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US4584351A Expired / Lapsed US ⏱️ 0.0 years remaining

Chlorosulfonation of chlorinated polyethylene

Assignee: Dow Chemical Co
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Filing: 1984-10-09
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Granted: 1986-04-22
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Expires: 2004-10-09
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Abstract

Abstract Chlorosulfonated polyethylene materials having (a) weight average molecular weight of from about 40,000 to about 300,000, (b) a chemically combined chlorine content of from about 20 to about 50 percent by weight of polymer, (c) a chemically combined sulfur content of from about 0.8 to about 2.5 percent by weight of polymer and (d) a 100 percent modulus of from about 0.6 to about 4.8 megapascals are prepared in an anhydrous process wherein an amorphous chlorinated polyethylene starting material is first fluidized and then exposed to a gaseous mixture of sulfur dioxide and chlorine having a ratio of sulfur dioxide to chlorine of from about 1:1 to about 16:1 in the presence of a chlorine free radical generator such as ultraviolet light, at a temperature of from about 25° to about 100° Centigrade, for a period of two hours or less.

Inventors

  • 👤 Robert R. Blanchard

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 06:28
CPC Classifications
C; C08; C08F; C08F8/00; C08F8/34; C08F8/38

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 238 words
An anhydrous process for preparing finely-divided, particulate chlorosulfonated polyethylene, the process comprising two sequential steps: A. providing a finely-divided, pulverulent, free-flowing chlorinated polyethylene starting material which is generally free of water and oxygen, the starting material (1) being prepared from high density polyethylene having a weight average molecular weight of from about 40,000 to about 300,000, and (2) having (a) a chlorine content of from about 20 to about 48 percent by weight of polymer, (b) a 100 percent modulus of from about 0.5 to about 4.8 Mega Pascals, and (c) a relative crystallinity of from about 0 to about 15 percent; and B. fluidizing the starting material with a gaseous mixture of sulfur dioxide and chlorine while said starting material is in the presence of chlorine free radicals, the gaseous mixture having a ratio of sulfur dioxide to chlorine of from about 1:1 to about 16:1, and the chlorine free radicals being generated by a means selected from the group consisting of ultraviolet light radiation having a wavelength sufficient to generate chlorine free radicals and chemical free radical initiators at a temperature within a temperature range of from about 20° to about 100° Centigrade and for a period of time sufficient to obtain chlorosulfonated polyethylene having a sulfur content of from about 0.8 to about 2.5 percent by weight of polymer and a chlorine content of from about 20 to about 50 percent by weight of polymer.
Claim 2
Dependent Claim 238 words
An anhydrous process for preparing finely-divided, particulate chlorosulfonated polyethylene, the process comprising two sequential steps: A. providing a finely-divided, pulverulent, free-flowing chlorinated polyethylene starting material which is generally free of water and oxygen, the starting material (1) being prepared from high density polyethylene having a weight average molecular weight of from about 40,000 to about 300,000, and (2) having (a) a chlorine content of from about 20 to about 48 percent by weight of polymer, (b) a 100 percent modulus of from about 0.5 to about 4.8 Mega Pascals, and (c) a relative crystallinity of from about 0 to about 15 percent; and B. fluidizing the starting material with a gaseous mixture of sulfur dioxide and chlorine while said starting material is in the presence of chlorine free radicals, the gaseous mixture having a ratio of sulfur dioxide to chlorine of from about 1:1 to about 16:1, and the chlorine free radicals being generated by a means selected from the group consisting of ultraviolet light radiation having a wavelength sufficient to generate chlorine free radicals and chemical free radical initiators at a temperature within a temperature range of from about 20° to about 100° Centigrade and for a period of time sufficient to obtain chlorosulfonated polyethylene having a sulfur content of from about 0.8 to about 2.5 percent by weight of polymer and a chlorine content of from about 20 to about 50 percent by weight of polymer.
Claim 3
Dependent Claim 18 words
The process of claim 1 wherein the period of time is from about 15 to about 120 minutes.
Claim 4
Dependent Claim 18 words
The process of claim 1 wherein the period of time is from about 15 to about 70 minutes.
Claim 5
Dependent Claim 18 words
The process of claim 1 wherein the period of time is from about 15 to about 35 minutes.
Claim 6
Dependent Claim 21 words
The process of claim 1 wherein the temperature is within a temperature range of from about 20° to about 80° Centigrade.
Claim 7
Dependent Claim 21 words
The process of claim 1 wherein the temperature is within a temperature range of from about 20° to about 50° Centigrade.
Claim 8
Dependent Claim 21 words
The process of claim 1 wherein the temperature is within a temperature range of from about 20° to about 45° Centigrade.
Claim 9
Dependent Claim 25 words
The process of claim 1 wherein the chlorosulfonated polyethylene has a sulfur content of from about 0.9 to about 1.4 percent by weight of polymer.
Claim 10
Dependent Claim 25 words
The process of claim 1 wherein the chlorosulfonated polyethylene has a sulfur content of from about 1.0 to about 1.2 percent by weight of polymer.
Claim 11
Dependent Claim 22 words
The process of claim 1 wherein the chlorosulfonated polyethylene has a weight average molecular weight of from about 90,000 to about 250,000.
Claim 12
Dependent Claim 22 words
The process of claim 1 wherein the chlorosulfonated polyethylene has a weight average molecular weight of from about 120,000 to about 180,000.
Claim 13
Dependent Claim 20 words
The process of claim 1 wherein the ratio of sulfur dioxide to chlorine is from about 1:1 to about 8:1.
Claim 14
Dependent Claim 20 words
The process of claim 1 wherein the ratio of sulfur dioxide to chlorine is from about 1:1 to about 4:1.

References Cited (Backward Citations)

US2889259A Cited
US4452953A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-04-21 1989-10-21 1990-04-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-04-21 1993-10-21 1994-04-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-04-21 1997-10-21 1998-04-22 $7700.00 Window Closed / Lapsed

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