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US4350798A Expired / Lapsed US ⏱️ 0.0 years remaining

Chlorination of poly(vinyl chloride) in liquid chlorine, and chlorinated poly(vinyl chloride) composition

Assignee: Goodrich Corp
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Filing: 1981-01-26
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Granted: 1982-09-21
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Expires: 2001-01-26
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Abstract

Abstract A process is disclosed for photochlorinating poly(vinyl chloride), ("PVC"), suspended in liquid chlorine ("Cl 2 ") which swells the PVC and permits chlorination to occur in a gel phase. PVC starting material is in the form of solid free-flowing macrogranules which are slurried in from about 5 to about 50 times their weight of liquid Cl 2 in a reaction zone maintained at a temperature in the range from about -50° C. to about 50° C., and a pressure sufficient to maintain the chlorine in its liquid state. Since liquid Cl 2 itself swells the PVC to provide a gel phase in which photochlorination occurs, no conventional chlorinated hydrocarbon swelling agents, catalytic materials and the like are necessary. The process may be operated as a batch process, or a continuous process. Typical chlorine content of PVC is about 56.7 percent by weight (% by wt), and the product of chlorination is chlorinated poly(vinyl chloride), ("CPVC"). When formed, this CPVC is dissolved in the liquid Cl 2 to form a thick syrup-like solution. CPVC is recovered as a solid by evaporation of the liquid Cl 2 , or as a finely divided solid by adding a halogenated lower alkane slowly to the CPVC syrup. The solid CPVC is homogeneously chlorinated, and its morphology and spectra, especially its 13 C nmr spectra, differentiate it from prior art compositions.

Inventors

  • 👤 Richard G. Parker

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 13:04
CPC Classifications
B; B01; B01J; B01J19/00; B01J19/18; B01J19/20; B01J19/08; B01J19/12; B01J19/122; B01J19/123; B01J19/1868; B01J19/1881; C; C08; C08F; C08F8/00; C08F8/18; C08F8/20; C08F8/22; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00074; B01J2219/00087; B01J2219/00094

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.

References Cited (Backward Citations)

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US2996489A Cited
US3100762A Cited
US3156636A Cited
US3334078A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-09-20 1986-03-22 1986-09-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-09-20 1990-03-22 1990-09-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-09-20 1994-03-22 1994-09-21 $7700.00 Window Closed / Lapsed

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