JPS5532784A - Production of liquefied carbon dioxide - Google Patents
Production of liquefied carbon dioxideInfo
- Publication number
- JPS5532784A JPS5532784A JP10707778A JP10707778A JPS5532784A JP S5532784 A JPS5532784 A JP S5532784A JP 10707778 A JP10707778 A JP 10707778A JP 10707778 A JP10707778 A JP 10707778A JP S5532784 A JPS5532784 A JP S5532784A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- tower
- methanol
- cooler
- press
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Carbon And Carbon Compounds (AREA)
Abstract
PURPOSE: To cheaply produce liquefied carbon dioxide by allowing CO2 gas to be absorbed in a low temp. hydrophilic org. solvent under a press. below the triple point while solidifying part of the gas if necessary and by fractionally distilling this liquid in a press. fractionating tower of above the triple point.
CONSTITUTION: Feed CO2 gas is introduced into packed tower 2 provided with LNG cooler 1, and the gas is countercurrently contacted to a cooled hydrophilic org. solvent such as methanol. The CO2-absorbed methanol is pressurized to above the triple point, e.g. 6 kg/cm2G with pump 3, preheated with heat exchanger 4, and fed to the medium stage of press. fractionating tower 5. CO2 gas leaving tower 5 is cooled with LNG or the like in condenser 7 and liquefied. Impure gas in the feed CO2 gas dissolved in the methanol is separated in reflux cooler 8 and exhausted from the system. The bottom residue in tower 5 is returned to absorption tower 2 through exchanger 4 and cooler 13, yet part of it is passed through rectifying tower 11 to remove water, and methanol is fed to cooler 13.
COPYRIGHT: (C)1980,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10707778A JPS5532784A (en) | 1978-08-31 | 1978-08-31 | Production of liquefied carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10707778A JPS5532784A (en) | 1978-08-31 | 1978-08-31 | Production of liquefied carbon dioxide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5532784A true JPS5532784A (en) | 1980-03-07 |
JPS6138124B2 JPS6138124B2 (en) | 1986-08-27 |
Family
ID=14449889
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10707778A Granted JPS5532784A (en) | 1978-08-31 | 1978-08-31 | Production of liquefied carbon dioxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5532784A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3802682A1 (en) * | 1987-01-30 | 1988-08-11 | Pentel Kk | LIQUID DISPENSER |
US4960340A (en) * | 1987-01-23 | 1990-10-02 | Kabushiki Kaisha Sakurakurepasu | Implement for applying liquid |
US4966483A (en) * | 1987-11-12 | 1990-10-30 | Ancos Co., Ltd. | Valve operating mechanism |
JP2013515232A (en) * | 2009-12-22 | 2013-05-02 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | Method and apparatus for drying and compressing a CO2 rich flow |
CN113959178A (en) * | 2021-11-29 | 2022-01-21 | 李欣锐 | Carbon capture method in hydrogen production process by LNG |
-
1978
- 1978-08-31 JP JP10707778A patent/JPS5532784A/en active Granted
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4960340A (en) * | 1987-01-23 | 1990-10-02 | Kabushiki Kaisha Sakurakurepasu | Implement for applying liquid |
DE3802682A1 (en) * | 1987-01-30 | 1988-08-11 | Pentel Kk | LIQUID DISPENSER |
US4867593A (en) * | 1987-01-30 | 1989-09-19 | Pentel Kabushiki Kaisha | Liquid dispenser with valve mechanism and flexible container |
US4966483A (en) * | 1987-11-12 | 1990-10-30 | Ancos Co., Ltd. | Valve operating mechanism |
JP2013515232A (en) * | 2009-12-22 | 2013-05-02 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | Method and apparatus for drying and compressing a CO2 rich flow |
CN113959178A (en) * | 2021-11-29 | 2022-01-21 | 李欣锐 | Carbon capture method in hydrogen production process by LNG |
CN113959178B (en) * | 2021-11-29 | 2023-01-20 | 李欣锐 | Carbon capture method in hydrogen production process by LNG |
Also Published As
Publication number | Publication date |
---|---|
JPS6138124B2 (en) | 1986-08-27 |
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