JPS6480405A - Separation of liquid mixture - Google Patents
Separation of liquid mixtureInfo
- Publication number
- JPS6480405A JPS6480405A JP13457688A JP13457688A JPS6480405A JP S6480405 A JPS6480405 A JP S6480405A JP 13457688 A JP13457688 A JP 13457688A JP 13457688 A JP13457688 A JP 13457688A JP S6480405 A JPS6480405 A JP S6480405A
- Authority
- JP
- Japan
- Prior art keywords
- liq
- film
- separation
- mixture
- vapor
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/36—Pervaporation; Membrane distillation; Liquid permeation
Abstract
PURPOSE:To reduce the temp. decrease of a liq. mixture on a separation membrane by vaporizing at least a part of a raw liq. mixture to be supplied, bringing the vapor into direct contact with the liq. film of the liq. mixture on the separation membrane and partially condensing the vapor into the liq. film. CONSTITUTION:In the separation by permeation and vaporization, the mixture at least part of which is vaporized, is introduced into one end of a module unit 2. A part of the vapor is brought into contact with the liq. film 4 flowing on the separation membrane 3, and condensed. The remaining vapor is liquefied by a condenser 5, and supplied as the liq. film 4 through a connecting pipe 6. The component 7 permeated through the membrane and a liq. residue 8 are further purified, as required, in a distillation tower, and used as the products. By this method, the temp. decrease of the liq. film in the module unit is reduced, the separation system is made compact, the capacity is increased, and the cost is reduced.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13457688A JP2528939B2 (en) | 1987-06-12 | 1988-05-31 | Separation method of mixed liquid |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14730587 | 1987-06-12 | ||
JP62-147305 | 1987-06-12 | ||
JP13457688A JP2528939B2 (en) | 1987-06-12 | 1988-05-31 | Separation method of mixed liquid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6480405A true JPS6480405A (en) | 1989-03-27 |
JP2528939B2 JP2528939B2 (en) | 1996-08-28 |
Family
ID=26468650
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13457688A Expired - Lifetime JP2528939B2 (en) | 1987-06-12 | 1988-05-31 | Separation method of mixed liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2528939B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007503976A (en) * | 2003-08-28 | 2007-03-01 | ビーピー・コーポレーション・ノース・アメリカ・インコーポレーテッド | Selective separation of fluid compounds using membrane separation process |
JP2010514543A (en) * | 2006-07-14 | 2010-05-06 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | Improved membrane separation process using gas-liquid feed |
WO2010125897A1 (en) * | 2009-05-01 | 2010-11-04 | 日本碍子株式会社 | Separation membrane for concentration of sulfuric acid, method for concentration of sulfuric acid, and apparatus for concentration of sulfuric acid |
WO2010125898A1 (en) * | 2009-05-01 | 2010-11-04 | 日本碍子株式会社 | Separation membrane for concentration of hydrochloric acid, method for concentration of hydrochloric acid, and apparatus for concentration of hydrochloric acid |
JP2011056431A (en) * | 2009-09-11 | 2011-03-24 | Hitachi Zosen Corp | Module for pervaporation membrane separation |
JP2013533100A (en) * | 2010-05-17 | 2013-08-22 | シュティヒティン・エネルギーオンデルツォイク・セントラム・ネーデルランド | Organophilic polysilsesquioxane membranes for solvent nanofiltration and pervaporation |
-
1988
- 1988-05-31 JP JP13457688A patent/JP2528939B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007503976A (en) * | 2003-08-28 | 2007-03-01 | ビーピー・コーポレーション・ノース・アメリカ・インコーポレーテッド | Selective separation of fluid compounds using membrane separation process |
JP2010514543A (en) * | 2006-07-14 | 2010-05-06 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | Improved membrane separation process using gas-liquid feed |
WO2010125897A1 (en) * | 2009-05-01 | 2010-11-04 | 日本碍子株式会社 | Separation membrane for concentration of sulfuric acid, method for concentration of sulfuric acid, and apparatus for concentration of sulfuric acid |
WO2010125898A1 (en) * | 2009-05-01 | 2010-11-04 | 日本碍子株式会社 | Separation membrane for concentration of hydrochloric acid, method for concentration of hydrochloric acid, and apparatus for concentration of hydrochloric acid |
JP2011056431A (en) * | 2009-09-11 | 2011-03-24 | Hitachi Zosen Corp | Module for pervaporation membrane separation |
JP2013533100A (en) * | 2010-05-17 | 2013-08-22 | シュティヒティン・エネルギーオンデルツォイク・セントラム・ネーデルランド | Organophilic polysilsesquioxane membranes for solvent nanofiltration and pervaporation |
Also Published As
Publication number | Publication date |
---|---|
JP2528939B2 (en) | 1996-08-28 |
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