GB824111A - Improvements in and relating to evaporators - Google Patents

Improvements in and relating to evaporators

Info

Publication number
GB824111A
GB824111A GB10297/56A GB1029756A GB824111A GB 824111 A GB824111 A GB 824111A GB 10297/56 A GB10297/56 A GB 10297/56A GB 1029756 A GB1029756 A GB 1029756A GB 824111 A GB824111 A GB 824111A
Authority
GB
United Kingdom
Prior art keywords
chamber
liquid
weir
orifices
chambers
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
GB10297/56A
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.)
Richardsons Westgarth and Co Ltd
Original Assignee
Richardsons Westgarth and Co 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 Richardsons Westgarth and Co Ltd filed Critical Richardsons Westgarth and Co Ltd
Priority to GB10297/56A priority Critical patent/GB824111A/en
Priority to US650217A priority patent/US2944599A/en
Publication of GB824111A publication Critical patent/GB824111A/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)
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00Distillation: processes, separatory
    • Y10S203/18Control

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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

<PICT:0824111/III/1> <PICT:0824111/III/2> <PICT:0824111/III/3> A multi-stage flash-type evaporator comprises a shell which is divided by a partition-walls 16 into a number of flash-chambers 10 arranged side by side in a straight line, the upper part of each chamber having an outlet 18 for the discharge of vapour; the lower portions of the walls 16 have orifices 14 for the passage of heated liquid through the chambers, and each chamber is provided with a weir 20 the top of which lies above the orifices through which the liquid enters and leaves the chamber, the horizontal distance of the upper edge of the weir from the inlet end of the chamber being equal to or less than its horizontal distance from the outlet end. The heated liquid enters the first chamber through pipe 12, and passes from chamber to chamber through orifices 14. For any given operating condition, from starting-up to full load, the liquid-level upstream of each orifice 14 adjusts itself so that the difference in static head across the opening plus the vapour-pressure difference on either side of the wall 16 are sufficient to transfer the liquid through the orifice and over the top of the weir lying downstream of the orifice. The liquid levels in the chambers on full load operation are shown at 24 and 26 in Fig. 1. Under low-load or no-load conditions, when the pressure difference from stage to stage is small or absent, the liquid levels in the chambers are higher, the levels on no-load being shown at 22. In the alternative embodiment shown in Fig. 3, each weir is arranged close to the upstream wall of the chamber and is bent over at the upper part to form, at the top of the weir, a secondary orifice 32 through which the liquid is projected upwards into the chamber. Baffle plates 34 are arranged above the orifices 32 in such a position that the liquid is projected on to them.
GB10297/56A 1956-04-04 1956-04-04 Improvements in and relating to evaporators Expired GB824111A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
GB10297/56A GB824111A (en) 1956-04-04 1956-04-04 Improvements in and relating to evaporators
US650217A US2944599A (en) 1956-04-04 1957-04-02 Flash evaporator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB10297/56A GB824111A (en) 1956-04-04 1956-04-04 Improvements in and relating to evaporators

Publications (1)

Publication Number Publication Date
GB824111A true GB824111A (en) 1959-11-25

Family

ID=9965262

Family Applications (1)

Application Number Title Priority Date Filing Date
GB10297/56A Expired GB824111A (en) 1956-04-04 1956-04-04 Improvements in and relating to evaporators

Country Status (2)

Country Link
US (1) US2944599A (en)
GB (1) GB824111A (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB901001A (en) * 1959-03-24 1962-07-11 Richardsons Westgarth & Co Improvements in or relating to steam generating plant
US3192132A (en) * 1960-06-20 1965-06-29 Aqua Chem Inc Apparatus for conducting feed through flash evaporators
US3161558A (en) * 1960-07-05 1964-12-15 Aqua Chem Inc Flash chamber structure
US3219553A (en) * 1961-01-17 1965-11-23 American Mach & Foundry Multi-stage flash type evaporators
US3142381A (en) * 1961-04-10 1964-07-28 Baldwin Lima Hamilton Corp Evaporator construction
US3180805A (en) * 1961-09-01 1965-04-27 Chicago Bridge & Iron Co Multi-stage flash evaporation system
NL271501A (en) * 1961-11-17
GB1051622A (en) * 1964-03-23
GB1086731A (en) * 1964-03-23 1967-10-11 American Mach & Foundry Improvements in or relating to distillation apparatus
US3172824A (en) * 1964-10-20 1965-03-09 Evaporator construction
US3398059A (en) * 1965-05-24 1968-08-20 Westinghouse Electric Corp Multi-stage flash evaporator with means to induce hydraulic jump
US3941663A (en) * 1972-07-03 1976-03-02 Aqua-Chem, Inc. Multi-effect evaporator

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US881523A (en) * 1904-10-31 1908-03-10 Winter Kunststoff Heinr J Apparatus for continuous evaporation.
US2693350A (en) * 1951-07-14 1954-11-02 Edw G Ragatz Co Construction for handling vapors and liquids as in bubble columns or the like
US2759882A (en) * 1954-07-30 1956-08-21 Bethlehem Steel Corp Combined flash and vapor compression evaporator

Also Published As

Publication number Publication date
US2944599A (en) 1960-07-12

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