Abstract A process is disclosed which permits the photochlorination of poly(vinyl chloride) resin ("PVC"), in an aqueous medium without the use of swelling agents such as are conventionally used. The chlorination reaction proceeds in an aqueous suspension having a high PVC concentration, yet allows the production of essentially uniformly chlorinated poly(vinyl chloride) resin ("CPVC") of excellent quality and uniformity, with a heat distortion temperature ("HDT") of at least 100° C. The transfer of chlorine from the gaseous phase into the aqueous phase, and then into the solid PVC phase, has been accelerated by this process which provides a critical combination of photo-illumination, elevated temperature and elevated pressure in a reactor devoid of oxygen and a swelling agent for the PVC. The "water-chlorination process" of this invention provides a "soak" period, after removal of oxygen from the aqueous PVC suspension, at a soak temperature of about 60° C. to about 75° C., from which the temperature is autogenously "ramped" during photochlorination under pressure to a finishing temperature in the range from about 80° C. to about 120° C. The suspension is exposed to an appropriate level of substantially constant ultraviolet light radiation, and the reactor pressure is maintained substantially constant in the range from about 10 psig to about 100 psig. Chlorination of a PVC starting material having a porosity in the range from about 0.1 cc/g to about 0.7 cc/g and a surface area in the range from about 0.7 m 2 /g to about 3 m 2 /g proceeds at a rapid rate.
A process for producing chlorinated poly(vinyl chloride) resin having a density within the range from about 1.50 to 1.65 g/cc at 25° C., comprising: (a) introducing an aqueous suspension of poly(vinyl chloride) containing from about 15 to about 35% by wt poly(vinyl chloride) into a reactor operable under elevated pressure; (b) removing essentially all oxygen from said suspension and reactor; (c) introducing chlorine into the reactor until the pressure therewithin is in the range from about 10 psig to about 100 psig; (d) soaking the poly(vinyl chloride) under said pressure for a period of from about 1 minute to about 45 minutes at a "soak" temperature in the range from about 60° C. to about 85° C.; (e) irradiating the poly(vinyl chloride) with ultraviolet light at a relatively high and constant intensity in the range from about 2 watts to about 50 watts per gallon of said aqueous suspension; (f) increasing the temperature of said suspension by at least 5° C. autogenously from said soak temperature to a finishing temperature in the range from about 80° C. to about 120° C.; (g) maintaining a finishing temperature in the range from about 80° C. to about 120° C. during chlorination; (h) continuing to introduce chlorine into the reactor as the reaction proceeds, so that the pressure in the reactor is maintained substantially constant within said range of pressure; (i) stopping flow of chlorine into the reactor when sufficient chlorine has been added to produce a suspension of chlorinated poly(vinyl chloride) having said density upon completion of the reaction; and, (j) separating solid macrogranular chlorinated poly(vinyl chloride) from said suspension of chlorinated poly(vinyl chloride) product characterized by having a heat distortion temperature measured by ASTM Test Method D648 which is in the range from about 100° C. to about 135° C.
Claim 2
Dependent Claim
299 words
A process for producing chlorinated poly(vinyl chloride) resin having a density within the range from about 1.50 to 1.65 g/cc at 25° C., comprising: (a) introducing an aqueous suspension of poly(vinyl chloride) containing from about 15 to about 35% by wt poly(vinyl chloride) into a reactor operable under elevated pressure; (b) removing essentially all oxygen from said suspension and reactor; (c) introducing chlorine into the reactor until the pressure therewithin is in the range from about 10 psig to about 100 psig; (d) soaking the poly(vinyl chloride) under said pressure for a period of from about 1 minute to about 45 minutes at a "soak" temperature in the range from about 60° C. to about 85° C.; (e) irradiating the poly(vinyl chloride) with ultraviolet light at a relatively high and constant intensity in the range from about 2 watts to about 50 watts per gallon of said aqueous suspension; (f) increasing the temperature of said suspension by at least 5° C. autogenously from said soak temperature to a finishing temperature in the range from about 80° C. to about 120° C.; (g) maintaining a finishing temperature in the range from about 80° C. to about 120° C. during chlorination; (h) continuing to introduce chlorine into the reactor as the reaction proceeds, so that the pressure in the reactor is maintained substantially constant within said range of pressure; (i) stopping flow of chlorine into the reactor when sufficient chlorine has been added to produce a suspension of chlorinated poly(vinyl chloride) having said density upon completion of the reaction; and, (j) separating solid macrogranular chlorinated poly(vinyl chloride) from said suspension of chlorinated poly(vinyl chloride) product characterized by having a heat distortion temperature measured by ASTM Test Method D648 which is in the range from about 100° C. to about 135° C.
Claim 3
Dependent Claim
54 words
The process of claim 1 wherein said poly(vinyl chloride) resin has a porosity in the range from about 0.1 cc/g to about 0.7 cc/g, a surface area in the range from about 0.7 m 2 /g to about 3 m 2 /g, and an inherent viscosity in the range from about 0.5 to 1.5.
Claim 4
Dependent Claim
46 words
The process of claim 1 wherein said poly(vinyl chloride) resin is suspension polymerized, has a porosity in the range from about 0.2 cc/g to about 0.6 cc/g and a surface area in the range from about 1.0 m 2 /g to about 1.5 m 2 /g.
Claim 5
Dependent Claim
46 words
The process of claim 1 wherein said poly(vinyl chloride) resin is mass polymerized, has a porosity in the range from about 0.1 cc/g to about 0.4 cc/g, and a surface area in the range from about 0.8 m 2 /g to about 1.0 m 2 /g.
Claim 6
Dependent Claim
21 words
The process of claim 3 wherein said finishing temperature is in the range from about 80° C. to about 100° C.
Claim 7
Dependent Claim
21 words
The process of claim 4 wherein said finishing temperature is in the range from about 80° C. to about 100° C.