GB1185824A - Improvements in or relating to Water Desalination Processes and apparatus - Google Patents

Improvements in or relating to Water Desalination Processes and apparatus

Info

Publication number
GB1185824A
GB1185824A GB03139/66A GB1313966A GB1185824A GB 1185824 A GB1185824 A GB 1185824A GB 03139/66 A GB03139/66 A GB 03139/66A GB 1313966 A GB1313966 A GB 1313966A GB 1185824 A GB1185824 A GB 1185824A
Authority
GB
United Kingdom
Prior art keywords
condenser
brine
conduit
tower
steam
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
GB03139/66A
Inventor
Peter Thomas Walker
Ivan Henry Newson
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.)
VWS Westgarth Ltd
Original Assignee
Weir Westgarth 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 Weir Westgarth Ltd filed Critical Weir Westgarth Ltd
Priority to GB03139/66A priority Critical patent/GB1185824A/en
Publication of GB1185824A publication Critical patent/GB1185824A/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
    • C02F1/02Treatment 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/06Flash distillation
    • B01D3/065Multiple-effect flash distillation (more than two traps)
    • 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)
  • Chemical Kinetics & Catalysis (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)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

1,185,824. Evaporators, flash type; desalination of water. WEIR WESTGARTH Ltd. 28 March, 1967 [24 March, 1966], No. 13139/66. Heading BIB. Desalinated water is produced from brine (e.g. sea water) by passing the heated brine upwards through a tower 1, divided by horizontal plates 2 into stages connected by riser pipes 3, wherein flash vaporization of water into steam takes place in each of the successive stages, withdrawing the steam from the stages through separate conduits 5 leading to separate condenser sections, and withdrawing residual brine from the upper part of the tower through conduit 7. Vacuum is applied to the top of the tower by line 8 so that the pressure at the top is about 1 p.s.i.a. As shown, there are two condensers 9, 10 connected to vacuum line 13. Each condenser is divided into sections by partitions 15 which do not make completely steam-proof with thewalls and cooling tubes 12 of the condensers, so that the degree of vacuum decreases from the right-hand or cool end of condenser 10 to the left-hand or hot end of condenser 9. The condensate formed in condenser 9 is collected in troughs 16 and conveyed by conduit 17 to the troughs 18 in condenser 10, from which the required fresh water product is withdrawn by conduit 19. Brine is introduced into the tubes of condenser 10, and the slightly warmed brine flowing out of the outlet header 11 is divided into two parts, one of which is discharged to waste through conduit 22. The other part is mixed with some of the residual brine from the top of the flash tower, and the mixture is passed through conduit 25 into the tubes of condenser 9. The brine leaving the other end of the tubes of condenser 9 is passed through steam-heater 27 and then introduced into the base of tower 1 through conduit 6.
GB03139/66A 1966-03-24 1966-03-24 Improvements in or relating to Water Desalination Processes and apparatus Expired GB1185824A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB03139/66A GB1185824A (en) 1966-03-24 1966-03-24 Improvements in or relating to Water Desalination Processes and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB03139/66A GB1185824A (en) 1966-03-24 1966-03-24 Improvements in or relating to Water Desalination Processes and apparatus

Publications (1)

Publication Number Publication Date
GB1185824A true GB1185824A (en) 1970-03-25

Family

ID=10017563

Family Applications (1)

Application Number Title Priority Date Filing Date
GB03139/66A Expired GB1185824A (en) 1966-03-24 1966-03-24 Improvements in or relating to Water Desalination Processes and apparatus

Country Status (1)

Country Link
GB (1) GB1185824A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990015652A1 (en) * 1989-06-14 1990-12-27 A. Ahlstrom Corporation Multistage evaporating system
US8287716B2 (en) 2009-03-31 2012-10-16 King Fahd University Of Petroleum And Minerals Desalination system and method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1990015652A1 (en) * 1989-06-14 1990-12-27 A. Ahlstrom Corporation Multistage evaporating system
US8287716B2 (en) 2009-03-31 2012-10-16 King Fahd University Of Petroleum And Minerals Desalination system and method

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Legal Events

Date Code Title Description
PS Patent sealed