GB958596A - A method of and apparatus for cooling and crystallising saline solutions - Google Patents

A method of and apparatus for cooling and crystallising saline solutions

Info

Publication number
GB958596A
GB958596A GB2837961A GB2837961A GB958596A GB 958596 A GB958596 A GB 958596A GB 2837961 A GB2837961 A GB 2837961A GB 2837961 A GB2837961 A GB 2837961A GB 958596 A GB958596 A GB 958596A
Authority
GB
United Kingdom
Prior art keywords
stage
vessel
liquid
vacuum
evaporation
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
GB2837961A
Inventor
John Anthony Gale
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.)
KESTNER EVAPORATOR AND ENGINEE
Original Assignee
KESTNER EVAPORATOR AND ENGINEE
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 KESTNER EVAPORATOR AND ENGINEE filed Critical KESTNER EVAPORATOR AND ENGINEE
Priority to GB2837961A priority Critical patent/GB958596A/en
Publication of GB958596A publication Critical patent/GB958596A/en
Expired legal-status Critical Current

Links

Classifications

    • 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)
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D9/00Crystallisation
    • B01D9/0018Evaporation of components of the mixture to be separated
    • B01D9/0022Evaporation of components of the mixture to be separated by reducing pressure

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

958,596. Crystallizing saline solutions by evaporation. KESTNER EVAPORATOR & ENGINEERING CO. Ltd. July 25, 1962 [Aug. 4, 1961], No. 28379/61. Heading B1B. Saline solutions, such as pickle and spin bath liquors, are crystallized by flash evaporation without external heating in a multi-stage vacuum evaporator, wherein the vacuum increases progressively from one stage to the next, and the solution flows by gravity through the successive stages of the vessel. The feed to the three stage vacuum vessel 10 enters the first stage 13 via pipe 16 and flows by gravity down pipe 17 into stage 14, down pipe 18 into stage 15, and finally leaves the vessel via pipe 20. Different degrees of vacuum are maintained in stages 13, 14 and 15 by the steam ejectors 30 connected via the manifold 31 to the direct contact condenser 32, which is connected to a vacuum pump via line 2. Evaporation of the feed occurs under the reduced pressure in stage 13, and the vapour produced is extracted from the system via the aperture 27 in the separator 26, which serves to remove entrained liquid from the vapour. The cooled liquid from stage 13 passes into stage 14 and is cooled further by evaporation under a lower pressure. Similarly, the liquid leaving stage 14 is cooled further in stage 15. The liquid in each stage is agitated by a controlled supply of air admitted via pipe 24 and distributer 25. The liquid finally withdrawn from the vessel via line 20, containing the crystals formed during its passage through the vessel, is pumped into a centrifuge or filter 23 having a discharge outlet 4 for the separated crystals and an outlet 5 for the mother liquor.
GB2837961A 1961-08-04 1961-08-04 A method of and apparatus for cooling and crystallising saline solutions Expired GB958596A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2837961A GB958596A (en) 1961-08-04 1961-08-04 A method of and apparatus for cooling and crystallising saline solutions

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2837961A GB958596A (en) 1961-08-04 1961-08-04 A method of and apparatus for cooling and crystallising saline solutions

Publications (1)

Publication Number Publication Date
GB958596A true GB958596A (en) 1964-05-21

Family

ID=10274721

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2837961A Expired GB958596A (en) 1961-08-04 1961-08-04 A method of and apparatus for cooling and crystallising saline solutions

Country Status (1)

Country Link
GB (1) GB958596A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5632867A (en) * 1992-05-19 1997-05-27 Exxon Research And Engineering Company Recovering a relatively volatile component of a solution from a less volatile component, e.g. as in solvent recovery
WO2010084484A1 (en) * 2009-01-22 2010-07-29 I.D.E. Technologies Ltd. Cooling crystallizer
CN108341897A (en) * 2017-01-24 2018-07-31 中国石油化工股份有限公司 A method of removing solvent from polymer solution
CN110478937A (en) * 2019-08-21 2019-11-22 西安航天源动力工程有限公司 A kind of crystallizer and crystal system
CN112097464A (en) * 2020-09-07 2020-12-18 衡阳百赛化工实业有限公司 Zinc sulfate vacuum cooling device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5632867A (en) * 1992-05-19 1997-05-27 Exxon Research And Engineering Company Recovering a relatively volatile component of a solution from a less volatile component, e.g. as in solvent recovery
WO2010084484A1 (en) * 2009-01-22 2010-07-29 I.D.E. Technologies Ltd. Cooling crystallizer
JP2012515646A (en) * 2009-01-22 2012-07-12 アイ・ディ・イー・テクノロジーズ・リミテッド Cooling crystallizer
US8763426B2 (en) 2009-01-22 2014-07-01 I.D.E. Technologies Ltd. Cooling crystallizer
CN108341897A (en) * 2017-01-24 2018-07-31 中国石油化工股份有限公司 A method of removing solvent from polymer solution
CN108341897B (en) * 2017-01-24 2021-03-16 中国石油化工股份有限公司 Method for removing solvent from polymer solution
CN110478937A (en) * 2019-08-21 2019-11-22 西安航天源动力工程有限公司 A kind of crystallizer and crystal system
CN112097464A (en) * 2020-09-07 2020-12-18 衡阳百赛化工实业有限公司 Zinc sulfate vacuum cooling device

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