This application claims priority to Indian provisional patent application No. 4223/MUM/2015 filed on Nov. 5, 2015 and to European patent application No. 16150135.8 filed on Jan. 5, 2016, the whole content of each of these applications being incorporated herein by reference for all purposes.
The present invention relates to polyamides, in particular to fluorine-containing polyamides useful as additives for other polyamides.
Thermoplastic polyamides are widespreadly used as engineering plastics, mainly in the manufacture of automotive and electronic components and in the field of packaging. For these applications, it is often required that the polyamides have:
It is known in the art that functional (per)fluoropolyethers (herein after “PFPEs”) can be used as additives or as comonomers (frequently referred to as “comacromers”) for the manufacture of additives for other polymers in order to modify certain physical/chemical properties of the polymer concerned.
For example, the following patent documents teach the use of functional PFPEs as comacromers in the course of polymerization, thereby obtaining modified polymers, namely polyurethanes (PUs), polyurethane/polyesters (PUs/PEs) or polyesters (PEs), having a PFPE covalently bound thereto EP 1864685 A (SOLVAY SOLEXIS S.P.A.), U.S. Pat. No. 5,476,910 (AUSIMONT S.P.A.), U.S. Pat. No. 5,686,522 (AUSIMONT S.P.A.) and U.S. Pat. No. 5,109,103 (AUSIMONT S.P.A.).
U.S. Pat. No. 6,127,498 (AUSIMONT S.P.A.) discloses modified hydrogenated polymers obtainable by polycondensation or polyaddition reaction or by grafting a monomer, oligomer or polymer with a PFPE derivative comprising a monofunctional PFPE chain wherein a reactive terminal group T is bound to the PFPE chain via a bivalent radical A which may comprise amidic groups. The modified polymers can be used for the manufacture of articles endowed with improved surface properties. This document does not specifically mention polyamides, nor does it provide working examples related to modified polymers wherein A contains an amide group.
WO 2009/010533 (SOLVAY SOLEXIS S.P.A.) discloses polymers obtained by reaction of a hydrogenated polymer containing optionally substituted aromatic groups with a PFPE peroxide. In the resulting polymer, the aromatic ring is linked to the PFPE chain via a non-hydrolysable covalent bond. Said polymers are endowed with improved stability to high temperature and oxidizing media, improved chemical resistance and improved surface properties. Even if the hydrogenated polymer reacted with the PFPE peroxide can be a polyamide, this document neither mentions nor suggests polymers wherein the PFPE chain is linked to the hydrogenated polymer via an amide bond.
U.S. Pat. No. 3,876,617 (MONTEDISON S.P.A.) discloses elastomeric polyamides and copolyamides which can be obtained by reacting a PFPE diacid of formula:
HOOC—CF2O—(C2F4O)l—(CF2O)n—CF2COOH
(in which l and n are integers selected in such a way that the C2F4O/CF2O ratio ranges from 0.2 to 1.5), preferably in the form of a reactive derivative, with a diamine. In particular, in U.S. Pat. No. 3,876,617 it is stated that the polyamides can also contain further monomeric units with more than two functions, like carboxylic groups, to an extent up to 30% in number with respect to the bifunctional units. The amount of PFPE diacid contained in these polyamides is high and, for this reason, the resulting polyamide is endowed with elastomeric properties. Furthermore, this document does not specifically disclose polyamides obtained by reaction of a PFPE diacid, a diamine and a polycarboxylic acid.
WO 2010/049365 (SOLVAY SOLEXIS S.P.A) relates to polymers comprising PFPE segments and non-fluorinated segments as additives for hydrogenated polymers to give them good surface properties, in particular a low coefficient of friction (page 1, lines 1-3). The non-fluorinated segments have at least one crystalline phase that melts at a temperature of at least 25° C. This document discloses, inter alia, polyamide additives which can be obtained by reacting a non-fluorinated diamine with a PFPE having ester or carboxyl functionality, in an equivalent amount of amino groups equal to that of the functional groups of the diamine (reference is made to page 10, lines 5 to 8). This document does not disclose the copolymerization of a PFPE diacid with a hydrogenated diamine and a hydrogenated diacid. Furthermore, it is understood that, in view of the high content of fluorine in these polymers, in order to use them as additives (otherwise referred to as masterbatches), they must be first be diluted in diluted in a hydrogenated polymer.
U.S. Pat. No. 5,143,963 (RES DEVELOPMENT CORP) discloses a composition of matter formed by melt-blending a thermoplastic polymer and from 0.01% to less than 1% wt of a fluorocarbon additive, the additive having a lower surface energy than the polymer, due to the fact that the fluorocarbon additive has a higher concentration at the surface of the composition. The thermoplastic polymer can be a polyamide (col. 4, line 31-39) and the fluorocarbon additive can be a PFPE (col. 5, lines 2-3). This document does not disclose or suggest polyamides incorporating PFPE segments.
WO 99/23148 (E.I. DU PONT DE NEMOURS AND COMPANY) relates to a wear-resistance article comprising a thermosetting polymer-fluorocarbon composition and to a method for making said article (page 1, lines 5 and 6). It is taught that the incorporation of the fluorocarbon in the polymer “greatly increases the longevity or permanence of the beneficial effect compared to surface treatment of the polymeric additive with a fluorocarbon”. Among the thermosetting polymers specifically mentioned on page 6, lines 9-17, polyamides are not mentioned.
WO 91/03523 (COATES BROTHERS PLC) discloses a coating composition comprising a fluorine-containing polyamide. The polyamide can be obtained by polycondensation of a polycarboxylic acid component, a polyamine component and, commonly, monocarboxylic acids or monoamines to control the molecular weight of the final polyamide. The fluorine atoms can be derived from one or more of the reactants or can be introduced during or after the polycondensation. Thus document does not provide any hint or suggestion to polyamides wherein the polycarboxylic or polyamine component is a carboxylic or amino derivative of a fully or partially fluorinated polyether.
WO 2015/097076 (SOLVAY SPECIALTY POLYMERS ITALY S.P.A.) discloses polyamides comprising recurring units derived from monomers (A) and (B), wherein:
monomer (A) is selected from at least one of:
(i) a mixture of:
These polyamides are characterised in that the amount of monomer (B) ranges from 0.1 to 10% wt, preferably from 1 to 5% wt, with respect to the overall weight of monomers (A) and (B).
Thus, this document teaches to modify a polyamide by inserting an amount of PFPE which can be as high as 10% wt with respect to the overall weight of monomers in order to improve the polyamide properties, in particular surface properties, chemical resistance, and to reduce brittleness. This document teaches that the PFPE monomer has an average functionality (F) of at least 1.80 preferably of at least 1.95.
It would be desirable to provide further modified polyamides comprising a high amount of PFPE units and that can be used as additives for other polyamides, in particular non-fluorinated polyamides, in order to improve their physical/chemical properties.
The Applicant has now found out a convenient method [method (M)] for the manufacture of further polyamides comprising (per)fluoropolyether segments [polyamides (F-PA)]. Polyamides (F-PA) obtainable through method (M) have a lower molecular weight than the polyamides disclosed in WO 2015/097076, contain a high amount of fluorine and can be conveniently used as additives for other polyamides.
Method (M) envisages the copolymerization of a mixture of:
It has indeed been observed that, under these conditions it possible to limit the growth of the polyamide chain in such a way that a molecular weight (Mw) of at most 16,000 is obtained.
The polyamides (F-PA) obtained with method (M) have two extremes, at least one of which comprises an end-capping group deriving from the hydrogenated monocarboxylic acid or monoamine and, optionally, an end-capping group deriving from the monofunctional species present in the PFPE amino or carboxyl derivative.
Polyamides (F-PA) obtainable with method (M) represent a further aspect of the present invention.
Further aspects of the invention are the use of polyamides (F-PA) as additives for the manufacture of polyamide blends [blends (B)] and formed articles obtained from such blends.
For the sake of clarity, throughout the present application:
Method (M)
In a first aspect, the present invention relates to a method (M) for the manufacture of a fluorinated polyamide (F-PA) which comprises, preferably consists of, the copolymerization of:
(a) a monomer (A), selected from at least one of:
(i) a mixture of:
The average functionality (FRM) is the ratio between the overall equivalents of monomers (A), (B) and compound (C) and the overall moles of monomers (A), (B) and compound (C), according to the following equation:
(FRM)=[eq(A)+eq(B)+eq(C)]/[mol(A)+mol(B)+mol(C)]
Diamine (NN) is generally selected from the group consisting of primary and secondary alkylene-diamines, cycloaliphatic diamines, aromatic diamines and mixtures thereof.
Diamine (NN) typically complies with general formula (NN-I)
R—HN—R1—NH—R′ (NN-I)
wherein:
In amine (NN-I), a divalent cycloalkyl group preferably comprises from 3 to 6 carbon atoms, and, optionally, one or more oxygen or sulphur atoms.
In one embodiment, diamine (NN) is a primary alkylene diamine. Primary alkylene diamines are advantageously selected from the group consisting of 1,2-diaminoethane, 1,2-diaminopropane, propylene-1,3-diamine, 1,3-diaminobutane, 1,4-diaminobutane, 1,5-diaminopentane, 1,5-diamino-2-methyl-pentane, 1,4-diamino-1,1-dimethylbutane, 1,4-diamino-1-ethylbutane, 1,4-diamino-1,2-dimethylbutane, 1,4-diamino-1,3-dimethylbutane, 1,4-diamino-1,4-dimethylbutane, 1,4-diamino-2,3-dimethylbutane, 1,2-diamino-1-butylethane, 1,6-diaminohexane, 1,7-diaminoheptane, 1,8-diamino-octane, 1,6-diamino-2,5-dimethylhexane, 1,6-diamino-2,4-dimethylhexane, 1,6-diamino-3,3-dimethylhexane, 1,6-diamino-2,2-dimethylhexane, 1,9-diaminononane, 1,8-diamino-2-methyloctane, 1,6-diamino-2,2,4-trimethylhexane, 1,6-diamino-2,4,4-trimethylhexane, 1,7-diamino-2,3-dimethylheptane, 1,7-diamino-2,4-dimethylheptane, 1,7-diamino-2,5-dimethylheptane, 1,7-diamino-2,2-dimethylheptane, 1,10-diaminodecane, 1,8-diamino-1,3-dimethyloctane, 1,8-diamino-1,4-dimethyloctane, 1,8-diamino-2,4-dimethyloctane, 1,8-diamino-3,4-dimethyloctane, 1,8-diamino-4,5-dimethyloctane, 1,8-diamino-2,2-dimethyloctane, 1,8-diamino-3,3-dimethyloctane, 1,8-diamino-4,4-dimethyloctane, 1,6-diamino-2,4-diethylhexane, 1,9-diamino-5-methylnonane, 1,11-diaminoundecane, 1,12-diaminododecane, and 1,13-diaminotridecane. The aliphatic alkylene diamine preferably comprises at least one diamine selected from the group consisting of 1,2-diaminoethane, 1,4-diamino butane, 1,6-diaminohexane, 1,8-diamino-octane, 1,10-diaminodecane, 1,12-diaminododecane and mixtures thereof. More preferably, the aliphatic alkylene diamine is selected from 1,2-diaminoethane, 1,6-diaminohexane, 1,10-diaminodecane and mixtures thereof.
Examples of primary alkylene diamines wherein the alkylene chain comprises an arylene group are meta-xylylene diamine (MXDA), and para-xylylene diamine. More preferably, the diamine is MXDA.
In another embodiment, diamine (NN) is a secondary diamine. Non-limiting examples of secondary diamines are N-methylethyelene diamine, N,N′-diethyl-1,3-propanediamine, N,N′-diisopropylethylenediamine, N,N′-diisopropyl-1,3-propanediamine and N,N′-diphenyl-para-phenylenediamine.
Derivatives of diamine (NN) can be used for carrying out method (M); such derivatives include notably salts thereof, equally able to form amide groups.
Diacid (AA) can be an aliphatic dicarboxylic acid [acid (AL)] or a dicarboxylic acid comprising at least one aryl or arylene group as defined above [acid (AR)]. Non limitative examples of diacids (AR) are notably phthalic acids, including isophthalic acid (IA), and terephthalic acid (TA), 2,5-pyridinedicarboxylic acid, 2,4-pyridinedicarboxylic acid, 3,5-pyridinedicarboxylic acid, 2,2-bis(4-carboxyphenyl)propane, bis(4-carboxyphenyl)methane, 2,2-bis(4-carboxyphenyl)hexafluoropropane, 2,2-bis(4-carboxyphenyl)ketone, bis(4-carboxyphenyl)sulfone, 2,2-bis(3-carboxyphenyl)propane, bis(3-carboxyphenyl)methane, 2,2-bis(3-carboxyphenyl)hexafluoropropane, 2,2-bis(3-carboxyphenyl)ketone, bis(3-carboxyphenoxy)benzene, naphthalene dicarboxylic acids, including 2,6-naphthalene dicarboxylic acid, 2,7-naphthalene dicarboxylic acid, 1,4-naphthalene dicarboxylic acid, 2,3-naphthalene dicarboxylic acid, 1,8-naphthalene dicarboxylic acid. Among acids (AL), mention can be notably made of oxalic acid (HOOC—COOH), malonic acid (HOOC—CH2—COOH), succinic acid [HOOC—(CH2)2—COOH], glutaric acid [HOOC—(CH2)3—COOH], 2,2-dimethyl-glutaric acid [HOOC—C(CH3)2—(CH2)2—COOH], adipic acid [HOOC—(CH2)4—COOH], 2,4,4-trimethyl-adipic acid [HOOC—CH(CH3)—CH2—C(CH3)2—CH2—COOH], pimelic acid [HOOC—(CH2)5—COOH], suberic acid [HOOC—(CH2)6—COOH], azelaic acid [HOOC—(CH2)7—COOH], sebacic acid [HOOC—(CH2)8—COOH], undecanedioic acid [HOOC—(CH2)9—COOH], dodecanedioic acid [HOOC—(CH2)10—COOH], tetradecanedioic acid [HOOC—(CH2)12—COOH], octadecanedioic acid [HOOC—(CH2)16—COOH], 2,5-furandicarboxylic acid and tetrahydrofuran-2,5-dicarboxylic acid. Preferably, diacid (AA) is an acid (AL), as above detailed. Preferred examples of acids (AL) are adipic acid and sebacic acid; more preferably, acid (AL) is adipic acid.
Derivatives of diacid (AA) can be used for carrying out method (M); such derivatives include notably salts, anhydrides, esters and acid halides, able to form amide groups.
Among suitable aminoacids (AN) for the manufacture of polyamide (PA), mention can be made of those selected from the group consisting of 6-amino-hexanoic acid, 9-aminononanoic acid, 10-aminodecanoic acid, 11-aminoundecanoic acid, 12-aminododecanoic acid. Derivatives of aminoacids (AN) can also be used for carrying out method (M); such derivatives include notably, salts, esters and acid halides, able to form amide groups.
Among suitable lactams (L) for the manufacture of polyamide (PA), mention can be made of β-lactam and ε-caprolactam.
Mixture (MN) is a mixture of fluoropolymers comprising a fully or partially fluorinated polyalkyleneoxy chain [(per)fluoropolyoxylakylene chain (Rf)] having two chain ends, wherein one or both chain ends comprise an amino group or a derivative thereof able to form amide groups, notably a salt. Mixture (MN) may also comprise negligible amounts of non-functional species, i.e. fully or partially fluorinated straight or branched polyalkyleneoxy chain [(per)fluoropolyoxylakylene chain (Rf) wherein both ends bear a non-functional group.
Mixture (MA) is a mixture of fluoropolymers comprising a fully or partially fluorinated straight or branched polyalkyleneoxy chain [(per)fluoropolyoxylakylene chain (Rf)] having two chain ends, wherein one or both chain ends comprise a —COOH group or a derivative thereof able to form amide groups; preferably, the derivative is an ester derivative. Mixture (MA) may also comprise negligible amounts of non-functional species, i.e. fully or partially fluorinated straight or branched polyalkyleneoxy chain [(per)fluoropolyoxylakylene chain (Rf) wherein both ends bear a non-functional group.
The amount of mono- and bifunctional polymers, and, optionally, non-functional polymers in mixtures (PFPE-M) is expressed by means of the average functionality [herein after (FB)], which is defined as:
(FB)=[2×moles of (PFPE-AA) or (PFPE-NN)+1×moles of (PFPE-A) or (PFPE-N)/(moles of non-functional PFPE+moles of (PFPE-A) or (PFPE-N)+moles of (PFPE-AA) or (PFPE-N)].
Average functionality (FB) can be calculated by means of 1H-NMR and 19F-NMR analyses according to methods known in the art, for example following the teaching of U.S. Pat. No. 5,910,614 (AUSIMONT SPA) with suitable modifications.
Typically, mixtures (PFPE-M) used in method (M) have an average functionality (FB) of at least 1.80; advantageously, (FB) ranges from 1.80 to 1.95, more advantageously from 1.85 to 1.90.
Chain (Rf) comprises recurring units R° having at least one catenary ether bond and at least one fluorocarbon moiety, said repeating units, randomly distributed along the chain, being selected from the group consisting of:
(i) —CFXO—, wherein X is F or CF3,
(ii) —CFXCFXO—, wherein X, equal or different at each occurrence, is F or CF3, with the proviso that at least one of X is —F,
(iii) —CF2CF2CW°2O—, wherein each of W°, equal or different from each other, is F, Cl, H,
(iv) —CF2CF2CF2CF2O—,
(v) —(CF2)j—CFZ*—O— wherein j is an integer from 0 to 3 and Z* is a group of general formula —ORf*T°, wherein Rf* is a fluoropolyoxyalkene chain comprising a number of repeating units from 0 to 10, said recurring units being chosen among the followings: —CFXO—, —CF2CFXO—, —CF2CF2CF2O—, —CF2CF2CF2CF2O—, with each of X being independently F or CF3 and T° being a C1-C3 perfluoroalkyl group.
Preferably, chain (Rf) complies with the following formula:
(CFX1O)g1(CFX2CFX3O)g2(CF2CF2CF2O)g3(CF2CF2CF2CF2O)g4— (Rf-I)
wherein:
More preferably, chain (Rf) is selected from chains of formula:
—(CF2CF2O)a1(CF2O)a2— (Rf-IIA)
wherein:
—(CF2CF2O)b1(CF2O)b2(CF(CF3)O)b3(CF2CF(CF3)O)b4— (Rf-IIB)
wherein:
b1, b2, b3, b4, are independently integers ≥0 such that the number average molecular weight is between 400 and 10,000, preferably between 400 and 5,000; preferably b1 is 0, b2, b3, b4 are >0, with the ratio b4/(b2+b3) being 1;
—(CF2CF2O)c1(CF2O)c2(CF2(CF2)cwCF2O)c3— (Rf-IIC)
wherein:
cw=1 or 2;
c1, c2, and c3 are independently integers ≥0 chosen so that the number average molecular weight is between 400 and 10,000, preferably between 400 and 5,000; preferably c1, c2 and c3 are all >0, with the ratio c3/(c1+c2) being generally lower than 0.2;
—(CF2CF(CF3)O)d— (Rf-IID)
wherein:
d is an integer >0 such that the number average molecular weight is between 400 and 10,000, preferably between 400 and 5,000;
—(CF2CF2C(Hal)2O)e1—(CF2CF2CH2O)e2—(CF2CF2CH(Hal)O)e3— (Rf-IIE)
wherein:
Still more preferably, chain (Rf) complies with formula (Rf-III) here below:
—(CF2CF2O)a1(CF2O)a2— (Rf-III)
wherein:
Mixture (PFPE-M) preferably complies with general formula (I) here below:
A-O—Rf-A′ (I)
wherein:
CF2-Lx-T
in which:
Typically, in groups CF2-Lx-T, x is 1 and linking group L comprises one of the following groups W, said group W being directly bound to the —CF2— group between chain (Rf) and linking group L: —CH2O—, —CH2OC(O)NH—, —CH2NR1— in which R1 is hydrogen or straight or branched C1-C3 alkyl, and —C(O)NH—. It has indeed been observed that monomers (B) wherein x is 1 are advantageous in that they are particularly reactive and compatible with amines (NN) and acids (AA) and in that they are also thermally and chemically stable.
Preferred examples of mixtures (PFPE-M) are those wherein A and/or A′ are selected from the following groups:
—CF2CH2O-alkylene-T; (a1)
—CF2CH2O(alkylene-O)n—C*alk-T; (b1)
—CF2CH2O-alkylene-C(O)NH-alkylene-T; (c1)
—CF2CH2NR1-alkylene-T; (d1)
—CF2CH2NR1(alkylene-NR1)n—C*alk-T; (e1)
—CF2CH2NR1-alkylene-C(O)O-alkylene-T; (f1)
—CF2CH2NR1-alkylene-C(O)NH-alkylene-T; (g1)
—CF2C(O)NH—(C*alk)-T (h1)
—CF2C(O)NH—(R*ali)-T; and (i1)
—CF2C(O)NH—(R*ar)-T (l1)
wherein:
In mixtures (PFPE-M) wherein A and/or A′ are groups of formula (b1), preferred (alkylene-O) moieties include —CH2CH2O—, —CH2CH(CH3)O—, —(CH2)3O— and —(CH2)4—.
Mixtures (PFPE-M) wherein x is 1 and L comprises a W group selected from —CH2O—, —CH2OC(O)NH— and —CH2NR1— in which R1 is hydrogen or straight or branched C1-C3 alkyl can be obtained using as precursor a PFPE alcohol of formula (II) below:
Y—O—Rf—Y′ (II)
wherein Rf is as defined above and Y and Y′, equal to or different from one another, represent a C1-C3 haloalkyl group, typically selected from —CF3, —CF2C1, —CF2CF2Cl, —C3F6Cl, —CF2Br and —CF2CF3 or a group of formula —CF2CH2OH.
Suitable PFPE alcohols of formula (II) can be prepared by photoinitiated oxidative polymerization (photooxidation reaction) of per(halo)fluoromonomers, as described in U.S. Pat. No. 3,715,378 (MONTECATINI EDISON S.P.A.) and U.S. Pat. No. 3,665,041 (MONTEDISON S.P.A.). Typically, mixtures of perfluoropolyethers can be obtained by combination of hexafluoropropylene and/or tetrafluoroethylene with oxygen at low temperatures, in general below −40° C., under U.V. irradiation, at a wavelength (A) of less than 3 000 Å. Subsequent conversion of end-groups as described in U.S. Pat. No. 3,847,978 (MONTEDISON S.P.A.) and in U.S. Pat. No. 3,810,874 notably carried out on crude products from photooxidation reaction. It is known to persons skilled in the art that PFPE alcohols (II) manufactured by photoinitiated oxidative polymerization are obtained as mixtures of bi- and mono-functional PFPE alcohols and non-functional (otherwise referred to as “neutral”) PFPEs. The monofunctional PFPE alcohols and the neutral PFPEs comprised in PFPE alcohols (II) have a C1-C3 haloalkyl group as defined above at one or both ends of chain Rf. Usually, the amount of neutral PFPEs is lower than 0.04% by moles with respect to the overall molar amount of bi-, mono-functional PFPE alcohols and neutral PFPEs. PFPE alcohols (II) are thus characterised by an average functionality (F°), defined as:
[(2×moles of bi-functional PFPE alcohol)+moles of monofunctional PFPE alcohol]/moles of bi-functional PFPE alcohol+moles of monofunctional PFPE alcohol+moles of neutral PFPE.
It will thus be understood by a person skilled in the art that, when a PFPE alcohol (II) having a functionality (F°) is used as precursor of a mixture (PFPE-M) by reaction with a suitable reaction partner at full conversion and 100% selectivity, the functionality of mixture (FB) will be equal to)(F°. Mixture (PFPE-M) will thus further comprise a PFPE-A or PFPE-N and neutral PFPEs wherein one of A or A′ or both A and A′ respectively is(are) the same as the C1-C3 haloalkyl group respectively present at one or both ends of the starting PFPE alcohol (II) [Y and Y′ in formula (II)].
Mixtures (PFPE-M) wherein W is —CH2O— can be obtained by reaction of PFPE alcohol (II) with a compound of formula E-B*-T, wherein E represents a leaving group, B* represents a group selected from Calk, R*ali and R*ar and T is amino or carboxy, optionally in a protected form. Suitable leaving groups E include halogens, preferably chlorine and bromine, and sulfonates like trifluoromethanesulfonate. Preferred protecting groups for —COOH groups are esters, while preferred protecting groups for —NH2 groups are amides and phthalimides. As an alternative, the terminal hydroxy groups in the PFPE alcohol of formula (II) can be transformed into a leaving group E as defined above and reacted with a compound of formula HO-B*-T wherein B* and T are as defined above.
Typically, mixtures (PFPE-M) wherein A and/or A′ represent groups of formula (a1) as defined above can be obtained by reaction of a PFPE alcohol (II) with a compound of formula E-C*alk-T, wherein E, C*alk and T are as defined above. A preferred example of mixture (PFPE-M) comprising (PFPE-AA) and (PFPE-A) wherein group (a1) is —CF2CH2O—CH2-T can be obtained by reaction of a PFPE-diol (II) with an ester of a 2-halo-acetic acid, for example with 2-chloroethyl acetate.
Mixtures (PFPE-M) wherein A and A′ represent groups of formula (b1) as defined above can be synthesised by condensation reaction of a PFPE alcohol (II) with a diol of the type HO-alkylene-OH or by ring-opening reaction of a PFPE alcohol (II) with ethylene oxide or propylene oxide, to provide a hydroxyl compound which is either reacted with compound of formula E-C*alk-T or submitted to conversion of the hydroxyl end groups into leaving groups E as defined above and reacted with a compound of formula HO—C*alk-T.
Mixtures (PFPE-M) wherein A and A′ represent groups (c1) as defined above can be synthesised by reaction of a Mixture (PFPE-M) wherein A and/or A′ represent groups —CF2CH2O-alkylene-COOH or derivative thereof with a diamine or aminoacid of formula NH2-alkylene-T, wherein alkylene and T are as defined above.
Mixtures (PFPE-M) wherein x is 1 and L comprises a W group of formula —CH2NHR1— in which R1 is as defined above can be obtained by reaction of a PFPE alcohol (II), whose hydroxyl end groups E have been transformed into leaving groups E, with a compound of formula R1HN-B*-T wherein R1, B* and T are as defined above.
For example, mixtures (PFPE-M) wherein A and/or A′ represent groups of formula (d1) as defined above can be synthesised by reaction of a PFPE alcohol (II) with an amine of formula R1NH-alkylene-T, wherein R1 and alkylene are as defined above and wherein T is optionally in a protected form.
Mixtures (PFPE-M) wherein A and/or A′ represent groups of formula (e1) as defined above can be synthesised by reaction of a PFPE alcohol (II) with a polyamine of formula R1NH— (alkylene-NR1)n-1alkylene-NHR1, wherein n and R1 are as defined above, followed by reaction with a compound of formula E-C*alk-T, wherein E, C and T are as defined above.
Mixtures (PFPE-M) wherein A and/or A′ represent groups of formula (f1) as defined above can be synthesised by reaction of a PFPE alcohol (II) with an aminoacid of formula R1NH-alkylene-T, followed by reaction with a compound of formula HO-alkylene-T, wherein R1 and T are as defined above.
Mixtures (PFPE-M) wherein A and/or A′ represent groups of formula (g1) as defined above can be synthesised by reaction of a PFPE alcohol (II) with an aminoacid of formula R1NH-alkylene-COOH, followed by reaction with a compound of formula NH2-alkylene-T, wherein R1 and T are as defined above.
As an alternative, mixtures (PFPE-M) wherein x is 1 and L comprises a W group of formula —CH2NHR1— in which R1 is as defined above can be obtained by converting a PFPE alcohol (II) into the corresponding sulfonic ester derivative, by reaction, for example, with CF3SO2F and reacting the sulfonic diester with anhydrous liquid ammonia to provide a PFPE diamine of formula (III) below:
Y′—O—Rf—CF2CH2NH2 (III)
wherein Rf is as defined above and Y′ is —CF2CH2NH2 or is the same as Y as defined above.
PFPE diamine (III) can be reacted with a compound of formula E-B*-T, wherein E, B* and T are as defined above.
Mixtures (PFPE-M) wherein x is 1 and L comprises a W group of formula —C(O)NH— can be obtained using as precursor a PFPE diacid of formula (IV) below:
Y″—O—Rf—CF2COOH (IV)
in which Rf is as defined above and Y″ is —CF2COOH or is the same as Y as defined above
or a reactive derivative thereof, preferably an ester derivative, typically a methyl or ethyl ester derivative.
Suitable PFPE ester derivatives of PFPE acids (IV) can be conveniently obtained as disclosed, for example, in U.S. Pat. No. 5,371,272 (AUSIMONT SPA). It is known to persons skilled in the art that, similarly to PFPE alcohols (II), also PFPE acids (IV) are obtained as mixtures of bi-, mono-functional and neutral species and that the functionality of PFPE acids (IV) used as precursor of mixtures (PFPE-M) affects the functionality (FB) of such mixtures in the same way as explained above for PFPE diols (II).
PFPE acids (IV) or reactive derivatives thereof can be reacted with compounds of formula N2H-B*-T, wherein B* and T are as defined above.
In particular, mixtures (PFPE-M) wherein A and A′ comply with formulae (h1)-(l1) as defined above can be prepared by reaction of an ester derivative of an acid (IV) with a compound of formula NH2—(C*alk)-T, NH2—(R*ali)-T or NH2—(R*ar)-T.
For the sake of clarity and accuracy, it is pointed out that, in certain instances, the synthesis of mixtures (PFPE-M) of formula (I) above can lead to the formation of a certain amount of dimeric or polymeric by-products; for example, in the synthesis of a mixture wherein A and/or A′ represent groups of formula:
—CF2CH2O-alkylene-C(O)NH-alkylene-NH2; (c″*)
dimeric by products of formula:
A-O—Rf—CF2CH2O-alkylene-C(O)NH-alkylene-NH(O)C-alkylene-OCH2CF2—Rf—O-A
are obtained, due to the reaction of a diamine of formula: H2N-alkylene-NH2 with diacid of formula: HOOC-alkylene-O—CH2CF2—O—Rf—CF2CH2O-alkylene-COOH in a molar amount of 1 to 2.
Furthermore, in the synthesis of a (PFPE-MN) by reaction of a PFPE alcohol with an amine of formula R1NH-alkylene-NH2 in which R1 is other than hydrogen, mixtures of regioisomers, for instance those of formulae: H2N-alkylene-N(R1)—CH2CF2—O—Rf—CF2CH2—N(R1)-alkylene-NH2. (R1) HN-alkylene-NH— CH2CF2—O—Rf—CF2CH2—NH-alkylene-NH(R1) can be obtained.
Thus, for the purposes of the present invention, the expressions “PFPE-MN”, “PFPE-MA”, are meant to encompass also any dimeric or polymeric by-products or regioisomers which may be formed in their synthesis.
Amine (N′) is at least one primary or secondary hydrogenated aliphatic, cycloaliphatic or aromatic amine or a derivative thereof.
Typically, amine (N′) complies with formula (N′-I):
R—NH—R2 (N′-I)
wherein:
Preferably, amine (N′) is at least one straight or branched primary alkylamine having from 1 to 36 carbon atoms. More preferably, amine (N′) is selected from: methylamine, ethylamine, propylamine, butylamine, pentylamine, hexylamine, heptylamine, octylamine, nonylamine, decylamine, undecylamine, docedylamine and trydecylamine, being understood that all these terms include all existing straight and branched structural isomers. For example, “propylamine” includes 1-aminopropane and 2-amino-propane; “butylamine” includes 1-aminobutane, 2-aminobutane, 1-amino-2-methyl-propane and so on.
Derivatives of amine (N′) that can be used for carrying out method (M) include notably salts thereof, equally able to form amide groups.
Acid (A′) is a hydrogenated aliphatic, cycloaliphatic or aromatic monocarboxylic acid or a derivative thereof. According to one embodiment, acid (A′) is at least one straight or branched aliphatic acid comprising from 1 to 26 carbon atoms; preferably, acid (A′) is selected from ethanoic acid (acetic acid), propanoic acid, butanoic acid, pentanoic acid, hexanoic acid, heptanoic acid, octanoic acid, nonanoic acid, decanoic acid, dodecanoic acid and tridecanoic acid, being understood that all these terms include all existing straight or branched structural isomers. For example, “butanoic acid” includes 1-butanoic acid and 2-methylpropanoic acid. Preferably, hydrogenated aliphatic acid (A′) is acetic acid.
According to another embodiment, acid (A′) is an aromatic acid comprising at least one 5- or 6-membered aromatic ring wherein one sp2 carbon atom bears a carboxy group covalently bound thereto and wherein one or more carbon atoms of the ring can be replaced with a heteroatom, said ring being optionally condensed with or covalently bound to, another 5- or 6-membered aromatic ring. The at least one aromatic ring can optionally be substituted on one or more sp2 carbon atoms with a straight or branched alkyl group, preferably a C1-C4 alkyl group. Example of suitable aromatic acids are benzoic acid, 2-methyl benzoic acid, 3-methyl benzoic acid, 4-methyl benzoic acid, 2,3-dimethyl benzoic acid, 2,4-dimethyl benzoic acid, 2,5-dimethyl benzoic acid, 2,6-dimethyl benzoic acid, 2,3,4-trimethyl benzoic acid, 2,3,5-trimethyl benzoic acid, 2,3,6 trimethylbenzoic acid and 3,4,5-trimethyl benzoic acid. Preferably, hydrogenated aromatic acid (A′) is benzoic acid.
Method (M) can be carried out according to procedures known in the art for the synthesis of polyamides. Preferably, monomers (A), (B) and compound (C) are mixed together in a reactor under nitrogen atmosphere in the absence of solvents to form a reaction mixture (MR) and heated at temperatures that can range from 50° C. to 300° C. for a time ranging from 1 to 10 hours. Typically, the progress of the reaction is monitored by checking the torque of the reaction mixture; usually, when the torque value reaches a plateau, the reaction is regarded as complete. At the end of the reaction, the resulting fluorinated polyamide (F-PA), which is in the form of a molten mass, is poured into ice-cold water and then separated.
The kind and amounts of monomers (A), (B) and compound (C) will be selected by a person skilled in the art in such a way as the average functionality (FRM) as defined above is lower than 1.96. Advantageously, (FRM) will be selected in the range from 1.90 to 1.95.
Preferably, monomer (A) is a mixture of a diamine (NN), preferably an aromatic diamine (NN), with a diacid (AA), preferably an aliphatic dicarboxylic acid (AA); in one preferred embodiment, monomer (A) is a mixture of MXDA with adipic acid.
Monomer (B) is preferably a mixture (MA). More preferably, mixture (MA) is a mixture of formula (I) as defined above wherein A and/or A′ are a group (a1). Still more preferably, mixture (MA) is a mixture of formula (I) as defined above in which A and/or A′ are a group (a1) of formula —CF2CH2OCH2COOH or a derivative thereof able to form amide groups, preferably an ester group, more preferably an ethyl ester group, and chain Rf is as defined above, preferably a chain (Rf-III). It has indeed been observed that fluorinated polyamides (F-PA) obtained using such mixture (M) are particularly stable to hydrolysis.
Preferably, compound (C) is an acid (A); preferred examples of acids (A) are acetic acid and benzoic acid.
The amount of monomers (A), (B) and (C) is selected in such a way as to achieve full balance between the equivalents of acid and amino groups (or derivatives thereof); in other words, the amount of said monomers is selected in such a way as the ratio between the equivalents of acid groups and amino groups is 1:1.
Monomer (B) is used in an equivalent amount preferably ranging from 0.50% to 20% with respect to monomer (A). Preferably, (PFPE-M) has an average functionality (FB) ranging from 1.80 to 1.99, more preferably from 1.90 to 1.95 and an average molecular weight Mn ranging from 400 to 2,000.
Compound (C) is preferably used in an equivalent amount ranging from 2% to 6% with respect to monomer (A).
A further aspect of the invention is represented by the fluorinated polyamides (F-PA) which can be obtained by method (M). The polyamides (F-PA) typically have an average molecular weight (Mw) lower than 16,000, preferably ranging from 8,000 to 16,000 and contain a weight amount of PFPE segments ranging from 5% to 50% wt with respect to the molecular weight of the polyamide, preferably from 5% to 40% wt, more preferably from 5% to 30% wt, even more preferably from 5% to 20% wt with respect to the weight of the polyamide. Average molecular weight (Mw) can be determined by gel permeation chromatography (GPC), according to methods known in the art.
The polyamides (F-PA) consist of recurring units deriving from monomers (A) and (B) and an end-capping group deriving from compound (C) and/or a (PFPE-N) and/or (PFPE-A) present in monomer (B).
Thus, polyamides (F-PA) according to the present invention consist of recurring units deriving from:
(a) a monomer (A), selected from at least one of:
(i) a mixture of:
Preferred polyamides (F-PA) are those wherein monomer (A) is a mixture of diamine (NN) and diacid (AA) and monomer (B) is a mixture (MN). Advantageously, diamine (NN) is MXDA and diacid (AA) is adipic acid.
Advantageously, the end-capping group derives from a compound (C) that is an acid (A′), preferably from benzoic acid or acetic acid.
Polyamide Blends [Blends (B)] Comprising Polyamides (F-PA), Shaped Articles Obtainable Therefrom and Methods for their Manufacture
In a further aspect, the present invention relates to blends (B) comprising a polyamide (F-PA) and a polyamide other than a polyamide (F-PA). Such other polyamide is preferably a hydrogenated polyamide [polyamide (H-PA)]obtainable by copolymerization reaction of:
(i) one or more hydrogenated aliphatic, cycloaliphatic or aromatic diamine(s) [diamine (NN)] or derivative(s) thereof with one or more hydrogenated aliphatic, cycloaliphatic or aromatic dicarboxylic acid(s) [diacid (AA)] or derivative(s) thereof; or
(ii) one or more aminoacid(s) [aminoacid (AN)] or derivative(s) thereof or lactam(s) [lactam (L)]
wherein diamine (NN), dicarboxylic acid (AA), aminoacid (AN) or derivative(s) thereof and lactam (L) are as defined above.
Diamine (NN), diacid (AA) and aminoacid (AN), independently from one another, can be equal to or different from those used for the preparation of polyamide (F-PA).
It has indeed been observed that, thanks to the structural features of polyamide (F-PA), namely molecular weight lower than 16,000 and content of PFPE segments, they can be used as additives for other polyamides to prepare blends and shaped articles that are endowed with improved hydro-/oleo-repellence and resistance to stain, improved chemical resistance and high impact strength.
Non-limiting examples of (H-PA) for the preparation of blends (B) are:
In a preferred embodiment, polyamide (H-PA) results from the polycondensation of an aromatic diamine (NN) and with an aliphatic dicarboxylic acid (AA). A preferred (H-PA) of this sort is a polyamide obtained by polycondensation of MXDA with adipic acid.
Blends (B) can also contain other ingredients and/or additives commonly known in the art. Non-limiting examples of further ingredients and/or additives include heat-stabilizers, light and UV-light stabilizers, hydrolysis stabilizers, anti-oxidants, lubricants, plasticizers, colorants, pigments, antistatic agents, flame-retardant agents, nucleating agents, catalysts, mold-release agents, fragrances, blowing agents, viscosity modifiers, flow aids, reinforcing fibers and the like. Among reinforcing fibers, carbon fibers and glass fibers can be mentioned. The kind and amount of ingredients and/or additives will be selected by the skilled person according to common practice, for example following the teaching of ZWEIFEL, H, et al. Plastics Additives Handbook. 5th edition. Edited by HANSEL. Munich: Hanser, 2001. ISBN 1569901449.
Preferred blends (B) comprise, preferably consist of:
(a) one or more polyamide (F-PA) as defined above
(b) one or more hydrogenated polyamide (H-PA) as defined above; and
(c) one or more glass fibers.
Typically, blends (B) contain from 1% to 5% wt polyamide (F-PA), from 35% to 99% polyamide (H-PA) and from 30% to 60% wt glass fiber.
Blends (B) can be prepared and formed into shaped articles by techniques known in the art for the manufacture and shaping of plastics, such as for example molding methods, including injection molding, extrusion, blow molding and rotational molding.
Shaped articles obtained from blends (B) include those for automotive, electrical and electronic applications and packages.
The invention will be illustrated in greater detail in the following Experimental Section by means of non-limiting Examples.
Should the disclosure of any patents, patent applications, and publications which are incorporated herein by reference conflict with the description of the present application to the extent that it may render a term unclear, the present description shall take precedence.
A mixture (PFPE-M) [(herein after PFPE ester (E-1)]
comprising the difunctional PFPE ester of formula:
EtO(O)CCH2OCH2O—RF—CH2OCH2C(O)OEt
wherein RF=CF2(OCF2)m(OCF2CF2)nOCF2 with n/m=1 and n+m selected in such a way as Mn=1,864 (determined by NMR) average functionality (FB)=1.87 and equivalent weight (Ew)=997
was prepared following a procedure analogous to the one disclosed in Example 1 of WO 2015/097076 by reaction of a corresponding PFPE alcohol (II) with functionality 1.87 and ethyl chloroacetate.
A mixture [(herein after PFPE ester (E-2)]
of bi- and mono-functional PFPE esters and neutral PFPEs comprising the PFPE ester of formula:
EtO(O)C—RF—C(O)OEt
as difunctional species
wherein RF=CF2(OCF2)m(OCF2CF2)nOCF2 with n/m=1 and n+m selected in such a way Mn=1,500, Ew=802 average functionality (FB)=1.87, was prepared according to methods known in the art.
Non fluorinated polyamide MXD6 was obtained by copolymerization of a mixture of adipic acid and m-xylene diamine in equivalent amounts according to methods known in the art. This polyamide has a Mn=24,000, a Mw=54,874, a polydispersity index of 2.29 and an acidic content of 108 meq/kg.
Glass fiber OCV EC10 983 is available from Oven Cornings®.
The other reagents and solvents are commercially available and were used as received from the manufacturer.
The polyamides of the Examples and Comparative Examples and polyamide MXD6 were completely dissolved in hexafluoroisopropanol (HFIPA) containing 0.05M potassium trifluoro acetate (KTFAT). Any fillers and insoluble additives then filtered through 0.2 micron PTFE disposable syringe filters. The filtered solutions were separated on a size exclusion chromatography (SEC) system consisting of a Waters HPLC pump (model no. 515), Shodex refractive index (RI) detector (model no. 109), Waters column oven (capable for room temperature to 150° C.) maintained at 40° C. during the analysis, set of two mini mixed B SEC columns and mini mix B guard column (from Agilent), Clarity SEC integration software (Version 5.0.00.323). Mobile phase—HFIPA/0.05M potassium trifluoro acetate (KTFAT) at a flow rate of 0.4 mL/minute. The system was calibrated using the set of narrow polydispersed PMMA standard samples. The molecular weights were calculated using a calibration file generated using PMMA standards with the aid of a Clarity SEC integration software.
About 0.3 g polyamide was weighed in a glass vial with a magnetic stirring bar and dissolved in 6 mL o-cresol with heating at 100° C. After dissolution, the sample was cooled and diluted with 6 mL chloroform. 50 μL formaldehyde was added with a syringe to react with the amine end groups so as to suppress salt formation between the carboxyl and amine end groups. The carboxyl end groups were then titrated with standard 0.05N KOH in methanol using a combination glass electrode with sleeve junction. The acidic end group concentration was calculated from titration data and titrant normality, according to the following calculation:
Acidic value (meq/g)=(Volume of titrant (mL)×Normality of KOH×1000)/sample weight (g)
About 1 g polyamide composition was placed in a pre-weighed quartz fibre crucible. The crucible was then placed in a microwave furnace (Phoenix Airwave Microwave furnace from OEM). The temperature program was as follows:
heating from room temperature to 500° C. in 2 hrs;
maintained at 500° C. for 2 minutes;
500° C. to 600° C. in 30 minutes;
maintained at 600° C. for 90 minutes;
cooling from 600° C. to room temperature in 2 hrs.
Once the furnace was cooled to room temperature, the crucible was removed and re-weighed using an analytical balance.
The glass filler content was calculated by means of the following formula:
% Glass filler=[(Wt. of residue+Wt. of empty crucible)−Wt. of empty crucible]*100/[(Wt. of sample+Wt. of empty crucible)−Wt. of empty crucible].
Static contact angles of the polyamide blends (B-1)-(B-4), (B-1bis), reference blends (B-1a)-(B-4a) were measured against 2 μl water on a 2 mm fibre-reinforced injection molded slabs using a Dataphysics Contact Angle System OCA 20 instrument using the Sessile drop method. The images were captured after a fixed time of 10 seconds after dispensing the liquid. Multiple data points (16-20) were collected and the average and standard deviation was calculated.
In order to measure the melt flow, an injection mold with a spiral flow was used. This mold was marked to measure the length (in mm) or the distance travelled by the polyamide blends during injection molding. Alternatively, the spiral mold specimen was weighed to measure the amount of polyamide in grams.
1 g test polyamide and 1.5 equivalents NaOH (0.1 M solution) were charged in a flask equipped with magnetic stirrer and condenser. The resulting mixture was left under stirring at room temperature for 3 weeks.
The amide group hydrolysis was determined by treatment with an excess of HCl and back titration of the resulting ammonium salt with a 0.1N solution of tetrabutylammonium hydroxide in isopropyl alcohol.
Adipic acid (91.8 g, 0.63 mol, 1.26 eq), benzoic acid (15.0 g, 0.12 mol, 0.12 eq), xylylenediamine (MXDA, 47.65 g, 0.35 mol, 0.7 eq) and PFPE-ester (E-1) (18.8 g, 0.01 mol, 0.02 eq)
were placed in a 1 L four-necked cylindrical glass kettle equipped with a mechanical stirrer, condenser and nitrogen inlet and immersed in an oil bath. Temperature was raised to 100° C., then further 47.65 g of MXDA was added with continuous stirring and the bath temperature was raised up to 200° C. The reaction slurry at 200° C. was then heated up to the final oil bath temperature of 275° C. at the rate of 10° C./5 min. Once this temperature was reached, the reaction was continued until the required torque reached a plateau. The resulting melt was poured from the kettle by quenching in ice-cold water to provide a polymer mass. The mass was then dried and ground for further analyses.
The acidic content was 94 meq/kg and amine groups were not detected.
Following the procedure of Example 1, a polyamide was prepared with the following reagents:
adipic acid: 99.2 g, 0.68 mol, 1.36 eq;
MXDA: 90.6 g, 0.66 mol, 1.32 eq;
PFPE ester (E-1): 38.58 g, 0.02 mol, 0.04 eq.
The acidic content was 370 meq/kg and the content of amine groups was 5 meq/kg.
The following reagents:
adipic acid: 460.5 g, 3.15 mol, 6.30 eq;
MXDA: 456.9 g, 3.42 mol, 6.84 eq;
PFPE ester (E-1): 192.3, 0.10 mol, 0.20 eq;
acetic acid: 20.0 g, 0.33 mol, 0.33 eq
were charged in an autoclave at a pressure of 4.5 Pa and at a temperature from 30° C. to 250° C. for 3 hours. The reaction was considered complete when the torque value reached a plateau. Upon completion of the reaction, the resulting melt was discharged from the autoclave and processed as according to Example 1.
The acidic content was 125 meq/kg, which corresponded to a conversion of the starting acidic groups of about 98%.
Following the procedure of Example 1, a polyamide was prepared with the following reagents:
adipic acid: 99.2 g, 0.68 mol, 1.36 eq;
MXDA: 96.0 g, 0.70 mol, 1.40 eq;
PFPE ester (E-1): 38.6 g, 0.02 mol, 0.04 eq.
The acidic content was 107 meq/kg and the amine group content was 32 meq/kg.
This polyamide was prepared with the following reagents:
adipic acid: 460.48 g, 3.151 mol, 6.30 eq;
MXDA: 458.3 g, 3.37 mol, 6.73 eq;
PFPE ester (E-1): 95 g, 0.051 mol, 0.102 eq;
acetic acid: 20.0 g, 0.333 mol, 0.33 eq
according to the procedure of Example 2.
The acidic content was 87 meq/kg and the amine group content was 22 meq/kg.
This polyamide was prepared according to the procedure of Example 1 with the following reagents:
adipic acid: 460.5 g, 3.15 mol, 6.30 eq,
MXDA: 435.8 g, 3.20 mol, 6.40 eq,
PFPE ester (E-1): 95.0 g, 0.05 mol, 0.10 eq.
The acidic content was 125 meq/kg and the amine group content was 36 meq/kg.
This polyamide was prepared according to the procedure of Example 1 with the following reagents:
adipic acid: 89.9 g, 0.61 mol, 1.23 eq
MXDA: 95.3 g, 0.70 mol, 1.4 eq
benzoic acid: 15.0 g, 0.12 mol, 0.12 eq
PFPE ester (E-1): 46.0 g, 0.02 mol, 0.05 eq.
The acidic group content was 179 meq/kg and the amine group content was 12 meq/kg.
This polyamide was prepared according to the procedure of Example 1 with the following reagents:
adipic acid: 99.22 g, 0.678 mol, 1.36 eq;
MXDA: 95.3 g, 0.70 mol, 1.40 eq;
PFPE ester (E-1): 38.58 g, 0.021 mol, 0.040 eq.
The acidic group content was 80 meq/kg and the amine group content was 164 meq/kg.
This polyamide was prepared with the same reagents as example 1, except that PFPE ester (E-2) was used.
The acid content was 90 meq/kg, which corresponded to a conversion of the starting acidic groups of about 99%.
This polyamide was prepared with the following reagents:
The content of acid groups was 108 meq/kg and the content of amine groups was 25 meq/kg.
It stems from Examples 1-4 according to the invention and from comparative Examples 1A-4A that, if compound (C) is not used and the average functionality (FRM) of the reaction mixture is higher than 1.96, the resulting polyamide has a molecular weight (Mw) higher than 20,000.
Non fluorinated polyamide MXD6 was blended with the fluorinated polyamides of Examples 1-4 and 1A-4A by means of two extrusion cycles.
1st cycle: mixing of MXD6 with the fluorinated polyamides of Examples 1-4 and 1A-4A to provide a first blend;
2nd cycle: coextrusion of OCV EC10 983 glass fiber (4.5 mm) with the first blend (30-60% wt glass fiber with respect to the mixture). The polyamides first blends were fed to the first barrel of zone-1 of an extruder comprising of 12 zones through a loss-in-weight feeder. The barrel settings were in the range of 220-250° C. The glass fibre was fed from zone 7 through a side stuffier via a loss-in-weight feeder. The screw rate was 100 rpm. The extrudates were cooled and pelletized using conventional equipment. The glass fiber content was determined by the ashing technique disclosed in the Methods section.
For the purpose of comparison, MXD6 was blended with glass fibers only according to the coextrusion cycle 2 described above.
The extruded fluorinated polyamides were molded in a Sumitomo 75 TON injection molding machine. The temperature range was 265-280° C. The mold temperature controller was set to 140-165° C. The cooling cycle time was fixed to 35-50 sec. Under these conditions, appropriate specimens such as ISO tensile test pieces (165×10×4 mm), ISO impact bars (unnotched: 80×10×4 mm), notched: 80×8×4 mm) and color plaques (75×50×2.6 mm) were molded.
Polyamide blends (B-1)-(B-4), (B-1bis), (Comparative Blends (B-1a)-(B1-d) and Reference blend (BR) were prepared according to the above-described general procedure. The ingredients and the glass fiber content (GF) of each blend are reported in the table below.
Contact angles versus water of specimens obtained from the polyamide blends of the invention, from the comparative blends and from the reference blends were measured according to the procedure disclosed in the Methods section. The results are reported in the Table below.
The results show that the contact angles of the blends according to the invention are higher than those of reference blend BR and of the comparative blends.
The results of the spiral flow length test are reported in the Table below for reference blend BR, (B-2) according to the invention and comparative composition (B-2a).
The length (distance travelled) or the weight for polyamide blend (B-2) according to the invention in the spiral mold was higher (which means better and easier flow), than that of reference blend (BR) and of comparative blend (B-2a).
This test was carried out to show the improved resistance of polyamide of comprising PFPE segments derived from PFPE ester (E-1) (in which the ester groups are bound to the PFPE chain via a hydrogenated ether spacer) with respect to that of polyamides comprising PFPE segments derived from PFPE ester (E-2) (in which the ester groups are directly bound to the PFPE chain).
The polyamides of Examples 1 and 5 were submitted to the stability test described above. The polyamide of Example 5 underwent about 8% hydrolysis, while the polyamide of Example 1 underwent about 1% hydrolysis.
All molded specimens were tested as “dry as molded”. For this purpose, the specimens were stored after injection molding for at least 48 h at room temperature in a desiccator in sealed aluminium bags. The tensile properties of the materials were measured according to ISO 527 test procedure, while the notched and unnotched Izod impact strengths were measured according to the ISO 180 test procedure. The table below reports the impact strength data for unnotched and notched specimens.
Number | Date | Country | Kind |
---|---|---|---|
4223/MUM/2015 | Nov 2015 | IN | national |
16150135.8 | Jan 2016 | EP | regional |
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/EP2016/076070 | 10/28/2016 | WO | 00 |