GB1565553A - Creation of Inventions and Patents with Artificial Intelligence

GB1565553A – Absorption refrigeration system
– Google Patents

GB1565553A – Absorption refrigeration system
– Google Patents
Absorption refrigeration system

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Publication number
GB1565553A

GB1565553A
GB40659/76A
GB4065976A
GB1565553A
GB 1565553 A
GB1565553 A
GB 1565553A
GB 40659/76 A
GB40659/76 A
GB 40659/76A
GB 4065976 A
GB4065976 A
GB 4065976A
GB 1565553 A
GB1565553 A
GB 1565553A
Authority
GB
United Kingdom
Prior art keywords
salt
water
composition
solution
alcohol
Prior art date
1975-10-02
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)

Expired

Application number
GB40659/76A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)

Arkla Industries Inc

Original Assignee
Arkla Industries Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
1975-10-02
Filing date
1976-09-30
Publication date
1980-04-23

1976-09-30
Application filed by Arkla Industries Inc
filed
Critical
Arkla Industries Inc

1980-04-23
Publication of GB1565553A
publication
Critical
patent/GB1565553A/en

Status
Expired
legal-status
Critical
Current

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Classifications

C—CHEMISTRY; METALLURGY

C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR

C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE

C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion

C09K5/02—Materials undergoing a change of physical state when used

C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa

C09K5/047—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for absorption-type refrigeration systems

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

F25B15/06—Sorption machines, plants or systems, operating continuously, e.g. absorption type without inert gas the refrigerant being water vapour evaporated from a salt solution, e.g. lithium bromide

Description

PATENT SPECIFICATION ( 11) 1 565 553
CO ( 21) Application No 40659/76 ( 22) Filed 30 Sept 1976 e ( 31) Convention Application No 619037 ( 19 ( 32) Filed 2 Oct 1975 in I ( 33) United States of America (US) U ( 44) Complete Specification published 23 April 1980 ( 51) INT CL 3 F 25 B 15/06 C 09 K 5/04 ( 52) Index at acceptance F 4 H GIA GIC GID GIH GIL GIM GI Xi G 5 A G 5 E C 4 X 2 X ( 54) ABSORPTION REFRIGERATION SYSTEM ( 71) We, ARKLA INDUSTRIES INC, a corporation organized under the laws of the State of Delaware, U S A, 810 East Franklin Street, Evansville, State of Indiana, United States of America do hereby declare the invention, for which we pray that a patent may be granted to us, and the method by which it is to be performed, to be particularly described in and by the following statement: 5
Absorption refrigeration systems of the general type contemplated by the present invention comprise a closed circuit containing a solution of salt in a liquid refrigerant composition Cooling is effected by vaporizing liquid refrigerant within an evaporator coil or the like which forms part of the closed circuit Air or other fluid medium is passed over the coil and thereby becomes chilled as it provides heat 10 of vaporization to the refrigerant The resulting refrigerant vapor passes to an absorber section where it is contacted with and absorbed into a stream of liquid absorbent comprising the dissolved salt Heat liberated by the absorption process is removed by heat exchange with an external cooling medium The resulting solution which has high refrigerant content passes to a generator section where it is heated 15 by an external heat source to expel refrigerant vapor The resulting solution which has low refrigerant content returns to the absorber section The refrigerant vapor is condensed by heat exchange with an external cooling medium and then again passes to the evaporator section.
The operation of a typical absorption circuit depends, among other things, on 20 the reduction of the vapor pressure of the refrigerant as it is absorbed into the absorbent The low pressure which is produced in the absorber section is transmitted to the evaporator section and causes the liquid refrigerant to evaporate until its temperature drops to a value at which the refrigerant vapor pressure approximately equals the pressure in the absorber section That is, the refrigerant 25 temperature varies directly with absorber pressure It is evident, therefore, that the cooling capacity of the circuit is directly related to absorber pressure, and for this reason it is common practice to employ an absorbent which has a low vapor pressure at the operating temperature of the absorber section.
It is recognized in the art that one way of obtaining a low absorber pressure, 30 and thereby achieving greater cooling capacity, is to employ a more highly concentrated salt solution On the other hand, it is also recognized that this advantage is offset by the fact that the highly concentrated salt solution has a greater tendency to crystallize, so of course the maximum concentration is limited by the solubility of the salt 35 These disadvantages are aggravated in an air-cooled refrigeration system, such as an air-cooled air conditioning unit employed to cool the interior of an enclosure, for two reasons First, a higher absorber temperature is required for a given evaporator temperature, and this in turn calls for the use of a salt solution having a particularly low vapor pressure, so low that the solubility characteristics of the 40 commonly employed salts preclude obtaining the desired vapor pressure Second, even if the first problem is overcome by employing a particularly soluble salt, the crystallization temperature of the concentrated solution may be so high that the solution will crystallize when the system is shut down For example, a solution having a crystallization temperature of 800 F will not crystallize at the operating 45 temperature, say 1300 F of the system, but after shut down the solution will cool toward ambient temperature which may well be below 800 F.
Further problems arise in selecting an absorbent refrigerant composition if it is required to use a relatively low temperature of the heat source, e g a stream of 2 1,565,5532 solar-heated fluid at a temperature of about 2001 F, for operating the vapor generator The refrigerant composition must be one which, under the pressure existing in the generator, is capable of boiling at the low temperature of the heat source.
The present invention lies in a selection of refrigeration system characteristics 5 which enables an efficient refrigeration to be performed with a favourable combination of absorption pressure and refrigerant boiling temperature values No.
3,524,815 (Hensel et al) discloses an aqueous lithium bromide/lithium iodide solution which has a sufficiently low crystallization temperature that is suitable for use in an ambient air-cooled system United States Patent No 2,802,344 discloses a 10 variety of electrolyte solutions as refrigerant compositions, including alcohol solutions of various inorganic salts.
According to the present invention there is provided an absorptionrefrigeration system wherein there is used a liquid absorbent-refrigerant composition comprising a salt solution (as absorbent, characterised in that said 15 composition contains at least one water-miscible lower aliphatic alcohol having not more than eight carbon atoms, water, which, and at least one dissolved salt selected from the group consisting of the alkali metal and alkaline earth metal salts of inorganic acids, the said salt(s) and the amount thereof in the composition, and the conditions of operation of the system being such that the alcohol(s) or the 20 alcohol(s) together with some water serve(s) as the refrigerant.
It has been found that compositions as above defined have advantageous properties for the purpose in view.
By appropriate choice of the relative proportions of the salt(s), water and alcohol(s), solutions can easily be formed which have properties, particularly 25 vapour pressures and viscosities, making them highly suitable in refrigeration systems, for example ambient air-cooled systems, operating at relatively low generator temperatures.
In the prior art absorption refrigeration systems are known wherein the absorbent-refrigerant composition comprises water as the liquid refrigerant and 30 contains in addition to a salt, a certain amount of relatively high boiling alcohol In such systems, the alcohol can serve various purposes For example, it can reduce the crystallisation temperature of the absorbent-refrigerant saline solution (see UK Patent 1 186 326) or it can be selected to serve as heat transfer promoting agent (see UK Patents 1 277 482 and 1 255 408), the alcohol then being used in a very small 35 proportion by weight.
The previously known absorption refrigeration systems also include systems wherein the absorbent-refrigerant composition is a solution of a salt in an alcohol.
Such compositions are suitable under some conditions, although it has been found that if the salt is highly hygroscopic it may tend to dehydrate the alcohol, thereby 40 forming water and an ether The presence of the ether adversely affects the operation of the refrigeration system By having water present initially as in a system according to the present invention the dehydration reaction is believed to be suppressed An additional advantage is that the water-alcohol mixture is capable of dissolving a greater amount of the salt, with the result that the more 45 concentrated solution produces a lower pressure in the absorber section of a refrigeration system The following table is relevant The solutions were made up first making a 62 5 % by weight aqueous lithium bromide solution and adding various amounts of methanol.
( 1) ( 2) ( 3) ( 4) ( 5) 50 Methanol, % based on total weight of solution 27 2 21 6 19 45 17 2 14 25 Temperature, IF at which the solution 55 has a vapor pressureof 40 mm 103 111 116 118 124 Solution ( 1) contained 45 5 % salt and 27 3 % water, based on total weight of solution Solution ( 5) contained 53 6 % salt and 32 2 % water, based on total weight of solution 60 As the proportion of water in the alcohol-water-salt solution is increased, the viscosity of the solution decreases The following data are relevant.
1,565,553 Solution A Solution B Li Br (anhydrous) 54 5/,, by weight 42 8 ‘ by weight methanol 35 6 28 6 water 11 0 28 6 viscosity 28 4 6 4 5 centipoise centipoise at 90 F at 900 F While it is within the scope of the invention to incorporate a mixture of lower aliphatic alcohols each having no more than 8 carbon atoms and/or a mixture of different salts belonging to the specified group in any given composition, the use of 10 a single alcohol and a single salt, which is preferred, will be assumed in the following further description to avoid repeated reference to the alternative.
In preferred embodiments of the invention, the solution contains the salt in the range 40 %-700 % by weight, alcohol in the range 10 %’-50 ‘ by weight, and water in the range 10 -50 a by weight, based on the total weight of the solution In 15 practice the maximum salt concentration will be the concentration at saturation at the lowest temperature experienced by the solution during operation.
The preferred salts are the halides of lithium, calcium, strontium and barium.
Other salts may be employed, such as the halides of the other alkali metals, and the chlorates and perchlorates of the alkali metals and of the alkaline earth metals 20 The preferred alcohols are methanol, ethanol n-propanol and isopropanol.
Other lower aliphatic alcohols having up to eight carbon atoms may be employed provided that the final solution has a boiling point not substantially higher than that of water The liquid phase should preferably be capable of holding a high concentration of the salt in solution Preferably the solution has a crystallization 25 temperature not higher than about 50 ‘F The solution preferably has a vapour pressure of not more than 40 mm of mercury at 1321 F.
Reference is now made to the accompanying drawing which diagrammatically illustrates an absorption refrigeration system suitable (subject to appropriate selection of the appropriate absorbent-refrigerant composition) for use in carrying 30 out the present invention.
The illustrated system comprises a refrigerant evaporator 10, shown in the form of a finned coil, in which the refrigerant liquid is vaporized under subatmospheric pressure thereby extracting heat from whatever fluid medium surrounds the coil The resulting vapor passes into an absorber 14 which is 35 illustrated in the form of a vessel having a tubular heat exchanger core 18 therein.
Absorbent-refrigerant composition, for example solution ( 5) identified above, flows from a header 20 into the open upper ends of one set of flow channels in the core 18 and presents a large surface area over which absorption of alcohol vapor takes place Heat liberated by the absorption process is removed by a stream of ambient 40 cooling air 22 which flows through the other set of core channels.
The resulting dilute salt solution flows downwardly by way of line 26, pump 27, heat exchanger 24 and line 28 into an alcohol vapor generator 30 In the generator the dilute salt solution is heated to boiling temperature by means of a heat source such as coil 32 through which solar heated water at approximately 2000 F to 45 2200 F flows, so that alcohol and water vapor is expelled from the solution.
Concentrated solution flows from the generator 30 through a line 38 to the heat exchanger 24 where it preheats the dilute salt solution before the latter passes to the generator 30 The cooler concentrated solution then flows upwardly through a line 40 to the header 20 in the absorber 14 50 The refrigerant vapor produced in the generator 30 passes through a line 42 to a condenser 44 which is illustrated in the form of a finned tube 45 The vapor flows through the tube 45 and is condensed by giving up heat to a stream of cooling air 22 flowing over the outside of the tube 45 The stream of condensed alcohol and water flows from the condenser 44 through an orifice 52 to the evaporator 10 where it 55 again vaporizes to effect the desired cooling action of the system.
The system requires that pressure difference be maintained between the high pressure and low pressure parts of the system More specifically, the orifice 52 helps to maintain a pressure differential between the low pressure in the evaporator 10 and the higher pressure in the condenser 44 The solution pump 27 maintains 60 pressure in the rich-in-refrigerant solution line, while a solution column in line 38 as shown at X or a restrictor maintains pressure in the weak-in-refrigerant solution circuit Alternatively, a float valve could be provided in the line 38.
I 1,565,553 A more detailed discussion of the operation of the absorber 14 will aid in clarifying the invention First, it will be appreciated that a low pressure must be maintained in the absorber 14 in order to reduce the pressure in the evaporator 10 to a value at which the alcohol refrigerant will vaporize at a satisfactory temperature The pressure in the absorber 14 is theoretically the vapor pressure of 5 the solution therein at the temperature of the solution In an air-cooled absorber 14, using ambient air at for example 900 F, the temperature will be relatively high as compared to the temperature which can be obtained with cooling water, and it follows that the vapor pressure of the solution will be relatively high In order to effect as low a pressure as possible in an air-cooled system it is necessary to employ 10 a highly concentrated salt solution in order to take advantage of the lower vapor pressure of such a solution The invention is particularly suitable for application in an ambient air-cooled system, especially one which operates with a heat source at relatively low temperature.

Claims (12)

WHAT WE CLAIM IS: 15

1 An absorption refrigeration system wherein there is used a liquid absorbentrefrigerant composition comprising a salt solution as absorbent, characterised in that said composition contains at least one water-miscible lower aliphatic alcohol having not more than eight carbon atoms, water, and at least one dissolved salt selected from the group consisting of the alkali metal and the alkaline earth metal 20 salts of inorganic acids, the salt(s) and the amount thereof in the composition, and the conditions of operation of the system being such that the alcohol(s) together with some water serve(s) as the refrigerant.

2 A system according to claim I, wherein the said composition has a vapour pressure of not more than 40 mm of mercury at 1321 F and a crystallization 25 temperature not higher than 500 F.

3 A system according to claim 1 or 2, wherein the said salt(s) is or are present in the range 40 %-70 %, the alcohol(s) is or are present in the range 10 %-50 % and water is present in the range 10 %-50 %, all percentages being by weight, based on the total weight of the composition 30

4 A system according to any preceding claim, wherein the salt ingredient is an alkali metal halide.

A system according to claim 4, wherein the salt ingredient is a halide of lithium, calcium or strontium or barium.

6 A system according to any of claims 1 to 3, wherein the salt ingredient 35 comprises a chlorate or perchlorate of an alkali metal or an alkaline earth metal.

7 A system according to any preceding claim, wherein the alcohol ingredient is methanol, ethanol, n-propanol or isopropanol.

8 A system according to claim I or 2, wherein the said composition contains 40 %-70 % by weight of a halide of lithium, calcium, strontium or barium, 10 % 40 % by weight of methanol, ethanol, n-propanol or isopropanol, and 10 %-50 % by weight of water.

9 A system according to any preceding claim, wherein the system operates with a heat source at a temperature of not more than 2000 F.

10 A system which is according to any preceding claim and which is an air 45 cooled system.

11 A system according to any preceding claim, wherein a solar-heated fluid is used as a heat source.

12 An absorption refrigeration system wherein an absorbent-refrigerant composition substantially as herein described is used 50 HYDE, HEIDE & O’DONNELL Chartered Patent Agents 2 Serjeants’ Inn London EC 4 Y ILL Agents for the Applicant.
Printed for Her Majesty’s Stationery Office, by the Courier Press, Leamington Spa 1980 Published by The Patent Office 25 Southampton Buildings, London, WC 2 A l AY, from which copies may be obtained.
1,565,553

GB40659/76A
1975-10-02
1976-09-30
Absorption refrigeration system

Expired

GB1565553A
(en)

Applications Claiming Priority (1)

Application Number
Priority Date
Filing Date
Title

US05/619,037

US4018694A
(en)

1975-10-02
1975-10-02
Absorption refrigerant composition

Publications (1)

Publication Number
Publication Date

GB1565553A
true

GB1565553A
(en)

1980-04-23

Family
ID=24480192
Family Applications (1)

Application Number
Title
Priority Date
Filing Date

GB40659/76A
Expired

GB1565553A
(en)

1975-10-02
1976-09-30
Absorption refrigeration system

Country Status (10)

Country
Link

US
(1)

US4018694A
(en)

JP
(1)

JPS5244442A
(en)

AU
(1)

AU511364B2
(en)

BE
(1)

BE846878A
(en)

CA
(1)

CA1082907A
(en)

DE
(1)

DE2644474C2
(en)

FR
(1)

FR2333846A1
(en)

GB
(1)

GB1565553A
(en)

IT
(1)

IT1068125B
(en)

NL
(1)

NL7610923A
(en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

GB2098623B
(en)

1981-05-19
1985-02-27
Exxon Research Engineering Co
Working fluid for heat pumps

US5186010A
(en)

1985-11-18
1993-02-16
Darrel H. Williams
Absorbent-refrigerant solution

US5186009A
(en)

1987-04-14
1993-02-16
Gas Research Institute
Aqueous absorption fluids

US4783277A
(en)

1987-08-19
1988-11-08
Hitachi, Ltd.
Absorption-type refrigerator

US5638696A
(en)

1995-11-15
1997-06-17
Cline; Calvin D.
Absorption refrigeration system

US6177025B1
(en)

1998-11-17
2001-01-23
University Of Utah
Absorption heat pumps having improved efficiency using a crystallization-inhibiting additive

US7918095B2
(en)

2007-06-12
2011-04-05
Foi Group, Llc
Heat actuated cooling system

US20170218793A1
(en)

2014-07-30
2017-08-03
Vasileios Ethimios STYLIARAS
Multi stage vapor compression for high efficiency power production and heat pump

Family Cites Families (6)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

US1791515A
(en)

1929-05-30
1931-02-10
Frigidaire Corp
Absorbent for refrigerating apparatus

US2301839A
(en)

1937-08-28
1942-11-10
Lincoln T Work
Ejector refrigeration

DE1544149A1
(en)

1964-10-19
1969-08-21
Trane Co

Absorption mixture for absorption cooling system

US3296814A
(en)

1965-10-28
1967-01-10
Trane Co
Absorption refrigeration systems, methods, and absorbent compositions

US3609087A
(en)

1968-02-01
1971-09-28
American Gas Ass Inc The
Secondary alcohol additives for lithium bromide-water absorption refrigeration system

US3580759A
(en)

1968-06-25
1971-05-25
Borg Warner
Heat transfer additives for absorbent solutions

1975

1975-10-02
US
US05/619,037
patent/US4018694A/en
not_active
Expired – Lifetime

1976

1976-08-27
CA
CA260,036A
patent/CA1082907A/en
not_active
Expired

1976-09-21
JP
JP51112546A
patent/JPS5244442A/en
active
Pending

1976-09-27
FR
FR7628981A
patent/FR2333846A1/en
active
Granted

1976-09-30
GB
GB40659/76A
patent/GB1565553A/en
not_active
Expired

1976-09-30
IT
IT27842/76A
patent/IT1068125B/en
active

1976-10-01
AU
AU18315/76A
patent/AU511364B2/en
not_active
Expired

1976-10-01
DE
DE2644474A
patent/DE2644474C2/en
not_active
Expired

1976-10-01
NL
NL7610923A
patent/NL7610923A/en
not_active
Application Discontinuation

1976-10-01
BE
BE171189A
patent/BE846878A/en
not_active
IP Right Cessation

Also Published As

Publication number
Publication date

JPS5244442A
(en)

1977-04-07

DE2644474C2
(en)

1983-06-01

DE2644474A1
(en)

1977-04-14

AU511364B2
(en)

1980-08-14

FR2333846B1
(en)

1981-08-07

AU1831576A
(en)

1978-04-06

BE846878A
(en)

1977-01-31

FR2333846A1
(en)

1977-07-01

US4018694A
(en)

1977-04-19

CA1082907A
(en)

1980-08-05

NL7610923A
(en)

1977-04-05

IT1068125B
(en)

1985-03-21

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