JPS57130502A - Vacuum-distillator - Google Patents

Vacuum-distillator

Info

Publication number
JPS57130502A
JPS57130502A JP1730181A JP1730181A JPS57130502A JP S57130502 A JPS57130502 A JP S57130502A JP 1730181 A JP1730181 A JP 1730181A JP 1730181 A JP1730181 A JP 1730181A JP S57130502 A JPS57130502 A JP S57130502A
Authority
JP
Japan
Prior art keywords
compressor
mixed liquid
steam
boiling tank
tank
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.)
Pending
Application number
JP1730181A
Other languages
Japanese (ja)
Inventor
Shoji Mishiro
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.)
Taga Electric Co Ltd
Original Assignee
Taga Electric Co 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 Taga Electric Co Ltd filed Critical Taga Electric Co Ltd
Priority to JP1730181A priority Critical patent/JPS57130502A/en
Publication of JPS57130502A publication Critical patent/JPS57130502A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE: To improve energy efficiency, by transmitting the thermal energy of steam generated in a boiling tank to mixed liquid with a heat exchanger located inside the tank, and arranging the second compressor at a discharge side.
CONSTITUTION: A fixed amount of mixed liquid 12 is introduced into a boiling tank 11 through a mixed liquid-inflow plug 14, while the internal pressures inside the boiling tank 11 and a steam pipe 17 are kept at a negative level by a compressor 18. At the start of operation, atmospheric pressure inside the boiling tank 11 is reduced slightly lower than that necessary for operation, so that the mixed liquid 12 is boiled to generate steam. The steam is then compressed by the first compressor 18 to raise its temperature, subjected to heat-exchange during its passage through a cooling pipe 20, liquidized into distilled liquid 24 by discharge of its latent heat, compressed up to the atmospheric pressure by the second compressor 22 and reserved in a vessel 25. As a result, distillation can be performed with high energy efficiency.
COPYRIGHT: (C)1982,JPO&Japio
JP1730181A 1981-02-06 1981-02-06 Vacuum-distillator Pending JPS57130502A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1730181A JPS57130502A (en) 1981-02-06 1981-02-06 Vacuum-distillator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1730181A JPS57130502A (en) 1981-02-06 1981-02-06 Vacuum-distillator

Publications (1)

Publication Number Publication Date
JPS57130502A true JPS57130502A (en) 1982-08-13

Family

ID=11940175

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1730181A Pending JPS57130502A (en) 1981-02-06 1981-02-06 Vacuum-distillator

Country Status (1)

Country Link
JP (1) JPS57130502A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001005709A1 (en) * 1999-07-19 2001-01-25 Ramjibhai Italiya Rasiklal Method of distillation of water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001005709A1 (en) * 1999-07-19 2001-01-25 Ramjibhai Italiya Rasiklal Method of distillation of water

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