US4539816A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat and liquid recovery using open cycle heat pump system
Assignee: 3M Co
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Filing: 1983-01-24
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Granted: 1985-09-10
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Expires: 2003-01-24
Abstract
Abstract The present invention relates to the recovery of heat and/or condensable liquid from a gaseous environment utilizing an open cycle heat pump system. The open cycle heat pump system is employed to alter the temperature of a gas by compression, expansion, heat exchange, and combinations thereof, to condense selected vapors carried in the gaseous environment for removal from the gas. The open cycle heat pump system can also be used to extract the heat from a gas for use as desired.
Inventors
- 👤 Bryce J. Fox
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 22:40
CPC Classifications
F; F25; F25B; F25B9/00; F25B9/002; F25B9/004; B; B01; B01D; B01D3/00; B01D3/007; B01D53/00; B01D53/002; B01D53/005; Y; Y02; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
107 words
Apparatus for removing condensable vapor from a gas entering at nominally atmospheric pressure consisting essentially of, in sequence, means for compressing said entering gas to pressures not exceeding about 60 psia, means for cooling said compressed gas, single expansion means for expanding said compressed gas back to its nominal entering pressure to further cool said gas to temperatures below 0° C. and means for separating condensate from said gas, said apparatus further including means for causing said expanded gas to cool said compressed gas prior to expansion, said compressing and expanding means having efficiencies at least about 70%, and pressure ratios of about 1.3:1 to about 4:1.
Claim 2
Dependent Claim
107 words
Apparatus for removing condensable vapor from a gas entering at nominally atmospheric pressure consisting essentially of, in sequence, means for compressing said entering gas to pressures not exceeding about 60 psia, means for cooling said compressed gas, single expansion means for expanding said compressed gas back to its nominal entering pressure to further cool said gas to temperatures below 0° C. and means for separating condensate from said gas, said apparatus further including means for causing said expanded gas to cool said compressed gas prior to expansion, said compressing and expanding means having efficiencies at least about 70%, and pressure ratios of about 1.3:1 to about 4:1.
Claim 3
Dependent Claim
28 words
An apparatus according to claim 1 wherein the work produced by the expander is utilized to provide at least a portion of the driving force for the compressor.
Claim 4
Dependent Claim
21 words
An apparatus according to claim 1 wherein said cooling means is a heat exchanger means having condensate separating means associated therewith.
Claim 5
Dependent Claim
27 words
An apparatus according to claim 1 wherein at least one of said condensate separating means is located so that the gas stream exiting the expander passes therethrough.
Claim 6
Dependent Claim
28 words
An apparatus according to claim 4 wherein said condensate separating means includes a separating device selected from the group consisting of a demister, a coalescer or combinations thereof.
Claim 7
Dependent Claim
26 words
An apparatus according to claim 1 where said apparatus also includes an ice separating means for trapping ice which may form in the cooled gas stream.
Claim 8
Dependent Claim
97 words
Apparatus for removing condensable vapor from a gas entering at nominally atmospheric pressure comprising, in sequence, expander means for expanding said entering gas to cause cooling of said gas to temperatures below 0° C. and condensation of at least a portion of the condensable vapor therein, means for separating vapor condensed from said gas, and compressor means for compressing said gas back to its nominal entering pressure thereby providing a pressure differential for the expander, said compressing and expanding means having efficiencies of at least about 70% and having pressure ratios of about 1.3:1 to about 4:1.
Claim 9
Dependent Claim
97 words
Apparatus for removing condensable vapor from a gas entering at nominally atmospheric pressure comprising, in sequence, expander means for expanding said entering gas to cause cooling of said gas to temperatures below 0° C. and condensation of at least a portion of the condensable vapor therein, means for separating vapor condensed from said gas, and compressor means for compressing said gas back to its nominal entering pressure thereby providing a pressure differential for the expander, said compressing and expanding means having efficiencies of at least about 70% and having pressure ratios of about 1.3:1 to about 4:1.
Claim 10
Dependent Claim
19 words
An apparatus according to claim 7 comprising, in addition, a cooling means for cooling said gas prior to expansion.
Claim 11
Dependent Claim
25 words
An apparatus according to claim 8 wherein said cooling means comprises means for causing gas leaving the expander to cool said gas prior to expansion.
Claim 12
Independent Claim
105 words
A method of separating condensable vapor from a gas existing at nominally atmospheric pressure, said method consisting essentially of steps wherein said gas is compressed to pressures not exceeding about 60 psia, cooled via a heat exchange means and expanded in substantially a single expansion step back to nominally atmospheric pressure to produce further cooling to temperature below 0° C., said expanded gas being redirected through said heat exchange means to effect cooling of said compressed gas, condensed vapor being collected and removed from the gas, said compression being in the ragne of about 1.3:1 to about 4:1 and being at least about 70% efficient.
Claim 13
Independent Claim
105 words
A method of separating condensable vapor from a gas existing at nominally atmospheric pressure, said method consisting essentially of steps wherein said gas is compressed to pressures not exceeding about 60 psia, cooled via a heat exchange means and expanded in substantially a single expansion step back to nominally atmospheric pressure to produce further cooling to temperature below 0° C., said expanded gas being redirected through said heat exchange means to effect cooling of said compressed gas, condensed vapor being collected and removed from the gas, said compression being in the ragne of about 1.3:1 to about 4:1 and being at least about 70% efficient.
Claim 14
Dependent Claim
15 words
A method according to claim 10 wherein said condensable vapor is a non-aqueous organic material.
Claim 15
Dependent Claim
22 words
A method according to claim 11 wherein said condensable vapor is an organic hydrocarbon which is liquid at standard temperature and pressure.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-09-09 | 1989-03-11 | 1989-09-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-09-09 | 1993-03-11 | 1993-09-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-09-09 | 1997-03-11 | 1997-09-10 | $7700.00 | Window Closed / Lapsed |