US4003215A
Expired / Lapsed
US
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Absorption refrigeration system
Assignee: Adelaide University
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Filing: 1975-06-20
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Granted: 1977-01-18
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Expires: 1995-06-20
Abstract
Abstract An absorption refrigeration system utilising a pair of refrigerant fluids one of which constitutes a distillate, the other of which constitutes an absorber, the fluids being separated from one another in a closed circuit, by a distillation process, the more volatile vapor phase (namely the distillate) being condensed to form a liquid phase, expanded, evaporated, and re-absorbed in the less volatile product (namely the absorbent) of the distillation process, each of the refrigerant fluids being a fluoro-carbon compound, the differences of respective boiling points of said pair of fluids being substantially smaller than the corresponding boiling point temperature difference pertaining to the ammonia/water absorption system, the system being characterized in that it is able to operate with a higher temperature cooling medium for the distillation column condenser while utilizing a lower grade of heat in the distillation column re-boiler.
Inventors
- 👤 John Robert Roach
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 18:33
CPC Classifications
F; F25; F25B; F25B15/00; C; C09; C09K; C09K5/00; C09K5/02; C09K5/04; C09K5/047; Y; Y02; Y02A; Y02A30/00; Y02A30/27; Y02B; Y02B30/00; Y02B30/62; Y02P; Y02P20/00; Y02P20/10
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
258 words
In an absorption refrigeration system utilizing a pair of fluids, said system comprising: a distillation column, a distillation column heat exchanger for introducing heat into the distillation column for distilling one of said fluids from the other said fluid to form a distilled fluid and a distillation residue, a condenser heat exchanger in fluid flow communication with said distillation column and arranged for condensing of the distilled fluid to produce a condensate, an expansion valve through which passes said condensate, an evaporator heat exchanger for evaporation of the condensate, an absorber and an absorber heat exchanger in fluid flow communication with said evaporator heat exchanger, wherein the evaporated condensate is absorbed into the distillation residue to thereby form a liquid mixture, said absorber heat exchanger being arranged to maintain the vapour pressure in the absorber, below the vapour pressure in the distillation column, and means to effect re-cycling of said liquid mixture within the system, the improvement wherein each fluid of said pair of fluids is a fluorocarbon compound having refrigerant properties, said fluids having different boiling points, and the absolute difference between respective boiling points of said fluids, at a given pressure, lies in the range of 30°-60° C, and the system operates (a) at a temperature for said condenser heat exchanger which is higher than is required when the boiling point difference is other than 30°-60° C and (b) with a grade of heat in said distillation column heat exchanger which is lower than is required when said boiling point difference is other than 30°-60° C.
Claim 2
Dependent Claim
258 words
In an absorption refrigeration system utilizing a pair of fluids, said system comprising: a distillation column, a distillation column heat exchanger for introducing heat into the distillation column for distilling one of said fluids from the other said fluid to form a distilled fluid and a distillation residue, a condenser heat exchanger in fluid flow communication with said distillation column and arranged for condensing of the distilled fluid to produce a condensate, an expansion valve through which passes said condensate, an evaporator heat exchanger for evaporation of the condensate, an absorber and an absorber heat exchanger in fluid flow communication with said evaporator heat exchanger, wherein the evaporated condensate is absorbed into the distillation residue to thereby form a liquid mixture, said absorber heat exchanger being arranged to maintain the vapour pressure in the absorber, below the vapour pressure in the distillation column, and means to effect re-cycling of said liquid mixture within the system, the improvement wherein each fluid of said pair of fluids is a fluorocarbon compound having refrigerant properties, said fluids having different boiling points, and the absolute difference between respective boiling points of said fluids, at a given pressure, lies in the range of 30°-60° C, and the system operates (a) at a temperature for said condenser heat exchanger which is higher than is required when the boiling point difference is other than 30°-60° C and (b) with a grade of heat in said distillation column heat exchanger which is lower than is required when said boiling point difference is other than 30°-60° C.
Claim 3
Dependent Claim
30 words
An absorption refrigeration system according to claim 1 wherein the absolute difference between respective boiling points of said fluids, at a given pressure, lies in the range of 35°-55° C.
Claim 4
Dependent Claim
30 words
An absorption refrigeration system according to claim 1 wherein the absolute difference between respective boiling points of said fluids, at a given pressure lies in the range of 40°-50° C.
Claim 5
Dependent Claim
46 words
An absorption refrigeration system according to claim 2 wherein said pair of fluids is selected from the group consisting of the following pairs of fluoro-carbon compounds: Trichloromonofluoromethane/Dichlorodifluoromethane; Trichloromonofluoromethane/Dichlorohexafluorocyclobutane; Dichlorodifluoromethane/Monochlorotrifluoromethane; Dichlorodifluoromethane/Trifluoromethane; Dichlorodifluoromethane/Monochloroheptafluorocyclobutane; Bromochlorodifluoromethane/Monobromotrifluoromethane; Bromochlorodifluoromethane/Monochlorodifluoromethane; Bromochlorodifluoromethane/Trichlorotrifluoroethane; Bromochlorodifluoromethane/Monochloropentafluoroethane; Monochlorotrifluoromethane/Monochlorodifluoromethane; Monochlorotrifluoromethane/Monochloropentafluoroethane; Monobromotrifluoromethane/Octafluorocyclobutane; Monochlorodifluoromethane/Trifluoromethane; Monochlorodifluoromethane/Dichlorotetrafluoroethane; Monochlorodifluoromethane/Octafluorocyclobutane; Trifluoromethane/Monochloropentafluoroethane; Trichlorotrifluoroethane/Dichlorotetrafluoroethane; Trichlorotrifluoroethane/Octafluorocyclobutane; Dichlorotetrafluoroethane/Monochloropentafluoroethane; Dichlorohexafluorocyclobutane/Monochloroheptafluorocyclo-butane.
Claim 6
Dependent Claim
33 words
An absorption refrigeration system according to claim 3 wherein said pair of fluids is selected from the group consisting of the following pairs of fluorocarbon compounds: Monochlorotrifluoromethane/Monochlorodifluoromethane; Monochlorotrifluoromethane/Monochloropentafluoroethane; Monochlorodifluoromethane/Trifluoromethane; Monochlorodifluoromethane/Dichlorotetrafluoroethane; Trifluoromethane/Monochloropentafluoroethane; Trichlorotrifluoroethane/Dichlorotetrafluoroethane; Dichlorotetrafluoroethane/Monochloropentafluoroethane.
Claim 7
Dependent Claim
22 words
An absorption refrigeration system according to claim 1 wherein the pair of fluorocarbon compounds differ by one chlorine and one fluorine atom.
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) | 1980-01-18 | 1980-07-19 | 1981-01-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-01-18 | 1984-07-19 | 1985-01-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-01-18 | 1988-07-19 | 1989-01-18 | $7700.00 | Window Closed / Lapsed |