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US4197386A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for chlorinating ethylene polymers

Assignee: Stamicarbon BV
•
Filing: 1978-02-16
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Granted: 1980-04-08
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Expires: 1998-02-16
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Abstract

Abstract An improved process for chlorinating high density polyethylene "in bulk" is described, with a two-stage reaction, the first at temperatures below the crystalline melting point, and the second above that temperature, and using a polyethylene starting material having a critical combination of characteristics, as described.

Inventors

  • 👤 Lowhardt A. A. Schoen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 22:51
CPC Classifications
C; C08; C08F; C08F8/00; C08F8/18; C08F8/20; C08F8/22

Claims Analysis

Total Claims: 13
Claim 1
Independent Claim 188 words
A process for chlorinating solid, finely divided high density ethylene polymers in bulk, which consists essentially in contacting a solid, finely divided high density ethylene polymer with chlorine gas in the absence of solvents and/or suspension agents in two stages while maintaining the temperature in the first stage below the crystalline melting point of said polymer, and conducting the second stage at a temperature above the said crystalline melting point, and wherein the time of operation of said first stage is sufficient to prevent sintering together and/or discoloration of the polymer particles in the second stage, and wherein said high density ethylene polymer has at the most 5 mol.-% of a second α-alkene of from 3 to 8 carbon atoms copolymerized therewith, has a density of between about 0.930 and 0.970, has a melt index of at most about 5, has a particle size distribution between from about 50 to about 2000μ, has a porosity of at most about 0.15 cm 3 /g, has a BET surface area of at most about 1 m 2 /g, and has a wax content of at most about 1% by weight.
Claim 2
Dependent Claim 188 words
A process for chlorinating solid, finely divided high density ethylene polymers in bulk, which consists essentially in contacting a solid, finely divided high density ethylene polymer with chlorine gas in the absence of solvents and/or suspension agents in two stages while maintaining the temperature in the first stage below the crystalline melting point of said polymer, and conducting the second stage at a temperature above the said crystalline melting point, and wherein the time of operation of said first stage is sufficient to prevent sintering together and/or discoloration of the polymer particles in the second stage, and wherein said high density ethylene polymer has at the most 5 mol.-% of a second α-alkene of from 3 to 8 carbon atoms copolymerized therewith, has a density of between about 0.930 and 0.970, has a melt index of at most about 5, has a particle size distribution between from about 50 to about 2000μ, has a porosity of at most about 0.15 cm 3 /g, has a BET surface area of at most about 1 m 2 /g, and has a wax content of at most about 1% by weight.
Claim 3
Dependent Claim 40 words
Process according to claim 1, wherein the chlorination in said first stage is conducted at temperatures between about 25° to 105° C., and the chlorination in the second stage is carried out at temperatures between about 110° and 150° C.
Claim 4
Dependent Claim 20 words
Process according to claim 2, wherein the first stage chlorination is conducted at temperatures between about 75° and 100° C.
Claim 5
Dependent Claim 20 words
Process according to claim 2, wherein the second stage chlorination is conducted at temperatures between about 135° and 150° C.
Claim 6
Dependent Claim 29 words
Process according to any of claims 1 to 4 wherein each said chlorination stage is carried out at a chlorine pressure of between 0.1 and 10 kg/cm 2 .
Claim 7
Dependent Claim 13 words
Process according to claim 1 wherein said melt index is at most 1.0.
Claim 8
Dependent Claim 15 words
Process according to claim 1 wherein said porosity is at most 0.10 cm 3 /g.
Claim 9
Dependent Claim 16 words
Process according to claim 1 wherein BET surface area is at least 0.1 m 2 /g.
Claim 10
Dependent Claim 26 words
Process according to claim 1 wherein water, liquid chlorine, or an inert liquid is sprayed or atomized in the reactor while said chlorination is carried out.
Claim 11
Dependent Claim 20 words
Process according to claim 9 wherein said polyethylene is mixed with at most an equal quantity by weight of water.
Claim 12
Dependent Claim 16 words
Process according to claim 1 wherein a chloropolyethylene with 5-70% by weight of chlorine is prepared.
Claim 13
Dependent Claim 16 words
Process according to claim 1 wherein a chloropolyethylene with 25-50% by weight of chlorine is prepared.

References Cited (Backward Citations)

GB834905A Cited
GB1228922A Cited
GB1228921A Cited
US4039732A Cited
US4029862A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-08 1983-10-08 1984-04-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-08 1987-10-08 1988-04-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-08 1991-10-08 1992-04-08 $7700.00 Window Closed / Lapsed

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