Process and catalyst for hydrogen mediated saline hydride initiated anionic chain transfer polymerization
AssigneeAlbemarle Corporation
InventorWilliam J. LAYMAN, JR.
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Abstract
This invention relates to processes for forming hydrogen mediated saline hydride initiated anionic polystyrene distributions via novel polymerization conditions. This invention also relates to novel hydrocarbon soluble super active saline hydride catalyst and reagent compositions useful in conducting the hydrogen mediated saline hydride initiated polymerizations of this invention. This invention also relates to novel low molecular weight polystyrene polymer composition formed exclusively from styrene and molecular hydrogen as the monomers.
Claims11
A polystyrene polymer composition formed exclusively from styrene and molecular hydrogen as the monomers and made from the process comprising feeding a vinyl aromatic and/or conjugated diene monomer under an atmosphere comprising molecular hydrogen to a reactor vessel containing a reaction mixture of an inert ethereal solvent and an alkali metal or alkali metal alloy, wherein the GPC molecular weight distribution is characterized where Mn is in the range of from 315 to 905 Daltons;
- Mw is in the range of from 392 to 1716 Daltons;
- and Mz is in the range of about 512 to 3031 Daltons;
- PDn is in the range of 1.24 to 1.90;
- with a standard deviation in the range of 156 to 857 Daltons and the asymmetry is in the range of 1.40 to 3.14.
A polystyrene polymer composition formed exclusively from styrene and molecular hydrogen as the monomers and made from the process comprising feeding a vinyl aromatic and/or conjugated diene monomer under an atmosphere comprising hydrogen to a reaction mixture in a reactor vessel, wherein said reaction mixture was formed from (a) an organolithium compound;
- (b) a polytertiaryamine compound;
- (c) an alkoxide, wherein said alkoxide is an alkali metal alkoxide, or a magnesium alkoxide;
- (d) an optional aromatic hydrocarbon having at least one C—H covalent bond pKa within the range of 2.75 pKa units above that of the pKa of toluene to −4.30 pKa units below the pKa of toluene;
- and in (e) a hydrocarbon solvent having a pKa greater than H2, wherein the partial pressure of hydrogen is maintained at pressures between about 1.0 Bar to about 19.0 Bar, the molar ratio of the alkoxide to organolithium compound charged in the reactor is in the range of about 0.25:1 to about 10:1;
- the molar ratio of monomer to organolithium compound is about 10:1 to about 1000:1, and the molar ratio of the tertiary amine to organolithium compound is in the range of about 1.5:1 to about 20:1 and the hourly feed rate of monomer to organolithium is in the range of 10 to 200 moles of monomer per hour per mole of organolithium, wherein the GPC molecular weight distribution is characterized where Mn is in the range of from 315 to 905 Daltons;
- Mw is in the range of from 392 to 1716 Daltons;
- and Mz is in the range of about 512 to 3031 Daltons;
- PDn is in the range of 1.24 to 1.90;
- with a standard deviation in the range of 156 to 857 Daltons and the asymmetry is in the range of 1.40 to 3.14.
A hydrocarbon soluble catalytic composition formed from:
- (a) molecular hydrogen;
- (b) an organolithium compound;
- (c) a polytertiaryamine compound;
- (d) an alkoxide, wherein said alkoxide is an alkali metal alkoxide, or a magnesium alkoxide;
- (e) an aromatic hydrocarbon having at least one C—H covalent bond pKa within the range of 2.75 pKa units above that of the pKa of toluene to −4.30 pKa units below the pKa of toluene;
- and (f) a hydrocarbon solvent;
- wherein the aromatic hydrocarbon and hydrocarbon solvent may be the same or different.
Dependencies are inferred from the claim text.