric and nonoligomeric.

6. The process as claimed in claim 1 , wherein said prepolymer corresponds to:
n=1 or 2,
X being a reactive functional group from: OH, NH 2 , COOH,
said chain P comprising a cycloaliphatic and/or aromatic structure comprising at least one ring of 4, 5 or 6 carbon atoms which is optionally substituted.

7. The process as claimed in claim 6 , wherein the choice of said chain extender with respect to X is as follows:
when X is NH 2 or OH:
either the chain extender Y-A-Y corresponds to:
Y chosen from the groups: maleimide, isocyanate which may be blocked, oxazinone and oxazolinone,

and
A is a carbon-based spacer or carbon-based radical carrying the functional groups Y and is chosen from:
a covalent bond between two Y functional groups in the case where Y=oxazinone or oxazolinone, or
an aliphatic hydrocarbon chain or an aromatic and/or cycloaliphatic hydrocarbon chain, the latter two comprising at least one ring of 5 or 6 carbon atoms which is optionally substituted, with optionally said aliphatic hydrocarbon chain having a molecular weight of 14 to 200 g·mol −1 ,

or the chain extender Y-A-Y corresponds to Y being a caprolactam group and to A being a carbonyl radical, or to A being a terephthaloyl or an isophthaloyl,
or said chain extender corresponds to Y being a cyclic anhydride group and this extender is chosen from a cycloaliphatic and/or aromatic dicarboxylic anhydride,

and
when X is COOH:
said chain extender Y-A-Y corresponds to:
Y chosen from the groups: oxazoline, oxazine, imidazoline or aziridine,

and to
A being a carbon-based spacer or a carbon-based radical as defined above for when X is NH 2 or OH.

8. The process as claimed in claim 1 , wherein, when Y is chosen from oxazinone, oxazolinone, oxazine, oxazoline or imidazoline, in this case, in the chain extender represented by Y-A-Y, A represents an alkylene, —(CH 2 ) m — with m ranging from 1 to 14, or A represents a cycloalkylene and/or an arylene which is alkyl-substituted or unsubstituted.

9. The process as claimed in claim 1 , wherein said prepolymer is a polyamide prepolymer obtained from:
the polycondensation of at least one linear or branched aliphatic diamine and of at least one aromatic and/or cycloaliphatic dicarboxylic acid comprising at least one ring having 4, 5 or 6 carbon atoms which is optionally substituted, and/or
the polycondensation of at least one cycloaliphatic diamine with at least one linear or branched aliphatic, cycloaliphatic or aromatic dicarboxylic acid, and optionally with the presence of at least one compound chosen from: a lactam, an aminocarboxylic acid or the stoichiometric combination of an aliphatic dicarboxylic acid and an aliphatic diamine.

10. The process as claimed in claim 1 , wherein said thermoplastic polymer is a semiaromatic and/or semicycloaliphatic polyamide, homopolyamide or copolyamide selected from the group consisting of:
polyamides selected from the group consisting of: 8.T, 9.T, 10.T, 11.T, 12.T, 6.T/9.T, 9.T/10.T, 9.T/11.T, 9.T/12.T, 9/6.T, 10/6.T, 11/6.T, 12/6.T, 10/9.T, 10/10.T, 10/11.T, 10/12.T, 11/9.T, 11/10.T, 11/11.T, 11/12.T, 12/9.T, 12/10.T, 12/11.T, 12/12.T, 6.10/6.T, 6.12/6.T, 9.10/6.T, 9.12/6.T, 10.10/6.T, 10.12/6.T, 6.10/9.T, 6.12/9.T, 9.10/9.T, 9.12/9.T, 10.10/9.T 10.12/9.T, 6.10/10.T, 6.12/10.T, 9.10/10.T, 9.12/10.T, 10.10/10.T, 10.12/10.T, 6.10/12.T, 6.12/12.T, 9.10/12.T, 9.12/12.T, 10.10/12.T, 11/6.T/9.T, 11/6.T/10.T, 11/6.T/11.T, 11/6.T/12.T, 11/9.T/10.T, 11/9.T/11.T, 11/9.T/12.T, 11/10.T/11.T, 11/10.T/12.T, 11/11.T/12.T, 6.T/10.T, 6.T/11.T, 6.T/12.T, 10.T/11.T, 10.T/12.T, 11.T/12.T, 12/6.T/10.T, 12/6.T/11.T, 12/6.T/12.T, 12/9.T/10.T, 12/9.T/11.T, 12/9.T/12.T, and 12/10.T/11.T, 12/10.T/12.T, 12/11.T/12.T,
preceding terpolymer polyamides with 12/replaced with 9/, 10/, 6.10/, 6.12/, 10.10/, 10.12/, 9.10/and 9.12/,
all the abovementioned polyamides where terephthalic (T) is partially or completely replaced with isophthalic (I), with naphthalene-2,6-dicarboxylic and/or with 1,3- or 1,4-CHDA (cyclohexanedicarboxylic acid), with it being possible for all or a portion of the aliphatic diamines to be replaced with cycloaliphatic diamines,
all the abovementioned polyamides, with replacement of the C 6 to C 12 aliphatic diamine with a cycloaliphatic diamine from BMACM, BACM and/or IPDA and with replacement of all or part of the aromatic diacid T with a linear or branched C 6 to C 18 aliphatic diacid.

11. The process as claimed in claim 1 , wherein said thermoplastic polymer is a semicrystalline polyamide having a melting point temperature Tm and a crystallization temperature Tc with the difference between the melting point temperature Tm of said polyamide and the crystallization temperature Tc being less than 100° C.

12. The process as claimed in claim 1 , wherein said thermoplastic polymer is an amorphous polyamide.

13. The process as claimed in claim 1 , wherein said synthetic reinforcing fibers are chosen from:
mineral fibers,
polymer fibers, these having a melting point temperature Tm′ or a glass transition temperature Tg′ greater than the polymerization temperature of said precursor composition,
or the mixtures of the abovementioned fibers.

14. The process as claimed in claim 13 , wherein said assemblages are chosen from fabrics, nonwovens or unidirectional fibrous reinforcements, laps or strips or plaits, or cut fibers.

15. The process as claimed in claim 1 , wherein the impregnation stage i) is carried out under a pressure ranging from 1 to 30 bar.

16. The process as claimed in claim 1 , wherein said polymerization of stage ii) is optionally completed, after the processing stage iii), by a separate fi

Assignees

• Arkema France

Inventors

• Hochstetter Gilles
• Briffaud Thierry
• Glotin Michel
• Nogues Pierre
• Khusrawy Maliha

Classifications

• B29C70/24

  oriented in at least three directions forming a three-dimensional [3D] structure · CPC title

• B29C67/246

  Moulding high reactive monomers or prepolymers, e.g. by reaction injection moulding [RIM], liquid injection moulding [LIM] (casting monomers B29C39/006, mixing construction B29B7/74) · CPC title

• C09D177/06 Primary

  Polyamides derived from polyamines and polycarboxylic acids (C09D177/10 takes precedence) · CPC title

• C08J5/24

  Impregnating materials with prepolymers which can be polymerised in situ, e.g. manufacture of prepregs · CPC title

• C08J2377/12

  Polyester-amides · CPC title