GB676675A - Improvements in continuous-cycle absorption type refrigerating apparatus - Google Patents

Improvements in continuous-cycle absorption type refrigerating apparatus

Info

Publication number
GB676675A
GB676675A GB27413/50A GB2741350A GB676675A GB 676675 A GB676675 A GB 676675A GB 27413/50 A GB27413/50 A GB 27413/50A GB 2741350 A GB2741350 A GB 2741350A GB 676675 A GB676675 A GB 676675A
Authority
GB
United Kingdom
Prior art keywords
heat exchanger
tube
gas
absorber
vessel
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
GB27413/50A
Inventor
Alvar Lenning
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.)
Bolinders Fabriks AB
Original Assignee
Bolinders Fabriks AB
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 Bolinders Fabriks AB filed Critical Bolinders Fabriks AB
Priority to GB27413/50A priority Critical patent/GB676675A/en
Publication of GB676675A publication Critical patent/GB676675A/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

676,675. Refrigerating. BOLINDER'S FABRIKS AKTIEBOLAG. Nov. 9,1950, No. 27413/50. Class 29 The gas heat exchanger of a continuouscycle inert gas absorption system comprises a single outer tube 9 and a single inner tube 10, entering substantially vertically from the collecting vessel 2 for rich solution and having a substantially horizontally U-shaped portion connected to the evaporator 8, the upper end of the absorber coil 3 being connected to the outer tube 9 at 4. The lower end of the gas heat exchanger is welded to the top of the vessel 2 and rich gas passes down the inner tube 10 to the absorber vessel. Weak solution flows from the generator through a tube 13, liquid heat exchanger 14 and tube 7 to the lower portion of the gas heat exchanger at 5, rises in the annular space 11 to the level 4 and flows downwardly through the absorber 3. Weak gas flows upwardly in the annular space 11 above the level 4 and passes to the evaporator 8 by a pipe 12. The inner tube 10 may be of non-circular cross section.
GB27413/50A 1950-11-09 1950-11-09 Improvements in continuous-cycle absorption type refrigerating apparatus Expired GB676675A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB27413/50A GB676675A (en) 1950-11-09 1950-11-09 Improvements in continuous-cycle absorption type refrigerating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB27413/50A GB676675A (en) 1950-11-09 1950-11-09 Improvements in continuous-cycle absorption type refrigerating apparatus

Publications (1)

Publication Number Publication Date
GB676675A true GB676675A (en) 1952-07-30

Family

ID=10259163

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27413/50A Expired GB676675A (en) 1950-11-09 1950-11-09 Improvements in continuous-cycle absorption type refrigerating apparatus

Country Status (1)

Country Link
GB (1) GB676675A (en)

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