GB458841A - Improvements in or relating to absorption type refrigerating apparatus - Google Patents

Improvements in or relating to absorption type refrigerating apparatus

Info

Publication number
GB458841A
GB458841A GB18215/35A GB1821535A GB458841A GB 458841 A GB458841 A GB 458841A GB 18215/35 A GB18215/35 A GB 18215/35A GB 1821535 A GB1821535 A GB 1821535A GB 458841 A GB458841 A GB 458841A
Authority
GB
United Kingdom
Prior art keywords
tube
flows
solution
absorber
separator
Prior art date
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
GB18215/35A
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.)
Ewart & Son Ltd
Original Assignee
Ewart & Son Ltd
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.)
Filing date
Publication date
Application filed by Ewart & Son Ltd filed Critical Ewart & Son Ltd
Priority to GB18215/35A priority Critical patent/GB458841A/en
Publication of GB458841A publication Critical patent/GB458841A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B15/00Sorption machines, plants or systems, operating continuously, e.g. absorption type
    • F25B15/10Sorption machines, plants or systems, operating continuously, e.g. absorption type with inert gas
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

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

Abstract

458,841. Refrigerating. EWART, J. H., HAWES, W. B., and EWART & SON, Ltd., 346, Euston Road, London. June 25, 1935, No. 18215. [Class 29] Absorption systems.-In a continuous - cycle system, the generator tubes 5, and the tube 16, by which weak liquor is raised to a vessel from which it flows by gravity to the absorber 4, discharge mixed refrigerant vapour and absorption solution into separators 10, 17, preferably of the centrifugal kind having a tangential inlet 19, Fig. 3, in which the solution is deposited as a flowing film over which the vapour flows. The tubes are disposed in a common heating- flue 9, and the solution separated in the separator 10 flows into a sump 13 from which a part passes down the tube 14, and returns to the generator with the strong solution returning through the pipe 8 to the lower header 7 of the generator. The other part of the solution flows into the pipe 15 and thence to the tube 16, which discharges into the separator 17 from which the weak solution flows through the pipe 24 to the absorber. Vapour passes from the separator 10 to the condenser 2, which discharges through a loop 26 to the evaporator, and from the separator 17 into a condenser tube 23 cooled by inert gas returning through the duct 28 from the absorber to the evaporator 3. The condensate from the tube 23 returns to the sump 13 or, if desired, directly to the generator or the tube 16. The flow of mixed inert gas and refrigerant vapour from the top of the evaporator to the absorber is produced by an injector 30 through which flows a part of the inert gas returning through the duct 28. Specifications 458,836 and 459,051 are referred to.
GB18215/35A 1935-06-25 1935-06-25 Improvements in or relating to absorption type refrigerating apparatus Expired GB458841A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB18215/35A GB458841A (en) 1935-06-25 1935-06-25 Improvements in or relating to absorption type refrigerating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB18215/35A GB458841A (en) 1935-06-25 1935-06-25 Improvements in or relating to absorption type refrigerating apparatus

Publications (1)

Publication Number Publication Date
GB458841A true GB458841A (en) 1936-12-28

Family

ID=10108619

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18215/35A Expired GB458841A (en) 1935-06-25 1935-06-25 Improvements in or relating to absorption type refrigerating apparatus

Country Status (1)

Country Link
GB (1) GB458841A (en)

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