Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
168 words
A process for photochlorinating poly(vinyl chloride) homopolymer macrogranules to obtain homogeneously chlorinated `chlorinated poly(vinyl chloride)` ("CPVC"), comprising, (a) suspending said homopolymer having a chlorine content in the range from about 55% to about 57% by weight, in liquid chlorine present in an amount at least 5 times the weight of said homopolymer, for a period of time sufficient to absorb said liquid chlorine into said macrogranules, (b) swelling said macrogranules at solid-liquid interfaces within and around said macrogranules to produce a gel phase by the action of said liquid chlorine, (c) photo-illuminating said gel phase until said homopolymer is converted to homogeneously chlorinated CPVC having at least 65% by weight of chlorine, and the mol ratio of PVC present in a sequence of 3 or more vinyl chloride units, to the mols of total vinyl chloride units, is always less than 0.30, (d) obtaining a solution of said homogeneously chlorinated CPVC in liquid chlorine, and, (e) recovering solid homogeneously chlorinated CPVC from said solution with halogenated lower alkane.
Claim 2
Dependent Claim
168 words
A process for photochlorinating poly(vinyl chloride) homopolymer macrogranules to obtain homogeneously chlorinated `chlorinated poly(vinyl chloride)` ("CPVC"), comprising, (a) suspending said homopolymer having a chlorine content in the range from about 55% to about 57% by weight, in liquid chlorine present in an amount at least 5 times the weight of said homopolymer, for a period of time sufficient to absorb said liquid chlorine into said macrogranules, (b) swelling said macrogranules at solid-liquid interfaces within and around said macrogranules to produce a gel phase by the action of said liquid chlorine, (c) photo-illuminating said gel phase until said homopolymer is converted to homogeneously chlorinated CPVC having at least 65% by weight of chlorine, and the mol ratio of PVC present in a sequence of 3 or more vinyl chloride units, to the mols of total vinyl chloride units, is always less than 0.30, (d) obtaining a solution of said homogeneously chlorinated CPVC in liquid chlorine, and, (e) recovering solid homogeneously chlorinated CPVC from said solution with halogenated lower alkane.
Claim 3
Dependent Claim
26 words
The process of claim 1 wherein said liquid chlorine is present in an amount from about 5 to about 30 times the weight of said homopolymer.
Claim 4
Dependent Claim
25 words
The process of claim 1 wherein said liquid chlorine is present at a temperature in the range from about -50° C. to about 50° C.
Claim 5
Dependent Claim
22 words
The process of claim 1 wherein said poly(vinyl chloride) has a molecular weight in the range from about 100,000 to about 1,000,000.
Claim 6
Dependent Claim
23 words
The process of claim 1 wherein said CPVC has a chlorine content in the range from 65 to about 72 percent by weight.
Claim 7
Dependent Claim
161 words
A mass of solid CPVC obtained by (a) suspending macrogranules of poly(vinyl chloride) homopolymer, having a chlorine content in the range from about 55% to about 57% by weight, in liquid chlorine present in an amount at least 5 times the weight of said homopolymer, for a period of time sufficient to absorb said liquid chlorine into said macrogranules, (b) swelling said macrogranules at solid-liquid interfaces within and around said macrogranules to produce a gel phase by the action of said liquid chlorine, (c) photo-illuminating said gel phase until said homopolymer is converted to homogeneously chlorinated CPVC having at least 65% by weight of chlorine, and the mol ratio of PVC present in a sequence of 3 or more vinyl chloride units, to the mols of total vinyl chloride units, is always less than 0.30, (d) obtaining a solution of said homogeneously chlorinated CPVC in liquid chlorine, and, (e) recovering solid homogeneously chlorinated CPVC from said solution with halogenated lower alkane.
Claim 8
Dependent Claim
161 words
A mass of solid CPVC obtained by (a) suspending macrogranules of poly(vinyl chloride) homopolymer, having a chlorine content in the range from about 55% to about 57% by weight, in liquid chlorine present in an amount at least 5 times the weight of said homopolymer, for a period of time sufficient to absorb said liquid chlorine into said macrogranules, (b) swelling said macrogranules at solid-liquid interfaces within and around said macrogranules to produce a gel phase by the action of said liquid chlorine, (c) photo-illuminating said gel phase until said homopolymer is converted to homogeneously chlorinated CPVC having at least 65% by weight of chlorine, and the mol ratio of PVC present in a sequence of 3 or more vinyl chloride units, to the mols of total vinyl chloride units, is always less than 0.30, (d) obtaining a solution of said homogeneously chlorinated CPVC in liquid chlorine, and, (e) recovering solid homogeneously chlorinated CPVC from said solution with halogenated lower alkane.