Treatment of coupled polymers prior to hydrogenation

Claim 2

The process of hydrogenation of an organopolyhalide-coupled rubbery conjugated diene polymer which comprises: treating said organopolyhalide-coupled rubbery conjugated diene polymer as a solution in a hydrocarbon diluent with an effective minor treating amount of an organometal treating agent under treating conditions, wherein said organometal treating agent is represented by R a H b M wherein M is selected from the group consiting of lithium, sodium, potassium, magnesium, calcium, zinc, and aluminum, R is a hydrocarbyl radical of 1 to 12 carbon atoms, a is an integer of 1 to 3, and b is 0 or an integer 1 or 2, depending on the valence of M, and thereafter hydrogenating the resulting treated polymer to substantially reduce at least the olefinic unsaturation thereof employing a hydrogenation catalyst and effective hydrogenation conditions, wherein said minor effective amount is sufficient to result in reduced olefinic unsaturation of said coupled conjugated diene polymer after said hydrogenation.

Claim 3

The process according to claim 1 wherein in said organometal treating agent represented by R a H b M R is a linear alkyl, branched alkyl, cycloalkyl, aryl, or combination thereof; H is hydrogen; a is 1 and b is zero where M is lithium, sodium or potassium; a is 2 and b is zero where M is magnesium zinc, or calcium; a is an integer of 1 to 3 inclusive and b is zero or an integer of 1 to 2 such that the sum of a and b is 3 where M is aluminum.

Claim 4

The process according to claim 2 wherein said organometal treating agent is methyllithium, n-butyllithium, sec-butyllithium, tert-butyllithium, n-dodecyllithium di-n-amylmagnesium, dimethylmagnesium, diethylmagnesium, n-amylsodium, 2-ethylhexylpotassium, trimethylaluminum, triethylaluminum, di-n-butylaluminum hydride, 2-ethylhexylaluminum dihydride, triphenylaluminum, benzyllithium, p-tolylsodium, cyclohexyl-bis-(2-ethylpentyl) aluminum, diethylzinc, di-n-amylcalcium, dimethylcalcium or diethylcalcium.

Claim 5

The process according to claim 1 wherein said effective amount of said organometal treating agent is in the range of about 0.1 to 25 gram millimoles per 100 grams of coupled polymer, and said treating is conducted at a temperature in the range of about 10° C. to 110° C.

Claim 6

The process according to claim 4 wherein said minor effective treating amount of said organometal treating agent is in the range of about 1 to 10 gram millimoles per 100 grams of polymer, and said treating temperature is in the range of about 20° C. to 90° C.

Claim 7

The process according to claim 4 wherein said polymer in solution in a hydrocarbon diluent represents a concentration of polymer in said diluent of about 1 to 50 weight percent based on total weight of polymer and diluent.

Claim 8

The process according to claim 6 wherein said hydrogenation step employs a heterogeneous hydrogenation catalyst selected from the group consisting of nickel on kieselguhr, Raney nickel, copper chromite, molybdenum sulfite, and finely divided platinum metal on a high surface area carrier.

Claim 9

The process according to claim 6 wherein said hydrogenation step employs a homogeneous hydrogenation catalyst comprising (A) a cobalt, nickel, or iron carboxylate, or alkoxide, and (B) an aluminum alkyl compound, wherein said (A) iron, nickel or cobalt carboxylate is represented by (RCOO) d M', and said alkoxide is represented by RCH 2 OM', wherein M' is said nickel, cobalt or iron, d is 2 or 3, wherein said (B) alkylaluminum is represented by R 3 Al, and wherein said homogeneous hydrogenation catalyst represents a mole ratio of (A):(B) in the range of about 0.15 to 1 to 1 to 1.

Claim 10

The process according to claim 8 wherein said homogeneous hydrogenation catalyst component (A) is said carboxylate and is a nickel or cobalt carboxylate, and wherein said homogeneous catalyst component (A) is employed in a concentration of about 0.1 to 20 gram millimoles per 100 grams of polymer, and wherein said hydrogenation is conducted at a temperature in the range of about 0° C. to 250° C., under hydrogen pressurization of up to about 1,000 psig.

Claim 11

The process according to claim 9 wherein said organopolyhalide-coupled conjugated diene polymer is a conjugated diene homopolymer, conjugated diene copolymer, or copolymer of at least one conjugated diene with at least one copolymerizable vinylidine monovinylarene group-containing comonomer.

Claim 12

The process according to claim 10 wherein said conjugated diene polymer is a homopolymer or copolymer of 1,3-butadiene, 2,3-dimethyl-1,3-butadiene, 3-butyl-1,3-octadiene, isoprene, or 2-phenyl-1,3-butadiene.

Claim 13

The process according to claim 10 wherein said conjugated diene polymer is a copolymer of at least one said conjugated diene of 4 to 12 carbon atoms per monomer molecule with at least one monovinylarene of 8 to 18 carbon atoms per monomer molecule, and wherein said monovinylarene is selected from the group consisting of styrene, 3-methylstyrene, 4-propylstyrene, 1-vinylnaphthalene, 4-cyclohexylstyrene, p-tolylstyrene, and 1-vinyl-5-hexylnaphthalene.

Claim 14

The process according to claim 12 wherein said conjugated diene polymer is a butadiene/styrene copolymer prepared with bis(4-chloromethylphenyl) ether as said organopolyhalide.

Claim 15

The process according to claim 13 wherein said copolymer is a block copolymer represented by a structure of about 15/70/15 styrene/butadiene/styrene.

Claim 16

A process for preparing a hydrogenated polymer which comprises the steps of: a. polymerizing in a hydrocarbon diluent under anionic solution polymerization conditions of temperature and pressure employing a hydrocarbylmonoalkali metal or alkaline earth metal initiator at least one conjugated diene monomer or at least one conjugated diene monomer with at least one copolymerizable vinylidene group-containing comonomer under polymerization conditions, thereby preparing a rubbery conjugated diene polymer, b. treating the resulting conjugated diene polymer from step (a), prior to quenching, with an organopolyhalide coupling agent containing at least two active halogen atoms selected from chlorine and bromine effective to couple said polymer, thereby preparing a coupled conjugated diene polymer, c. treating said coupled conjugated diene polymer with an effective minor amount of an organometal treating agent under treating conditions wherein said organometal treating agent is represented by R a H b M, wherein M is lithium, sodium, potassium, magnesium, calcium, zinc, or aluminum, and a and b are integers, said effective amount being sufficient to result in reduced olefinic unsaturation of said coupled conjugated diene polymer after hydrogenation, d. hydrogenating said organometal treated coupled conjugated diene polymer under hydrogenation conditions of catalyst, time, temperature, and pressure, effective to substantially saturate at least the olefinic unsaturation of said polymer, thereby producing a hydrogenated polymer.

Claim 17

A process for preparing a hydrogenated polymer which comprises the steps of: a. polymerizing in a hydrocarbon diluent under anionic solution polymerization conditions of temperature and pressure employing a hydrocarbylmonoalkali metal or alkaline earth metal initiator at least one conjugated diene monomer or at least one conjugated diene monomer with at least one copolymerizable vinylidene group-containing comonomer under polymerization conditions, thereby preparing a rubbery conjugated diene polymer, b. treating the resulting conjugated diene polymer from step (a), prior to quenching, with an organopolyhalide coupling agent containing at least two active halogen atoms selected from chlorine and bromine effective to couple said polymer, thereby preparing a coupled conjugated diene polymer, c. treating said coupled conjugated diene polymer with an effective minor amount of an organometal treating agent under treating conditions wherein said organometal treating agent is represented by R a H b M, wherein M is lithium, sodium, potassium, magnesium, calcium, zinc, or aluminum, and a and b are integers, said effective amount being sufficient to result in reduced olefinic unsaturation of said coupled conjugated diene polymer after hydrogenation, d. hydrogenating said organometal treated coupled conjugated diene polymer under hydrogenation conditions of catalyst, time, temperature, and pressure, effective to substantially saturate at least the olefinic unsaturation of said polymer, thereby producing a hydrogenated polymer.

Claim 18

The process according to claim 15 wherein said polymerization employs said at least one conjugated diene monomer wherein said conjugated diene monomer contains 4 to 12 carbon atoms per molecule and is selected from the group consisting of 1,3-butadiene, 2,3-dimethyl-1,3-butadiene, 1,3-pentadiene, 1,3-octadiene, isoprene, 2-phenyl-1,3-butadiene, and 3-n-butyl-1,3-octadiene.

Claim 19

The process according to claim 15 wherein said polymerization is said copolymerization of a conjugated diene monomer with a copolymerizable vinylidine group-containing monomer which is a monovinylarene, monopropenylbenzene, vinylnaphthalene, vinylpyridine, vinylquinoline, or vinylisoquinoline.

Claim 20

The process of claim 17 wherein said copolymerizable monomer is a monovinylarene, said monovinylarene contains 8 to 18 carbon atoms per molecule, said monovinylarene is selected from the group consisting of styrene, 3-methylstyrene, 4-propylstyrene, 1-vinylnaphthalene, 4-cyclohexylstyrene, p-tolylstyrene, and 1-vinyl-5-hexylnaphthalene, and wherein said conjugated diene monomer contains 4 to 12 carbon atoms per molecule and is selected from the group consisting of 1,3-butadiene, 2,3-dimethyl-1,3-butadiene, 3-butyl-1,3-octadiene, isoprene, 2-phenyl-1,3-butadiene.

Claim 21

The process according to claim 15 wherein in said organometal treating agent represented by R a H b M, R is a linear alkyl, branched alkyl, cycloalkyl, aryl, or combination hydrocarbyl radical; a is 1 and b is zero where M is lithium, sodium or potassium; a is 2 and b is zero where M is magnesium, zinc, or calcium; a is 1, 2 or 3 and b is 0, 1 or 2, such that the sum of a and b is 3, wherein M is aluminum.

Claim 22

The process according to claim 19 wherein in said step (c) said effective minor amount is in the range of about 0.1 to 25 millimoles of said organometal treating agent per 100 grams of coupled polymer.

Claim 23

The process according to claim 20 wherein said organometallic treating agent is selected from the group consisting of methyllithium, n-butyllithium, sec-butyllithium, tert-butyllithium, n-dodecyllithium, di-n-amylmagnesium, dimethylmagnesium, diethylmagnesium, n-amylsodium, 2-ethylhexylpotassium, trimethylaluminum, triethylaluminum, di-n-butylalminum hydride, 2-ethylhexylaluminum dihydride, triphenylaluminum, benzyllithium, p-tolylsodium, cyclohexyl-bis(2-ethylpentyl)aluminum, diethylzinc, di-n-amylcalcium, dimethylcalcium, and diethylcalcium.

Claim 24

The process according to claim 20 wherein the amount of said organopolyhalide coupling agent employed in said step (b) is in the range of about 0.1 to 1.5 equivalents of coupling agent based on alkali metal or alkaline earth metal present in said polymer.

Claim 25

The process according to claim 22 wherein said organopolyhalide coupling agent is represented by R"X m wherein X is chlorine or bromine, m is an integer of at least 2, and R" is a hydrocarbyl or silicon, tin, or oxygen-substituted hydrocarbyl radical, such that said organopolyhalide compound contains not more than 6 halogen atoms per molecule.

Claim 26

The process according to claim 23 wherein said organopolyhalide coupling agent is methylene chloride, 1,4-dichlorobutane, 1,4-dichloro-2-butene, ethyltrichlorosilane, 1,3-dichloro-2-propanone, 3,5,5-tribromo-4-octanone, 1,3,5-tri(2-bromoethyl)benzene, benzyltribromosilane, 2,5,6,9-tetrachloro-3,7-decadiene, pentachlorocyclohexyl chloromethylether, tetra(2-chloroethyl)stannane, 2-chloro-4-bromo-5-phenylpentyl pentachlorophenyl ether, or bis(4-chloromethylphenyl)ether.

Claim 27

The process according to claim 24 wherein said step (b) approximately one equivalent of coupling agent is employed, and the coupling step is conducted at a temperature in the range of about 0° to 150° C.

Claim 28

The process according to claim 23 wherein said hydrogenation step employs a heterogeneous catalyst selected from the group consisting of nickel on kieselguhr, Raney nickel, copper chromite, molybdenum sulfite, and finely divided noble metal on a high surface area carrier.

Claim 29

The process according to claim 23 wherein said hydrogenation step employes a homogeneous catalyst system comprising (A) a cobalt, nickel, or iron carboxylate or alkoxide, with (B) an aluminum alkyl compound, in an effective ratio of (A):(B), and wherein said (A) cobalt, nickel, or iron carboxylate is represented by (RCOO) d M', and said alkoxide is represented by RCH 2 OM', wherein M' is said iron, nickel, or cobalt, d is 2 or 3, and R is a hydrocarbyl radical of 1 to 12 carbon atoms.

Claim 30

The process according to claim 27 wherein said (A) carboxylate or alkoxide is selected from the group consisting of nickel, iron, or cobalt acetate, propionate, benzoate, octanoate, butoxide, and isopropoxide; and wherein said (B) alkyl aluminum is selected from the group consisting of triisobutylaluminum, triethylaluminum, and tripropylaluminum, wherein said ratio of said (A):(B) is in the range of about 0.15:1 to 1:1, and wherein said hydrogenation is carried out at a temperature in the range of about 0° C. to 250° C., employing a hydrogenation pressurization of up to about 1,000 psig.

Claim 31

The process according to claim 28 wherein said coupled conjugated diene polymer is a block copolymer of butadiene and styrene.

Claim 32

The process according to claim 29 wherein said block copolymer represents a styrene/butadiene/styrene block copolymer composition of about 15/70/15 weight relationship, prepared employing bis(4-chloromethylphenyl) ether as organopolyhalide coupling agent, and said hydrogenation step employes nickel octanoate and triethylaluminum in a 1:2 nickel:aluminum atom ratio.

Claim 33

The process according to claim 20 wherein said hydrogenation step (d) substantially saturates aromatic unsaturation as well as olefinic unsaturation.