GB958522A - Improvements relating to the desalination of saline water - Google Patents

Improvements relating to the desalination of saline water

Info

Publication number
GB958522A
GB958522A GB5059/61A GB505961A GB958522A GB 958522 A GB958522 A GB 958522A GB 5059/61 A GB5059/61 A GB 5059/61A GB 505961 A GB505961 A GB 505961A GB 958522 A GB958522 A GB 958522A
Authority
GB
United Kingdom
Prior art keywords
chamber
water
gases
pipe
saline
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
GB5059/61A
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.)
CHARLES SIDNEY GALE
Original Assignee
CHARLES SIDNEY GALE
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 CHARLES SIDNEY GALE filed Critical CHARLES SIDNEY GALE
Priority to GB5059/61A priority Critical patent/GB958522A/en
Publication of GB958522A publication Critical patent/GB958522A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/10—Treatment of water, waste water, or sewage by heating by distillation or evaporation by direct contact with a particulate solid or with a fluid, as a heat transfer medium
    • 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
    • Y02A20/00—Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124—Water desalination

Landscapes

  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

958,522. Distilling saline water. C. S. GALE. Feb. 28, 1962 [Feb. 10, 1961], No. 5059/61. Heading B1B. Saline water is distilled by spraying it from nozzles in pipes 9 into hot combustion gases flowing through chamber 1 which contains parallel baffles 8 arranged in zig-zag formation extending at right angles to the direction of flow of the gases ; the water is instantly evaporated by contact with the hot gases, and the mixture of gases and vapour flows to condenser 13, from which the warm condensate, i.e. distilled water, is withdrawn through pipe 14. Water is also sprayed through nozzles 11 against baffles 8 so as to remove saline deposits. Saline residues are removed from chamber 1 through pipe 12. The hot combustion gases are produced in gas turbine plant 6, in which gas or oil is burned, and are supplied to chamber 1 through pipe 21. If desired, the fuel may be burned in burners 7 at the fore-end of chamber 1. The saline water to be treated is pumped through condenser 13, where it is preheated, before it is sprayed into the chamber 1. The mixture of hot gases and water vapour passes through wire-mesh filter 15 before it reaches the condenser 13. The warm condensate may. be passed to tank 23 which is maintained under reduced pressure by Venturi-tube 28, operated by the compressed effluent gases from chamber 1. Some of the condensate evaporates, and the remainder is chilled. The chilled condensate is withdrawn from the system through pipe 26. The turbine is used to drive the pumps and compressors.
GB5059/61A 1961-02-10 1961-02-10 Improvements relating to the desalination of saline water Expired GB958522A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB5059/61A GB958522A (en) 1961-02-10 1961-02-10 Improvements relating to the desalination of saline water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5059/61A GB958522A (en) 1961-02-10 1961-02-10 Improvements relating to the desalination of saline water

Publications (1)

Publication Number Publication Date
GB958522A true GB958522A (en) 1964-05-21

Family

ID=9788994

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5059/61A Expired GB958522A (en) 1961-02-10 1961-02-10 Improvements relating to the desalination of saline water

Country Status (1)

Country Link
GB (1) GB958522A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3448013A (en) * 1966-08-10 1969-06-03 Westinghouse Electric Corp Distillate cooling means for flash evaporators
US3468761A (en) * 1966-09-02 1969-09-23 Westinghouse Electric Corp Staged vapor-liquid operated ejector arrangement for multi-stage evaporator system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3448013A (en) * 1966-08-10 1969-06-03 Westinghouse Electric Corp Distillate cooling means for flash evaporators
US3468761A (en) * 1966-09-02 1969-09-23 Westinghouse Electric Corp Staged vapor-liquid operated ejector arrangement for multi-stage evaporator system

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