US4898645A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the production of pure tetrafluoroethylene
Assignee: Hoechst AG
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Filing: 1988-08-30
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Granted: 1990-02-06
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Expires: 2008-08-30
Abstract
Abstract A process is described for the production of pure tetrafluoroethylene from a gas formed in the pyrolysis of a fluorocarbon compound having 1 to 4 carbon atoms, which can contain a hydrogen atom and a chlorine atom. The pyrolysis gas, after hydrogen chloride or hydrogen fluoride and also if necessary steam have been separated off, is condensed under pressure and distilled in a plurality of columns, in the first column the low boilers being distilled off, preferably with a reflux ratio of 6 to 15 kg per kg of tetrafluoroethylene produced, and in the second column tetrafluoroethylene, preferably with a reflux ratio of 3 to 5 kg per kg of tetrafluoroethylene produced. Per kg of tetrafluoroethylene produced, from 0.6 to 2 kg of difluoromonochloromethane are fed into the second column as a distillation aid. The novel process makes it possible to produce pure tetrafluoroethylene at comparatively reduced energy and apparatus costs.
Inventors
- 👤 Hartmut Voigt
- 👤 Reinhold Freudenreich
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 21:10
CPC Classifications
C; C07; C07C; C07C17/00; C07C17/38
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
235 words
In a process for the production of pure tetrafluoroethylene from the gaseous pyrolysis products of a pyrolyzable C 1 to C 4 fluorocarbon which is pyrolyzable to form tetrafluoroethylene, said gaseous pyrolysis products comprising 20 to 70 percent by weight of tetrafluoroethylene and being essentially dry and essentially freed of any hydrogen chloride or hydrogen fluoride, condensing said pyrolysis gas to obtain a liquefied portion of the gas, introducing this liquefied portion of the gas into a first distillation column and separating by distillation at the top end of this column as a top product of the first column components boiling at a lower temperature than does tetrafluoroethylene, thereby forming a bottom product of the first distillation column and introducing this bottom product through an inlet into a second distillation column, distilling off pure tetrafluoroethylene as a top product of the second distillation column and discharging at the bottom of said column components boiling at a higher temperature than does tetrafluoroethylene, the improvement which comprises introducing into the second distillation column above the inlet for the bottom product of the first distillation column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second distillation column above the inlet for the bottom product of the first distillation column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second distillation column.
Claim 2
Dependent Claim
235 words
In a process for the production of pure tetrafluoroethylene from the gaseous pyrolysis products of a pyrolyzable C 1 to C 4 fluorocarbon which is pyrolyzable to form tetrafluoroethylene, said gaseous pyrolysis products comprising 20 to 70 percent by weight of tetrafluoroethylene and being essentially dry and essentially freed of any hydrogen chloride or hydrogen fluoride, condensing said pyrolysis gas to obtain a liquefied portion of the gas, introducing this liquefied portion of the gas into a first distillation column and separating by distillation at the top end of this column as a top product of the first column components boiling at a lower temperature than does tetrafluoroethylene, thereby forming a bottom product of the first distillation column and introducing this bottom product through an inlet into a second distillation column, distilling off pure tetrafluoroethylene as a top product of the second distillation column and discharging at the bottom of said column components boiling at a higher temperature than does tetrafluoroethylene, the improvement which comprises introducing into the second distillation column above the inlet for the bottom product of the first distillation column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second distillation column above the inlet for the bottom product of the first distillation column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second distillation column.
Claim 3
Dependent Claim
42 words
The process as claimed in claim 1, wherein 3 to 5 kg of the top product of the second distillation column per 1 kg of tetrafluoroethylene discharged at the top of the second distillation column are condensed and recycled into this column.
Claim 4
Dependent Claim
44 words
The process as claimed in claim 1, wherein 6 to 15 kg of the top product of the first distillation column per 1 kg of tetrafluoroethylene discharged from the top of the second distillation column are condensed and recycled into the first distillation column.
Claim 5
Dependent Claim
25 words
The process as claimed in claim 1, wherein the first and second distillation columns are operated in the pressure range from 0.4 to 0.5 MPa.
Claim 6
Dependent Claim
13 words
The process as claimed in claim 1, wherein the compound pyrolyzed is difluoromonochloromethane.
Claim 7
Dependent Claim
24 words
The process as claimed in claim 1, wherein the C 1 to C 4 fluorocarbon is difluoromonochloromethane, tetrafluoromonochloroethane, trifluoromethane, perfluorocyclobutane or a mixture thereof.
Claim 8
Dependent Claim
26 words
The process as claimed in claim 1, wherein the components discharged at the bottom of the second distillation column are processed to recover additional fluorocarbon compounds.
Claim 9
Dependent Claim
179 words
A process for the production of pure tetrafluoroethylene from the gaseous pyrolysis products of a C 1 to C 4 fluorocarbon which is pyrolyzable to form a gas containing 20 to 70 weight-% tetrafluoroethylene, said gas being condensable to form a liquefied portion comprising tetrafluoroethylene, high-boiling constituents having a boiling temperature higher than that of tetrafluoroethylene, and low-boiling constituents having a boiling temperature lower than that of tetrafluoroethylene, said process comprising: condensing said gas to form said liquefied portion, introducing said liquefied portion into a first distillation column and separating by distillation at the top of the this column said high-boiling constituents while removing as a bottom product tetrafluoroethylene and said low-boiling constituents from the bottom of this column, introducing said bottom product into a second distillation column and distilling off pure tetrafluoroethylene as a top product of the second distillation column, and introducing into the second distillation column above the inlet for the bottom product of the first column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second column.
Claim 10
Dependent Claim
179 words
A process for the production of pure tetrafluoroethylene from the gaseous pyrolysis products of a C 1 to C 4 fluorocarbon which is pyrolyzable to form a gas containing 20 to 70 weight-% tetrafluoroethylene, said gas being condensable to form a liquefied portion comprising tetrafluoroethylene, high-boiling constituents having a boiling temperature higher than that of tetrafluoroethylene, and low-boiling constituents having a boiling temperature lower than that of tetrafluoroethylene, said process comprising: condensing said gas to form said liquefied portion, introducing said liquefied portion into a first distillation column and separating by distillation at the top of the this column said high-boiling constituents while removing as a bottom product tetrafluoroethylene and said low-boiling constituents from the bottom of this column, introducing said bottom product into a second distillation column and distilling off pure tetrafluoroethylene as a top product of the second distillation column, and introducing into the second distillation column above the inlet for the bottom product of the first column 0.6 to 2 kg of difluoromonochloromethane per 1 kg of tetrafluoroethylene discharged from the top of the second column.
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) | 1993-02-05 | 1993-08-07 | 1994-02-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-02-05 | 1997-08-07 | 1998-02-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-02-05 | 2001-08-07 | 2002-02-06 | $7700.00 | Window Closed / Lapsed |