SILANE-CROSSLINKABLE COPOLYMER COMPOSITIONS

Abstract: A silane-crosslinkable copolymer composition compris­ es (A) 100 parts by weight of a copolymer prepared by radically polymerizing a polymerizable monomeric mixture consisting essentially of ethylene and an ethylenically un­ saturated silane compound having a hydrolyzable organic group under a high pressure, and containing said silane compound in an amount of from 0.1 to 5 wt%; (B) from 0.001 to 10 parts by weight of a silanol condensation catalyst; and (C) from 0.01 to 5 parts by weight of a silane compound having a hydrolyzable organic group. Use of the compositions prevents condensation reaction in the extruder during the initial stage of extrusion, and consequent surface unevenness.

Description: This invention relates to silane-crosslinkable ethylene copolymer compositions which can provide extrudates having improved appearance without requiring a decrease in the crosslinking rate during the initial stage of crosslinking. the composition can be used for molding in various fields. A method of silane-crosslinking a product molded from an ethylene copolymer graft-modified with an unsaturated silane compound, using water is described, in for example, Japanese Patent Publication 1711/73. This crosslinking method is advantageous over other methods, e.g., crosslinking using organic peroxides or radiation, in that the equipment required is simple. the limitations on the molding conditions are small; and the operation is easy to carry out. For example, in the production of crosslinked electric power cables, the molding temperature range required in the crosslinking method using organic peroxides is from 120 to 140°C, whereas it is possible in the silane-crosslinking method to mold at the molding temperature of an uncrosslinked ethylene polymer, i.e., at a high temperature. Thus, the silane-crosslinking method which is industrialiy excellent is widely utilized in various fields, e.g. electric power cables, pipes, tubes, films, sheets, hollow moldings and foamed moldings. The use of an ethylene copolymer obtained by radical polymerization of ethylene and an unsaturated silane compound is economically advantageous and is described in, for example, Japanese Patent Application (OPI) 9611/80 (the term "OPI" as used herein refers to a "published unexamined Japanese patent application"). However, in molding the ethylene copolymer and then crosslinking it by the silane-crosslinking method, a condensation reaction occurs in the extruder during the initial stage of extrusion molding and unevenness tends to occur on the surface of the molding. This is an extremely great defect which detracts from the commercial value of the product, and there has been a strong demand for improvement in this respect. As a result of various studies to overcome the problems encountered in the prior art, it has been found that they can be overcome without decreasing the rate of crosslinking in the initial stage if a specified amount of a silane compound having an organic group which is hydrolyzable during extrusion is added to a silane-crosslinkable ethylene copolymer containing a silanol condensation catalyst. U.S. 4,043,953 discloses a polymeric organosilane composition, for use as a coating composition, comprising a copolymer of an organosilane and an ethylenically unsaturated monomer and that stability of the composition is improved by the addition of from 0.5% to 15% by weight of the polymeric organosilane of a monomeric hydrolytically reactive silane. EP-A-0007765 discloses a polymeric organosilane composition for use as an adhesion promoter, in which stability of the composition against viscosity and gelation is provided with a composition comprising a copolymer of an organosilane and an ethylenically unsaturated monomer by incorporation thereinto of an admixture of a monomeric hydrolytically reactive compound and from 2 to 50 parts by weight per 100 parts by weight of the polymeric organosilane of a C₁₋₄ alkyl alcohol. Unlike the prior art composition, the polymeric organosilane composition of the present invention is designed to overcome the problem of surface unevenness of a molded product formed therefrom and comprises ethylene as a comonomer rather than as an ethylenically unsaturated monomer. In order for copolymerisation between the ethylene and the organosilane to occur, the polymerisation is conducted under a high pressure and preferably in the presence of a chain transfer agent. According to the present invention we provide a process for producing a silane-crosslinkable copolymer composition in the form of a molded product, comprising radically polymerizing a copolymerizable monomeric mixture consisting of ethylene and an ethylenically unsaturated silane compound selected from vinyltrimethoxysilane and γ-methacryloxypropyltrimethoxysilane and optionally up to 30 wt% of other copolymerisable monomers, under a pressure of from 500 to 4,000 kg/cm², in the presence of a radical polymerization initiator and a chain transfer agent, and containing said silane compound in an amount of from 0.1 to 5 wt% to produce a copolymer; kneading a mixture comprising (A) 100 parts by weight of the copolymer, (B) from 0.001 to 10 parts by weight of a catalyst for accelerating condensation between silanol groups of the ethylenically unsaturated silane compound; and (C) from 0.01 to 5 parts by weight of a silane compound having an organic group which is hydrolyzable during extrusion. The ethylene copolymer used as Component (A) in the composition of the present invention is a copolymer derived essentially from ethylene and an ethylenically unsaturated silane compound having a hydrolyzable organic group. The term "consisting essentially of" used herein means that the ethylene copolymer can be derived from up to 30 wt% of copolymerizable monomers other than ethylene and the ethylenically unsaturated silane compound having a hydrolyzable organic group. Examples of such optional monomers include α-olefins such as propylene, hexane-1 and 4-methylpentene-1; vinyl esters such as vinyl acetate and vinyl butyrate; unsaturated organic acid derivatives such as methyl acrylate and methyl methacrylate; unsaturated aromatic monomers such as styrene and α-methylstyrene. and vinyl ethers such as vinylmethyl ether and vinylphenyl ether. These optional monomers can be present in the ethylene copolymer in any form, e.g. a graft form, a random form or a block form. The ethylenically unsaturated silane compound which can be used is selected from various compounds having an ethylenically unsaturated bond copolymerizable with ethylene, and a hydrolyzable silane group. These compounds are preferably represented by the formula: RSiR′ n Y 3-n wherein R is an ethylenically unsaturated hydrocarbyl or an ethylenically unsaturated hydrocarbyloxy group; R′ is an aliphatic saturated hydrocarbyl group; Y which is the same or different is a hydrolyzable organic group; and n is 0, 1 or 2. Examples of the unsaturated silane compounds are the compounds of the above described formula wherein R is vinyl, allyl, isopropenyl, butenyl, cyclohexenyl or γ-methacryloxypropyl; Y is methoxy, ethoxy, formyloxy, acetoxy, propionoxy, alkyl or arylamino; and R′ is methyl, ethyl, propyl, decyl or phenyl. The particularly preferred unsaturated silane compounds are compounds represented by the following formula, and γ-methacryloxypropyltrimethoxysilane: CH₂=CHSi(OA)₃ wherein A is a hydrocarbyl group having 1 to 8, preferably 1 to 4, carbon atoms. The most preferred unsaturated silane compounds are vinyltrimethoxysilane, vinyltriethoxysilane and γ-methacryloxypropyltrimethoxysilane. Ethylene and the unsaturated silane compound are copolymerized under any conditions such that copolymerization of the two monomers occur. More specifically, those monomers are copolymerized under a pressure of 500 to 4,000 kg/cm², preferably 1,000 to 4,000 kg/cm², and at a temperature of 100 to 400°C, preferably 150 to 350°C, in the presence of a radical polymerization initiator, optionally together with up to about 30 wt% of a comonomer and a chain transfer agent. The two monomers are brought into contact with each other simultaneously or stepwise in a vessel or tube type reactor, preferably in a vessel type reactor. In the copolymerization of ethylene and the unsaturated silane compound, any radical polymerization initiators, comonomers and chain transfer agents, which are conventionally used in homopolymerization of ethylene or copolymerization of ethylene with other monomers can be used. Examples of radical polymerization initiators include (a) organic peroxides such as lauroyl peroxide, dipropionyl peroxide, benzoyl peroxide, di-t-butyl peroxide, t-butyl hydroperoxide, and t-butyl peroxyisobutyrate; (b) molecular oxygen; and (c) azo compounds such as azobisisobutyronitrile and azoisobutylvaleronitrile. Examples of the optional comonomers are the same as the above described copolymerizable monomers. Examples of the chain transfer agent include (a) paraffinic hydrocarbons such as methane, ethane, propane, butane and pentane. (b) α-olefins such as propylene, butene-1 and hexene-1; (c) aldehydes such as formaldehyde, acetaldehyde and n-butylaldehyde; (d) ketones such as acetone, methyl ethyl ketone and cyclohexanone; (e) aromatic hydrocarbons; and (f) chlorinated hydrocarbons. The copolymer used in the composition of the present invention contains 0.1 to 5 wt%, preferably 0.3 to 3 wt%, and more preferably 0.5 to 2 wt%, of the unsaturated silane compound unit. The higher the content of the unsaturated silane compound in the copolymer, the greater the mechanical strength and heat resistance of the silane-crosslinked product thereof. However, if the content of such unsaturated silane compound is excessively high, the tensile elongation and heat sealability of the crosslinked product are reduced. In view of this, the content of the unsaturated silane compound in the copolymer is limited to the range of 0.1 to 5 wt%. This copolymer can be blended with other olefinic polymers, and even in this case, the content of the unsaturated silane compound in the blend must be limited to the range of 0.1 to 5 wt%. The silanol condensation catalyst used as Component (B) in the composition of the present invention is generally selected from the compounds which can be conventionally used as a catalyst for accelerating dehydration condensation between silanol groups. Examples of the silanol condensation catalysts are carboxylic acid salts of metals such as tin, zinc, iron, lead and cobalt, organic bases, inorganic acids, and organic acids. Representative examples of the silanol condensation catalysts are (1) carboxylic acids of metals such as dibutyltin dilaurate, dibutyltin diacetate, dibutyltin dioctoate, stannous acetate, stannous caprylate, lead naphthenate, lead caprylate and cobalt naphthenate; (2) organic bases such as ethylamine, dibutylamine, hexylamine and pyridine; (3) inorganic acids such as sulfuric acid and hydrochloric acid; and (4) organic acids such as toluenesulfonic acid, acetic acid, stearic acid and maleic acid. The silanol condensation catalyst is used in an amount of 0.001 to 10 parts, preferably 0.01 to 5 parts, and more preferably 0.01 to 3 parts, by weight per 100 parts by weight of the ethylene copolymer as Component (A). If the amount of the silanol condensation catalyst is less than 0.001 part by weight per 100 parts by weight of Component (A), the crosslinking reaction does not proceed sufficiently. If, on the other hand, the amount of the silanol condensation catalyst is more than 10 parts by weight per 100 parts by weight of Component (A), local gelation proceeds in the extruder during extrusion and the extrudate has a very poor appearance. or unsaturated silane as long as it has such hydrolyzable organic group. In view of its easy availability, the ethylenically unsaturated silane compound constituting Component (A) is preferaby used. The most preferred silane compounds are vinyltrimethoxysilane, vinyltriethoxysilane, and γ-methacryloxypropyltrimethoxysilane. Component (C) is used in an amount of 0.01 to 5 parts, preferably 0.05 to 3 parts, and more preferably 0.1 to 2 parts, by weight per 100 parts by weight of the ethylene copolymer used as Component (A). If the amount of Component (C) is less than 0.01 part by weight per 100 parts by weight of the ethylene copolymer, the desired effect of the present invention cannot be obtained. If, on the other hand, the amount of Component (C) is more than 5 parts by weight per 100 parts by weight of the ethylene copolymer, the rate of crosslinking at the initial stage decreases considerably and, in order to obtain a product having a sufficient heat resistance, the crosslinking treatment time must be increased, resulting in impairment of operational efficiency. The composition of the present invention is effective provided it has fulfilled the above definition prior to kneading. For example, Components (A), (B) and (C) may be prepared into the desired composition in a kneader. Kneading can be conducted by conventional methods, and use of an extruder is preferred. The kneaded product is then silane-crosslinked with water (including moisture). The composition of the present invention exhibits a remarkable effect such that the appearance of the molded product obtained is improved by the simple expedient of adding a suitable amount of the silane compound as Component (C) at extrusion kneading, and this greatly increases the practical value of the composition of the present invention as a molding material for a resin molding. The following Examples and Comparative Examples are provided to further illustrate the composition of the present invention but are by no means intended as limiting. Examples and Comparative Examples The ethylene copolymer of Example 1 shown in the Table below was prepared by the following procedure. A reactor (inner capacity: 1.5 liters) equipped with a stirrer was fed with a mixture of ethylene, vinyltrimethoxysilane and propylene (molecular weight modifier), and t-butyl peroxyisobutyrate (radical generator) under the conditions shown below, so as to continuously produce an ethylene-vinyltrimethoxysilane copolymer. Amount Fed: Ethylene 43 kg/hr Vinyltrimethoxysilane 0.39 kg/hr Propylene 0.65 kg/hr t-Butylperoxyisobutyrate 2.1 g/hr Temperature of Monomers Fed: 65°C. Polymerization Pressure: 2,000 kg/cm². Maximum Reaction Temperature: 241 °C. Amount Produced: 5.8 kg/hr. In Examples 2 to 12 and Comparative Examples 1 to 18, copolymers were prepared in the same manner as in Example 1 except that the starting materials and their amounts fed were changed as shown in the Table below. To 100 parts by weight of each of the copolymers, 5 parts by weight of a catalyst master batch composed of polyethylene containing 1 wt% of dibutyltin dilaurate and a silane compound having a hydrolyzable organic group (the type and amount of the silane compound are shown in the Table) were added. The mixture was fed into a full tapered type screw extruder (diameter: 20 mm. LD: 20; compression ratio: 2.5) and extrusion molded into a columnar strand having a diameter of 2 mm at extrusion temperature of 200°C and a number of revolution of screw of 50 rpm. The strands were evaluated for their appearance by the following criteria. ○: Completely smooth surface ▵: Appreciable unevenness of the surface ×: Remarkable unevenness over the entire surface The strands were immersed in hot water (80°C) for 7 hours and their gel fractions were measured by extracting a 0.5 g sample of each strand with boiling xylene in a Soxhlet extractor for 16 hours. The content of the ethylenically unsaturated silane compound in each of the copolymers was measured with an infrared spectrophotometer. The results of evaluation are shown in the Table below.

Claims: A process for producing a silane-crosslinkable copolymer composition in the form of a molded product, comprising radically polymerizing a copolymerizable monomeric mixture consisting of ethylene and an ethylenically unsaturated silane compound selected from vinyltrimethoxysilane and γ-methacryloxypropyltrimethoxysilane and optionally up to 30 wt% of other copolymerisable monomers, under a pressure of from 500 to 4,000 kg/cm², in the presence of a radical polymerization initiator and a chain transfer agent, and containing said silane compound in an amount of from 0.1 to 5 wt% to produce a copolymer; kneading a mixture comprising (A) 100 parts by weight of the copolymer, (B) from 0.001 to 10 parts by weight of a catalyst for accelerating condensation between silanol groups of the ethylenically unsaturated silane compound; and (C) from 0.01 to 5 parts by weight of a silane compound having an organic group which is hydrolyzable during extrusion. A process as claimed in Claim 1, further comprising extruding the kneadate, and exposing the extrudate to water or moisture. A process as claimed in either of the preceding claims, wherein the content of units derived from said unsaturated silane compound in the copolymer is from 0.3 to 3 wt%. A process as claimed in any preceding claims, wherein said silane compound having a hydrolyzable organic group is vinyltrimethoxysilane, vinyltriethoxysilane or γ-methacryloxypropyltrimethoxysilane. A process as claimed in any of the preceding claims, wherein the amount of Compound (C) is from 0.05 to 3 parts by weight per 100 parts by weight of Component (A).

Inventors: ISAKA, TSUTOMU, ISHINO, IWAO, OHNO, AKIHIKO
Applicants: MITSUBISHI PETROCHEMICAL CO., LTD.
Application year: 1986
Main classification: C08J3
IPC codes: C08K5, C08L23, C08L33, C08L101, C08L43, C08L51, C08K3, C08L77, C08L7, C08L21, H01B3, C08K13