GB997501A - Improvements in and relating to evaporators - Google Patents
Improvements in and relating to evaporatorsInfo
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/10—Evaporators with vertical tubes with long tubes, e.g. Kestner evaporators
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C1/00—Concentration, evaporation or drying
- A23C1/12—Concentration by evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0088—Cascade evaporators
-
- 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
- B01D1/2803—Special features relating to the vapour to be compressed
- B01D1/2812—The vapour is coming from different sources
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
- B01D3/065—Multiple-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.
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)
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 |
-
0
- NL NL279567D patent/NL279567A/xx unknown
- NL NL136374D patent/NL136374C/xx active
-
1963
- 1963-04-23 DE DE19631444352 patent/DE1444352A1/en not_active Withdrawn
- 1963-05-03 GB GB175363A patent/GB997501A/en not_active Expired
Cited By (6)
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 |
---|---|
NL279567A (en) | |
NL136374C (en) | |
DE1444352A1 (en) | 1969-02-20 |
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