US5062273A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for removal of gas from refrigeration system
Assignee: EIDP Inc
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Filing: 1990-07-12
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Granted: 1991-11-05
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Expires: 2010-07-12
Abstract
Abstract An improved process for separating and removing non-condensible gaseous contaminants (e.g., nitrogen, oxygen and the like) from a conventional halocarbon vapor compression refrigeration system by withdrawing a vapor stream above liquified refrigerant exiting the condenser on the high pressure side of the expansion valve and then processing this vapor by use of a second compression step, followed by condensation into a receiver. The liquid halocarbon from the receiver is returned to the evaporator while the vapor phase is sent to a semipermeable membrane separation unit. The halocarbon enriched effluent from the semipermeable membrane unit is recycled to the inlet side of the second compressor while the non-condensible contaminant enriched stream is vented from the refrigeration system. Such a high pressure purge loop is useful in selectively removing non-condensible gaseous with minimum halocarbon refrigerant loss.
Inventors
- 👤 Kung H. Lee
- 👤 Earl M. Clark
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 05:07
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/22; B01D53/229; B01D53/002; F; F25; F25B; F25B43/00; F25B43/04; F25B43/043
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
247 words
In a process wherein a halocarbon refrigerant is circulated, by use of a first compressor, from the high pressure outlet of the first compressor sequentially through a first condenser, a fluid expansion valve and an evaporator and then back to the low pressure inlet side of the compressor, the specific improvement comprising the steps of: (a) withdrawing at least a portion of the vapor phase present between the high pressure outlet of said first compressor and the high pressure side of said expansion valve means, wherein said vapor phase withdrawn contains non-condensible contaminants; (b) subjecting said vapor phase containing non-condensible contaminant of step (a) to a second compression to an even higher pressure; (c) passing the high pressure compressed vapor phase of step (b) through a second condenser to produce a condensed liquid phase halocarbon and a vapor phase enriched in non-condensible contaminant; (d) separating said liquid phase halocarbon produced in step (c) and returning said liquid phase halocarbon back to the liquid phase halocarbon refrigerant to be passed through an evaporator; (e) passing said vapor phase enriched in non-condensible contaminant produced in step (c) through a semipermeable membrane means to form a halocarbon enriched/non-condensible contaminant depleted first stream and a non-condensible contaminant enriched/halo-carbon depleted second stream; (f) recycling said halocarbon enriched/non-condensible contaminant depleted first stream produced in step (e) to the inlet side of said second compression step (b); and (g) removing said non-condensible contaminant enriched/halocarbon depleted second stream produced in step (e) from further circulation.
Claim 2
Dependent Claim
247 words
In a process wherein a halocarbon refrigerant is circulated, by use of a first compressor, from the high pressure outlet of the first compressor sequentially through a first condenser, a fluid expansion valve and an evaporator and then back to the low pressure inlet side of the compressor, the specific improvement comprising the steps of: (a) withdrawing at least a portion of the vapor phase present between the high pressure outlet of said first compressor and the high pressure side of said expansion valve means, wherein said vapor phase withdrawn contains non-condensible contaminants; (b) subjecting said vapor phase containing non-condensible contaminant of step (a) to a second compression to an even higher pressure; (c) passing the high pressure compressed vapor phase of step (b) through a second condenser to produce a condensed liquid phase halocarbon and a vapor phase enriched in non-condensible contaminant; (d) separating said liquid phase halocarbon produced in step (c) and returning said liquid phase halocarbon back to the liquid phase halocarbon refrigerant to be passed through an evaporator; (e) passing said vapor phase enriched in non-condensible contaminant produced in step (c) through a semipermeable membrane means to form a halocarbon enriched/non-condensible contaminant depleted first stream and a non-condensible contaminant enriched/halo-carbon depleted second stream; (f) recycling said halocarbon enriched/non-condensible contaminant depleted first stream produced in step (e) to the inlet side of said second compression step (b); and (g) removing said non-condensible contaminant enriched/halocarbon depleted second stream produced in step (e) from further circulation.
Claim 3
Dependent Claim
22 words
An improved process of claim 1 wherein said semipermeable membrane means produces a permeate enriched in halocarbon and depleted in non-condensible contaminant.
Claim 4
Dependent Claim
22 words
An improved process of claim 1 wherein said semipermeable membrane means produces a permeate enriched in non-condensible contaminant and depleted in halocarbon.
Claim 5
Dependent Claim
44 words
An improved process of claims 1, 2 or 3 wherein said separating of liquid phase halocarbon is performed by passing through a receiver and wherein said vapor phase enriched in non-condensible contaminant is passed through a filter before passing through said semipermeable membrane means.
Claim 6
Dependent Claim
207 words
In a halocarbon vapor compression refrigeration system wherein a primary compressor is used to circulate a halocarbon refrigerant from the high pressure outlet of said primary compressor sequentially through a primary condenser, a fluid expansion valve and an evaporator and then back to the low pressure inlet side of said primary compressor, the specific improvement comprising: (a) a second compressor in fluid communication with the vapor phase exiting said primary condenser before passing through said expansion valve; (b) a second condenser in fluid communication with the high pressure outlet side of said second compressor; (c) a receiver in fluid communication with the outlet of said second condenser; (d) a conduit means for returning condensed liquid phase halocarbon from said receiver back to said evaporator; (e) a semipermeable membrane separator means in fluid communication with the vapor phase of said receiver for separating said vapor phase from said receiver into a halocarbon enriched/non-condensible contaminant depleted stream and a non-condensible contaminant enriched/halocarbon depleted stream; (f) a conduit means to recycle said halocarbon enriched non-condensible contaminant depleted stream from said semipermeable membrane separator means to the inlet side of said second compressor; and (g) a means to vent said non-condensible contaminant enriched/halocarbon depleted stream from said semipermeable membrane separator means.
Claim 7
Dependent Claim
207 words
In a halocarbon vapor compression refrigeration system wherein a primary compressor is used to circulate a halocarbon refrigerant from the high pressure outlet of said primary compressor sequentially through a primary condenser, a fluid expansion valve and an evaporator and then back to the low pressure inlet side of said primary compressor, the specific improvement comprising: (a) a second compressor in fluid communication with the vapor phase exiting said primary condenser before passing through said expansion valve; (b) a second condenser in fluid communication with the high pressure outlet side of said second compressor; (c) a receiver in fluid communication with the outlet of said second condenser; (d) a conduit means for returning condensed liquid phase halocarbon from said receiver back to said evaporator; (e) a semipermeable membrane separator means in fluid communication with the vapor phase of said receiver for separating said vapor phase from said receiver into a halocarbon enriched/non-condensible contaminant depleted stream and a non-condensible contaminant enriched/halocarbon depleted stream; (f) a conduit means to recycle said halocarbon enriched non-condensible contaminant depleted stream from said semipermeable membrane separator means to the inlet side of said second compressor; and (g) a means to vent said non-condensible contaminant enriched/halocarbon depleted stream from said semipermeable membrane separator means.
Claim 8
Dependent Claim
27 words
An improved halocarbon vapor compression refrigeration system of claim 5 wherein said semipermeable membrane separator means produces a permeate enriched in non-condensible contaminant and depleted in halocarbon.
Claim 9
Dependent Claim
27 words
An improved halocarbon vapor compression refrigeration system of claim 5 wherein said semipermeable membrane separator means produces a permeate enriched in halocarbon and depleted in non-condensible contaminant.
Claim 10
Dependent Claim
29 words
An improved halocarbon vapor compression refrigeration system of claims 5, 6 or 7 further comprising a filter means for purifying said vapor phase entering said semipermeable membrane separator means.
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) | 1994-11-04 | 1995-05-06 | 1995-11-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1998-11-04 | 1999-05-06 | 1999-11-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2002-11-04 | 2003-05-06 | 2003-11-05 | $7700.00 | Window Closed / Lapsed |