GB338935A - Process for refrigeration and apparatus connected therewith - Google Patents

Process for refrigeration and apparatus connected therewith

Info

Publication number
GB338935A
GB338935A GB23103/29A GB2310329A GB338935A GB 338935 A GB338935 A GB 338935A GB 23103/29 A GB23103/29 A GB 23103/29A GB 2310329 A GB2310329 A GB 2310329A GB 338935 A GB338935 A GB 338935A
Authority
GB
United Kingdom
Prior art keywords
rectifier
evaporator
liquid
generator
condenser
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
GB23103/29A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB338935A publication Critical patent/GB338935A/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

Abstract

338,935. Maiuri, G., and Bossini, R. F. May 31, 1929, [Convention date]. Refrigerating.-A mixture of fluids of different boiling points, e.g. ammonia and water, is heated in a generator and rectifier column 2, 1 to separate the fluids in gaseous form, the less condensible fluid passing from the top of the rectifier through a conduit 5 to a condenser 6 cooled externally, as by cooling water, whence it flows as liquid through a liquid seal 7 into an evaporator 8. Some of the more condensible medium in gaseous form is led from the generator to a nozzle 9 to induce a flow of mixed gases from the evaporator to a condenser member 10 preferably located in the rectifier and of fairly high temperature, whence the readily condensible medium returns through a seal 14 to the lower part of the generator. The less condensible medium of the mixture passes up into a further condenser element 11, 12 surrounded by the cooling water and is returned in liquid form through a seal 13 into the upper part of the rectifier. In the example shown an inert gas circulates through the evaporator and the condenser elements 10, 12, this gas being led in a cooled condition to the upper end of the evaporator. The inert gas may be used to balance only a part of the pressure differences, or in place of using inert gas the condensed refrigerant may be expanded through a valve in place of the seal 7, and pumps may be employed to overcome the pressure differences. Baffle plates are provided in the generator and rectifier, the lower ones 3 forming liquid head pockets sufficient to provide pressure head for the nozzle 9, while the upper ones 4 do not retain liquid. A heat exchanger for gasesentering and leaving the evaporator may be provided. The condensers may be fitted with plates over which the condensate flows slowly. In a modification the rectifier and condenser elements are in the form of coils, the upper condensers being air cooled and the lower one united, as by soldering, to the rectifier to exchange heat therewith. The rectifier coil terminates in a bell dipping into liquid in the generator so that a pressure head for the gas nozzle is obtained. The Specification as open to inspection under Sect. 91 (3) (a) mentions also the use of sulphur dioxide and carbon dioxide, and ethyl alcohol and methyl chloride as mixed fluids. This subjectmatter does not appear in the Specification as accepted.
GB23103/29A 1929-05-31 1929-07-27 Process for refrigeration and apparatus connected therewith Expired GB338935A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR338935X 1929-05-31

Publications (1)

Publication Number Publication Date
GB338935A true GB338935A (en) 1930-11-27

Family

ID=8891634

Family Applications (1)

Application Number Title Priority Date Filing Date
GB23103/29A Expired GB338935A (en) 1929-05-31 1929-07-27 Process for refrigeration and apparatus connected therewith

Country Status (1)

Country Link
GB (1) GB338935A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117109195A (en) * 2023-10-19 2023-11-24 逸励柯环境科技(江苏)有限公司 Transcritical carbon dioxide cold and hot combined supply unit

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN117109195A (en) * 2023-10-19 2023-11-24 逸励柯环境科技(江苏)有限公司 Transcritical carbon dioxide cold and hot combined supply unit
CN117109195B (en) * 2023-10-19 2024-01-05 逸励柯环境科技(江苏)有限公司 Transcritical carbon dioxide cold and hot combined supply unit

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