US3980723A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purging of inerts in chlorinated hydrocarbon production
Assignee: Lummus Technology LLC
•
Filing: 1974-12-23
•
Granted: 1976-09-14
•
Expires: 1994-12-23
Abstract
Abstract In the production of chlorinated hydrocarbons, a gas stream, containing hydrocarbon and carbon monoxide and/or nitrogen, as inerts, is separated from the effluent, and contacted with chlorinated hydrocarbon, as an absorption liquid, to absorb unreacted hydrocarbon. The absorbed hydrocarbon is stripped from the solution and recycled to the chlorinated hydrocarbon production. The process is particularly applicable to the production of chlorinated methanes and vinyl chloride.
Inventors
- 👤 Herbert Riegel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 20:39
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/38; B; B01; B01D; B01D11/00; B01D11/04; B01D11/0426; B01D11/0488
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
142 words
In a process for producing chlorinated hydrocarbons wherein an effluent containing chlorinated hydrocarbons, unreacted hydrocarbon and inert gas selected from the group consisting of carbon monoxide, nitrogen and mixtures thereof is withdrawn from a chlorinated hydrocarbon production reaction zone, the improvement comprising: recovering from the effluent a gaseous stream comprising unreacted hydrocarbon and said inert gas; contacting said gaseous stream with a liquid absorbent comprising a chlorinated hydrocarbon having a number of carbon atoms equal to the number of carbon atoms of the unreacted hydrocarbon to absorb unreacted hydrocarbon from said gaseous stream, said contacting being effected at a temperature of from 80°F to 200°F and a pressure of from 50 to 400 psig; separating the liquid absorbent containing absorbed unreacted hydrocarbon from the gaseous stream; stripping unreacted hydrocarbon from the liquid absorbent; and recycling stripped unreacted hydrocarbon to the reaction zone.
Claim 2
Dependent Claim
142 words
In a process for producing chlorinated hydrocarbons wherein an effluent containing chlorinated hydrocarbons, unreacted hydrocarbon and inert gas selected from the group consisting of carbon monoxide, nitrogen and mixtures thereof is withdrawn from a chlorinated hydrocarbon production reaction zone, the improvement comprising: recovering from the effluent a gaseous stream comprising unreacted hydrocarbon and said inert gas; contacting said gaseous stream with a liquid absorbent comprising a chlorinated hydrocarbon having a number of carbon atoms equal to the number of carbon atoms of the unreacted hydrocarbon to absorb unreacted hydrocarbon from said gaseous stream, said contacting being effected at a temperature of from 80°F to 200°F and a pressure of from 50 to 400 psig; separating the liquid absorbent containing absorbed unreacted hydrocarbon from the gaseous stream; stripping unreacted hydrocarbon from the liquid absorbent; and recycling stripped unreacted hydrocarbon to the reaction zone.
Claim 3
Dependent Claim
26 words
The process of claim 1 wherein the gaseous stream further comprises carbon dioxide, said carbon dioxide being absorbed with the unreacted hydrocarbon by the liquid absorbent.
Claim 4
Dependent Claim
32 words
The process of claim 2 wherein the gaseous stream further comprises at least one chlorinated hydrocarbon, said at least one chlorinated hydrocarbon being absorbed by the liquid absorbent with the unreacted hydrocarbon.
Claim 5
Dependent Claim
32 words
The process of claim 1 wherein the unreacted hydrocarbon is methane and said liquid absorbent comprises at least one member selected from the group consisting of methylene chloride, chloroform and carbon tetrachloride.
Claim 6
Dependent Claim
29 words
The process of claim 4 where in the gaseous stream further comprises carbon dioxide and chlorinated methanes, said carbon dioxide and chlorinated methanes being absorbed by the liquid absorbent.
Claim 7
Dependent Claim
27 words
The process of claim 5 wherein the stripping is effected at a temperature of from 180°F to 280°F and a pressure of from 1 to 50 psig.
Claim 8
Dependent Claim
12 words
The process of claim 5 wherein the liquid absorbent is carbon tetrachloride.
Claim 9
Dependent Claim
23 words
The process of claim 1 wherein the unreacted hydrocarbon is a member selected from the group consisting of ethane, ethylene and mixtures thereof.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-09-14 | 1980-03-15 | 1980-09-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-09-14 | 1984-03-15 | 1984-09-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-09-14 | 1988-03-15 | 1988-09-14 | $7700.00 | Window Closed / Lapsed |