US3742726A - Absorption refrigeration system - Google Patents

Absorption refrigeration system Download PDF

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US3742726A
US3742726A US00149280A US3742726DA US3742726A US 3742726 A US3742726 A US 3742726A US 00149280 A US00149280 A US 00149280A US 3742726D A US3742726D A US 3742726DA US 3742726 A US3742726 A US 3742726A
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fluid
pump means
refrigerant
pump
inlet
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R English
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Carrier Corp
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00—Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/02—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas
    • F25B15/04—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being ammonia evaporated from aqueous solution
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S62/00—Refrigeration
    • Y10S62/02—Refrigerant pumps

Definitions

  • An absorptlon refrlgeratlon system employmg a sec-,- ondary refrigerant to transfer heat from a suitable heat [56] References Cited exchanger to the system evaporator; pump means to circulate absorbent solution and the secondary refrig- UNITED STATES PATENTS erant; and ejec tors for increasing pump inlet pressures (I) gllsgandj 5 to prevent refrigerant flashing at the pump inlets. 0e er, 1'.
  • an absorption refrigeration system is provided with a secondary circuit employing chilled water.
  • the water chilled by the absorption refrigeration machine is circulated to a heat exchanger within the conditioned space, warm air from the space being circulated over the heat exchanger to cool the air for distribution throughout the conditioned space.
  • the warm water from the heat exchanger is returned to the absorption refrigeration machine for transferring the heat therein to the evaporator or chiller of the refrigerationmachine.
  • a halogenated hydrocarbon refrigerant such as dichlorodifluoromethane in the secondary circuit.
  • Pump means are ordinarily provided to circulate the absorbent solution within the absorption machine circuit and to circulate the chilled water or the halogenated hydrocarbon refrigerant to the heat exchangers within the conditioned space.
  • the pressuresat the pump inlets may be below the vapor pressure of the fluid being pumped, resulting in flashing of the fluid andinefficient pump operation.
  • This invention relates to an absorption refrigeration system including an absorber, a condenser, an evaporator and a generator connected to provide refrigeration.
  • a heat exchanger is operatively associated with the evaporator for circulation of refrigerant between the evaporatorand the heat exchanger.
  • First pump means to transfer solution from the absorber to the generator and second pump means to circulate refrigerant between the evaporator and the heat exchanger are provided.
  • At least one of said pump means is provided with an ejector including nozzle means for discharging a portion of the fluid from the discharge side of the pump associated therewith into the throat of the ejector to maintain pressure at the pump inlet above the vapor pressure of the fluid being pumped to prevent flashing of the fluid at the pumpinlet.
  • FIG. [of the drawings there is shown a refrigeration system comprising an absorber 10, a
  • condenser I2 a chiller l4 and a generator 16 connected to provide refrigeration.
  • a pump 20 is employed to circulate weak absorbent solution from absorber [0 to generator 16.
  • weak solution or weak absorbent-solution refer to solution which is weak in absorbent power and the terms strong solution or “strong absorbent solution refer to solution which is strong in absorbent power.
  • strong absorbent solution refer to solution which is strong in absorbent power.
  • suitable absorbent for use in the system described is water and a suitable refrigerant is ammonia.
  • Liquid refrigerant condensed in condenser 12 passes through refrigerant liquid'passage 22 and refrigerant restrictor 24 to heat exchange tube 26 of liquid suction heat exchanger 27
  • the liquid refrigerant which is cooled in tube 26 passes through refrigerant restriction 28 into heat exchange coil 30 of chiller 14.
  • a heat exchange medium such as a halogenated hydrocarbon refrigerant for example, dichlorodifluoromethane, is passed over the exterior of coil 30 where it is chilled by giving up heat to evaporate the refrigerant within heat exchange coil 30.
  • a halogenated hydrocarbon refrigerant for example, dichlorodifluoromethane
  • the chilled heat exchange medium is collected in the lower portion of chiller 1 4 for subsequent passage through line 32 to a pulser type pump 34.
  • the pump 34 includes a housing 36 having an inlet opening 38 and discharge opening 40.
  • a suction valve 42 is disposed within inlet opening 38 and a discharge valve 44 is disposed within discharge opening 40.
  • a flexible diaphragm 46 is mounted within housing 36.
  • a pulsating flow, of hydraulic fluid from a suitable hydraulic pump 48 is provided to the interior of diaphragm 46.
  • diaphragm 46 When hydraulic fluid under. pressure is supplied to diaphragm 46, the diaphragm is expanded outwardly toward the housing walls. The heat exchange medium in space St) between the diaphragm and housing is forced through discharge valve 44 into discharge line 52. When the hydraulic pressure within the diaphragm is released, the diaphragm contracts. This allows heat exchange medium to pass through suction valve 42 into space 50. Thus, the pulsing hydraulic pressure in diaphragm 46* causes heat exchange medium to be pumped from line 32 to line 52.
  • an ejector 54 having a throat 56 is provided in line 32 to increase the pressure of the heat exchange medium at the pumpinlet.
  • a nozzle 58, disposed adjacent throat 56 is adapted to inject a portion of the heat exchange medium flowing through line 52 into throat 56 to provide a pressure downstream from the ejector sufflcient to prevent flashing of the heat exchange medium.
  • the chilled heat exchange medium passes through line 52 to suitable remote heat exchangers (not shown) after which it is returned to the chiller through line 68.
  • the refrigerant evaporated in heat exchange coil 30 passes through refrigerant vapor passage of liquid suction heat exchanger 27 in heat exchange relation with liquid refrigerant passing through tube 26.
  • Refrig erant vapor having a small proportion of absorbent liqmote the absorption of the refrigerant vapor by the solution.
  • the same cooling medium may be supplied to condenser 12 in heat exchange relation with refrigerant vapor therein to condense the refrigerant.
  • Cold weak absorbent solution passes from absorber through a line 80 into weak solution pump 20.
  • Pump may be of the same general design as pump 34, the hydraulic pump 48 being adapted to supply a pulsating flow of hydraulic fluid to pump 20 and pump 34.
  • Liquid from pump 20 passes through pump discharge line 82 to rectifier heat exchange coil 84.
  • the weak solution passes through coil 84 in heat exchange relation with hot strong solution passing through heat exchange coil 86 disposed within coil 84 and with the hot refrigerant vapor flowing through rectifier shell 87 in contact with the outer surface of coil 84.
  • the weak solution from coil 84 is discharged into the upper portion of generator 16 along with any vapor which is formed in coil 84 due to heat exchange with the hot vapor passing thereover and the hot solution flowing therethrough.
  • I Generator 16 comprises a shell 90 having fins 92 suitably affixed thereto, as by welding.
  • the generator is heated by a gas burner 94 or other suitable heating means.
  • the weak solution is boiled in generator 16 to concentrate the solution, thereby forming a strong solution and refrigerant vapor.
  • the hot strong absorbent solution passes upwardly through the analyzer section of generator 16 through analyzer coil 96 in heat exchange with weak solution passing downwardly over the coil.
  • the warm strong solution then passes through heat exchange coil 86 and line 76 into vapor distributor 74.
  • a restrictor 98 is provided in line 76 so that the solution supplied to the vapor distributor is at the same pressure as the vapor in vapor distributor 74.
  • Refrigerant vapor formed in generator 16 passes upwardly through the analyzer section thereof where it is concentrated by mass heat transfer with weak solution passing downwardly over analyzer coil 96.
  • Analyzer plates 102 in generator 16 provide a tortuous path for flow of solution and vapor, assuring intimate contact therebetween to improve the mass heat transfer.
  • the vapor passes through rectifier 87 in heat exchange relation with the weak solution passing through coil 84.
  • Absorbent condensed in rectifier 87 flows downwardly onto the generator 16.
  • the vapor formed in the generator is a mixture of refrigerant vapor and absorbent vapor.
  • the analyzer plates and rectifier purify the refrigerant vapor by condensing the water or absorbent vapor from the mixture.
  • the purified refrigerant vapor is passed from rectifier 87 through line 104 to condenser 12 to complete the refrigeration cycle.
  • FIG. 2 which illustrates a second embodiment of my invention
  • a system similar to the system illustrated in FIG. 1 with the exception of an ejector 106 associated with pump 20.
  • the ejector 106 having a-throat 108 is disposed in line 80 to increase the pressure of the absorbent solution at the pump inlet.
  • a nozzle 110 disposed adjacent throat 108 is adapted to inject a portion of the solution flowing through line 82 into throat 108 to provide a pressure downstream from the ejector sufficient to prevent flashing of the refrigerant in the absorbent solution when the pump inlet pressure is below the vapor pressure of the refrigerant, thereby increasing pump efficiency and preventing noise normally generated by flashing refrigerant.
  • an absorption refrigeration system including an absorber, a condenser, a chiller and a generator connected to provide refrigeration, apparatus comprising:
  • pulser type pump means for circulating refrigerant fluid in a refrigeration cycle through said chiller, said pump means having an inlet and a discharge side;
  • an ejector for receiving refrigerant fluid and for passing the fluid to said pulser type pump means, said ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the refrigerant fluid from the discharge side of said pulser type pump means into the throat of said ejector to maintain pressure at the inlet of said pulser type pump means above the vapor pressure of the refrigerant fluid being pumped to prevent flashing of the fluid at said inlet.
  • said pulser type pump means includes:
  • pump means for transferring absorbent fluid from said absorber to said generator, said pump means having an inlet and a discharge side;
  • a second ejector for receiving absorbent fluid from said absorber and for passing the absorbent fluid to said absorbent fluid pump means, said second ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the absorbent fluid from the discharge side of said absorbent fluid pump means into the throat of said second ejector to maintain pressure at the pump inlet above the vapor pressure of the refrigerant in said absorbent fluid to prevent flashing of the refrigerant at the pump inlet.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Sorption Type Refrigeration Machines (AREA)

Abstract

An absorption refrigeration system employing a secondary refrigerant to transfer heat from a suitable heat exchanger to the system evaporator; pump means to circulate absorbent solution and the secondary refrigerant; and ejectors for increasing pump inlet pressures to prevent refrigerant flashing at the pump inlets.

Description

United States Patent 11 1 English 1 'July 3, 1973 ABSORPTION REFRIGERATION SYSTEM 2,343,486 3/1944 sge anor 467/83 2.272.906 2/l942 :1 Col 4l7/83 [75] Inventor: Richard A. English, lnd1anapol1s, 2.095.534 |0l1937- Schmidt" 7,80
- 2,434,221 1/1948 Newton 62/333 x i 4 r 3,586,462 6/l97l English et al. 62/476 UX [73] f" Corpommmsyracuse 3,553,977 1/1971 Holman 62/489 [22] Filed: June 2, 1971 21 A L N 149 280 Primary Examiner-Merlin Perlin 1 pp 0 Assistant ExaminerPeter D. Ferguson Attorney-Harry G. Martin, Jr. and J. Raymond Cutting [52] US. Cl 62/476, 62/DIG. 2, 417/79 [5 Int. Cl- .f. [58] Field of Search 62/333,'47 6,,483, 1
62/487 488 485 DIG 417/79 80 83, 383 An absorptlon refrlgeratlon system employmg a sec-,- ondary refrigerant to transfer heat from a suitable heat [56] References Cited exchanger to the system evaporator; pump means to circulate absorbent solution and the secondary refrig- UNITED STATES PATENTS erant; and ejec tors for increasing pump inlet pressures (I) gllsgandj 5 to prevent refrigerant flashing at the pump inlets. 0e er, 1'. v 2,730,870 1/1956 Steele 417/79 X Claims, 2 Drawing Figures :q I 90A" 7 8o '6 2 3 14 I as Q 92 E 78 102 7 f "1:; 4 c: :1: 28 24 74 2 27 26 [:76 g: 7O 42 a: 32 54 38 =3 l PATENTEIJJUL3 191s 3.742.726
sum 1 or 2 (D LO INVENTOR. RICHARD A. ENGLISHv BYj 5M ATTORNEY PATENTEDJUL 3 I973 'SNEEIZNZ INVENTOR. RICHARD A. ENGLISH BYEL 5W AT TORNE Y 1 ABSORPTION REFRIGERATION SYSTEM BACKGROUND OF THE INVENTION In many applications, for example, air conditioning systems, an absorption refrigeration system is provided with a secondary circuit employing chilled water. The water chilled by the absorption refrigeration machine is circulated to a heat exchanger within the conditioned space, warm air from the space being circulated over the heat exchanger to cool the air for distribution throughout the conditioned space. The warm water from the heat exchanger is returned to the absorption refrigeration machine for transferring the heat therein to the evaporator or chiller of the refrigerationmachine.
In certain installations, it may be desirable to utilize a halogenated hydrocarbon refrigerant such as dichlorodifluoromethane in the secondary circuit. Pump means are ordinarily provided to circulate the absorbent solution within the absorption machine circuit and to circulate the chilled water or the halogenated hydrocarbon refrigerant to the heat exchangers within the conditioned space. Under certain circumstances, the pressuresat the pump inlets may be below the vapor pressure of the fluid being pumped, resulting in flashing of the fluid andinefficient pump operation.
SUMMARY OF THE INVENTION This invention relates to an absorption refrigeration system including an absorber, a condenser, an evaporator and a generator connected to provide refrigeration. A heat exchanger is operatively associated with the evaporator for circulation of refrigerant between the evaporatorand the heat exchanger. First pump means to transfer solution from the absorber to the generator and second pump means to circulate refrigerant between the evaporator and the heat exchanger are provided. At least one of said pump means is provided with an ejector including nozzle means for discharging a portion of the fluid from the discharge side of the pump associated therewith into the throat of the ejector to maintain pressure at the pump inlet above the vapor pressure of the fluid being pumped to prevent flashing of the fluid at the pumpinlet.
BRIEF DESCRIPTION OF THE DRAWING DESCRIPTION OF THE. PREFERRED EMBODIMENTS Referring to FIG. [of the drawings, there is shown a refrigeration system comprising an absorber 10, a
condenser I2, a chiller l4 and a generator 16 connected to provide refrigeration. A pump 20 is employed to circulate weak absorbent solution from absorber [0 to generator 16.
As used herein the terms weak solution or weak absorbent-solution" refer to solution which is weak in absorbent power and the terms strong solution or "strong absorbent solution refer to solution which is strong in absorbent power.'A suitable absorbent for use in the system described is water and a suitable refrigerant is ammonia.
Liquid refrigerant condensed in condenser 12 passes through refrigerant liquid'passage 22 and refrigerant restrictor 24 to heat exchange tube 26 of liquid suction heat exchanger 27 The liquid refrigerant which is cooled in tube 26 passes through refrigerant restriction 28 into heat exchange coil 30 of chiller 14.
A heat exchange medium such as a halogenated hydrocarbon refrigerant for example, dichlorodifluoromethane, is passed over the exterior of coil 30 where it is chilled by giving up heat to evaporate the refrigerant within heat exchange coil 30.
The chilled heat exchange medium is collected in the lower portion of chiller 1 4 for subsequent passage through line 32 to a pulser type pump 34. The pump 34 includes a housing 36 having an inlet opening 38 and discharge opening 40. A suction valve 42 is disposed within inlet opening 38 and a discharge valve 44 is disposed within discharge opening 40. A flexible diaphragm 46 is mounted within housing 36. A pulsating flow, of hydraulic fluid from a suitable hydraulic pump 48 is provided to the interior of diaphragm 46.
When hydraulic fluid under. pressure is supplied to diaphragm 46, the diaphragm is expanded outwardly toward the housing walls. The heat exchange medium in space St) between the diaphragm and housing is forced through discharge valve 44 into discharge line 52. When the hydraulic pressure within the diaphragm is released, the diaphragm contracts. This allows heat exchange medium to pass through suction valve 42 into space 50. Thus, the pulsing hydraulic pressure in diaphragm 46* causes heat exchange medium to be pumped from line 32 to line 52.
For optimum pump efficiency it is desirable to supply liquid heat exchange medium to pump 34. However, the suction pressure at the pump inlet may be below the vapor pressure of the heat exchange medium which could result in'flashing of a portion of the heat exchange medium. The resulting flash gas would reduce pump efficiency. To obviate this problem, an ejector 54 having a throat 56 is provided in line 32 to increase the pressure of the heat exchange medium at the pumpinlet. A nozzle 58, disposed adjacent throat 56 is adapted to inject a portion of the heat exchange medium flowing through line 52 into throat 56 to provide a pressure downstream from the ejector sufflcient to prevent flashing of the heat exchange medium.
The chilled heat exchange medium passes through line 52 to suitable remote heat exchangers (not shown) after which it is returned to the chiller through line 68.
The refrigerant evaporated in heat exchange coil 30 passes through refrigerant vapor passage of liquid suction heat exchanger 27 in heat exchange relation with liquid refrigerant passing through tube 26. Refrig erant vapor having a small proportion of absorbent liqmote the absorption of the refrigerant vapor by the solution. The same cooling medium may be supplied to condenser 12 in heat exchange relation with refrigerant vapor therein to condense the refrigerant.
Cold weak absorbent solution passes from absorber through a line 80 into weak solution pump 20. Pump may be of the same general design as pump 34, the hydraulic pump 48 being adapted to supply a pulsating flow of hydraulic fluid to pump 20 and pump 34. Liquid from pump 20 passes through pump discharge line 82 to rectifier heat exchange coil 84. The weak solution passes through coil 84 in heat exchange relation with hot strong solution passing through heat exchange coil 86 disposed within coil 84 and with the hot refrigerant vapor flowing through rectifier shell 87 in contact with the outer surface of coil 84. The weak solution from coil 84 is discharged into the upper portion of generator 16 along with any vapor which is formed in coil 84 due to heat exchange with the hot vapor passing thereover and the hot solution flowing therethrough.
I Generator 16 comprises a shell 90 having fins 92 suitably affixed thereto, as by welding. The generator is heated by a gas burner 94 or other suitable heating means. The weak solution is boiled in generator 16 to concentrate the solution, thereby forming a strong solution and refrigerant vapor.
The hot strong absorbent solution passes upwardly through the analyzer section of generator 16 through analyzer coil 96 in heat exchange with weak solution passing downwardly over the coil. The warm strong solution then passes through heat exchange coil 86 and line 76 into vapor distributor 74. A restrictor 98 is provided in line 76 so that the solution supplied to the vapor distributor is at the same pressure as the vapor in vapor distributor 74.
Refrigerant vapor formed in generator 16 passes upwardly through the analyzer section thereof where it is concentrated by mass heat transfer with weak solution passing downwardly over analyzer coil 96. Analyzer plates 102 in generator 16 provide a tortuous path for flow of solution and vapor, assuring intimate contact therebetween to improve the mass heat transfer. The vapor passes through rectifier 87 in heat exchange relation with the weak solution passing through coil 84. Absorbent condensed in rectifier 87 flows downwardly onto the generator 16. The vapor formed in the generator is a mixture of refrigerant vapor and absorbent vapor. The analyzer plates and rectifier purify the refrigerant vapor by condensing the water or absorbent vapor from the mixture. The purified refrigerant vapor is passed from rectifier 87 through line 104 to condenser 12 to complete the refrigeration cycle.
Referring to FIG. 2 which illustrates a second embodiment of my invention, there is disclosed a system similar to the system illustrated in FIG. 1 with the exception of an ejector 106 associated with pump 20. The ejector 106, having a-throat 108 is disposed in line 80 to increase the pressure of the absorbent solution at the pump inlet. A nozzle 110 disposed adjacent throat 108 is adapted to inject a portion of the solution flowing through line 82 into throat 108 to provide a pressure downstream from the ejector sufficient to prevent flashing of the refrigerant in the absorbent solution when the pump inlet pressure is below the vapor pressure of the refrigerant, thereby increasing pump efficiency and preventing noise normally generated by flashing refrigerant.
While I have described a preferred embodiment of my invention, it is to be understood the invention is not limited thereto but may be otherwise embodied within the scope of the following claims.
I claim:
1. In an absorption refrigeration system including an absorber, a condenser, a chiller and a generator connected to provide refrigeration, apparatus comprising:
pulser type pump means for circulating refrigerant fluid in a refrigeration cycle through said chiller, said pump means having an inlet and a discharge side; and
an ejector for receiving refrigerant fluid and for passing the fluid to said pulser type pump means, said ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the refrigerant fluid from the discharge side of said pulser type pump means into the throat of said ejector to maintain pressure at the inlet of said pulser type pump means above the vapor pressure of the refrigerant fluid being pumped to prevent flashing of the fluid at said inlet.
2. Apparatus according to claim 1, wherein said pulser type pump means includes:
a housing;
a diaphragm disposed within said housing; and
means for providing a pulsating supply of hydraulic fluid to one side of said diaphragm for pulsing said diaphragm to circulate the refrigerant fluidin the v refrigerant cycle.
3. Apparatus according to claim 1, and further comprising:
pump means for transferring absorbent fluid from said absorber to said generator, said pump means having an inlet and a discharge side; and
a second ejector for receiving absorbent fluid from said absorber and for passing the absorbent fluid to said absorbent fluid pump means, said second ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the absorbent fluid from the discharge side of said absorbent fluid pump means into the throat of said second ejector to maintain pressure at the pump inlet above the vapor pressure of the refrigerant in said absorbent fluid to prevent flashing of the refrigerant at the pump inlet.
4. Apparatus according to claim 3 wherein said refrigerant fluid pump means and said absorbent fluid pump means are operable by hydraulic pressure, and said apparatus further includes a hydraulic pump connected to both of said pump means for transmitting the hydraulic pressure for operating each of said pump means.

Claims (4)

1. In an absorption refrigeration system including an absorber, a condenser, a chiller and a generator connected to provide refrigeration, apparatus comprising: pulser type pump means for circulating refrigerant fluid in a refrigeration cycle through said chiller, said pump means having an inlet and a discharge side; and an ejector for receiving refrigerant fluid and for passing the fluid to said pulser type pump means, said ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the refrigerant fluid frOm the discharge side of said pulser type pump means into the throat of said ejector to maintain pressure at the inlet of said pulser type pump means above the vapor pressure of the refrigerant fluid being pumped to prevent flashing of the fluid at said inlet.
2. Apparatus according to claim 1, wherein said pulser type pump means includes: a housing; a diaphragm disposed within said housing; and means for providing a pulsating supply of hydraulic fluid to one side of said diaphragm for pulsing said diaphragm to circulate the refrigerant fluid in the refrigeration cycle.
3. Apparatus according to claim 1, and further comprising: pump means for transferring absorbent fluid from said absorber to said generator, said pump means having an inlet and a discharge side; and a second ejector for receiving absorbent fluid from said absorber and for passing the absorbent fluid to said absorbent fluid pump means, said second ejector including nozzle means and a throat, said throat leading to the inlet of said pump means and said nozzle means discharging a portion of the absorbent fluid from the discharge side of said absorbent fluid pump means into the throat of said second ejector to maintain pressure at the pump inlet above the vapor pressure of the refrigerant in said absorbent fluid to prevent flashing of the refrigerant at the pump inlet.
4. Apparatus according to claim 3 wherein said refrigerant fluid pump means and said absorbent fluid pump means are operable by hydraulic pressure, and said apparatus further includes a hydraulic pump connected to both of said pump means for transmitting the hydraulic pressure for operating each of said pump means.
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Cited By (9)

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US4599873A (en) * 1984-01-31 1986-07-15 Hyde Robert E Apparatus for maximizing refrigeration capacity
US4966007A (en) * 1989-05-12 1990-10-30 Baltimore Aircoil Company, Inc. Absorption refrigeration method and apparatus
US5038574A (en) * 1989-05-12 1991-08-13 Baltimore Aircoil Company, Inc. Combined mechanical refrigeration and absorption refrigeration method and apparatus
US5719377A (en) * 1994-08-15 1998-02-17 Sunbeam Products, Inc. Dual heating element electric grill having a smoker heating element for vaporizing grease and juices from foodstuff
US5771710A (en) * 1995-03-17 1998-06-30 Gas Research Institute Thermosyphon cooled absorber for air cooled absorption cycles
US8776539B2 (en) 2010-07-23 2014-07-15 Carrier Corporation Ejector-type refrigeration cycle and refrigeration device using the same
US9459027B2 (en) 2014-04-22 2016-10-04 King Fahd University Of Petroleum And Minerals Intermittent absorption refrigeration system
US9857101B2 (en) 2010-07-23 2018-01-02 Carrier Corporation Refrigeration ejector cycle having control for supercritical to subcritical transition prior to the ejector
US10480831B2 (en) 2013-03-25 2019-11-19 Carrier Corporation Compressor bearing cooling

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US3509732A (en) * 1965-10-20 1970-05-05 Whirlpool Co Absorption refrigeration system
US3553977A (en) * 1968-11-05 1971-01-12 Trane Co Absorption refrigeration apparatus including means cooling strong absorption solution
US3586462A (en) * 1969-05-01 1971-06-22 Carrier Corp Absorption refrigeration machine pump

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US2095534A (en) * 1935-04-23 1937-10-12 Westinghouse Electric & Mfg Co Condensate removal apparatus
US2212281A (en) * 1938-03-17 1940-08-20 Servel Inc Refrigeration
US2272906A (en) * 1940-01-12 1942-02-10 Fairbanks Morse & Co Centrifugal pump
US2343486A (en) * 1943-04-23 1944-03-07 Ingersoll Rand Co Pump
US2434221A (en) * 1943-07-02 1948-01-06 Honeywell Regulator Co Control means for plural stage refrigerating systems
US2730870A (en) * 1950-06-15 1956-01-17 Air Prod Inc Method and apparatus for pumping volatile liquids
US3509732A (en) * 1965-10-20 1970-05-05 Whirlpool Co Absorption refrigeration system
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US9857101B2 (en) 2010-07-23 2018-01-02 Carrier Corporation Refrigeration ejector cycle having control for supercritical to subcritical transition prior to the ejector
US10480831B2 (en) 2013-03-25 2019-11-19 Carrier Corporation Compressor bearing cooling
US9459027B2 (en) 2014-04-22 2016-10-04 King Fahd University Of Petroleum And Minerals Intermittent absorption refrigeration system

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