← Back to Patent Explorer
US4906796A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying 1,1,1,2-tetrafluoroethane

Assignee: Honeywell International Inc
•
Filing: 1989-03-08
•
Granted: 1990-03-06
•
Expires: 2009-03-08
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract R-1122 (2-chloro-1,1-difluoro-ethylene) can be substantially removed from a stream of R-134a over a zeolite or carbon molecular sieve having a mean pore size of about 3.8 to 4.8 Angstroms. Preferred are 5A synthetic zeolites or calcium chabazite.

Inventors

  • 👤 Stephen F. Yates

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 03:19
CPC Classifications
C; C07; C07C; C07C19/00; C07C19/08; C07C17/00; C07C17/38; C07C17/389

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 62 words
A process for removing impurities from 1,1,1,2-tetrafluoroethane (R-134a) containing about 50-10,000 ppm by weight of 2-chloro-1,1-difluoro-ethylene (R-1122) comprising passing said 1,1,1,2-tetrafluoroethane over a zeolite having a mean pore size between 3.8 and 4.8 Angstroms at a temperature of -10° to 100° C. and a pressure of 100 to 860 kPa and recovering 1,1,1,2-tetrafluoroethane containing less than 10 ppm by weight of 2-chloro-1,1-difluoro-ethylene.
Claim 2
Dependent Claim 62 words
A process for removing impurities from 1,1,1,2-tetrafluoroethane (R-134a) containing about 50-10,000 ppm by weight of 2-chloro-1,1-difluoro-ethylene (R-1122) comprising passing said 1,1,1,2-tetrafluoroethane over a zeolite having a mean pore size between 3.8 and 4.8 Angstroms at a temperature of -10° to 100° C. and a pressure of 100 to 860 kPa and recovering 1,1,1,2-tetrafluoroethane containing less than 10 ppm by weight of 2-chloro-1,1-difluoro-ethylene.
Claim 3
Dependent Claim 13 words
The process of claim 1 wherein said zeolite is a 5A synthetic zeolite.
Claim 4
Dependent Claim 11 words
The process of claim 1 wherein said zeolite is calcium chabazite.
Claim 5
Dependent Claim 31 words
The process of claim 1 wherein said zeolite is a fixed bed of zeolite particles and the gas hourly space velocity of said 1,1,1,2-tetrafluoroethane is 130 to 3600 hr -1 .
Claim 6
Dependent Claim 25 words
The process of claim 1 wherein said zeolite is calcined to provide a loss on ignition at 900° C. of less than 6% by weight.
Claim 7
Dependent Claim 31 words
The process of claim 1 wherein said zeolite is a fixed bed of zeolite particles and the liquid hourly space velocity of said 1,1,1,2-tetrafluoroethane is 1 to 30 hr -1 .
Claim 8
Dependent Claim 62 words
A process for removing impurities from 1,1,1,2-tetrafluoroethane containing about 500-10000 ppm by weight of 2-chloro-1,1-difluoro-ethylene comprising passing said 1,1,1,2-tetrafluoroethane over a carbon molecular sieve having a mean pore size between 3.8 and 4.8 Angstroms at a temperature of -10° to 100° C. and a pressure of 100 to 860 kPa and recovering 1,1,1,2-tetrafluoroethane containing less than 10 ppm by weight of 2-chloro-1,1-difluoro-ethylene.
Claim 9
Dependent Claim 62 words
A process for removing impurities from 1,1,1,2-tetrafluoroethane containing about 500-10000 ppm by weight of 2-chloro-1,1-difluoro-ethylene comprising passing said 1,1,1,2-tetrafluoroethane over a carbon molecular sieve having a mean pore size between 3.8 and 4.8 Angstroms at a temperature of -10° to 100° C. and a pressure of 100 to 860 kPa and recovering 1,1,1,2-tetrafluoroethane containing less than 10 ppm by weight of 2-chloro-1,1-difluoro-ethylene.
Claim 10
Dependent Claim 33 words
The process of claim 7 wherein said carbon molecular sieve is a fixed bed of carbon particles and the gas hourly space velocity of said 1,1,1,2-tetrafluoroethane is 130 to 3600 hr -1 .
Claim 11
Dependent Claim 33 words
The process of claim 7 wherein said carbon molecular sieve is a fixed bed of carbon particles and the liquid hourly space velocity of said 1,1,1,2-tetrafluoroethane is 1 to 30 hr -1 .

References Cited (Backward Citations)

GB846677A Cited
US3215747A Cited
US3804910A Cited
US3819493A Cited
US4158675A Cited
US4129603A Cited
DE3311751A1 Cited
US4849558A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-03-05 1993-09-04 1994-03-06 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-03-05 1997-09-04 1998-03-06 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-03-05 2001-09-04 2002-03-06 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag