GB1093791A - Process and apparatus for continuous regenerative distillation - Google Patents

Process and apparatus for continuous regenerative distillation

Info

Publication number
GB1093791A
GB1093791A GB7883/65A GB788365A GB1093791A GB 1093791 A GB1093791 A GB 1093791A GB 7883/65 A GB7883/65 A GB 7883/65A GB 788365 A GB788365 A GB 788365A GB 1093791 A GB1093791 A GB 1093791A
Authority
GB
United Kingdom
Prior art keywords
trays
water
vessel
pipe
chamber
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
GB7883/65A
Inventor
John James Cowley
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.)
Desal Ltd
Original Assignee
Desal 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 Desal Ltd filed Critical Desal Ltd
Publication of GB1093791A publication Critical patent/GB1093791A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0088Cascade evaporators
    • 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
    • C02F1/08Thin film 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

Abstract

1,093,791. Distillation apparatus, vapour-compression type; desalination of water. DESAL Ltd. Feb. 24, 1965, No. 7883/65. Headings B1B and B1M. Impure water, e.g. sea water, is distilled in an evacuated vessel divided into an evaporato chamber 26 and a condenser chamber 27 by a zig-zag barrier comprising heat-conductive trays 28, 29 connected together and arrangec one above the other and in such a way tha each tray has a slight inclination to the hori zontal, trays 28 sloping in the opposite direc tion to trays 29. Trays 28 and 29 are shapes to form V-channels 170 and U-shaped chan nels 171, respectively. The water-to-be-distillec is first de-aerated by causing it to flow as film down the inside wall of a conical vessel 121 (Fig. 11) which is maintained under vacuum at pipe 125. The water is drawn into vessel 121 through perforations 124 in a circular manifold attached to inlet pipe 120 The de-aerated water is then preheated an< introduced through pipe 94 (Fig. 1) into the distillation vessel, where it is sprayed into the upper ends of trays 28. The water flows turbulently down channels 170, which are heated from below, and vapour is evolved. The vapour is withdrawn from chamber 26 by compressor 85 and is forced into chamber 27 on the other side of the zig-zag barrier, where it condenses on the undersides of trays 28, which are pre ferably coated with silicone material. The con denser chamber is preferably provided with ar electrically-operated vibrating-diaphragm. The condensate, i.e. pure water, immediately drips off the undersides of trays 28 into channels 171 of trays 29, and is withdrawn from the distil lation-vessel via pipe 99. Residual air, and some water-vapour, is drawn through close mesh screens at the upper ends of trays 29 into an axial pipe, and is then withdrawn from the distillation-vessel through pipe 107 by means of an ejector operated by a stream of pure water. Residual brine is withdrawn from the vessel via pipe 103, and may be recirculated to attain any desired degree of brine concentration. Alternatively, the brine may be passed to a second distillation vessel. It is stated that a centrifuge may be used in conjunction with, or in place of, compressor 85 in order to separate heavy water.
GB7883/65A 1967-01-28 1965-02-24 Process and apparatus for continuous regenerative distillation Expired GB1093791A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DED0052132 1967-01-28

Publications (1)

Publication Number Publication Date
GB1093791A true GB1093791A (en) 1967-12-06

Family

ID=7053933

Family Applications (1)

Application Number Title Priority Date Filing Date
GB7883/65A Expired GB1093791A (en) 1967-01-28 1965-02-24 Process and apparatus for continuous regenerative distillation

Country Status (2)

Country Link
DE (1) DE1619690A1 (en)
GB (1) GB1093791A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108905241A (en) * 2018-06-29 2018-11-30 江苏海容热能环境工程有限公司 A kind of brine concentration and concentration regulator
CN113423666A (en) * 2019-02-11 2021-09-21 阿曼特希股份有限公司 Fully regenerative distillation system for low cost water desalination
CN113648676A (en) * 2021-09-23 2021-11-16 连云港诺信食品配料有限公司 Evaporation plant is used in calcium propionate production

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10328911A1 (en) * 2003-06-26 2005-02-03 Institut für Luft- und Kältetechnik gGmbH Vaporizer-condenser heat exchanger

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108905241A (en) * 2018-06-29 2018-11-30 江苏海容热能环境工程有限公司 A kind of brine concentration and concentration regulator
CN113423666A (en) * 2019-02-11 2021-09-21 阿曼特希股份有限公司 Fully regenerative distillation system for low cost water desalination
CN113423666B (en) * 2019-02-11 2023-10-27 阿曼特希股份有限公司 Complete regenerative distillation system for low cost water desalination
CN113648676A (en) * 2021-09-23 2021-11-16 连云港诺信食品配料有限公司 Evaporation plant is used in calcium propionate production

Also Published As

Publication number Publication date
DE1619690A1 (en) 1971-06-03

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