JPS54102287A - Distilling method - Google Patents

Distilling method

Info

Publication number
JPS54102287A
JPS54102287A JP886678A JP886678A JPS54102287A JP S54102287 A JPS54102287 A JP S54102287A JP 886678 A JP886678 A JP 886678A JP 886678 A JP886678 A JP 886678A JP S54102287 A JPS54102287 A JP S54102287A
Authority
JP
Japan
Prior art keywords
gas
cooling
cold
overhead
distilling column
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
JP886678A
Other languages
Japanese (ja)
Inventor
Kanae Fujinaga
Hiroyuki Hara
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP886678A priority Critical patent/JPS54102287A/en
Publication of JPS54102287A publication Critical patent/JPS54102287A/en
Pending legal-status Critical Current

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Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE: To contrive the energy economization of surrounding equipment of distilling column, by cooling and condensing overhead gas of distilling column and utilizing each cold and hot gas obtained by inducing uncondensed gas to heat separation apparatus, as cold heat source of cooling of each overhead gas and reheating heat source of circulating liquid of distilling column.
CONSTITUTION: Overhead gas discharged from the distilling column 2, is separated in condensed liquid and uncondensed gas at the gas-liquid separator 8 after the overhead gas is cooled and condensed at the condenser 7. Then, the uncondensed gas is induced to the heat separating apparatus 21 and is made cold gas by reducing pressure and bringing down temperature and on the one hand, residual gas in the apparatus 21 is made high temperature gas. Next, the above cold gas is induced to the cooler 22 and is used for cooling and condensing the overhead gas after cooling and condensing by the cooling condenser 7 moreover. On the one hand, the above high temperature ga is induced to the heater 23 and is used for reheating of the circularing liquid 4. As a result of it, increase or decrease of the equipment of the condenser 7 and quantity of cooling medium, is able to contrive and at the same time, that of the equipment of the reboiler 5 and quantity of heating medium, is able to contrive.
COPYRIGHT: (C)1979,JPO&Japio
JP886678A 1978-01-31 1978-01-31 Distilling method Pending JPS54102287A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP886678A JPS54102287A (en) 1978-01-31 1978-01-31 Distilling method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP886678A JPS54102287A (en) 1978-01-31 1978-01-31 Distilling method

Publications (1)

Publication Number Publication Date
JPS54102287A true JPS54102287A (en) 1979-08-11

Family

ID=11704606

Family Applications (1)

Application Number Title Priority Date Filing Date
JP886678A Pending JPS54102287A (en) 1978-01-31 1978-01-31 Distilling method

Country Status (1)

Country Link
JP (1) JPS54102287A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS574202A (en) * 1980-06-06 1982-01-09 Asia Sekiyu Kk Operating method for distilling column
US4471619A (en) * 1982-08-23 1984-09-18 Uop Inc. Fractionation process with power generation by depressurizing the overhead vapor stream
CN103950935A (en) * 2014-03-31 2014-07-30 中国恩菲工程技术有限公司 System for purifying chlorosilane through non-relevant tower differential pressure thermal coupling

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS574202A (en) * 1980-06-06 1982-01-09 Asia Sekiyu Kk Operating method for distilling column
JPS6327042B2 (en) * 1980-06-06 1988-06-01 Asia Oil Co Ltd
US4471619A (en) * 1982-08-23 1984-09-18 Uop Inc. Fractionation process with power generation by depressurizing the overhead vapor stream
CN103950935A (en) * 2014-03-31 2014-07-30 中国恩菲工程技术有限公司 System for purifying chlorosilane through non-relevant tower differential pressure thermal coupling

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