US4299606A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Recovery of HF and HCl from gaseous mixtures thereof
Assignee: Occidental Chemical Corp
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Filing: 1978-01-03
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Granted: 1981-11-10
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Expires: 1998-01-03
Abstract
Abstract A process is disclosed for recovering HF and HCl in substantially purified form from a gaseous mixture containing HF, HCl and halogenated organic vapors. The process comprises: A. feeding the gaseous mixture to the lower part of a rectification column to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40 DEG C. to about -85 DEG C., and having a temperature in its lower part in the range of from about -30 DEG C. to about 19 DEG C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gas from the top of the rectification column, and feeding the thus withdrawn gas to a condenser, D. condensing at least a portion of the withdrawn gas of step C to a liquid, E. feeding a portion of the condensed liquid of step D to the upper part of the rectification column, and F. recovering HCl gas from the condenser.
Inventors
- 👤 Stephen Robota
- 👤 Alastair J. H. McGregor
- 👤 Gregory A. R. Trollope
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 03:36
CPC Classifications
C; C01; C01B; C01B7/00; C01B7/01; C01B7/07; C01B7/0706; C01B7/0712; C01B7/19; C01B7/191; C01B7/195; C01B7/196; Y; Y10; Y10S; Y10S62/00; Y10S62/931
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
137 words
A substantially anhydrous process for separating HF and HCl from a gaseous mixture thereof comprising A. feeding the gaseous mixture to the lower part of a rectification column, to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40° C. to about -85° C., and having a temperature in its lower part in the range of from about -30° C. to about 19° C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gaseous HCl from the upper part of the rectification column, D. feeding liquid HCl to the upper part of the rectification column to provide a downward flow of liquid countercurrent to the upward flow of gases.
Claim 2
Dependent Claim
137 words
A substantially anhydrous process for separating HF and HCl from a gaseous mixture thereof comprising A. feeding the gaseous mixture to the lower part of a rectification column, to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40° C. to about -85° C., and having a temperature in its lower part in the range of from about -30° C. to about 19° C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gaseous HCl from the upper part of the rectification column, D. feeding liquid HCl to the upper part of the rectification column to provide a downward flow of liquid countercurrent to the upward flow of gases.
Claim 3
Dependent Claim
167 words
A process according to claim 1 for separating HF and HCl from a gaseous mixture thereof comprising A. feeding the gaseous mixture to the lower part of a rectification column to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40° C. to about -85° C., and having a temperature in its lower part in the range of from about -30° C. to about 19° C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gas from the top of the rectification column, and feeding the thus withdrawn gas to a condenser, D. condensing at least a portion of the withdrawn gas of step C to a liquid, E. feeding at least a portion of the condensed liquid of step D to the rectification column in the upper part of the column, F. recovering HCl gas from the condenser.
Claim 4
Dependent Claim
198 words
A process according to claim 1 for separating HF, HCl and halogenated organic compounds from a gaseous mixture thereof comprising A. feeding the gaseous mixture to the lower part of a rectification column to provide an upward flow of gases therein, the column having a temperature in the lower part of about -30° C. to about 19° Celsius, and having a temperature in the upper part of about -85° to about -40° Celsius; B. withdrawing a gas from the upper portion of the rectification column, and feeding the withdrawn gas to a condenser; C. condensing at least a portion of the withdrawn gas of step B to a liquid, D. feeding at least a portion of the liquid of step C to the upper part of the rectification column to provide a downward flow of liquid, countercurrent to the upward flow of gases, E. withdrawing HCl gas from the condenser, F. withdrawing a liquid mixture of HF and halogenated organic compounds from the bottom of the rectification column, G. transferring the liquid mixture of step F to a settling tank and separating the mixture by gravity into a liquid HF phase and a liquid halogenated organic phase; and
Claim 5
Dependent Claim
24 words
A process according to claim 3 wherein said halogenated organic compounds are characterized by a freezing point of about -60° to about 20° Celsius.
Claim 6
Dependent Claim
23 words
A process according to claim 4 wherein said gaseous mixture comprises less than about 25 percent by weight of said halogenated organic compounds.
Claim 7
Dependent Claim
30 words
A process according to claim 5 wherein said gaseous mixture comprises the effluent gas from a process for the fluorination of a chloromethyl aromatic compound by reaction with hydrogen fluoride.
Claim 8
Dependent Claim
14 words
A process according to claim 6 wherein said halogenated organic compound is a benzotrihalide.
Claim 9
Dependent Claim
169 words
In a process which comprises reacting a chloromethyl aromatic compound with an excess of hydrogen fluoride to form a fluoromethyl aromatic compound, the improvement which comprises treating the off-gas therefrom, comprising a gaseous mixture of HF, HCl and fluoromethyl aromatic vapors, by a substantially anhydrous process comprising A. feeding the gaseous mixture to the lower part of a rectification column, to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40° C. to about -85° C., and having a temperature in its lower part in the range of from about -30° C. to about 19° C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gaseous HCl from the upper part of the rectification column, D. feeding liquid HCl to the upper part of the rectification column to provide a downward flow of liquid countercurrent to the upward flow of gases.
Claim 10
Dependent Claim
169 words
In a process which comprises reacting a chloromethyl aromatic compound with an excess of hydrogen fluoride to form a fluoromethyl aromatic compound, the improvement which comprises treating the off-gas therefrom, comprising a gaseous mixture of HF, HCl and fluoromethyl aromatic vapors, by a substantially anhydrous process comprising A. feeding the gaseous mixture to the lower part of a rectification column, to provide an upward flow of gases therein, the column having a temperature in the upper part of from about -40° C. to about -85° C., and having a temperature in its lower part in the range of from about -30° C. to about 19° C., the column also having a countercurrent flow of a liquid and a gas, B. withdrawing liquid HF from the bottom of the rectification column, C. withdrawing a gaseous HCl from the upper part of the rectification column, D. feeding liquid HCl to the upper part of the rectification column to provide a downward flow of liquid countercurrent to the upward flow of gases.
Claim 11
Dependent Claim
62 words
A process according to claim 8 wherein the gaseous HCl withdrawn from the upper part of the rectification column is fed to a condenser and at least a portion of gaseous HCl is condensed therein and the liquid returned to the upper part of the column to provide the liquid HCl of Step (D) and HCl gas is recovered from the condenser.
Claim 12
Dependent Claim
24 words
A process according to claim 9 wherein the gaseous mixture entering the lower part of the rectification column comprises HF, HCl, and benzotrifluoride vapors.
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) | 1984-11-09 | 1985-05-11 | 1985-11-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-11-09 | 1989-05-11 | 1989-11-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-11-09 | 1993-05-11 | 1993-11-10 | $7700.00 | Window Closed / Lapsed |