US4625522A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing cold and/or heat by using a non-azeotropic mixture of fluids in a cycle with ejector
Assignee: IFP Energies nouvelles
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Filing: 1986-01-09
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Granted: 1986-12-02
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Expires: 2006-01-09
Abstract
Abstract Process for producing cold and/or heat by using a non-azeotropic mixture of fluids in a cycle with ejector. The working fluid is condensed (C), then separated in two fractions (2 and 7); the first fraction (2) is evaporated (EV) at relatively low temperature, the second fraction (7) is evaporated (B) at a relatively high temperature, and then the two vaporized fractions pass through an ejector (E) and are fed back to condenser (C). This process can be used for domestic heating or for refrigeration.
Inventors
- 👤 Jacques Cheron
- 👤 Alexandre Rojey
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 08:41
CPC Classifications
F; F25; F25B; F25B9/00; F25B9/002; F25B9/006; F25B1/00; F25B1/06
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
233 words
A process for producing cold and/or heat by using a working fluid (F), characterized by the steps of : (a) subjecting a working fluid (F), in gaseous state, to condensation under a pressure (CP) by transferring the condensation heat of fluid (F) to an external fluid, said fluid (F) comprising a non-azeotropic mixture of 5-95 %, in molar proportion, of a first constituent and 95-5 %, in molar proportion, of a second constituent miscible in liquid phase with the first consituent the constituents of said mixture being chemically different and capable of evaporating but not to crystallizing under the operating conditions of the process, (b) subjecting the resultant condensate to a pressure decrease and supplying heat thereto under said decreased pressure (EP) so as to partly evaporate it and separating the vaporized fraction (F1) from the liquid phase remaining fraction (F2), (c) increasing the pressure of fraction (F2) up to a pressure (BP) higher than the pressure (CP) of step (a) and supplying heat to said fraction (F2), so as to obtain it (F2) in vapor phase, and (d) subjecting the vapor phase fraction (F2) obtained in step (c) to expansion through ejection means and driving along with said expanded fraction the vapor phase fraction (F1) obtained from step (b), so as to admix said two fractions and to reconstitute the fluid (F) in gaseous state at the pressure (CP) of step (a).
Claim 2
Dependent Claim
233 words
A process for producing cold and/or heat by using a working fluid (F), characterized by the steps of : (a) subjecting a working fluid (F), in gaseous state, to condensation under a pressure (CP) by transferring the condensation heat of fluid (F) to an external fluid, said fluid (F) comprising a non-azeotropic mixture of 5-95 %, in molar proportion, of a first constituent and 95-5 %, in molar proportion, of a second constituent miscible in liquid phase with the first consituent the constituents of said mixture being chemically different and capable of evaporating but not to crystallizing under the operating conditions of the process, (b) subjecting the resultant condensate to a pressure decrease and supplying heat thereto under said decreased pressure (EP) so as to partly evaporate it and separating the vaporized fraction (F1) from the liquid phase remaining fraction (F2), (c) increasing the pressure of fraction (F2) up to a pressure (BP) higher than the pressure (CP) of step (a) and supplying heat to said fraction (F2), so as to obtain it (F2) in vapor phase, and (d) subjecting the vapor phase fraction (F2) obtained in step (c) to expansion through ejection means and driving along with said expanded fraction the vapor phase fraction (F1) obtained from step (b), so as to admix said two fractions and to reconstitute the fluid (F) in gaseous state at the pressure (CP) of step (a).
Claim 3
Dependent Claim
45 words
A process according to claim 1, wherein the liquid phase fraction (F2) at pressure (BP), before being subjected to vaporization in step (c), is contacted in heat exchange conditions with the liquid phase resulting from the condensation of fluid (F), before decreasing the pressure thereof.
Claim 4
Dependent Claim
41 words
A process according to claim 1 , wherein the vaporized fraction (F1), before being fed to the ejection means, is contacted in heat exchange conditions with the liquid phase resulting from the condensation of fluid (F), before decreasing the pressure thereof.
Claim 5
Dependent Claim
23 words
A process according to claim 1, comprising means for keeping apart a portion of the liquid phase obtained by condensation of fluid (F).
Claim 6
Dependent Claim
45 words
A process according to claim 1, wherein the working fluid (F) consists of a non-azeotropic mixture containing (in molar proportion) 80-95 % of water and 5-20% of at least one compound soluble in water whose normal boiling point ranges from 100° C. to -50° C.
Claim 7
Dependent Claim
22 words
A process according to claim 1, wherein the working fluid (F) consists of a mixture of water with at least one alcohol.
Claim 8
Dependent Claim
19 words
A process according to claim 1, wherein the working fluid (F) consists of a mixture of water with ammonia.
Claim 9
Dependent Claim
22 words
A process according to claim 1, wherein the working fluid (F) consists of a mixture of water with at least one ketone.
Claim 10
Dependent Claim
22 words
A process according to claim 1, wherein fractions (F1) and (F2) respectively amount to 20-80% and 80-20% by mole of mixture (F).
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) | 1989-12-01 | 1990-06-02 | 1990-12-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-12-01 | 1994-06-02 | 1994-12-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-12-01 | 1998-06-02 | 1998-12-02 | $7700.00 | Window Closed / Lapsed |