Minimum residence time hydrogenation process for polyisoprene-polybutadiene block copolymers
AssigneeShell Oil Company
InventorDavid Karl Schisla
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Abstract
This invention is a method for producing butadiene-isoprene block copolymers with a specified amount of residual unsaturation in the polyisoprene blocks utilizing a hydrogenation catalyst wherein the hydrogenation residence time is minimized.
Claims18
A process for selectively hydrogenating a block copolymer having at least one butadiene polymer block and at least one isoprene polymer block with a hydrogenation catalyst that hydrogenates isoprene blocks and butadiene blocks at a different rate, comprising:
- a) choosing a desired polymer molecular weight and a desired level of residual unsaturation in the isoprene block(s) and in the butadiene block(s) and determining molecular weights of the butadiene block(s) and isoprene block(s) such that times required to hydrogenate the butadiene block(s) and isoprene block(s) with the hydrogenation catalyst to the desired levels of residual unsaturation are substantially the same;
- b) anionically polymerising butadiene and isoprene to form a block copolymer as determined in step (a), wherein the block copolymer comprises from about 40% to about 60% by weight of butadiene incorporated by 1.2-addition;
- and
- c) selectively hydrogenating the block copolymer with the hydrogenation catalyst until the butadiene block(s) and the isoprene block(s) have reached the desired levels of residual unsaturation wherein the desired level of residual unsaturation in the butadiene block is about 0.2 to 0.5 milliequivalents per gram of the block copolymer.
A method for producing hydrogenated block copolymers having at least one polybutadiene block, at least one polyisoprene block, and a specified amount of residual unsaturation in the polyisoprene block wherein hydrogenation residence time is minimized, comprising:
- a) determining average relative rates of hydrogenation of butadiene incorporated by 1,2addition to butadiene incorporated by 1,4-addition (S1) and butadiene incorporated by 1,4-addition to isoprene incorporated by 1,4-addition (S2) for a particular batch of hydrogenation catalyst to be used, including significant rate changes as conversion increases;
- b) choosing a desired polybutadiene block residual unsaturation (RUBd);
- c) choosing a desired polyisoprene block residual unsaturation (RUIp) and calculating the desired total residual unsaturation (RUTot);
- d) choosing a desired overall polymer molecular weight or a desired butadiene block molecular weight;
- e) determining a relative molecular weight ratio of the polyisoprene blocks to the polybutadiene blocks from an equation of:
- RUTot=1000((FBd((1−V12)(1-14BdC)+V12(1-14BdC) S1))/54+(FIp(1-14BdC)1/S2)/68)
- whereby FBd is the weight fraction of polybutadiene in the polymer, FIp is the weight fraction of polyisoprene in the polymer, V12 is the weight fraction of 1,2-addition in the polybutadiene blocks, and 14BdC is the fraction of butadiene incorporated by 1,4-addition which is hydrogenated, thereby defining the overall polymer molecular weight and the polybutadiene and polyisoprene block molecular weights,
- f) anionically polymerizing butadiene and isoprene to form a block copolymer having the block molecular weights as determined in step (e);
- and
- g) hydrogenating the block copolymer to the desired polybutadiene residual unsaturation.
A method for producing hydrogenated block copolymers having at least one polybutadiene block, at least one polyisoprene block, and a specified amount of residual unsaturation in the polyisoprene block wherein hydrogenation residence time is minimized when a relative rate of hydrogenation of butadiene incorporated by 1,4-addition to isoprene incorporated by 1,4-addition changes as conversion of butadiene incorporated by 1,4-addition increases, which comprises:
- a) determining an average relative rate of hydrogenation of butadiene incorporated by 1,2-addition to butadiene incorporated by 1,4-addition (S1) and butadiene incorporated by 1,4-addition to isoprene incorporated by 1,4-addition (S2, S2′) for a particular batch of hydrogenation catalyst to be used, including significant rate changes as conversion increases;
- b) choosing a desired polybutadiene block residual unsaturation (RUBd);
- c) choosing a desired polyisoprene block residual unsaturation (RUIp) and calculating the desired total residual unsaturation (RUTot);
- d) choosing a desired overall polymer molecular weight or a desired butadiene block molecular weight;
- e) determining a relative molecular weight ratio of the polyisoprene blocks to the polybutadiene blocks from an equation of:
- RUTot=(1−(14BdC−X)/(1−X))1/S2′×1000((Fip(1−X) 1/S2)/68)+(1−(14BdC−X)/(1−X))×1000((Fbd((1−V12)(1−X)+V12(1−X)S1))/54)
- where X is the degree of Bd conversion of butadiene incorporated by 1,4-addition at which the selectivity changes from S2 to S2′, FBd is the weight fraction of polybutadiene in the polymer, FIp is the weight fraction of polyisoprene in the polymer, V2 is the weight fraction of 1,2-addition in the polybutadiene blocks, and 14BdC is the fraction of butadiene incorporated by 1,4-addition which is hydrogenated, thereby defining an overall polymer molecular weight and the polybutadiene and polyisoprene block molecular weights;
- f) anionically polymerizing butadiene and isoprene to form a block copolymer having the block molecular weights as determined in step (c);
- and
- g) hydrogenating the block copolymer to the desired polybutadiene residual unsaturation.
Dependencies are inferred from the claim text.