Process for producing polyolefin thermoplastic elastomer composition

Claim 2

A process for producing a polyolefin thermoplastic elastomer composition, comprising the steps of: forming a blend of (a) 50 to 80% by weight of an ethylene-propylene copolymer rubber and/or an ethylene-propylene-diene terpolymer as a soft segment component, (b) 50 to 20% by weight of a crystalline ethylene-propylene block copolymer having an ethylene content of at least 5% by weight and a melt flow index of 0.5 to 30 g/10 minutes and/or a crystalline ethylene-propylene random copolymer having an ethylene content of at least 1.5% by weight and a melt flow index of 0.5 to 30 g/10 minutes as a hard segment, and based upon 100 parts by weight of the total of (a) and (b), (c) 0.3 to 5 parts by weight of an organosilane, (d) 0.1 to 3 parts by weight of an organic radical-generator exhibiting a half-life period for one minute at a temperature of 170° C. or higher, (e) 0 to 100 parts by weight of an extender oil to obtain a resulting blend, and (f) up to five parts by weight of white carbon; followed by subjecting the resulting blend to dynamic partial crosslinking carried out by using a twin-screw extruder under the conditions of a temperature of 190° C. to 270° C. and a retention time of 20 to 180 seconds in said extruder so that the residue in xylene after reflux for 6 hours is in the range of 20 to 70% by weight in the resultant partially crosslinked composition, a specific energy W of 0.08 to 0.8, expressed by the formula W=√3·(I-I.sub.O)·E·φ/1000·Q wherein W=specific energy (KwHr/Kg), I=loaded current (A), I O =loaded current at the time of empty-driven screw (A), E=voltage (V), φ=power factor and Q=extruded quantity (Kg/hr).

Claim 3

A process for producing a polyolefin thermoplastic elastomer composition comprising the steps of: forming a blend of (a) 50 to 80% by weight of an ethylene-propylene copolymer rubber and/or an ethylene-propylene-diene terpolymer, as a soft segment component, (b) 50 to 20% by weight of a crystalline ethylene-propylene block copolymer obtained by copolymerizing ethylene with propylene at two stages, in the first stage of which an ethylene-propylene copolymer having an ethylene content of 0 to 5% by weight is formed so as to occupy 20 to 95% by weight of the total quantity polymerized, and in the second stage of which an ethylene-polyethylene copolymer having an ethylene content of 50 to 85% by weight is formed so as to occupy 80 to 5% by weight of the total quantity polymerized, said crystalline ethylene-propylene block copolymer having an ethylene content of at least 5% by weight and a melt flow index of 0.5 to 30 g/10 minutes and/or a crystalline ethylene-propylene random copolymer having an ethylene content of at least 1.5% by weight and a melt flow index of 0.5 to 30 g/10 minutes as a hard segment, and based upon 100 parts by weight of the total of (a) and (b), (c) 0.3 to 5 parts by weight of an organosilane, (d) 0.1 to 3 parts by weight of an organic radical-generator exhibiting a half-life period for one minute at a temperature of 170° C. or higher, (e) 0 to 100 parts by weight of an extender oil to obtain a resulting blend, and (f) up to five parts by weight of white carbon; followed by subjecting the resulting blend to dynamic partial crosslinking carried out by using a twin-screw extruder so as to give a specific energy W, of 0.08 to 0.8, expressed by the following formula: W=√3·(I-I.sub.O)·E·φ/1000·Q wherein W=specific energy (KwHr/Kg), I=loaded current (A) I O =loaded current at the time of empty-driven screw (A) E=voltage (V) φ=power factor Q=extruded quantity (Kg/hr).

Claim 4

A process for producing a polyolefin thermoplastic elastomer composition comprising the steps of: forming a blend of (a) 50 to 80% by weight of an ethylene-propylene copolymer rubber and/or an ethylene-propylene-diene terpolymer, as a soft segment component, (b) 50 to 20% by weight of a crystalline ethylene-propylene block copolymer obtained by copolymerizing ethylene with propylene at two stages, in the first stage of which an ethylene-propylene copolymer having an ethylene content of 0 to 5% by weight is formed so as to occupy 20 to 95% by weight of the total quantity polymerized, and in the second stage of which an ethylene-polyethylene copolymer having an ethylene content of 50 to 85% by weight is formed so as to occupy 80 to 5% by weight of the total quantity polymerized, said crystalline ethylene-propylene block copolymer having an ethylene content of at least 5% by weight and a melt flow index of 0.5 to 30 g/10 minutes and/or a crystalline ethylene-propylene random copolymer having an ethylene content of at least 1.5% by weight and a melt flow index of 0.5 to 30 g/10 minutes as a hard segment, and based upon 100 parts by weight of the total of (a) and (b), (c) 0.3 to 5 parts by weight of an organosilane, (d) 0.1 to 3 parts by weight of an organic radical-generator exhibiting a half-life period for one minute at a temperature of 170° C. or higher, (e) 0 to 100 parts by weight of an extender oil to obtain a resulting blend, and (f) up to five parts by weight of white carbon; followed by subjecting the resulting blend to dynamic partial crosslinking carried out by using a twin-screw extruder so as to give a specific energy W, of 0.08 to 0.8, expressed by the following formula: W=√3·(I-I.sub.O)·E·φ/1000·Q wherein W=specific energy (KwHr/Kg), I=loaded current (A) I O =loaded current at the time of empty-driven screw (A) E=voltage (V) φ=power factor Q=extruded quantity (Kg/hr).

Claim 5

A process for producing a polyolefin thermoplastic elastomer composition comprising the steps of: forming a blend of (a) 50 to 80 percent by weight of an ethylene-propylene copolymer rubber and/or an ethylene-propylene-diene terpolymer, as a soft segment component, (b) 50 to 20% by weight of a crystalline ethylene-propylene block copolymer having an ethylene content of at least 5% by weight in a melt flow index of 0.5 to 30 g/10 minutes and/or a crystalline ethylene-propylene random copolymer having an ethylene content of at least 1.5 percent by weight in a melt flow index of 0.5 to 30 g/10 minutes as a hard segment, and based upon 100 parts by weight of the total of (a) and (b), (c) 0.3 to 5 parts by weight of an organosilane, (d) 0.1 to three parts by weight of an organic radical-generator exhibiting a half-life, for one minute at a temperature of 170° C. or higher, (e) 0 to 100 parts by weight of an extender oil, and (f) up to five parts by weight of white carbon; followed by subjecting the resulting blend to dynamic partial cross-linking carried out by means of a twin-screw extruder so as to give a specific energy W, of 0.08 to 0.8, expressed by the following formula: W=√3·(I-I.sub.O)·E·φ/1000·Q wherein W=specific energy (KwHr/Kg), I=loaded current (A) I O =loaded current at the time of empty-driven screw (A) E=voltage (V) φ=power factor Q=extruded quantity (Kg/hr).

Claim 6

A process for producing a polyolefin thermoplastic elastomer composition comprising the steps of: forming a blend of (a) 50 to 80 percent by weight of an ethylene-propylene copolymer rubber and/or an ethylene-propylene-diene terpolymer, as a soft segment component, (b) 50 to 20% by weight of a crystalline ethylene-propylene block copolymer having an ethylene content of at least 5% by weight in a melt flow index of 0.5 to 30 g/10 minutes and/or a crystalline ethylene-propylene random copolymer having an ethylene content of at least 1.5 percent by weight in a melt flow index of 0.5 to 30 g/10 minutes as a hard segment, and based upon 100 parts by weight of the total of (a) and (b), (c) 0.3 to 5 parts by weight of an organosilane, (d) 0.1 to three parts by weight of an organic radical-generator exhibiting a half-life, for one minute at a temperature of 170° C. or higher, (e) 0 to 100 parts by weight of an extender oil, and (f) up to five parts by weight of white carbon; followed by subjecting the resulting blend to dynamic partial cross-linking carried out by means of a twin-screw extruder so as to give a specific energy W, of 0.08 to 0.8, expressed by the following formula: W=√3·(I-I.sub.O)·E·φ/1000·Q wherein W=specific energy (KwHr/Kg), I=loaded current (A) I O =loaded current at the time of empty-driven screw (A) E=voltage (V) φ=power factor Q=extruded quantity (Kg/hr).

Claim 7

A process for producing a polyolefin thermoplastic elastomer composition according to claim 3, wherein said organosilane is expressed by the formula RR'SiX 2 , wherein R represents vinyl group, chloro group, amino group, mercapto group, glycidoxy group or methacryloxy group, X represents methoxy or ethoxy group, and R' represents R or X.

Claim 8

A process for producing a polyolefin thermoplastic elastomer composition according to claim 4, wherein said organosilane is at least one compound selected from vinyltrimethoxysilane, vinyltriethoxysilane, 3-aminopropyltriethoxysilane, n-(2-aminoethyl)-3-aminopropyltrimethoxysilane, 3-glycydoxypropyltrimethoxysilane, 3-chloropropyltrimethoxysilane, 3-methacryloxypropyltrimethoxysilane, and, 3-mercaptopropyltrimethoxysilane.

Claim 9

A process for producing a polyolefin thermoplastic elastomer composition according to claim 3, wherein said organic radical-generator is at least one compound selected from di-t-butylperoxydiisopropylbenzene, 2,5-dimethyl-2,5-di-(t-butylperoxy)hexane and dicumyl peroxide.

Claim 10

A process for producing a polyolefin thermoplastic elastomer composition according to claim 3, wherein said soft segment component is an ethylene-propylene copolymer rubber having a Mooney viscosity ML 1+4 (100° C.) of 10 to 100 and a propylene content of 20 to 50% by weight, or an ethylene-propylene-diene terpolymer having a Mooney viscosity ML 1+4 (100° C.) of 10 to 110, using as the third component diene to be copolymerized, any one of ethylidene, norbornene and 1,4-hexadiene, and having a iodine value (degree of unsaturation) of preferably 16 or less.

Claim 11

A process for producing a polyolefin thermoplastic elastomer according to claim 3, wherein said extender oil is at least one compound selected from paraffin, naphthene or aromatic compounds.