Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
218 words
A process for producing a polyether-polycarbonate block copolymer having a molecular weight within the range of from about 50,000 to about 750,000 as determined by the intrinsic viscosity measurement and containing from about 5 to about 35 percent by weight of repeating alkylene ether units and correspondingly from about 95 to about 65 percent by weight of repeating bisphenol A-carbonate units for use in forming membranes comprising: dissolving a polyether glycol compound, bisphenol A, and pyridine in a solvent to give a total solids content of about 5 percent to about 16 percent, by weight, reacting the dissolved bisphenol A, polyether glycol compound, and pyridine with phosgene by adding phosgene, at an initial feed rate, to said solution with vigorous stirring while maintaining the solution in the temperature range of about 20° C. to about 43° C. until crystals of pyridine hydrochloride begin to form; thereafter adding a chain terminator to the reacted solution and reducing the phosgene feed rate to about one-fiftieth of initial phosgene rate until the reaction solution undergoes a permanent color change, thereafter precipitating said polyether-polycarbonate block copolymer by mixing the reaction solution with an acidified liquid chosen from the group consisting of isopropyl alcohol, hexane and a 80:20 by volume mixture of acetone and water, and separating the precipitated polymer from the liquid.
Claim 2
Dependent Claim
218 words
A process for producing a polyether-polycarbonate block copolymer having a molecular weight within the range of from about 50,000 to about 750,000 as determined by the intrinsic viscosity measurement and containing from about 5 to about 35 percent by weight of repeating alkylene ether units and correspondingly from about 95 to about 65 percent by weight of repeating bisphenol A-carbonate units for use in forming membranes comprising: dissolving a polyether glycol compound, bisphenol A, and pyridine in a solvent to give a total solids content of about 5 percent to about 16 percent, by weight, reacting the dissolved bisphenol A, polyether glycol compound, and pyridine with phosgene by adding phosgene, at an initial feed rate, to said solution with vigorous stirring while maintaining the solution in the temperature range of about 20° C. to about 43° C. until crystals of pyridine hydrochloride begin to form; thereafter adding a chain terminator to the reacted solution and reducing the phosgene feed rate to about one-fiftieth of initial phosgene rate until the reaction solution undergoes a permanent color change, thereafter precipitating said polyether-polycarbonate block copolymer by mixing the reaction solution with an acidified liquid chosen from the group consisting of isopropyl alcohol, hexane and a 80:20 by volume mixture of acetone and water, and separating the precipitated polymer from the liquid.
Claim 3
Dependent Claim
47 words
The process of claim 1 wherein the polyether-polycarbonate block copolymer has a molecular weight of from about 200,000 to about 500,000 as determined by intrinsic viscosity measurement and the polyether glycol compound is chosen from the group consisting of polyethylene glycol and polypropylene oxide-polyethylene oxide block copolymers.
Claim 4
Dependent Claim
19 words
The process of claim 1 wherein the bisphenol A, polyether glycol and pyridine are dissolved in a halogenated alkane.
Claim 5
Dependent Claim
11 words
The process of claim 3 wherein the halogenated alkane is dichloromethane.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein about 3 moles of pyridine are present for each mole of bisphenol A and polyether glycol.
Claim 7
Dependent Claim
11 words
The process of claim 1 wherein the chain terminator is phenol.
Claim 8
Dependent Claim
22 words
The process of claim 1 wherein the precipitated polymer is additionally ground to a hard crumb, washed with hot water and dried.
Claim 9
Dependent Claim
35 words
The process of claim 1 wherein the bisphenol A is of a grade chosen from the group consisting of epoxy grade bisphenol A which has been further recrystallized from toluene and polycarbonate grade bisphenol A.
Claim 10
Dependent Claim
21 words
The process of claim 1 wherein the initial feed rate of phosgene is from about 500 ml/min to about 2000 ml/min.