GB1350766A - Water desalination device - Google Patents

Water desalination device

Info

Publication number
GB1350766A
GB1350766A GB1181370A GB1350766DA GB1350766A GB 1350766 A GB1350766 A GB 1350766A GB 1181370 A GB1181370 A GB 1181370A GB 1350766D A GB1350766D A GB 1350766DA GB 1350766 A GB1350766 A GB 1350766A
Authority
GB
United Kingdom
Prior art keywords
chamber
tray
condenser
evaporator
trays
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
GB1181370A
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.)
UK Secretary of State for Defence
Original Assignee
UK Secretary of State for Defence
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 UK Secretary of State for Defence filed Critical UK Secretary of State for Defence
Publication of GB1350766A publication Critical patent/GB1350766A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4604Treatment of water, waste water, or sewage by electrochemical methods for desalination of seawater or brackish water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/06Flash evaporation
    • 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
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

1350766 Evaporators, flash type; desalination of water DEFENCE SECRETARY OF STATE FOR 19 April 1971 [12 March 1970] 11813/70 Heading B1B Irrigation water is obtained from brine or well water by passing it through a series of adjoining flash chambers 11 each comprising an evaporator tray, a condenser and a condensate tray, the chambers being arranged so that they are vertically staggered in helical array; and the preheated feedwater flows upwards through the evaporator trays from the lowest chamber. The apparatus shown comprises a hexagonal shell 10 of reinforced concrete which contains eighteen trapezoidal chambers 11 accommodated in three turns of a helix. Two-thirds of the shell 10 is below the ground. The top chamber is connected to a vacuum pump. The side walls of each chamber are common to the adjoining chambers, while the evaporator tray form the bottom of one chamber and the top of the chamber vertically below (where there is such a chamber). The trays are connected by reverse siphon devices each comprising holes in the side walls and a duct wall. The condensate tray divides the chamber into a minor upper portion and a major lower portion, and is provided with apertures and bubble-caps. A bundle of finned condenser tubes passes through the upper space of each chamber. The vapours evolved from the water in the evaporator tray pass through the bubble caps of the condenser trays and flow to the condenser tubes from which the condensate drips into the condenser tray. In the central tube 12 of the apparatus there is mounted a gas turbine 14 which drives an electrical generator 13. Air for the turbine is supplied through intake filter 18. The hot gases exhausted from the turbine flow to thermal transformer 15 which comprises a pair of interconnected heat exchangers wherein heat is transferred from the hot gases to the feedwater by means of a circulating mixture of diphenyl and diphenyl oxide which is vaporized in one heat exchanger and condensed in the other. Before discharge from the system, the exhaust gases are passed in heat exchange with the liquid in the lowest evaporator tray. The feedwater is preheated in heat exchanger 20 and then flows into tank 19 where it is mixed with some of the brine leaving the highest flash chamber; the mixture (if desired, after treatment by electro-dialysis) is passed through the condenser tubes and the thermal transformer 15, and the hot mixture is then introduced into the evaporator tray of the lowest chamber 11. Condensate (purified water) flows up through the condenser trays, and is withdrawn from the system through coil 22. Brine is discharged from the system through coil 21.
GB1181370A 1970-03-12 1970-03-12 Water desalination device Expired GB1350766A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1181370 1970-03-12

Publications (1)

Publication Number Publication Date
GB1350766A true GB1350766A (en) 1974-04-24

Family

ID=9993164

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1181370A Expired GB1350766A (en) 1970-03-12 1970-03-12 Water desalination device

Country Status (1)

Country Link
GB (1) GB1350766A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2224801A1 (en) * 2002-07-29 2005-03-01 Desalacion Integral Systems, S.L. Integral dual high vacuum desalinator includes a vacuum chamber, with water as drive fluid and drying of the collected brine
WO2013052248A1 (en) * 2011-10-06 2013-04-11 General Electric Company Seawater desalination process and apparatus
CN110078283A (en) * 2019-04-24 2019-08-02 中国神华能源股份有限公司 Saliferous equipment for treating water from mine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2224801A1 (en) * 2002-07-29 2005-03-01 Desalacion Integral Systems, S.L. Integral dual high vacuum desalinator includes a vacuum chamber, with water as drive fluid and drying of the collected brine
WO2013052248A1 (en) * 2011-10-06 2013-04-11 General Electric Company Seawater desalination process and apparatus
US9382135B2 (en) 2011-10-06 2016-07-05 General Electric Company Seawater desalination process
CN110078283A (en) * 2019-04-24 2019-08-02 中国神华能源股份有限公司 Saliferous equipment for treating water from mine

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Legal Events

Date Code Title Description
PS Patent sealed [section 19, patents act 1949]
PLNP Patent lapsed through nonpayment of renewal fees