Patent classifications
C08L23/083
RUBBER COMPOSITION AND A SEALING MATERIAL FOR FUEL CELL SEPARATORS
A rubber composition comprising 1 to 10 parts by weight of an organic peroxide crosslinking agent having a one-hour half-life temperature of 110 to 130 C., based on 100 parts by weight of an ethylene-butene-non-conjugated diene copolymer. The ethylene-butene-non-conjugated diene copolymer can be used by being blended with EPDM in an amount of 50 wt % or less in the total amount of the ethylene-butene-non-conjugated diene copolymer and EPDM. A sealing material for fuel cell separators comprising a crosslinked molded article of the rubber composition has, in addition to functions required as a sealing material for separators, improved low temperature sealing properties.
RUBBER COMPOSITION AND A SEALING MATERIAL FOR FUEL CELL SEPARATORS
A rubber composition comprising 1 to 10 parts by weight of an organic peroxide crosslinking agent having a one-hour half-life temperature of 110 to 130 C., based on 100 parts by weight of an ethylene-butene-non-conjugated diene copolymer. The ethylene-butene-non-conjugated diene copolymer can be used by being blended with EPDM in an amount of 50 wt % or less in the total amount of the ethylene-butene-non-conjugated diene copolymer and EPDM. A sealing material for fuel cell separators comprising a crosslinked molded article of the rubber composition has, in addition to functions required as a sealing material for separators, improved low temperature sealing properties.
Devolatilization Processes
In at least one embodiment, a process of forming a polymer includes supplying a feed having one or more olefin monomers and a solvent; contacting the feed with a catalyst to form a reaction mixture; treating the reaction mixture in a first separator to form a first polymer-rich mixture; introducing the first polymer-rich mixture into a second separator; introducing a volatile component and/or inert component into the first separator, the second separator and/or a line between the first separator and the second separator; treating the first polymer-rich mixture to form a second polymer-rich mixture; and devolatilizing the second polymer-rich mixture to obtain the polymer.
Devolatilization Processes
In at least one embodiment, a process of forming a polymer includes supplying a feed having one or more olefin monomers and a solvent; contacting the feed with a catalyst to form a reaction mixture; treating the reaction mixture in a first separator to form a first polymer-rich mixture; introducing the first polymer-rich mixture into a second separator; introducing a volatile component and/or inert component into the first separator, the second separator and/or a line between the first separator and the second separator; treating the first polymer-rich mixture to form a second polymer-rich mixture; and devolatilizing the second polymer-rich mixture to obtain the polymer.
RUBBER COMPOSITION FOR TORSIONAL DAMPER AND TORSIONAL DAMPER
A rubber composition for a torsional damper has (A) a minimum value of tan at 30 C. to 120 C. of 0.140 or more, (B) a ratio of tan at 30 C. to tan at 60 C. of 3.5 or less, and (C) a ratio of E at 30 C. to E at 60 C. of 21 or less.
RUBBER COMPOSITION FOR TORSIONAL DAMPER AND TORSIONAL DAMPER
A rubber composition for a torsional damper has (A) a minimum value of tan at 30 C. to 120 C. of 0.140 or more, (B) a ratio of tan at 30 C. to tan at 60 C. of 3.5 or less, and (C) a ratio of E at 30 C. to E at 60 C. of 21 or less.
RUBBER COMPOSITION MADE FROM A HIGHLY SATURATED DIENE ELASTOMER AND A DITHIOSULFATE SALT
A rubber composition based at least on an elastomer matrix, on a reinforcing filler and on a vulcanization system is provided. The elastomer matrix comprises a highly saturated elastomer and from 0 to less than 30 phr of natural rubber. The highly saturated diene elastomer contains 1,3-diene units and more than 50 mol % of ethylene units. The vulcanization system comprises a dithiosulfate salt of formula MO.sub.3SS-A-SSO.sub.3M in which the symbol A represents an alkanediyl group or a group comprising two or more alkanediyl units, which units are connected in pairs via an oxygen or sulfur atom, via a group of formula SO.sub.2, NH, NH.sub.2.sup.+, N(C.sub.1-C.sub.16 alkyl)- or COO, or via an arylene or cycloalkylene group, and the symbol M represents a metal atom. The invention makes it possible to achieve an improved compromise between bubble formation in the rubber composition on exiting from the curing presses and its hysteresis.
RUBBER COMPOSITION MADE FROM A HIGHLY SATURATED DIENE ELASTOMER AND A DITHIOSULFATE SALT
A rubber composition based at least on an elastomer matrix, on a reinforcing filler and on a vulcanization system is provided. The elastomer matrix comprises a highly saturated elastomer and from 0 to less than 30 phr of natural rubber. The highly saturated diene elastomer contains 1,3-diene units and more than 50 mol % of ethylene units. The vulcanization system comprises a dithiosulfate salt of formula MO.sub.3SS-A-SSO.sub.3M in which the symbol A represents an alkanediyl group or a group comprising two or more alkanediyl units, which units are connected in pairs via an oxygen or sulfur atom, via a group of formula SO.sub.2, NH, NH.sub.2.sup.+, N(C.sub.1-C.sub.16 alkyl)- or COO, or via an arylene or cycloalkylene group, and the symbol M represents a metal atom. The invention makes it possible to achieve an improved compromise between bubble formation in the rubber composition on exiting from the curing presses and its hysteresis.
Bimodal PE resins with improved melt strength
A method comprising introducing a polymerization feed comprising an -olefin, a diluent, and a diene to a polymerization system, under polymerization conditions, whereby a polymer product is produced, wherein the diene is present at a level in the range of from about 1 ppm to about 1000 ppm based on the diluent.
Bimodal PE resins with improved melt strength
A method comprising introducing a polymerization feed comprising an -olefin, a diluent, and a diene to a polymerization system, under polymerization conditions, whereby a polymer product is produced, wherein the diene is present at a level in the range of from about 1 ppm to about 1000 ppm based on the diluent.