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GB312089A - Evaporating method and means therefor - Google Patents

Evaporating method and means therefor

Info

Publication number
GB312089A
GB312089A GB15554/29A GB1555429A GB312089A GB 312089 A GB312089 A GB 312089A GB 15554/29 A GB15554/29 A GB 15554/29A GB 1555429 A GB1555429 A GB 1555429A GB 312089 A GB312089 A GB 312089A
Authority
GB
United Kingdom
Prior art keywords
vapour
air
evaporating
pipe
heating
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
GB15554/29A
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.)
Industrikemiska AB
Original Assignee
Industrikemiska AB
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 Industrikemiska AB filed Critical Industrikemiska AB
Publication of GB312089A publication Critical patent/GB312089A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/22Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • B01D1/222In rotating vessels; vessels with movable parts
    • B01D1/228In rotating vessels; vessels with movable parts horizontally placed cylindrical container or drum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/22Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • 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
    • B01D3/34Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances
    • B01D3/343Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances the substance being a gas
    • B01D3/346Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping with one or more auxiliary substances the substance being a gas the gas being used for removing vapours, e.g. transport gas

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

312,089. Industrikemiska Aktiebolaget, (Assignees of Oman, E.). May 18, 1928, [Convention date]. Heating arrangements.-Liquids are evaporated and solids are dried in a multiple-effect apparatus in which heat is supplied by a gasvapour mixture not in contact with the liquid or solid, and the vaporized liquid is removed by a current of non-condensable gas. In a quadruple-effect apparatus (Fig. 3) solution is sprayed in at a' - - a<4>, so as to flow in a thin film down heating surfaces; the temperature of the entering solution is lowest at a<1> and highest at a<4>. Air circulated by a pump A<1> flows through the first evaporating chamber c<1> and takes up vapour from the liquid film; it then passes by a pipe d' to the evaporating chamber c<2> of the second effect, and the temperature being higher, the air absorbs more vapour. The process is continued in the third and fourth effects, and the air-vapour mixture leaves by a pipe d<4> leading to a heater C' where it is completely saturated with vapour and raised to a temperature above that of the solution entering at a<4>. The hot air-vapour mixture passing by a pipe g<4> to the heating chamber e<4> gives up a portion of its heat to the evaporating film, and then passes at successively lower temperatures through the heating chambers e<3>, e<2>, e<1>, in each of which it gives up a further portion of its heat. Condensate is removed by pipes f<1> - - f<4>. The air issuing from the chamber e<1>, is finally freed from vapour in a condenser D, and is re-circulated through a pipe H to the evaporating chambers c<1> - - c<4>. Concentrated solution is drawn off by pipes b<1> - - b<4>, and may be returned, with or without preheating, to the corresponding inlets a<1>, a<4>, or to different inlets, as from the outlet b<2> to the inlet a<1>. The pressure in the whole apparatus is kept substantially atmospheric by liquid seals as at E, F, G. Intimate contact between the liquid film and the air current may be obtained by baffles and obstructions as in Figs. 8<a>, 8<b>, 9<a>, 9<b>, 9<c> Several heating or evaporating chambers may be worked in parallel. The method may be applied to the rotating drum type of evaporator.
GB15554/29A 1928-05-18 1929-05-17 Evaporating method and means therefor Expired GB312089A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE312089X 1928-05-18

Publications (1)

Publication Number Publication Date
GB312089A true GB312089A (en) 1930-07-24

Family

ID=20307638

Family Applications (1)

Application Number Title Priority Date Filing Date
GB15554/29A Expired GB312089A (en) 1928-05-18 1929-05-17 Evaporating method and means therefor

Country Status (5)

Country Link
US (1) US2032182A (en)
DE (1) DE615845C (en)
FR (1) FR675258A (en)
GB (1) GB312089A (en)
NL (1) NL32410C (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2734565A (en) * 1956-02-14 lockman
US2707991A (en) * 1949-12-22 1955-05-10 Rosenblad Corp Heat treating a fluid substance
DE934217C (en) * 1953-02-05 1956-02-02 Paul Dr-Ing Gatzweiler Processes and systems for thickening milk, whey and vitamin liquids
AT313039B (en) * 1971-05-07 1974-01-25 Studiengesellschaft Kohle Mbh Process for obtaining caffeine from green coffee
FR2488379B1 (en) * 1980-08-11 1986-05-23 Centre Nat Rech Scient METHOD AND DEVICES FOR RECOVERY OF LOW LEVEL THERMAL ENERGY USING EVAPORATION AND MIXTURE PHENOMENA OF TWO VAPOR PRESSURE BALANCED FLUIDS
EP0046112B1 (en) * 1980-08-11 1986-02-26 Etablissement Public dit: CENTRE NATIONAL DE LA RECHERCHE SCIENTIFIQUE (CNRS) Device and systems for the revaluation of low-level thermal energy using phenomena of evaporation, and solution of two fluids being in equilibrium of vapour pressure at different temperatures
SE425079B (en) * 1981-10-22 1982-08-30 Eka Ab METHOD OF PREPARING VETEPEROXIDE THROUGH THE ANTRAKINON PROCESS
US4687546B1 (en) * 1985-07-19 1996-06-04 Anglo American Clays Corp Method of concentrating slurried kaolin
US4982782A (en) * 1986-07-09 1991-01-08 Walter F. Albers Method and apparatus for simultaneous heat and mass transfer
US4832115A (en) * 1986-07-09 1989-05-23 Albers Technologies Corporation Method and apparatus for simultaneous heat and mass transfer
US5123481A (en) * 1986-07-09 1992-06-23 Walter F. Albers Method and apparatus for simultaneous heat and mass transfer
US4767498A (en) * 1987-08-20 1988-08-30 Kreisler Lawrence M Method of reducing waste volume and an apparatus therefor
EP2194320A1 (en) * 2008-06-12 2010-06-09 Siemens Aktiengesellschaft Method for operating a once-through steam generator and once-through steam generator
US10584042B2 (en) * 2016-01-27 2020-03-10 T.S.D. Desalination Ltd Standalone humidification-dehumidification water purification method and system

Also Published As

Publication number Publication date
DE615845C (en) 1935-07-13
NL32410C (en) 1934-04-16
US2032182A (en) 1936-02-25
FR675258A (en) 1930-02-07

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