GB1300472A - Improvements in or relating to evaporation plant - Google Patents

Improvements in or relating to evaporation plant

Info

Publication number
GB1300472A
GB1300472A GB3895370A GB3895370A GB1300472A GB 1300472 A GB1300472 A GB 1300472A GB 3895370 A GB3895370 A GB 3895370A GB 3895370 A GB3895370 A GB 3895370A GB 1300472 A GB1300472 A GB 1300472A
Authority
GB
United Kingdom
Prior art keywords
stages
evaporator
line
vapour
compressor
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
GB3895370A
Inventor
Denis Taylor
Robin Mcilraith Gray
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.)
SPX Flow Technology Crawley Ltd
Original Assignee
APV Corp 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 APV Corp Ltd filed Critical APV Corp Ltd
Priority to GB3895370A priority Critical patent/GB1300472A/en
Publication of GB1300472A publication Critical patent/GB1300472A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/28—Evaporating with vapour compression
    • B01D1/2803—Special features relating to the vapour to be compressed
    • B01D1/2806—The vapour is divided in at least two streams and only a part of the vapour is compressed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/26—Multiple-effect evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/28—Evaporating with vapour compression
    • B01D1/284—Special features relating to the compressed vapour
    • B01D1/2843—The compressed vapour is divided in at least two streams

Landscapes

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

Abstract

1300472 Evaporation plant; concentration of distillers spent wash APV CO Ltd 16 July 1971 [12 Aug 1970] 38953/70 Heading BIB Distillers spent wash, or other liquor which contains dissolved solids, is concentrated by evaporation in a series of primary evaporation stages A1, A2, A3, and two further evaporator stages Cl, C2; there also being connected, between stages A1 and A2, an evaporator B which is operated under pressure and heated by live steam (e.g. at 120 psi) supplied through line 19 and a thermo-compressor 21 which entrains some of the vapour evolved from the liquor as it flows through evaporator B, that portion of the vapour not entrained by compressor 21 being passed through line 24 for use as heating-medium in stages C1 and C2. In the plant shown, stages A1 A2, A3 are associated with mechanical compressors for the vapour; and the compressed vapours are used for heating these stages. Stages C1 and C2 may be plate-type evaporators. Distillers spent wash containing 1.4% dissolved solids is pumped through line 2 to evaporator Al; and the final concentrate containing 30% solids is withdrawn from evaporator C2 and separator 53 by pump 54. Evaporator Al is operated by compressor 8. The uncondensed vapours and the condensate leaving the heating elements of Al pass to separator 11. The separated vapour flows through line 14 and may be used to preheat the feed liquor. Similarly the separated condensate (together with that from stages B, A2 and A3) in line 13 may be used in a preheating heat exchanger, and constitutes a supply of soft water. Part of the liquor withdrawn from each of the stages A1, B, A2, A3, is recycled to the stage from which it is withdrawn, and the remainder is passed to the succeeding stage. Evaporators A2 and A3 are operated by a single compressor 33.
GB3895370A 1970-08-12 1970-08-12 Improvements in or relating to evaporation plant Expired GB1300472A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3895370A GB1300472A (en) 1970-08-12 1970-08-12 Improvements in or relating to evaporation plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3895370A GB1300472A (en) 1970-08-12 1970-08-12 Improvements in or relating to evaporation plant

Publications (1)

Publication Number Publication Date
GB1300472A true GB1300472A (en) 1972-12-20

Family

ID=10406716

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3895370A Expired GB1300472A (en) 1970-08-12 1970-08-12 Improvements in or relating to evaporation plant

Country Status (1)

Country Link
GB (1) GB1300472A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2442886A1 (en) * 1978-05-09 1980-06-27 Tepral Grpt Interet Economique Continuous cooking of beer wort reduces energy requirement - by recycling vapour from boiling vessels via compressor back to vessel heaters
FR2467912A1 (en) * 1979-10-23 1981-04-30 Laguilharre Sa Concn. of black liquor in paper-making - carried out in three stages prior to burning
EP0193206A1 (en) * 1985-02-28 1986-09-03 GEA Wiegand GmbH Method and apparatus for the dealcoholization of beer, brewers' yeast, wine, champagne, sparkling wine or such
WO2014053373A1 (en) * 2012-10-01 2014-04-10 Gea Wiegand Gmbh Plant for de-alcoholizing a product containing alcohol, particularly ethanol
CN110433514A (en) * 2018-05-03 2019-11-12 温州龙强机械科技有限公司 Double-effect falling film evaporator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2442886A1 (en) * 1978-05-09 1980-06-27 Tepral Grpt Interet Economique Continuous cooking of beer wort reduces energy requirement - by recycling vapour from boiling vessels via compressor back to vessel heaters
FR2467912A1 (en) * 1979-10-23 1981-04-30 Laguilharre Sa Concn. of black liquor in paper-making - carried out in three stages prior to burning
EP0193206A1 (en) * 1985-02-28 1986-09-03 GEA Wiegand GmbH Method and apparatus for the dealcoholization of beer, brewers' yeast, wine, champagne, sparkling wine or such
WO2014053373A1 (en) * 2012-10-01 2014-04-10 Gea Wiegand Gmbh Plant for de-alcoholizing a product containing alcohol, particularly ethanol
CN110433514A (en) * 2018-05-03 2019-11-12 温州龙强机械科技有限公司 Double-effect falling film evaporator

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee