Patent US4650832A successfully refreshed from Google Patents.
US4650832A
Expired / Lapsed
US
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Process for the manufacture of halogenated polymers
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1985-10-17
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Granted: 1987-03-17
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Expires: 2005-10-17
Abstract
Abstract In a process for the continuous halogenation of polymers by contacting polymer and halogenating agent in a continuous flow device in which means are provided for disengaging reaction by-products and unreacted halogenating agent from the reaction mixture, by deforming and disrupting the halogenated polymer surface and injecting an inert and/or reactive gas into the halogenated polymers immediately after reaction thereby neutralizing the product. In a preferred embodiment the process is carried out in an extruder-reactor and an optional, supplementary inert and/or reactive gas scrubbing zone is included. The process is amenable to saturated and unsaturated polymers.
Inventors
- 👤 Ronald C. Kowalski
- 👤 William M. Davis
- 👤 Neil F. Newman
- 👤 Zisis A. Foroulis
- 👤 Francis P. Baldwin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 12:04
CPC Classifications
C; C08; C08F; C08F8/00; C08F8/18; C08F8/20
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
106 words
A process for the continuous production of halogenated polymer, the process comprising contacting a cohesive polymer mass and halogenating agent in a continuous flow device comprisng means for conveying said polymer through said device wherein by-product of the halogenation reaction and unreacted halogenating agent are disengaged from said halogenated polymer mass in said continuous flow device downstream of said contact between said polymer and said halogenating agent by means comprising deforming and disrupting said halogenated polymer, thereby continually generating new polymer surface and injecting an effective amount of inert and/or reactive gas thereby neutralizing said halogenated polymer by disengaging halogenation reaction by-products and unreacted halogenating agent.
Claim 2
Dependent Claim
106 words
A process for the continuous production of halogenated polymer, the process comprising contacting a cohesive polymer mass and halogenating agent in a continuous flow device comprisng means for conveying said polymer through said device wherein by-product of the halogenation reaction and unreacted halogenating agent are disengaged from said halogenated polymer mass in said continuous flow device downstream of said contact between said polymer and said halogenating agent by means comprising deforming and disrupting said halogenated polymer, thereby continually generating new polymer surface and injecting an effective amount of inert and/or reactive gas thereby neutralizing said halogenated polymer by disengaging halogenation reaction by-products and unreacted halogenating agent.
Claim 3
Dependent Claim
70 words
The process of claim 1 wherein said polymer mass is subjected to deformation and disruption and wherein said polymer and said halogenating agent are present during contact as either co-continuous phases or wherein said halogenating agent is present as a continuous phase and said polymer is present as a discontinuous phase or wherein the region in which said polymer and said halogenating agent are contacted is filled with said polymer.
Claim 4
Dependent Claim
34 words
The process of claim 1 wherein said polymer is an ethylenically unsaturated polymer selected from the group consisting of butyl rubber, EPDM rubber, styrene butadiene rubber, polyisoprene rubber, polybutadiene rubber and poly(butadiene-isoprene) copolymer rubber.
Claim 5
Dependent Claim
34 words
The process of claim 1 wherein said polymer is selected from the group consisting of polyisobutylene, ethylene-propylene copolymer, high density polyethylene, low density polyethylene, linear low density polyethylene, ethylene-vinyl acetate copolymer and polyvinyl chloride.
Claim 6
Dependent Claim
40 words
The process of claim 1 wherein said halogenating agent is selected from the group consisting of chlorine gas, chlorine liquid, sulfuryl chloride, N-chlorosuccinimide, 1,3-dihalo-5,5-dimethylhydantoin, iodobenzene dichloride, iodine monochloride, bromine gas, bromine liquid, bromine chloride, sodium hypobromite, sulfur bromide and N-bromosuccinimide.
Claim 7
Dependent Claim
141 words
A process for the continuous production of halogenated polymer, the process comprising reacting said polymer and a halogenating agent in an extruder-reactor, said extruder-reactor comprising zones (A), (B) and (C) and conveying means traversing said zones; zone A, feed zone, in which conditions of temperature and pressure are sufficient to generate a cohesive polymer mass; zone (B), reaction zone, in which said halogenating agent and said polymer are contacted, resulting in a product mixture comprising halogenated polymer, reaction by-products and unreacted halogenating agent; and zone (C), neutralization zone, wherein reaction by-products and unreacted halogenating agent are disengaged from said halogenated polymer mass by means comprising deforming and disrupting said halogenated polymer, thereby continually generating new polymer surface and injecting an effective amount of inert and/or reactive gas thereby neutralizing said halogenated polymer by disengaging halogenation reaction by-products and unreacted halogenating agent.
Claim 8
Dependent Claim
141 words
A process for the continuous production of halogenated polymer, the process comprising reacting said polymer and a halogenating agent in an extruder-reactor, said extruder-reactor comprising zones (A), (B) and (C) and conveying means traversing said zones; zone A, feed zone, in which conditions of temperature and pressure are sufficient to generate a cohesive polymer mass; zone (B), reaction zone, in which said halogenating agent and said polymer are contacted, resulting in a product mixture comprising halogenated polymer, reaction by-products and unreacted halogenating agent; and zone (C), neutralization zone, wherein reaction by-products and unreacted halogenating agent are disengaged from said halogenated polymer mass by means comprising deforming and disrupting said halogenated polymer, thereby continually generating new polymer surface and injecting an effective amount of inert and/or reactive gas thereby neutralizing said halogenated polymer by disengaging halogenation reaction by-products and unreacted halogenating agent.
Claim 9
Dependent Claim
77 words
The process of claim 6 wherein said polymer mass is subjected to deformation and disruption in said reaction zone and wherein said polymer and said halogenating agent form co-continuous phases within said reaction zone or are present during contact as either co-continuous phases or wherein said halogenating agent is present as a continuous phase and said polymer is present as a discontinuous phase or wherein said halogenating agent is injected at a position filled with said polymer.
Claim 10
Dependent Claim
34 words
The process of claim 7 wherein said polymer is an ethylenically unsaturated polymer selected from the group consisting of butyl rubber, EPDM rubber, styrene butadiene rubber, polyisoprene rubber, polybutadiene rubber and poly(butadiene-isoprene) copolymer rubber.
Claim 11
Dependent Claim
37 words
The process of claim 6 wherein said polymer is selected from the group of saturated polymers consisting of polyisobutylene, ethylene-propylene copolymer, high density polyethylene, low density polyethylene, linear low density polyethylene, ethylene-vinyl acetate copolymer and polyvinyl chloride.
Claim 12
Dependent Claim
34 words
The process of claim 9 wherein said conveying means comprises screw means wherein said screw means is configured so as to avoid restricting the exiting flow of inert and/or reactive gas and disengaged materials.
Claim 13
Dependent Claim
25 words
The process of claim 1 wherein said inert and/or reactive gas is selected from the group consisting of nitrogen, argon, carbon dioxide, air and ammonia.
References Cited (Backward Citations)
US3023191A
Cited
US3242148A
Cited
US3510416A
Cited
US3936430A
Cited
GB1483064A
Cited
GB1483063A
Cited
US4185057A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1990-03-16 | 1990-09-15 | 1991-03-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-03-16 | 1994-09-15 | 1995-03-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-03-16 | 1998-09-15 | 1999-03-17 | $7700.00 | Window Closed / Lapsed |