GB794379A - Improvements in or relating to flash evaporating and condensing systems - Google Patents

Improvements in or relating to flash evaporating and condensing systems

Info

Publication number
GB794379A
GB794379A GB327356A GB327356A GB794379A GB 794379 A GB794379 A GB 794379A GB 327356 A GB327356 A GB 327356A GB 327356 A GB327356 A GB 327356A GB 794379 A GB794379 A GB 794379A
Authority
GB
United Kingdom
Prior art keywords
water
vapour
partitions
sections
shell
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
GB327356A
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.)
Westinghouse Electric International Co
Original Assignee
Westinghouse Electric International Co
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
Priority to BE547045D priority Critical patent/BE547045A/xx
Application filed by Westinghouse Electric International Co filed Critical Westinghouse Electric International Co
Priority to GB327356A priority patent/GB794379A/en
Priority to FR1153153D priority patent/FR1153153A/en
Publication of GB794379A publication Critical patent/GB794379A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • F28B1/02Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • 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
    • 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

Landscapes

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

Abstract

In apparatus wherein preheated liquid is introduced into a vessel maintained at reduced pressure so that flash-vaporization of part of the liquid occurs, and the vapour is condensed in another section of the same vessel, the partitions between the evaporator and the vapour-condensing sections are partly shaped to form a nozzle passage arranged so that the vapour flows from the evaporator section through the nozzle passage and then undergoes a sharp change of direction, whereby entrained liquid is separated out of the vapour, before the vapour enters the condensation section. The apparatus is suitable for distilling sea water to make boilerfeed water or drinking water. In the apparatus shown, partitions 16, 16 and 17, 17 divide the interior of shell 10 into evaporator sections 18, 18 and separator sections 20, 20; the lower parts of partitions 16 being submerged in a pool of unevaporated water in the bottom of the shell. The curved portions 25 of partitions 16 define a nozzle passage extending from one end of the shell to the other; and a vapour-deflector 30 is mounted below the outlet of the nozzle passage. The upper edges 28 of partitions 17 are disposed inwardly of, and in overlapping spaced-relationship with, the curved portions 25 of partitions 16, whereby two passages 29 are formed which lead from separator-sections 20 <PICT:0794379/III/1> <PICT:0794379/III/2> to the condensing spaces within the partitions. Passages 29 are provided with baffles 29a. The condensing spaces are provided with tubes 33, through which cooling-water is circulated in four passes from boxes 38, 39 mounted on the end-plates 12 of the shell. The apparatus is maintained at a low absolute pressure by a pump connected to conduits 32. Water, at a temperature higher than the boiling-point at the pressure in the shell, is supplied to pipes 27 which have openings through which the water is sprayed downwards into sections 18, where flash-vaporization takes place. The vapour flows down through the nozzle passage, and then undergoes a sharp reversal in direction so as to pass up passages 29 into the condensing-sections Entrained water is forced out of the vapour by centrifugal action during the change of direction; and residual droplets are removed by baffles 29a. The vapour condenses on tubes 33, and the condensate is withdrawn from the apparatus through conduits 31. Residual water is removed through outlet 22, and is pumped through heater 44 before being returned to spray-pipes 27. A periodic discharge is made by means of blow-down valve 49 in order to avoid undue concentration of salts in the spraywater. Make-up water is supplied through connection 50 having a valve 51 which is opened by float 52 when the water-level at the bottom of the shell falls below a predetermined height. In a modification (not shown) the arrangement is such that a portion of the vapour flows upwards through the condensing-sections, thereby heating the falling condensate; the hot water withdrawn from the apparatus is free from oxygen and is suitable for use as boiler feed water.
GB327356A 1956-02-02 1956-02-02 Improvements in or relating to flash evaporating and condensing systems Expired GB794379A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BE547045D BE547045A (en) 1956-02-02
GB327356A GB794379A (en) 1956-02-02 1956-02-02 Improvements in or relating to flash evaporating and condensing systems
FR1153153D FR1153153A (en) 1956-02-02 1956-04-27 Instant vaporization and condensation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB327356A GB794379A (en) 1956-02-02 1956-02-02 Improvements in or relating to flash evaporating and condensing systems

Publications (1)

Publication Number Publication Date
GB794379A true GB794379A (en) 1958-04-30

Family

ID=9755222

Family Applications (1)

Application Number Title Priority Date Filing Date
GB327356A Expired GB794379A (en) 1956-02-02 1956-02-02 Improvements in or relating to flash evaporating and condensing systems

Country Status (3)

Country Link
BE (1) BE547045A (en)
FR (1) FR1153153A (en)
GB (1) GB794379A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1280762B (en) * 1960-02-26 1968-10-17 American Mach & Foundry Heating device in a seawater evaporator operated with waste heat from internal combustion engines
DE1299564B (en) * 1961-06-29 1969-07-17 Aqua Chem Inc Multi-stage high-speed evaporator
DE1299565B (en) * 1960-07-05 1969-07-17 Aqua Chem Inc Multi-stage evaporator for the extraction of fresh water
DE2628147A1 (en) * 1976-06-23 1978-01-05 Risto Dipl Ing Saari Flash evaporator for e.g. seawater or industrial effluent - has tapering duct to flash nozzles and diverging evaporator duct in each stage
CN102381964A (en) * 2010-09-01 2012-03-21 天华化工机械及自动化研究设计院 Integral process for washing and filtering terephthalic acid and water recovery
CN110028121A (en) * 2019-05-10 2019-07-19 成都三顶环保科技有限公司 Desulfurization wastewater treatment system

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GT199500016A (en) * 1994-04-15 1996-10-02 OCEAN THERMAL ENERGY CONVERSION SYSTEM

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1280762B (en) * 1960-02-26 1968-10-17 American Mach & Foundry Heating device in a seawater evaporator operated with waste heat from internal combustion engines
DE1299565B (en) * 1960-07-05 1969-07-17 Aqua Chem Inc Multi-stage evaporator for the extraction of fresh water
DE1299564B (en) * 1961-06-29 1969-07-17 Aqua Chem Inc Multi-stage high-speed evaporator
DE2628147A1 (en) * 1976-06-23 1978-01-05 Risto Dipl Ing Saari Flash evaporator for e.g. seawater or industrial effluent - has tapering duct to flash nozzles and diverging evaporator duct in each stage
CN102381964A (en) * 2010-09-01 2012-03-21 天华化工机械及自动化研究设计院 Integral process for washing and filtering terephthalic acid and water recovery
CN110028121A (en) * 2019-05-10 2019-07-19 成都三顶环保科技有限公司 Desulfurization wastewater treatment system
CN110028121B (en) * 2019-05-10 2021-10-22 成都三顶环保科技有限公司 Desulfurization wastewater treatment system

Also Published As

Publication number Publication date
FR1153153A (en)
BE547045A (en)

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