Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
248 words
A bulk polymerization process for producing a homopolymer or a copolymer of propylene, which comprises polymerizing propylene or a mixture of propylene and another unsaturated hydrocarbon monomer in liquid propylene in the presence of a catalyst system consisting essentially of (a) an activated titanium compound obtained by (1) reducing titanium tetrachloride with an organoaluminum compound represented by the formula R.sub.n AlX.sub.3-n (I) wherein R represents a straight or branched chain alkyl group having 1 to 18 carbon atoms, an alicylic hydrocarbon group or an aromatic hydrocarbon group, X represents a halogen atom, an n is a value of from 1 to 3, inclusive to obtain a β-type titanium trichloride, (2) reacting the resulting β-type titanium trichloride with an ether, (3) reacting the solid catalyst thus obtained with (i) an organoaluminum compound represented by the formula R'.sub.m AlX.sub.3-m (II) wherein R' represents a straight or branched chain alkyl group having 1 to 18 carbon atoms, an alicyclic hydrocarbon group or an aromatic hydrocarbon group, X represents a halogen atom, and m is a value of 0<m<1.5, followed by further reacting the resulting solid catalyst with an ether, or (ii) titanium tetrachloride and (b) an organoaluminum compound, withdrawing the obtained polymer slurry from the polymerization zone, introducing the polymer slurry into an upper part of a counter-current washing zone and counter-currently contacting the polymer slurry with liquid propylene introduced into a lower part of the washing zone, whereby the polymer and catalyst residue dissolved in the polymer slurry are removed.
Claim 2
Dependent Claim
248 words
A bulk polymerization process for producing a homopolymer or a copolymer of propylene, which comprises polymerizing propylene or a mixture of propylene and another unsaturated hydrocarbon monomer in liquid propylene in the presence of a catalyst system consisting essentially of (a) an activated titanium compound obtained by (1) reducing titanium tetrachloride with an organoaluminum compound represented by the formula R.sub.n AlX.sub.3-n (I) wherein R represents a straight or branched chain alkyl group having 1 to 18 carbon atoms, an alicylic hydrocarbon group or an aromatic hydrocarbon group, X represents a halogen atom, an n is a value of from 1 to 3, inclusive to obtain a β-type titanium trichloride, (2) reacting the resulting β-type titanium trichloride with an ether, (3) reacting the solid catalyst thus obtained with (i) an organoaluminum compound represented by the formula R'.sub.m AlX.sub.3-m (II) wherein R' represents a straight or branched chain alkyl group having 1 to 18 carbon atoms, an alicyclic hydrocarbon group or an aromatic hydrocarbon group, X represents a halogen atom, and m is a value of 0<m<1.5, followed by further reacting the resulting solid catalyst with an ether, or (ii) titanium tetrachloride and (b) an organoaluminum compound, withdrawing the obtained polymer slurry from the polymerization zone, introducing the polymer slurry into an upper part of a counter-current washing zone and counter-currently contacting the polymer slurry with liquid propylene introduced into a lower part of the washing zone, whereby the polymer and catalyst residue dissolved in the polymer slurry are removed.
Claim 3
Dependent Claim
109 words
The process according to claim 1, wherein said counter-current washing zone is a counter-current multi-compartment washing tower having more than 5 compartments each provided with a conical agitator and an opposite conical fixed partition plate, each plate having a ratio of an opened area to an inner cross-sectional area of the tower of 20 to 50% and, a declivity of 10° to 80°, and the ratio of the flow rate of the rising liquid introduced into the lower part of the tower to that of a feed of liquid in the slurry introduced into the upper part of the tower being within a range of from 1/2 to 2.
Claim 4
Dependent Claim
47 words
The process according to claim 1, wherein said counter-current washing zone is a counter-current fluidized washing tower comprising multiagitators constructed simply with straight paddles, installed in the vertical position with respect to the agitating axis, in the lower part of the tower and providing a fluidized bed.
Claim 5
Dependent Claim
14 words
The process according to claim 1, wherein the other unsaturated hydrocarbon monomer is ethylene.
Claim 6
Dependent Claim
34 words
The process according to claim 1, wherein the polymerizing is at a temperature of about 30° to 90° C. under a pressure such that the propylene is liquid for about 1 to 20 hours.