GB997501A - Improvements in and relating to evaporators - Google Patents

Improvements in and relating to evaporators

Info

Publication number
GB997501A
GB997501A GB175363A GB175363A GB997501A GB 997501 A GB997501 A GB 997501A GB 175363 A GB175363 A GB 175363A GB 175363 A GB175363 A GB 175363A GB 997501 A GB997501 A GB 997501A
Authority
GB
United Kingdom
Prior art keywords
heater
vapour
milk
conduit
separator
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
GB175363A
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.)
Machinenfabriek J & H W Van De
Original Assignee
Machinenfabriek J & H W Van De
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 Machinenfabriek J & H W Van De filed Critical Machinenfabriek J & H W Van De
Publication of GB997501A publication Critical patent/GB997501A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/06Evaporators with vertical tubes
    • B01D1/10Evaporators with vertical tubes with long tubes, e.g. Kestner evaporators
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C1/00Concentration, evaporation or drying
    • A23C1/12Concentration by evaporation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/0088Cascade evaporators
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/26Multiple-effect evaporating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/28Evaporating with vapour compression
    • B01D1/2803Special features relating to the vapour to be compressed
    • B01D1/2812The vapour is coming from different sources
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/28Evaporating with vapour compression
    • B01D1/284Special features relating to the compressed vapour
    • B01D1/2843The compressed vapour is divided in at least two streams
    • 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)

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Apparatus For Making Beverages (AREA)

Abstract

997,501. Multi-stage evaporators of the falling-film type. MACHINENFABRIK J. & H. W. VAN DER PLOEG N.V. May 3, 1963 [June 12, 1962], No. 17523/63. Heading BIB. In an evaporator comprising a plurality of tubular heaters wherein the liquid being evaporated flows in film-form down the inside surfaces of the tubes, the heaters being connected in series for the liquid, the rate of fall of the liquid-film in at least one of the heaters (other than the first) is increased by introducing into the top of the heater the vapour obtained by expansion of the liquid withdrawn from a preceding heater to the pressure prevailing in the first-mentioned heater. The apparatus shown comprises a three-stage evaporator in which milk flows through heaters 3, 14 and 6, successively. Milk at 185 ‹F. is pumped through conduit 2 to the top of heater 3 in which a temperature of 158 ‹F. prevails. Flash evaporation takes place in the top or the heater, and further evaporation takes place as the milk flows down the tubes in the form of a film. The mixture of milk and vapour is discharged into centrifugal separator 4. Part of the separated vapour is compressed in steam-jet compressor 7 and then used as heating-medium in heater 3. The remainder of the vapour removed from separator 4 is introduced, via conduit 5, as heating-medium into heater 6. The liquid withdrawn from separator 4 is pumped, together with the liquid accumulated at the bottom of heater 3, through conduit 10 into expansion vessel 11 where flash evaporation occurs, and the temperature of the milk decreases to 131 ‹F. The vapour is introduced through conduit 12 into the top of heater 6. The milk is lead from vessel 11 into the top of heater 14, which is operated at a temperature of 113 ‹F. The mixture of liquid and vapour discharged from heater 14 enters separator 15, from which the vapour passes to condenser 17. The milk withdrawn from separator 15 is pumped through conduit 19 into the top of heater 6. The conduit 19 includes a coil 20 which is heated to 158 ‹F. by the vapour in conduit 5. The temperature of the milk as it enters heater 6 is at a temperature of 131 ‹F. In the top of heater 6, the milk mixes with the vapour from expansion vessel 11, and is driven at high velocity down the internal surfaces of the tubes of the heater. A mixture of concentrated milk and vapour is discharged from the bottom of heater 6 into separator 21. The concentrated milk is withdrawn from the system via valve 23, but some of it may, if desired, be recirculated via valve 24 to heater 6. The vapour obtained in separator 21 is supplied as heating medium to heater 14. Part of the condensate of the heating-medium of heater 14 is vaporized in generator 26, and the vapour is passed through conduit 27 to expansion vessel 11. A four-stage evaporator, comprising two steam-jet compressors, is also described.
GB175363A 1962-06-12 1963-05-03 Improvements in and relating to evaporators Expired GB997501A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL279567 1962-06-12

Publications (1)

Publication Number Publication Date
GB997501A true GB997501A (en) 1965-07-07

Family

ID=19753895

Family Applications (1)

Application Number Title Priority Date Filing Date
GB175363A Expired GB997501A (en) 1962-06-12 1963-05-03 Improvements in and relating to evaporators

Country Status (3)

Country Link
DE (1) DE1444352A1 (en)
GB (1) GB997501A (en)
NL (2) NL136374C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4303468A (en) * 1979-04-19 1981-12-01 Laguilharre S.A. Mechanical vapor recompression evaporators
US6132555A (en) * 1996-11-01 2000-10-17 Kvaerner Pulping Oy Method and arrangement for increasing evaporation capacity of a multi-stage evaporator of spent liquor in a pulp mill
WO2009114907A1 (en) * 2008-03-20 2009-09-24 Australian Creative Technologies Pty Ltd Fluid fractionation process and apparatus

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4303468A (en) * 1979-04-19 1981-12-01 Laguilharre S.A. Mechanical vapor recompression evaporators
US6132555A (en) * 1996-11-01 2000-10-17 Kvaerner Pulping Oy Method and arrangement for increasing evaporation capacity of a multi-stage evaporator of spent liquor in a pulp mill
WO2009114907A1 (en) * 2008-03-20 2009-09-24 Australian Creative Technologies Pty Ltd Fluid fractionation process and apparatus
CN102036725A (en) * 2008-03-20 2011-04-27 创新水科技有限公司 Fluid fractionation process and apparatus
US8591704B2 (en) 2008-03-20 2013-11-26 Creative Water Technology Ltd. Fluid fractionation process and apparatus
CN102036725B (en) * 2008-03-20 2013-11-27 创新水科技有限公司 Fluid fractionation process and apparatus

Also Published As

Publication number Publication date
NL136374C (en)
NL279567A (en)
DE1444352A1 (en) 1969-02-20

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