GB174572A - A new or improved flash evaporator - Google Patents

A new or improved flash evaporator

Info

Publication number
GB174572A
GB174572A GB28204/21A GB2820421A GB174572A GB 174572 A GB174572 A GB 174572A GB 28204/21 A GB28204/21 A GB 28204/21A GB 2820421 A GB2820421 A GB 2820421A GB 174572 A GB174572 A GB 174572A
Authority
GB
United Kingdom
Prior art keywords
liquid
pump
chamber
pipe
supply
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
GB28204/21A
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.)
Griscom Russell Co
Original Assignee
Griscom Russell 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
Application filed by Griscom Russell Co filed Critical Griscom Russell Co
Publication of GB174572A publication Critical patent/GB174572A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0094Evaporating with forced circulation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/04Evaporators with horizontal tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/30Accessories for evaporators ; Constructional details thereof
    • B01D1/305Demister (vapour-liquid separation)
    • 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
    • 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
    • Y10S159/00Concentrating evaporators
    • Y10S159/901Promoting circulation

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)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

174,572. Griscom-Russell Co., (Assignees of Sebald, L. E.). Jan. 27, 1921, CG'onvention date]. Generating by reduction of pressures of heated water.-In an apparatus for vaporizing liquids, particularly for evaporating brine or other impure water in producing distilled water for boilerfeed &c., a heating-agent such as steam or flue gases is passed through an inlet 2 on to the outside of a group of tubes 3 through which the liquid to be evaporated is forced by a pump 8. The heated liquid is sprayed through a pipe 11 above the surface of the liquid in the chamber 12. The vapour formed rises through baffles 13 to an outlet 14. A regulating-valve 4 on the pipe 11 retains sufficient pressure in the tubes 3 to prevent evaporation and consequent formation of scale therein. Residual liquid is withdrawn from the chamber 12 by a pipe 15 and recirculated by the pump 8. A continuous supply of fresh liquid and withdrawal of concentrated residual liquid in suitable proportions are maintained by pumps 20, 21 of different capacity mounted on the same shaft and operated by a motor 22. The proportions of liquid supplied and withdrawn may be varied by a by-pass 23, which enables liquid from the supply pump to pass to the withdrawal pump. The Specification as open to inspection under Sect. 91 (3) (a) describes also that the motor 22 may be controlled automaticall to maintain a definite level of liquid in the chamber 12. A separate float-controlled pump for the supply and separate regulator for withdrawing residual liquid may be used. This subject-matter does not appear in the Specification as accepted.
GB28204/21A 1921-01-27 1921-10-24 A new or improved flash evaporator Expired GB174572A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US440327A US1516314A (en) 1921-01-27 1921-01-27 Flash evaporator

Publications (1)

Publication Number Publication Date
GB174572A true GB174572A (en) 1923-04-24

Family

ID=23748331

Family Applications (1)

Application Number Title Priority Date Filing Date
GB28204/21A Expired GB174572A (en) 1921-01-27 1921-10-24 A new or improved flash evaporator

Country Status (3)

Country Link
US (1) US1516314A (en)
FR (1) FR543102A (en)
GB (1) GB174572A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108046362A (en) * 2017-12-15 2018-05-18 鲁西化工集团股份有限公司煤化工分公司 A kind of efficient corrosion-proof flash separation equipment

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2718493A (en) * 1953-04-23 1955-09-20 Jr Paul Lawler Distillation test apparatus
US3293151A (en) * 1963-03-29 1966-12-20 American Mach & Foundry Aqueous radioactive waste concentrator
US3382157A (en) * 1964-05-18 1968-05-07 William A. Barnstead Steam jacketed cylindrical water still with demister and access door
FR1531361A (en) * 1966-09-21 1968-07-05 Evaporator improvements
US3519054A (en) * 1969-01-06 1970-07-07 Colgate Palmolive Co Process for producing a particulate product
US3623977A (en) * 1970-06-25 1971-11-30 Fmc Corp Sewage treatment process
US3978681A (en) * 1974-09-16 1976-09-07 Research Corporation Method and apparatus for the adiabatic expansion of liquid anhydrous ammonia
US4385500A (en) * 1974-09-16 1983-05-31 Research Corporation Method and apparatus for the adiabatic expansion of liquid anhydrous ammonia
US5376238A (en) * 1992-08-24 1994-12-27 The Glidden Company Latex paint recovery process by vacuum evaporation
JPH09156082A (en) * 1995-12-07 1997-06-17 Mitsubishi Heavy Ind Ltd Method and apparatus for recovering solvent from washing waste solution of printing press
GB9804479D0 (en) * 1998-03-02 1998-04-29 Chemtech International Ltd Stripping of volatile substances from less volatile fluids
US6454907B1 (en) * 1999-04-19 2002-09-24 Minerals Technologies, Inc. Method and apparatus for concentrating slurried solids
US8709257B2 (en) * 2010-04-20 2014-04-29 King Abdulaziz City for Science and Technology (KACST) Method and system for purifying liquid using waste heat

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108046362A (en) * 2017-12-15 2018-05-18 鲁西化工集团股份有限公司煤化工分公司 A kind of efficient corrosion-proof flash separation equipment
CN108046362B (en) * 2017-12-15 2021-03-26 鲁西化工集团股份有限公司煤化工分公司 High-efficient anticorrosive flash distillation splitter

Also Published As

Publication number Publication date
FR543102A (en) 1922-08-28
US1516314A (en) 1924-11-18

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