WO2000009571A1 - Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide - Google Patents

Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide Download PDF

Info

Publication number
WO2000009571A1
WO2000009571A1 PCT/US1999/018513 US9918513W WO0009571A1 WO 2000009571 A1 WO2000009571 A1 WO 2000009571A1 US 9918513 W US9918513 W US 9918513W WO 0009571 A1 WO0009571 A1 WO 0009571A1
Authority
WO
WIPO (PCT)
Prior art keywords
nylon
polyamide
silicate
mixture
polymerization
Prior art date
Application number
PCT/US1999/018513
Other languages
English (en)
Inventor
Lloyd A. Goettler
Saikat S. Joardar
John C. Middleton
Bruce A. Lysek
Original Assignee
Solutia Inc.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Solutia Inc. filed Critical Solutia Inc.
Priority to CA002331670A priority Critical patent/CA2331670A1/fr
Priority to AU55621/99A priority patent/AU5562199A/en
Priority to EP99942188A priority patent/EP1086144A1/fr
Publication of WO2000009571A1 publication Critical patent/WO2000009571A1/fr

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
    • C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
    • C08G69/04—Preparatory processes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00—Use of pretreated ingredients
    • C08K9/08—Ingredients agglomerated by treatment with a binding agent

Definitions

  • This invention relates to a process to prepare a nanocomposite material comprising a polymer matrix having dispersed therein a silicate. More particularly, this invention relates to a process to prepare a nanocomposite material comprising forming a flowable mixture of a polyamide and a silicate material, dissociating the silicate, and subjecting the dissociated flowable mixture to a solid state polymerization step to produce the nanocomposite material.
  • BACKGROUND OF THE INVENTION International Application WO 93/04118 discloses a process of preparing a polymer nanocomposite having platelet particles dispersed therein.
  • the process involves melt-processing the polymer with a swellable and polymer-compatible intercalated layered material and subjecting it to a shear rate sufficient to dissociate the layers.
  • the layered material is compatibilized with one or more "effective swelling/compatibilizing agents" having a silane function or an onium cation function.
  • the selected swelling/compatibilizing agents "...render their surfaces more organophilic than those compatibilized by tertiary and quaternary ammonium ion complexes", facilitate exfoliation, resulting in less shear in mixing and less decomposition of the polymer, and heat stabilize the composite more than other cations (such as quaternary ammonium cation) swelling/compatibilizing agents.
  • International Patent Application WO 94/22430 discloses a nanocomposite composition having a polymer matrix comprising at least one gamma phase polyamide, and dispersed in the polyamide is a matrix of a nanometer-scale particulate material.
  • the addition of the particulate material to nylon 6 resulted in an improvement of flexural modulus and fiexural strength (from 7 to 35%), when compared to unfilled nylon 6.
  • International Patent Application WO 93/10098 discloses a polymer composite made by melt-processing a polymer with swellable and polymer-compatible intercalated layered material comprising layers having reactive organo- silane species covalently bonded to their surfaces.
  • International Patent Application WO 95/14733 discloses a method of producing a polymer composite that does not demonstrate melting or glass transition by melt-processing a polymer with a layered gallery-containing crystalline silicate.
  • the examples include intercalated sodium silicate and a crystalline poly(ethylene oxide), montmorillonite intercalated with a quaternary ammonium and polystyrene, and montmorillonite intercalated with a quaternary ammonium and nylon 6.
  • U.S. Patent No. 5,514,734 (issued May 7, 1996) describes polymer composites containing layered or fibrillar particles derivatized with organosilanes, organotitanates, or organozirconates. Composite materials are characterized by thickness, diameter, and interlayer distances.
  • International Patent Application WO 93/11190 describes a polymer composite containing an exfoliated material derivatized with a reactive organosilane. Polymers are added prior to mixing in an extruder.
  • International Patent Application WO 94/11430 describes gamma crystalline phase polyamides containing dispersed layered inorganic materials.
  • EPO application 0 358 415 A1 describes a polyamide resin containing a dispersed layered silicate which has been treated with an organic cation of a lactam as a swelling agent.
  • Japanese Kokai Patent No. SHO 62[1987]-252426 describes polymerization of a nylon 6 monomer in the presence of a silicate. The cooling rate of the polymer is controlled to achieve particular crystalline structures in the resulting composite.
  • This invention relates to a process to prepare a polymer nanocomposite composition suitable for automotive, electronic, film and fiber applications, where a combination of tensile strength, tensile modulus and flexural modulus are required. Additionally, the claimed polymer nanocomposite composition has a desirable surface appearance, toughness, ductility and dimensional stability. The composition processes well and tolerates a wide range of molding conditions.
  • the present invention relates to a process to prepare the above polymer nanocomposite composition comprising forming a flowable mixture of a polyamide and a silicate material and dissociating (as that term is described in more detail below) at least about 50% but not all of the silicate, and subjecting the polyamide in the dissociated flowable mixture to a solid state polymerization step.
  • the silicate is a silicate material treated with at least one ammonium ion of the formula: NR 1 R 2 R 3 R 4 wherein:
  • Ri, R 2 , R 3 and R_t are independently selected from a group consisting of a saturated or unsaturated Ci to C 2 hydrocarbon, substituted hydrocarbon and branched hydrocarbon, or where Ri and R 2 form a N,N-cyclic ether.
  • Examples include saturated or unsaturated alkyls, including alkylenes; substituted alkyls such as hydroxyalkyls, alkoxyalkyls, alkoxys, amino alkyls, acid alkyls, halogenated alkyls, sulfonated alkyls, nitrated alkyls and the like; branched alkyls; aryls and substituted aryls, such as alkylaryls, alkyoxyaryls, alkylhydroxyaryls, alkylalkoxyaryls and the like.
  • one of Ri, R , R 3 and R 4 is hydrogen.
  • the milligrams of treatment per 100 grams of silicate (MER) of the treated silicate is preferably from about 10 milliequivalents/100 g below the cation exchange capacity of the untreated silicate to about 30 milliequivalents/100 g above the cation exchange capacity of the untreated silicate.
  • An additional embodiment of the invention relates to nanocomposite compositions comprising a polyamide and a silicate.
  • the polyamide may have a concentration of amine groups at least 10 mole % greater than the concentration of the carboxylic acid end groups.
  • the polyamide has a weight average molecular weight in the range of about 30,000 D to about 40,000 D.
  • the polyamide may have a weight average molecular weight of at least 40,000 D.
  • a further embodiment is directed towards a nanocomposite composition
  • a nanocomposite composition comprising a polyamide and a silicate, wherein the silicate is treated with an ammonium ion of the formula: wherein R a , R D and R ⁇ is hydrogen (H) and and R d includes a carboxylic acid moiety.
  • the composite polymer matrix material of the present invention demonstrates, when tested, an improvement in tensile modulus and flexural modulus, without a substantial decrease in tensile strength or toughness when compared to that of the polymer without the silicate.
  • Polyamides of the present invention are synthetic linear polycarbonamides characterized by the presence of recurring carbonamide groups as an integral part of the polymer chain which are separated from one another by at least two carbon atoms.
  • Polyamides of this type include polymers, generally known in the art as nylons, which can be obtained from diamines and dibasic acids having the recurring unit represented by the general formula:
  • R 5 is an alkylene group of at least 2 carbon atoms, preferably from about 2 to about 11 or arylene having at least about 6 carbon atoms, preferably about 6 to about 17 carbon atoms; and R ⁇ 5 is selected from R 5 and aryl groups.
  • copolyamides, terpolyamides and the like obtained by known methods, for example, by condensation of hexamethylene diamine and a mixture of dibasic acids consisting of terephthalic acid and adipic acid.
  • Polyamides of the above description are well-known in the art and include, for example, polyQiexamethylene adipamide) (nylon 6,6), poly(hexamethylene sebacamide) (nylon 6,10), poly(hexamethylene isophthalamide), poly(hexamethylene terephthalamide), poly(heptamethylene pimelamide) (nylon 7,7), poly(octamethylene suberamide) (nylon 8,8), poly(nonamethylene azelamide) (nylon 9,9), poly (decamethylene sebacamide) (nylon 10,9), poly(decamethylene sebacamide) (nylon 10,10), poly [bis(4-amino cyclohexyl)methane-l,10-decanecarboxamide)], poly(m-xylene adipamide), poly(p-xylene sebacamide), poly(2,2,2-trimethyl hexamethylene terephthalamide), poly(piperazine sebacamide), poly(p-phenylene terephthalamide), poly(
  • useful polyamides are those formed by polymerization of amino acids and derivatives thereof, as for example, lactams.
  • Illustrative of these useful polyamides are poly(caprolactam) (nylon 6), poly(4-aminobutyric acid) (nylon 4), poly(7-aminoheptanoic acid) (nylon 7), poly(8-aminooctanoic acid) (nylon 8), poly(9-aminononanoic acid) (nylon 9), poly(10-aminodecanoic acid) (nylon 10), poly(l 1-aminoundecanoic acid) (nylon 11), poly(12- aminodocecanoic acid) (nylon 12) and the like.
  • the preferred polyamide is Vydyne® nylon, which is poly(hexamethylene adipamide)
  • nylon 6 which gives a composite with the desired combination of tensile strength, tensile modulus and flexural modulus for the applications contemplated herein (Vydyne ® is a registered trademark of Solutia Inc.).
  • the preferred molecular weight of the polyamide is in the range of about 30,000 to about 80,000 D (weight average) with a more preferred molecular weight in the range of about 30,000 to about 40,000 D.
  • the most preferred molecular weight of the polyamide is at least about 40,000 D (weight average).
  • Increasing the weight average molecular weight of the polyamide from about 35,000 to about 55,000 D results in an unexpected increase in toughness as indicated by the notched Izod impact test. Whereas an increase in the weight average molecular weight of from about 35,000 to about 55,000 D in the polyamide neat results in a small increase in toughness, the same increase in molecular weight in the nanocomposite results about twice the increase in toughness. Therefore, the increase in toughness is enhanced in the nanocomposite when compared to that of the polyamide neat.
  • the polyamide has an amine end group/acid end group ratio greater than one (1). More preferably, the concentration of amine end groups is at least 10 mole % greater than the concentration of the carboxylic acid end groups. In an even more preferred embodiment, the polyamide has a concentration of amine end groups at least 20 mole % greater than the concentration of the carboxylic acid end groups, and in a most preferred embodiment, the polyamide has a concentration of amine end groups at least 30 mole % greater than the concentration of the carboxylic acid end groups. In another embodiment, the concentration of amine end groups is essentially equal to the concentration of carboxylic acid end groups.
  • nylon 6, nylon 6,6, blends thereof and copolymers thereof is nylon 6, nylon 6,6, blends thereof and copolymers thereof.
  • the range of ratios of the nylon 6/nylon 6,6 in the blends is from about 1/100 to 100/1.
  • the range is from about 1/10 to 10/1.
  • the range of ratios of the nylon 6/nylon 6,6 in the copolymers is about 1/100 to 100/1.
  • the range is from about 1/10 to 10/1.
  • the nanocomposite composition comprises at least one additional polymer.
  • suitable polymers include polyethyleneoxide, polycarbonate, polyethylene, polypropylene, poly(styrene-acrylonitrile), poly(acrylonitrile-butadiene-styrene), poly(ethylene terephthalate), poly(butylene terephthalate), poly(trimethylene terephthalate), poly(ethylene naphthalate), poly(ethylene terephthalate-co-cyclohexane dimethanol terephthalate), polysulphone, poly(phenylene oxide) or poly(phenylene ether), poly(hydroxybenzoic acid-co- ethylene terephthalate), poly(hydroxybenzoic acid-co-hydroxynaphthenic acid), poly(esteramide), poly(etherimide), poly(phenylene sulfide), poly(phenylene terephthalamide).
  • the mixture may include various optional components which are additives commonly employed with polymers.
  • optional components include surfactants, nucleating agents, coupling agents, fillers, impact modifiers, chain extenders, plasticizers, compatibilizers, colorants, mold release lubricants, antistatic agents, pigments, fire retardants, and the like.
  • Suitable examples of fillers include carbon fiber, glass fiber, kaolin clay, wollastonite, mica and talc.
  • Suitable examples of compatibilizers include acid-modified hydrocarbon polymer, such as maleic anhydride-grafted propylethylene, maleic anhydride-grafted polypropylene, maleic anhydride-grafted ethylenebutylene-styrene block copolymer.
  • Suitable examples of mold release lubricant includes alkyl amine, stearamide, and di-or tri- aluminum stearate.
  • Suitable examples of impact modifiers include ethylene-propylene rubber, ethylene- propylene diene rubber, methacrylate-butadiene-styrene (with core-shell morphology), poly(butylacrylate) with or without carboxyl modification, poly(ethylene acrylate), poly(ethylene methylacrylate), poly(ethylene acrylic acid), poly(ethylene acrylate) ionomers, poly(ethylene methacrylate acrylic acid) terpolymer, poly(styrene-butadiene)block copolymers, poly(styrene-butadiene-styrene)block terpolymers, poly(styrene-ethylene/butylene-styrene) block terpolymers and poly(styrene-ethylene/butylene-styrene carboxylate) block terpolymers.
  • Suitable coupling agents include silane, titanate and zirconate coupling agents.
  • Silane coupling agents are well-known in the art and are useful in the present invention.
  • suitable coupling agents include octadecyltnmethoxysilane, gamma-aminopropyltriethoxysilane, gamma-aminopropyltrimethoxysilane, gamma-aminopropylphenyldimethoxysilane, gamma- glycidoxypropyl tripropoxysilane, 3,3-epoxycyclohexylethyl trimethoxysilane, gamma- proprionamido trithoxysilane, N-trimethoxysilylpropyl-N(beta-aminoethyl) amine, trimethoxysilylundecylamine, trimethoxysilyl-2-chloromethylphenylethane, trimethoxy
  • the preferred silane is gamma- aminopropyltriothexy silane.
  • the silane coupling agent is optionally added to the polymer composite in the range of about 0.5 to about 5 weight % of the layered silicate.
  • the preferred concentration range of silane coupling agent is about 1 to about 3 weight % of the layered silicate in the composite.
  • the nanocomposite composition further comprises a composition wherein an end group of the polyamide is bonded to a surface of the treated silicate by a silane coupling agent.
  • the silicate materials of the present invention are selected from the group consisting of layered silicates and fibrous, chain-like silicates, and include phyllosilicates.
  • fibrous, chain-like silicates include chain-like minerals, for example sepiolite and attapulgite, with sepiolite being preferred.
  • Such silicates are described, for example, in Japanese Patent Application Kokoku 6-84435 published October 26, 1994.
  • layered silicates include layered smectite clay minerals such as montmorillonite, nontronite, beidellite, volkonskoite, Laponite ® synthetic hectorite, natural hectorite, saponite, sauconite, magadiite, and kenyaite; vermiculite; and the like.
  • Other useful materials include layered illite minerals such as ledikite and admixtures of illites with one or more of the clay minerals named above.
  • the preferred layered silicates are the smectite clay minerals such as montmorillonite, nontronite, beidellite, volkonskoite, Laponite ® synthetic hectorite, natural hectorite, saponite, sauconite, magadite, and kenyaite.
  • the layered silicate materials suitable for use in the present invention are well-known in the art, and are sometimes referred to as "swellable layered material". A further description of the claimed layered silicates and the platelets formed when melt processed with the polyamide is found in International Patent Application WO 93/04117, which is hereby incorporated by reference.
  • the layered silicate materials typically have planar layers arrayed in a coherent, coplanar structure, where the bonding within the layers is stronger than the bonding between the layers such that the materials exhibit increased interlayer spacing when treated.
  • the layered silicate materials may be treated as described in more detail below with the subject ammonium ion to enhance the interlayer swelling and/or spacing useful for the performance of the treated silicate of the present invention.
  • inter layer spacing refers to the distance between the faces of the layers as they are assembled in the treated material before any delamination (or exfoliation) takes place.
  • the preferred clay materials generally include interlayer or exchangeable cations such as Li + , Na + , Ca 2+ , K + , Mg 2+ and the like. In this state, these materials have interlayer spacings usually equal to or less than about 4 A and only delaminate to a low extent in host polymer melts regardless of mixing.
  • the cationic treatment is a ammonium species which is capable of exchanging with the interlayer cations such as Li + , Na + , Ca 2+ , K + , Mg 2+ and the like in order to improve delamination of the layered silicate.
  • the treated silicate of the present invention is a silicate material as described above which is treated with at least one ammonium ion of the formula
  • R 1 R 2 R 3 R 4 wherein: Rj, R 2 , R 3 and R are independently selected from a group consisting of a saturated or unsaturated Ci to C 2 hydrocarbon, substituted hydrocarbon and branched hydrocarbon, or where Ri and R 2 form a N,N-cyclic ether.
  • Examples include saturated or unsaturated alkyls, including alkylenes; substituted alkyls such as hydroxyalkyls, alkoxyalkyls, alkoxys, amino alkyls, acid alkyls, halogenated alkyls, sulfonated alkyls, nitrated alkyls and the like; branched alkyls; aryls and substituted aryls, such as alkylaryls, alkyoxyaryls, alkylhydroxyaryls, alkylalkoxyaryls and the like.
  • a mixture of two or more ammonium ions is contemplated by the present invention.
  • Ri is selected from the group consisting of hydrogenated tallow, unsaturated tallow or a hydrocarbon having at least 6 carbons, and R 2 , R 3 and R 4 independently have from one to eighteen carbons.
  • Tallow is composed predominantly of octadecyl chains with small amounts of lower homologues, with an average of from 1 to 2 degrees of unsaturation.
  • the approximate composition is 70% 8 , 25% C 16 , 4% Cj and 1% C 12 .
  • Rj and R 2 are independently selected from the group consisting of hydrogenated tallow, unsaturated tallow or a hydrocarbon having at least 6 carbons and R 3 and R 4 independently have from one to twelve carbons.
  • Ri, R 2 , R3 and R_ ⁇ groups are alkyl such as methyl, ethyl, octyl, nonyl, tert-butyl, ethylhexyl, neopentyl, isopropyl, sec-butyl, dodecyl and the like; alkenyl such as 1-propenyl, 1-butenyl, 1-pentenyl, 1-hexenyl, 1-heptenyl, 1-octenyl and the like; cycloalkyl such as cyclohexyl, cyclopentyl, cyclooctyl, cycloheptyl and the like; alkoxy such as ethoxy; hydroxyalkyl; alkoxyalkyl such as methoxymethyl, ethoxymethyl, butoxymethyl, propoxyethyl, pentoxybutyl and the like; aryloxyalkyl and aryloxyaryl such as phenoxy
  • Suitable ammoniums used in treating the silicate materials include oniums such as dimethyldi(hydrogenated tallow) ammonium, dimethylbenzyl hydrogenated tallow ammonium, dimethyl(ethylhexyl) hydrogenated tallow ammonium, trimethyl hydrogenated tallow ammonium, methylbenzyldi(hydrogenated tallow) ammonium, N,N-2- cyclobutoxydi(hydrogenated tallow) ammonium, trimethyl tallow ammonium, methyldihydroxyethyl tallow ammonium, octadecylmethyldihydroxyethyl ammonium, dimethyl (ethylhexyl) hydrogenated tallow ammonium and mixtures thereof.
  • oniums such as dimethyldi(hydrogenated tallow) ammonium, dimethylbenzyl hydrogenated tallow ammonium, dimethyl(ethylhexyl) hydrogenated tallow ammonium, tri
  • ammoniums include quaternary ammoniums, for example, dimethyldi(hydrogenated tallow) ammonium, dimethylbenzyl hydrogenated tallow ammonium, methyldihydroxyethyl tallow ammonium, octadecylmethyldihydroxyethyl ammonium, dimethyl(ethylhexyl) hydrogenated tallow ammonium and mixtures thereof.
  • the treatment with the ammonium ion(s), also called “cationic treatments" includes introduction of the ions into the silicate material by ion exchange.
  • the cationic treatments may be introduced into the spaces between every layer, nearly every layer, or a large fraction of the layers of the layered material such that the resulting platelet layers comprise less than about 20 particles in thickness.
  • the platelet layers are preferably less than about 8 particles in thickness, more preferably less than about 5 particles in thickness, and most preferably, about 1 or about 2 particles in thickness.
  • the treated silicate has a MER of from about 10 milliequivalents/100 g below the cation exchange capacity of the untreated silicate to about 30 milliequivalents/100 g above the cation exchange capacity of the untreated silicate.
  • the MER is the milliequivalents of treatment per 100 g of silicate.
  • Each untreated silicate has a cation exchange capacity, which is the milliequivalents of cations available for exchange per 100 g of silicate.
  • the cation exchange capacity of the layered silicate montmorillonite can be about 95, and the exchange capacity of sepiolite is in the range of about 10 to about 20.
  • a first nanocomposite sample may have a higher concentration of treated silicate but a lower concentration of silicate, than a second nanocomposite sample, because the first sample has a higher MER than the second sample. If the MER value of the treated silicate is substantially less than its exchange capacity, for example about 85 MER for the preferred montmorillonite, there is too little of the cationic treatment to have a beneficial effect.
  • the excess ammonium may be detrimental to the properties of the nylon.
  • the untreated montmorillonite has an exchange capacity of about 95
  • the treated layered silicate has a cation exchange capacity of from about 85 to about 125.
  • the amount of silicate included in the composition is in the range of about 0.1 to about 12 weight % of the composite.
  • the concentration is adjusted to provide a composite polymer matrix material which demonstrates, when tested, an increase in tensile modulus and flexural modulus, without a substantial decrease in tensile strength.
  • the increase in tensile modulus and flexural modulus is at least about 10%. More preferably, the increase in tensile modulus and flexural modulus is at least about 20%o. Too little silicate fails to provide the desired increase in tensile modulus and flexural modulus. Too much silicate provides a polyamide composite with a decreased tensile strength. Further, it may be desirable to have the crystalline regions of the polyamide in the nanocomposite composition be less than about 1.0 ⁇ m.
  • the particle size of the silicate is such that optimal contact between the polymer and the silicate is facilitated.
  • the range of particle size can vary from about 10 microns to about 100 microns.
  • the particle size is in the range of from about 20 to about 80 microns.
  • the particle size is below about 30 microns, such as those that pass through 450 mesh screens, in that the resulting polymer nanocomposite has improved performance properties.
  • the silicate can be treated with one or more ammonium ions of the formula
  • R a R b RcRd wherein at least one of R a , R D and R c is hydrogen (H) and R ⁇ j is selected from a group consisting of a saturated or unsaturated Ci to C 2 hydrocarbon, substituted hydrocarbon and branched hydrocarbon.
  • Examples include saturated or unsaturated alkyls, including alkylenes; substituted alkyls such as hydroxyalkyls, alkoxyalkyls, alkoxys, amino alkyls, acid alkyls, halogenated alkyls, sulfonated alkyls, nitrated alkyls and the like; branched alkyls; aryls and substituted aryls, such as alkylaryls, alkyoxyaryls, alkylhydroxyaryls, alkylalkoxyaryls and the like.
  • the Rd group for the ammonium ion is generally the same as the definition for the I ⁇ t group in the ammonium ion, the Examples set forth above for the R 4 group are also exemplary of the R d group.
  • R a , R D and R c are hydrogen (H), and the R d group contains a carboxylic acid moiety such that the ammonium ion
  • NR a R b RcRd is an amino acid, for example 12-aminolauric acid ammonium.
  • the amine end groups/acid end groups ratio of the polyamide is greater than one (1) .
  • the above ammonium ions may be mixed with at least one quaternary ammonium ion, said mixture used to treat the silicate.
  • the quaternary ammonium ion preferably has a hydrocarbon chain.
  • the hydrocarbon chain may be saturated or unsaturated.
  • the hydrocarbon chain may be obtained from a natural source such as tallow, or from a synthetic source such as a synthesized or purified C 12 , Cj 4 , C 16 , or C 18 chain.
  • a preferred mixture includes at least one of dimethyldi(hydrogenated tallow) ammonium, methyl dihydroxyethyl tallow ammonium, dimethylbenzyl hydrogenated tallow ammonium and/or dimethyl(ethylhexyl) hydrogenated tallow ammonium, either alone or in combination with 12-aminolauric acid ammonium.
  • the silicate can be further treated with azine cationic dyes, such as nigrosines or anthracines.
  • azine cationic dyes such as nigrosines or anthracines.
  • Said cationic dyes would impart color-fastness and uniformity of color in addition to increasing the intercalation of the polymer molecules.
  • the nanocomposite composition is prepared using a three step process.
  • One step includes forming a flowable mixture of the polyamide as a polymer melt and the silicate material.
  • the second step includes dissociating at least 50% but not all of the silicate material.
  • dissociating means delaminating or separating the silicate material into submicron-scale structures comprising individual or small multiple units.
  • this dissociating step includes delaminating the silicate material into submicron scale platelets comprising individual or small multiple layers.
  • this dissociating step includes separating the silicate material into sub- micron scale fibrous structures comprising individual or small multiple units.
  • a flowable mixture is a mixture which is capable of dispersing dissociated silicate material at the submicron scale.
  • a polymer melt is a melt processable polymer or mixture of polymers which has been heated to a temperature sufficiently high to produce a viscosity low enough for submicron scale mixing to occur.
  • the process temperature should be at least as high as the melting point of the polyamide employed and below the degradation temperature of the polyamide and of the organic treatment of the silicate.
  • the actual extruder temperature may be below the melting point of the polyamide employed, because heat is generated by the flow.
  • the process temperature is high enough that the polymer will remain in the polymer melt during the conduct of the process.
  • a typical nylon 6, having a melting point of about 225°C can be melted in an extruder at any temperature equal to or greater than about 225°C, as for example between about 225°C and about 260°C.
  • a temperature of preferably from about 260°C to about 320°C is normally employed.
  • the flowable mixture can be prepared through use of conventional polymer and additive blending means, in which the polymer is heated to a temperature sufficient to form a polymer melt and combined with the desired amount of the silicate material in a granulated or powdered form in a suitable mixer, as for example an extruder, a B anbury ® type mixer, a Brabender ® type mixer, Farrell continuous mixers, and the like.
  • a suitable mixer as for example an extruder, a B anbury ® type mixer, a Brabender ® type mixer, Farrell continuous mixers, and the like.
  • the flowable mixture may be formed by mixing the polyamide with a previously formed silicate-containing concentrate.
  • the concentrate includes the silicate and a polymer carrier.
  • the concentration of the silicate material in the concentrate, and the amount of concentrate are selected to provide the desired silicate concentration for the final nanocomposite composition.
  • suitable polymers for the carrier polymer of the concentrate include polyamide, ethylene propylene rubber, ethylene propylene diene rubber, ethylene-ethylacrylate, ethylene-ethylmethacrylate or ethylene methacrylate.
  • Examples include Iotek ® ionomer and Escor ® ATX acid terpolymer, both available from Exxon.
  • the polyamide polymers suitable for the carrier polymer include nylons such as nylon 6, nylon 6,6, nylon 4,6, nylon 6,9, nylon 6,10, nylon 6,12, nylon 11, nylon 12, amorphous nylons, aromatic nylons and their copolymers.
  • the polymer of the carrier may be the same as or different from the polyamide of the flowable mixture.
  • both polymers may be a polyamide, particularly nylon 6,6, but may have the same or different molecular weight.
  • the preferred weight average molecular weight of the carrier polymer of the concentrate is in the range of about 5,000 D to about 60,000 D.
  • the most preferred range of the weight average molecular weight for the carrier polymer is in the range of about 10,000 to about 40,000 D.
  • the dissociation step of the present process may occur at least in part via the forming of the concentrate such that the dissociation step may precede the step of forming the flowable mixture. It is therefore understood that the process steps (e.g., forming and dissociating) may occur sequentially without regard to order, simultaneously or a combination thereof.
  • the flowable mixture is sufficiently mixed to form the dispersed nanocomposite structure of dissociated silicate in the polymer melt, and it is thereafter cooled.
  • the silicate can be dissociated by being subjected to a shear having an effective shear rate.
  • an effective shear rate is a shear rate which is effective to aid in dissociation of the silicate and provide a composition comprising a polyamide matrix having silicate substantially homogeneously dispersed therein without substantially breaking the individual units (e.g., platelets or fibrous chains).
  • any method which can be used to apply a shear to a flowable mixture or any polymer melt can be used.
  • the shearing action can be provided by any appropriate method, such as by mechanical means, by thermal shock, by pressure alteration, or by ultrasonics.
  • the flowable polymer mixture is sheared by mechanical methods in which portions of the melt are caused to flow past other portions of the mixture by use of mechanical means such as stirrers, Banbury ® type mixers, Brabender ® type mixers, Farrel ® continuous mixers, and extruders.
  • the mixture is subjected to multiple shearings.
  • increased residence time is also provided, which results in improved performance properties.
  • shearing is achieved by alternatively raising or lowering the temperature of the mixture causing thermal expansions and resulting in internal stresses which cause the shear.
  • shear is achieved by sudden pressure changes in pressure alteration methods; by ultrasonic techniques in which cavitation or resonant vibrations which cause portions of the mixture to vibrate or to be excited at different phases and thus subjected to shear.
  • Shearing can be achieved by introducing the polymer pellets at one end of the extruder (single or twin screw) and receiving the sheared polymer at the other end of the extruder.
  • a preferred twin screw extruder is a co-rotating fully intermeshing type, such as the ZSK series manufactured by Werner and Pfleiderer Company.
  • the silicate can be fed into the twin screw extruder at the feed throat or at the downstream vent.
  • the preferred method is to feed the silicate at the downstream vent, which produces a composite polymer with improved performance properties.
  • FCM Farrel Continuous Mixer
  • the polymer melt containing nano-dispersed dissociated silicate material may also be formed by reactive extrusion in which the silicate material is initially dispersed as aggregates or at the nanoscale in a liquid or solid monomer and this monomer is subsequently polymerized in an extruder or the like.
  • the polymer may be granulated and dry mixed with the treated silicate material, and thereafter, the composition may be heated in a mixer until the polymer is melted forming the flowable mixture.
  • the third process step is a solid state polymerization step, wherein the compounded pellets are held for several hours at a high temperature at least about 20°C below the melting or softening point of the polymer.
  • typical solid state polymerization conditions are heating the solid polymer in the range of about 200°C to about 240°C for a period of from about 2 to about 5 hours. It is desirable to remove water produced during polymerization, e.g. by a dry nitrogen stream. Said additional process step results in an increase in molecular weight and an improvement in toughness, ductility and tensile strength of the nanocomposite.
  • the solid state polymerization step can be further effected with a catalyst that increases the molecular weight of the polyamide, e.g., a phosphorous-containing catalyst such as monosodium phosphate.
  • a catalyst that increases the molecular weight of the polyamide e.g., a phosphorous-containing catalyst such as monosodium phosphate.
  • phosphorous-containing catalysts are disclosed in U.S. Patent No. 4,966,949.
  • milder treatment conditions are needed to effect the desired polymerization.
  • the treatment temperature can be below the temperature used in solid state polymerization absent the catalyst using the same polyamide, i.e., more than 20°C below the melting or softening point of the polyamide.
  • the treatment time can be lowered to the range of about 0.5 hours to about 5 hours.
  • An optional processing step is a heat treatment step, where the composition is heated to improve intercalation of the nylon molecules into the silicate structure.
  • Said heat treatment step is performed by heating the composition at a temperature in the range of about 200°C to about 240°C for a period of about 2 to about 5 hours.
  • the heat treatment step can optionally be incorporated into the dissociating step by increasing the residence time of the mixture in the mixer or extruder, thereby heat treating under melt conditions.
  • the process to form the nanocomposite is preferably carried out in the absence of air, as for example in the presence of an inert gas, such as argon, neon or nitrogen.
  • the process can be carried out in a batchwise or discontinuous fashion, as for example, carrying out the process in a sealed container.
  • the process can be carried out in a continuous fashion in a single processing zone, as for example, by use of an extruder, from which air is largely excluded, or in a plurality of such reaction zones in series or in parallel.
  • the process to prepare a polymer nanocomposite composition comprises forming a first flowable mixture of a polyamide, at least one monomer and a silicate material; dissociating at least 50% but not all of the silicate material; polymerizing the monomer; and subjecting the polyamide in the mixture to solid state polymerization.
  • the polymerization of the monomer step can occur simultaneously or sequentially with one or more other steps in the process of this embodiment.
  • at least one monomer of the this embodiment includes monomers such as ⁇ - caprolactam, lauryllactam, and their corresponding lactones.
  • the process to prepare a polymer nanocomposite composition comprises forming a flowable mixture of a polyamide and a treated silicate material; dissociating the at least about 50% but not all of the treated silicate material; adding an additional amount of said polyamide, most preferably during said dissociating step; and subjecting the polyamide in the mixture to solid state polymerization.
  • Each of the above embodiments of the process to prepare the polymer nanocomposite composition can be followed by additional steps or treatments, or additional melt polymerization of the composition by increasing the residence time in the mixer with the removal of water condensation product.
  • the increased residence time can also improve the intercalation of the polyamide into the silicate, as discussed above.
  • composition of the present invention may be made into, but is not limited to, the form of a fiber, film or a molded article.
  • Solid state polymerization increases toughness, strength, and ductility of the produced polymer, while generally maintaining processability and modulus. Solid-state polymerization may improve properties such as elongation at yield, tensile elongation at break, flexural modulus, elastic modulus and both notched and unnotched Izod impact strength. Additional catalysts may be added, but are not required. Acid-functional clay treatments are particularly amenable to SSP (e.g., SCPX 1016 and SCPX 1255). They may serve to build polymer-clay linkages by tethering nylon molecules to the adsorbed acid moieties. The stoichiometric balance of amine and acid groups can impact the properties of the resulting polymer.
  • SSP e.g., SCPX 1016 and SCPX 1255
  • a higher amine:acid ratio in the nylon is desirable, especially in the case of aminoacid-treated silicates.
  • the use of solid state polymerization to finish the nanocomposite would allow starting with a lower RV nylon that would enhance intercalation, leading to greater exfoliation of the clay layers.
  • the inherent brittleness of nanocomposites compounded on the FCM may be overcome with SSP finishing, to make the FCM a viable low cost process alternative.
  • nylon 6,6 polymers have been employed in nanocomposites described herein.
  • the montmorillonite clay used has an exchange capacity of about 95 millieqivalents per 100 g of silicate.
  • Example 1 Conventional compounding without SSP
  • a high molecular weight in the nylon matrix of nanocomposites has been found to be even more beneficial for the ductility and toughness of the nanocomposites than for the neat nylon polymer.
  • the smectic silicates reduce nylon molecular weight during the compounding operation, especially in the first pass, resulting in a loss of ductility and toughness.
  • the molecular weight of nylon b was observed to drop from 36,500 to 31,500 D in a single pass of 7% montmorillonite treated with dimethyl di(hydrogenated tallow) ammonium cation (2M2HT-montmorillonite) through a 40 mm ZSK twin screw extruder manufactured by Krup Werner & Pfleiderer Company.
  • the second pass under dry conditions could instead improve mechanical performance both due to molecular weight building as well as enhanced exfoliation and dispersion of the nano-platelets.
  • Solid state polymerization (SSP) can be implemented in compounded nanocomposites under similar conditions used for the neat polymer as a more efficient method for building molecular weight. Improvements are obtained in tensile strength and elongation, as well as notched and un-notched Izod impact strength. Slight losses in modulus sometimes occur, perhaps due to breakage of the thin delaminated platelets during flow of the higher viscosity nylon matrix.
  • a higher amine/ carboxyl end group ratio on the nylon is preferable for nanocomposites, including those that are later subjected to SSP.
  • Amino acid exchanged grades would have higher acid levels according to the degree of substitution, as measured by the milliequivalenet exchange ratio (MER) in milliequivalents of cation per 100 g of silicate.
  • MER milliequivalenet exchange ratio
  • nylons a, and c are preferred to nylon b.
  • the higher amine end group concentration of nylon d would be especially important in the case of silicates treated with amino acid cations, which can react with the amine end groups of the nylon.
  • These treated silicates show a stronger response to the effects of SSP, resulting in larger increases in the above properties than nanocomposites containing pristine silicates or those treated with unreactive moieties.
  • the molecular weight changes to the high amine nylon d due to compounding with 4% montmorillonite exchanged with 12-aminolauric acid (ALA-montmorillonite) and subsequent solid state polymerized have been analyzed via GPC.
  • the extrusion process is seen in the above table to not change the molecular weight or its distribution in the nylon significantly. While a large increase in molecular weight of the nanocomposite does occur during SSP, it is reduced from that of the neat resin (which gels) by the presence of the acid moieties on the clay. There is, furthermore, evidence that the nylon matrix is being bound to the clay even during the compounding operation. During solid state polymerization, the nylon either branches or couples further with the organosilicate to form very high molecular weight species that become insoluble.
  • Solid state polymerization was practiced by heating the plastic pellets to 200-240°C (typically 220°C) with a dry nitrogen sweep to remove the water of condensation for a period of 2-4 hours (typically 4 hours). It was not necessary to add additional catalysts above those present from the initial melt polymerization, although mono- or di- sodium phosphate could have been added at 100-500 ppm. In one instance, adding 1 ,000 ppm monosodium phosphate resulted in an increase of compounded molecular weight from 27,400 to 30,600 D (SSP was not performed).
  • the SSP dryer is set to 470°F (243 °C) oil temperature and the nylon nanocomposite is heated for four hours at 220°C (230°C shell temperature) following an approximately 2-hour heat-up period.
  • the resulting time-temperature profiles are shown below for representative nanocomposite solid state polymerization runs.
  • Intrinsic viscosity builds linearly with time in the SSP dryer, as for example shown by the following data and graph ( Figure 5).
  • Example: 5 Injection molding of solid state polymerized nanocomposites
  • Solid-state polymerized nanocomposites based on nylons c and d mold easier with higher temperature setpoints than at lower temperature.
  • the nylon d-based nanocomposites mold more easily than those based on the nylon c, perhaps because the nylon c matrix reaches a higher viscosity level than the nylon d.
  • Lower pack and hold pressures can also be used.
  • Example 6 Mechanical properties for concentrate route using high amine nylon matrix The use of a high amine end carrier nylon in a concentrate to enhance the properties induced by solid state polymerization of the final nanocomposite composition was evaluated.
  • a high amine nylon concentrate comprising 17% ALA-montmorillonite in nylon d was then let down into three different resins having a range in molecular weight and amine/acid end group concentration, with and without subsequent solid-state polymerization prior to molding.
  • a fairly intense screw design was used in the ZSK 40mm twin screw extruder with a feed rate of 100 lbs/hr (43.5 kg/hr) and screw speed of 250 rpm. The barrel zone temperatures were set at 270°C.
  • the polymerization dryer was set to 470°F (243 °C) oil temperature from start to finish, giving a residence time of up to four hours at a 220°C resin temperature and 230°C shell temperature. Sample descriptions and mechanical properties are given in the table below.
  • the previous table shows the beneficial effect of solid state polymerization in improving the ultimate mechanical properties of tensile strength and elongation, as well as both notched and un-notched Izod impact strength. Its strong effect on nanocomposites comprising the ALA- montmorillonite compensates any molecular weight degradation of the nylon that might have occurred during compounding.
  • the effects of the parameters can be analyzed more quantitatively by use of the neural network CAD/Chem software (AlWare, Cleveland, OH).
  • the nylons are described by their nominal weight-average molecular weight and the nominal ratio of amine/acid end groups.
  • the mineral content of the nanocomposite is retained as a correlating variable to account for the minor differences between samples. On this basis, the following linear correlation coefficients are obtained.
  • SSP refers to the solid state polymerization time, in hours.
  • a nanocomposite comprising 4.9% by weight ALA-montmorillonite (3.9% mineral ash) in a 40,000 Mw nylon having balanced end groups is predicted to have the following properties: 14.00 Kpsi tensile strength, 612 Kpsi Young's modulus, 21.6% ultimate elongation, 558 Kpsi flex modulus, 18.68 Kpsi flex stress at 5% strain (below breaking strain), 0.91 ft-lb/in notched Izod, 43.9 ft-lb/in un-notched Izod and 9.5 mil/in shrinkage.
  • Figure 7 shows increasing tensile strength with SSP time when nanoclay is present, but not in the neat nylon.
  • the ductility and toughness of nanocomposites are increased significantly by solid state polymerization and to a lesser extent by higher amine/acid ratio and initial molecular weight of the nylon ( Figures 8, 9 and 10).
  • the ALA-montmorillonite concentration in the last two figures is 4.9%.
  • Stiffness tensile modulus
  • compositions, SSP time and mechanical property data is given in the table below for all of the ALA-montmorillonite, 2M2HT-montmorillonite, 2MBHT- montmorillonite and sepiolite nanocomposite preparations involving solid state polymerization.
  • Aminoacid organoclay is seen to provide the most favorable combination of nanocomposite properties following SSP. However, it may cause more embrittlement than other clay types if SSP is not practiced.
  • the acid functionalization is believed to compete for the amine end groups on the nylon chains, thus upsetting the end group balance and degrading nylon molecular weight during compounding. Higher initial molecular weight or amine/acid end group ratio in the selected nylon would help to counteract this effect, but SSP preferably would be performed following compounding to restore or even further increase the nylon molecular weight.
  • Pristine sepiolite is observed to be less destructive to ductility and toughness than is the montmorillonite. Nanocomposite material compounded with a single pass through the Farrell Continuous
  • In-situ polymerization holds great promise for improving clay dispersion and enhancing the strength of the silicate-nylon interface over that obtained by melt compounding.
  • Efficient reinforcement comprising more than 20% increase in modulus has been found for a nanocomposite containing only 0.1 % by weight nano-silicate.
  • Silane may be added to the reactor feed to improve interfacial bonding in the final nanocomposite.
  • Polyamide nanocomposite compositions may be formed by a process comprising forming an aqueous mixture of a treated silicate material and a polyamide monomer, treating the mixture to polymerize the polyamide monomer, and dissociating at least about 50% of the silicate material to form a polyamide nanocomposite composition.
  • layered (montmorillonite, saponite, hectorite, laponite) and chain-like (sepiolite) silicates may be incorporated into nylon 6,6 and nylon 6,6/6 copolymers by exfoliating and dispersing the clay in the hexamethylene adipamide (HMA) nylon 6,6 salt solution prior to polymerization.
  • Nylon 6,6/6 copolymers may be produced by including a component of epsilon-caprolactam in the monomer feed. The process has been demonstrated in both laboratory and pilot (250 pound (113 kg)) scale autoclaves.
  • the silicates may be pre-dispersed in the caprolactam component prior to its addition to the salt solution.
  • concentrates may be made in nylon 6 or in its precursor caprolactam solution, preferably with the addition of a peptizer, for later addition to the nylon 6,6 polymerization mixture.
  • Low molecular weight liquid polyamides may be used as carriers for the nanoclay. Concentrates of the nanoclay exfoliated in these carriers by high shear homogenization may be added later in the nylon 6,6 polymerization cycle after the aqueous ionic environment is driven off.
  • the following parameters may affect the performance of the process: a. Prior dispersion of the clay in water, or use of wet never-dried clay, before introduction to the polymerization mixture; b. Application of high shear, ultrasonic energy or venturi cavitation flow to enhance exfoliation of the clay layers prior to polymerization; c. Salt concentration; d. pH; e. Diamine/acid ratio in the HMA salt solution; f. Ion exchange of cations on the clay surface to alter its hydrophobicity and reactivity or physical interaction with the nylon polymer matrix; g. Clay concentration; h. Type of silicate; i. Molecular weight of the nylon at the point clay is added to the polymerization; and j. Composition of the nylon polymer/copolymer.
  • a diamine spike i.e., a higher molar concentration of hexamethylene diamine (HMD) than adipic acid in the mixture to counter any acidity due to the clay or its treatment, as well as to compensate for the loss of HMD by vaporization during the polymerization cycles.
  • HMD hexamethylene diamine
  • the resulting higher viscosity of the polymerized melt indicates a greater molecular weight build in the polymer matrix.
  • Certain mineral types are preferable for use in the in-situ polymerization process, including synthetic Laponite, commercially available from SCP under the trade name Laponite®, hectorite, sepiolite, saponite, and montmorillonite at various points in the reaction cycle. It has been found to be preferable to first achieve a good dispersion of the exfoliated silicate layers in water prior to contact with the salt solution. In this regard it may be useful to start with a never-dried aqueous dispersion or aqueous suspension instead of dry silicate. Alternatively, dry silicate may be hydrated prior to its participation in the polymerization process. Silicate may be dispersed through high shear homogenization or cavitation generated ultrasonically or by throttling the aqueous suspension through a venturi tube or other methods known in the art.
  • the silicate material may be organically modified to produce a stronger interface with the nylon matrix phase of the final nanocomposite.
  • Such organoclays are more hydrophobic than the pristine minerals and so may not form stable colloidal dispersions in water or in the nylon 6,6 salt solution.
  • polymer can intercalate the layered clay structure later in the polymerization cycle after the aqueous phase has been largely removed by vaporization.
  • its lower molecular weight should actually enhance the rate of intercalation, leading to a more complete state of layer exfoliation and higher reinforcement of the final composite by the resulting smaller particle thicknesses than is obtained by direct melt compounding with a pre-polymerized nylon resin.
  • the silicate material may be added later in the polymerization cycle after the salt has been converted to oligomers or low molecular weight polymers.
  • An alternate approach to avoiding ionic effects is to start the process with molten anhydrous salt in place of the salt solution.
  • concentration may be 2% or possibly up to 4% of the other minerals. Higher concentrations up to about twice these limits may be feasible when a peptizer is also present in the mixture.
  • These contain phosphate ions which may retard the buildup of structure in aqueous suspensions. The phosphates also act as buffers to control pH, which may also be desirable in achieving a high degree of clay dispersion. Examples:
  • aminolauric acid clay treatment provides improved stability to the colloidal clay suspension in salt solution. Indeed, a macroscopically uniform product of 4% aminolauric acid treated montmorillonite was polymerized into nylon 6,6 in a lab autoclave. However, transmission electron microscopy (TEM) and wide angle x-ray scattering (WAXS) revealed that the silicate of this composite is not fully exfoliated. The mechanical properties of injection molded specimens were not enhanced by the presence of the clay.
  • TEM transmission electron microscopy
  • WAXS wide angle x-ray scattering
  • Optical microscopy indicated the absence of any micron-sized clay residue, suggesting a higher degree of clay delamination than for the earlier homopolymer. This was confirmed by transmission electron microscopy (TEM). Injection molded properties of this sample were high, showing a 25% increase in tensile modulus and 50% increase in yield strength, with only about 1% silicate on a volume basis - a high reinforcement efficiency.
  • TEM transmission electron microscopy
  • Alkoxy-modified organoclays comprising the more polar ammonium ions synthesized from alkoxy-functional Jeffamines were observed to produce more stable colloidal suspensions in mixed HMA/caprolactam solutions.
  • In-situ polymerization was successfully performed with an ethoxy-modified montmorillonite. Initially, temperature was kept low ( ⁇ 260°C) to safeguard against degradation of the clay coating. Smaller test tube sized polymerizations were performed without stirring in a Parr reactor over a range in ethylene oxide / propylene oxide sequencing on the ammonium cation of the treated montmorillonite. WAXS measurements showed the same degree of polymer intercalation into the silicate structure as in samples made with stirring in a lab autoclave. Coating compositions allowed the nylon 6,6 content to be raised as high as 12% without obstructing the silicate intercalation.
  • One polypropylene oxide quat produced a particularly stable colloidal suspension in a 50/50 mixture of nylon 6,6 salt solution and caprolactam solution that did not phase separate for several days at room temperature.
  • pristine sodium montmorillonite suspensions were found not to be stable at room temperature across a range of HMA/caprolactam mixture compositions, though in-situ polymerization of straight nylon 6 nanocomposite from caprolactam solution comprising Gelwhite pristine Ca-montmorillonite supplied by Southern Clay Products, Inc. produced a smooth-flowing concentrate that could later be let down into nylon 6,6 to form a blended nanocomposite.
  • montmorillonite when fully pre-hydrated, either as a never-dried slurry or by first completely suspending dry clay in water, it forms a more stable colloidal suspension in hexamethylene adipamide salt solution.
  • the following types were found to produce stable 3% colloidal suspensions in water following high shear mixing with an Omni homogenizer: Gelwhite H and Gelwhite L (sodium-exchanged Ca-montmorillonite), Mineral Colloid BP (pristine Na-montmorillonite), poly(propylene oxide) treated montmorillonite, and a hydroxy-terminated poly (ethylene oxide / propylene oxide) copolymer treated montmorillonite.
  • nylon 6 nanocomposites were prepared in-situ from a water solution of caprolactam containing a range of pristine nanoclays, including Ca-montmorillonite, Na-montmorillonite, laponite RD synthetic hectorite and attapulgite.
  • the laponite appeared to disperse most readily, showing no peaks in the WAXS spectrum of the resulting nanocomposite.
  • the relative viscosity (RV) of the resulting nanocomposite was equal to the neat control and its translucency indicated good clay dispersion.
  • a 4-9°C rise in recrystallization temperature vs. the control indicates that the nanoparticles are altering the crystal structure of the nylon matrix in the manner of nucleating agents.
  • Nylon 6 nanocomposite fiber spun from the polymerization autoclave and comprising 2.5% laponite RD silicate showed a measure of electrical conductivity under high voltage testing. At 5% and 10% concentrations, the melt viscosity was so high that the nanocomposite melt could not be discharged from the autoclave.
  • Nylon 6,6 nanocomposites may be polymerized by standard industrial procedures as described in the "Nylon Plastics Handbook" (Melvin I. Kohan, Hanser Publishers, Kunststoff, 1995, pp. 17-23). Gelwhite L may be made into a concentrate of up to 20%> in nylon 6 via in-situ polymerization (with Tamol 850, a sodium polymethacrylate from Rohm and Haas Company, to aid clay dispersion). These concentrates were extruded at the end of the third cycle of the standard polymerization process and given a water quench. The nanocomposites were pulverized and added back to a nylon 6,6 polymerization, either to the salt solution at the beginning of the process or later after the batch achieved a temperature of 220°C. The latter technique generated gels, and neither resulted in any enhancement to the mechanical properties of spun fiber.
  • a never-dried slurry of an ion exchanged Ca-montmorillonite in which the Ca 2+ ions have all been exchanged for Na + , and containing polyacrylate as peptizer was also polymerized into nylon 6,6 fiber at 1%> concentration, but with no improvement in yarn properties. Melt viscosity was high, but spinnable. The resulting yarn appearance was smooth, but delustered.
  • the Ca 2+ mined ores are attractive for fiber applications because of their whiter color. However, the aspect ratio of their exfoliated platelets is known to be lower than those from mined Na- montmorillonite. If the clay dispersion in nylon 6,6 salt solution is allowed to age for even a few hours, it begins to coagulate. Polymerization of a one-day old dispersion resulted in a lower RV of the nylon 6,6.
  • An alternative embodiment for the preparation of silicate / polyamide nanocomposites via in-situ polymerization is to pre-disperse the clay at high concentration in a carrier (as a "concentrate") for addition to the polymerization vessel.
  • a carrier as a "concentrate”
  • Gelwhite L concentrations of 10-30% in an aqueous solution comprising 25% (based on the weight of the clay component) of a solution of 70% epsilon caprolactam in water and 1%- 5% Tamol 850 dispersing agent. These dispersions remained stable for over three weeks at room temperature. Without the dispersing agent, the dispersion of Gelwhite L at concentrations of or above 10% become unpourable gels.
  • Laponite RD could be dispersed at a high concentration of 10% in a 70% solution of caprolactam in water by combining 3% Tamol® 850 with 100%) ethylene glycol, both concentrations based on the weight of the clay.
  • Tetrasodium pyrophosphate (TSPP) and carboxymethyl cellulose (CMC) were found to not be effective peptizers to stabilize montmorillonite suspensions after addition to the nylon 6,6 salt solution, according to WAXS data.
  • Tamol® dispersing agent was effective in polymerizing 1.5-2% nanocomposites of Mineral Colloid BP in nylon blends comprising 20-30% nylon 6 in nylon 6,6 from aqueous mixtures of caprolactam and hexamethylene adipamide.
  • the copolymer composition is attractive because the lower salt concentration reduces clay flocculation while the caprolactam component enhances intercalation of the clay structure, leading to more efficient exfoliation.
  • Potassium tripolyphosphate (KTPP) has been found to be an effective peptizer for nanosilicates in nylon 6,6 salt solution. It is also believed to suppress gel formation.
  • Spun and drawn fibers prepared by injecting stabilized Gelwhite slurry later in the nylon 6,6 polymerization cycle were bright and gel-free, unlike the nubs and fluorescent gels routinely obtained with TSPP and Tamol® 850 peptizers. Fiber containing 0.3% nanoclay retained its matrix properties.
  • GELWHITE L slurry in 70% aqueous caprolactam solution was prepared with various amounts of KTPP. In 5820350* and 5820351*, however, GELWHITE L/caprolactam solution was kept at 1/1. Fiber comprising 0.6% Mineral Colloid BP, 1%> KTPP based on the clay weight and a small amount of caprolactam also appeared bright with only minor nub generation.
  • Nylon 6,6 nanocomposites comprising 1%> nanoclay were prepared from never-dried aqueous suspensions, with the exception of dry Gel-White H which had to be re-dispersed in water.
  • the pre-dispersions are further mixed under high shear with an Omni homogenizer for 10 minutes after introduction to the salt solution.
  • the Ca-montmorillonite slurry was ion exchanged with sodium ions and also contained an acrylic peptizer.
  • Samples 8515, 8517 and 8520 could not be extruded out of the polymerization autoclave due to their high melt viscosity, suggesting a significant degree of clay exfoliation despite the presence of a residual WAXS peak at 14.4 A.
  • the greater breadth of the peak does indicate that the original lamina stacks in the clay have been reduced somewhat in thickness.
  • a nylon 6,6 nanocomposite comprising 1% nanoclay from Na-montmorillonite never-dried slurry showed high reinforcement efficiency with a 15% increase in tensile modulus.
  • Sample 8522 was injection molded into tensile test bars which showed a 15%> increase in modulus from 435 to 500 kpsi, a highly efficient reinforcement from the small amount of clay present.
  • the presence of clay does not appear to have any significant effect on the molecular weight of the polymer formed, or its distribution.
  • the presence of CMC in Sample No. 8515 reduces molecular weight, as expected.
  • a significant level of nano-reinforcement was achieved in injection molded nylon 6,6 nanocomposites made by in-situ polymerization in a 250-pound (113 kg) batch with a very low mineral concentration.
  • a tensile modulus enhancement of 90 kpsi (20%) over neat nylon due to incorporation of only 0.072% mineral content by weight of laponite RD synthetic hectorite represents ten times the maximum benefit that could be anticipated from classical reinforcement mechanisms.
  • Pristine sepiolite a chain-like silicate, has been demonstrated to be equally effective as montmorillonite or hectorite for nylon fiber reinforcement via in-situ polymerization. At 0.1 %> concentration it provides a high draw capability and enhanced mechanical properties. At 6.5 draw ratio the following fiber properties were obtained vs. a neat nylon control fiber: 84 vs. 76 g/d modulus, 10.2 vs. 9.1 g/d tenacity and 12.3 vs. 10.4% elongation to fail. The nylon matrix RV was equivalent to the neat nylon control.
  • Sepiolite (1%) increased flex modulus by 13%> in nylon 6,6 polymerized in a lab autoclave.
  • the sepiolite nanocomposites did not demonstrate as great an improvement on the nanocomposite as in the smaller scale experiments.
  • Injection moldings containing 0.09%) by weight pristine sepiolite showed lower reinforcement than the corresponding laponite materials.
  • Tensile strength still increased significantly from 11.1 to 12.0 kpsi in comparison to the unreinforced nylon 6,6 control. The increase in modulus was only a modest 6%, while elongation still reached 30% strain.
  • Silane particularly aminopropyltriethoxysilane
  • polyamides such as nylon 6,6
  • the salt solution may be added to the salt solution along with the nanoclay prior to polymerization.
  • it provided no significant benefit to the properties of the resulting nanocomposite fibers also comprising low (0.1 %>) levels of nanoclay.
  • the higher concentrations of both silane (up to 0.5%>) and nanoclay (up to 2%o) used for injection molding it does serve to enhance the nanocomposite ductility.
  • the interfacial strengthening usually attributed to silanes in melt compounded systems can also be effective via in-situ polymerization.
  • the silane alone showed some reinforcing potential of its own in drawn fiber.
  • the higher aspect ratio reinforcements in general produce higher properties in fiber drawn from in-situ polymerized nylon 6,6 nanocomposites.
  • montmorillonite and hectorite are more effective than laponite B, which in turn is more effective than laponite RD.
  • Crystallinity is increased slightly and recrystallization temperatures generally increased
  • fibers spun and drawn from in-situ polymerized nylon 6,6 nanocomposites at the pilot plant scale comprise montmorillonite, hectorite and laponite B, both pristine and ion exchanged with ammonium cations.
  • Increases of 15% in modulus and tenacity were achieved along with a 30% increase in creep resistance at a low mineral concentration of only 0.1% by weight that would be significant for tire cord applications.
  • Higher increases of up to 30% in modulus with 10% in tenacity were observed at the bench scale.
  • the 2% secant modulus of 0.1 %> pristine hectorite nanocomposite drawn carpet yam of 16.6 g/denier was 44% higher than the 11.7 g/denier control yam produced in the same test and drawn to the same denier. Elongation to fail was equivalent to the control, while tenacity was enhanced slightly.
  • the good performance of this nanocomposite may be attributed to pre-dispersion of the silicate in a minor caprolactam component of the formulation. Dihydroxyethyl octadecylammonium is the preferred cation exchanged onto the phyllosilicate minerals for in-situ polymerization in nylon 6,6.
  • a nanocomposite in-situ polymerized with either 0.2 and 0.4% of montmorillonite previously treated with this cation showed improved appearance retention in carpet walk testing. Due to their less hydrophilic nature, organoclays are pre-dispersed at up to 5% concentration directly in nylon salt solution rather than in pure water, as is preferred for the pristine minerals. A slight inhibition of nylon 6,6 polymerization that may occur at higher silicate concentrations (e.g., 2%) may be overcome by increasing reactor residence time in the finishing cycle by about 30%).
  • the ideal mineral concentration for fiber spinning appears to be below about 1%, preferably from about 0.1% to about 0.2% by weight.
  • high injection molded properties were found for 1.5% silicate content: tensile strength of 91 MPa, modulus of 3.4 GPa and ultimate elongation of 47%, whereas a typical near nylon 6,6 homopolymer would display 80 MPa, 3.0 GPa, and 60%>, respectively.
  • Fiber applications via the in-situ polymerization approach benefit from the lower modulus targets vs. plastic molding applications, such that lower clay concentration levels may be used where nanoscale interactions play a greater role.
  • Higher orientation levels can be generated in the fiber spinning and drawing processes than in injection molding.
  • the use of higher draw temperature further improves nanocomposite yam performance by controlling molecular deformation.
  • Luster, smoothness (absence of nubbs) and opacity are indicators of the residual particle size of the clay inclusions in spun and drawn fibers.
  • Solid State Polymerization of in-situ polymerized nanocomposites Solid statepolymerization was performed for 1.5 hours at 200°C using nylon 6,6 which had been in-situ polymerized with four different silicates. Molecular weights were determined before and after solid state polymerization. The nanocomposite samples were found to increase in molecular weight similarly to neat nylon 6.6.
  • compositions and processes of this invention have been described in terms of preferred embodiments, it will be apparent to those of skill in the art that variations may be applied to the compositions, processes, and apparatus and in the steps or in the sequence of steps of the processes described herein without departing from the concept, spirit and scope of the invention. More specifically, it will be apparent that certain agents which are chemically related may be substituted for the agents described herein while the same or similar results would be achieved. All such similar substitutes and modifications apparent to those skilled in the art are deemed to be within the spirit, scope and concept of the invention.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

Une polymérisation in situ de monomères de polyamide et de matières de silicate, suivie d'une polymérisation à l'état solide permet de produire des matières de nanocomposites de polyamide présentant des propriétés physiques voulues. Les matières de nanocomposites produites comprennent des homopolymères et des copolymères. Les propriétés des matières de nanocomposites peuvent varier en fonction du choix des monomères, du type de silicate et des conditions de polymérisation.
PCT/US1999/018513 1998-02-13 1999-08-13 Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide WO2000009571A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CA002331670A CA2331670A1 (fr) 1999-02-12 1999-08-13 Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide
AU55621/99A AU5562199A (en) 1998-02-13 1999-08-13 Methods for the preparation of polyamide nanocomposite compositions by in situ and solid state polymerizations
EP99942188A EP1086144A1 (fr) 1999-02-12 1999-08-13 Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US60/074,639 1998-02-13
US24905499A 1999-02-12 1999-02-12
US09/249,054 1999-02-12
USPCT/US99/03097 1999-02-12

Publications (1)

Publication Number Publication Date
WO2000009571A1 true WO2000009571A1 (fr) 2000-02-24

Family

ID=22941868

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1999/018513 WO2000009571A1 (fr) 1998-02-13 1999-08-13 Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide

Country Status (4)

Country Link
EP (1) EP1086144A1 (fr)
CN (1) CN1306543A (fr)
CA (1) CA2331670A1 (fr)
WO (1) WO2000009571A1 (fr)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7012108B2 (en) 2000-12-15 2006-03-14 Agrolinz Melamin Gmbh Modified inorganic particles
US7173104B2 (en) 2001-11-19 2007-02-06 Ami - Agrolinz Melamine International Gmbh Products, especially moulding materials of polymers containing triazine segments, method for the production thereof and uses of the same
US7196131B2 (en) 2000-12-15 2007-03-27 Agrolinz Melamin Gmbh Polymer-modified inorganic particles
US7208540B2 (en) 2000-12-15 2007-04-24 Agrolinz Melamin Gmbh Process for curing aminoplast resins
US7619107B2 (en) 2004-07-30 2009-11-17 E.I. Du Pont De Nemours And Company Copper (II) complexes for deposition of copper films by atomic layer deposition
US10844172B2 (en) 2015-07-29 2020-11-24 Dsm Ip Assets B.V. Process for preparing a polymer composition, and polymer composition obtainable by said process
CN115521611A (zh) * 2022-10-25 2022-12-27 厦门市嘉能科技有限公司 一种用于密封圈的高流动性尼龙材料及其制备方法

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101063227B1 (ko) * 2009-10-12 2011-09-07 현대자동차주식회사 나일론-4 복합재료 조성물
KR101459973B1 (ko) * 2013-12-04 2014-11-07 지에스칼텍스 주식회사 흡습율 및 수축율이 개선된 나일론 블렌드 조성물, 이로부터 제조되는 나일론계 섬유 및 그 제조방법

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4739007A (en) * 1985-09-30 1988-04-19 Kabushiki Kaisha Toyota Chou Kenkyusho Composite material and process for manufacturing same
US4810734A (en) * 1987-03-26 1989-03-07 Kabushiki Kaisha Toyota Chuo Kenkyusho Process for producing composite material
EP0398551A2 (fr) * 1989-05-19 1990-11-22 Ube Industries, Ltd. Procédé de préparation d'un matériau composite à base de polyamide

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4739007A (en) * 1985-09-30 1988-04-19 Kabushiki Kaisha Toyota Chou Kenkyusho Composite material and process for manufacturing same
US4810734A (en) * 1987-03-26 1989-03-07 Kabushiki Kaisha Toyota Chuo Kenkyusho Process for producing composite material
EP0398551A2 (fr) * 1989-05-19 1990-11-22 Ube Industries, Ltd. Procédé de préparation d'un matériau composite à base de polyamide

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7012108B2 (en) 2000-12-15 2006-03-14 Agrolinz Melamin Gmbh Modified inorganic particles
US7196131B2 (en) 2000-12-15 2007-03-27 Agrolinz Melamin Gmbh Polymer-modified inorganic particles
US7208540B2 (en) 2000-12-15 2007-04-24 Agrolinz Melamin Gmbh Process for curing aminoplast resins
US7173104B2 (en) 2001-11-19 2007-02-06 Ami - Agrolinz Melamine International Gmbh Products, especially moulding materials of polymers containing triazine segments, method for the production thereof and uses of the same
US7619107B2 (en) 2004-07-30 2009-11-17 E.I. Du Pont De Nemours And Company Copper (II) complexes for deposition of copper films by atomic layer deposition
US10844172B2 (en) 2015-07-29 2020-11-24 Dsm Ip Assets B.V. Process for preparing a polymer composition, and polymer composition obtainable by said process
CN115521611A (zh) * 2022-10-25 2022-12-27 厦门市嘉能科技有限公司 一种用于密封圈的高流动性尼龙材料及其制备方法
CN115521611B (zh) * 2022-10-25 2023-09-19 厦门市嘉能科技有限公司 一种用于密封圈的高流动性尼龙材料及其制备方法

Also Published As

Publication number Publication date
EP1086144A1 (fr) 2001-03-28
CN1306543A (zh) 2001-08-01
CA2331670A1 (fr) 2000-02-24

Similar Documents

Publication Publication Date Title
EP1214356A1 (fr) Procedes pour la preparation de compositions de nanocomposites de polyamide par polymerisation in situ
EP1089866A1 (fr) Procede d'elaboration d'une composition polymere nanocomposite
JP2003517488A (ja) ポリマーナノコンポジット組成物
JP4646352B2 (ja) 交換イオンとして多荷電オニウムイオンを有する層状組成物、ならびにモノマー、オリゴマー及びポリマーインターカレーション物を調製するための当該組成物の適用と、当該インターカレーション物の層状組成物を用いて調製したナノ複合体
US6407155B1 (en) Intercalates formed via coupling agent-reaction and onium ion-intercalation pre-treatment of layered material for polymer intercalation
US6906127B2 (en) Intercalates, exfoliates and concentrates thereof formed with low molecular weight; nylon intercalants polymerized in-situ via ring-opening polymerization
Akkapeddi Glass fiber reinforced polyamide‐6 nanocomposites
US5385776A (en) Nanocomposites of gamma phase polymers containing inorganic particulate material
US5747560A (en) Melt process formation of polymer nanocomposite of exfoliated layered material
US6225394B1 (en) Intercalates formed by co-intercalation of onium ion spacing/coupling agents and monomer, oligomer or polymer ethylene vinyl alcohol (EVOH) intercalants and nanocomposites prepared with the intercalates
WO1993004118A1 (fr) Formation par traitement en fusion d'un nanocomposite polymere en materiau stratifie ecaille
Basurto et al. Nanocomposites of ABS and sepiolite: Study of different clay modification processes
Gensler et al. Application of nanoparticles in polymers for electronics and electrical engineering
WO2000009571A1 (fr) Procedes de preparation de compositions de nanocomposites de polyamide par des polymerisations in situ et a l'etat solide
Gupta et al. Polyamide-6/clay nanocomposites: a critical review
JP4199538B2 (ja) 改良された機械的特性を有する重合体組成物
US7446143B2 (en) Intercalates, exfoliates and concentrates thereof formed with protonated, non-carboxylic swelling agent and nylon intercalants polymerized in-situ via ring-opening polymerization
MXPA00007917A (en) Polymer nanocomposite composition

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 99807694.5

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): AE AL AM AT AU AZ BA BB BG BR BY CA CH CN CR CU CZ DE DK DM EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT UA UG US UZ VN YU ZA ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GH GM KE LS MW SD SL SZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
ENP Entry into the national phase

Ref document number: 2331670

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 1999942188

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: PA/a/2000/011151

Country of ref document: MX

REG Reference to national code

Ref country code: DE

Ref legal event code: 8642

WWP Wipo information: published in national office

Ref document number: 1999942188

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1999942188

Country of ref document: EP