JPS5497597A - Purification of hydrochloric acid gas - Google Patents

Purification of hydrochloric acid gas

Info

Publication number
JPS5497597A
JPS5497597A JP484178A JP484178A JPS5497597A JP S5497597 A JPS5497597 A JP S5497597A JP 484178 A JP484178 A JP 484178A JP 484178 A JP484178 A JP 484178A JP S5497597 A JPS5497597 A JP S5497597A
Authority
JP
Japan
Prior art keywords
gas
tower
water
hcl
hcl gas
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
Application number
JP484178A
Other languages
Japanese (ja)
Other versions
JPS5611643B2 (en
Inventor
Michio Nishimura
Ryosaku Takigawa
Fujio Omori
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP484178A priority Critical patent/JPS5497597A/en
Publication of JPS5497597A publication Critical patent/JPS5497597A/en
Publication of JPS5611643B2 publication Critical patent/JPS5611643B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE: To purify HCl gas by the procedure in which HCl gas containing inpurities, small amounts of water, and O2 gas are introduced into a reaction zone to manufacture HCl gas by the reaction of H2 gas and Cl2 in order to prevent the pollution of burner and also the admixture of the decomposition products of impurities into purified hydrochloric acid.
CONSTITUTION: The H2 gas 6 and the chlorine gas 7 are sent into a reaction zone in the neighborhood of the burner 1 in the purification system in which the burner 1-mounted combustion tower 2, the cooler 3, the adsorption tower 4, and the recovery tower 5 are by turns connected, and also the purified HCl gas 8, the water 12, and the O2 gas 13 are added to the chlorine gas 7. And, organic compound, e.g., acetic acid, etc., contained in the gas 8 is completely converted into CO2 gas, H2 and HCl gas by heating by means of hydrogen-chlorine flame in the presence of water vapor and O2 gas in the reaction zone. And, the reaction product formed in the tower 2 and the main component HCl gas of crude HCl gas not taking part in reaction are cooled and then absorbed in water to revover as aqueous solution. The amount of water used in the tower 2 is more than 10 times as much as the organic compound in mole, and also O2 is more than 0.3 mole % of Cl2 raw gas.
COPYRIGHT: (C)1979,JPO&Japio
JP484178A 1978-01-20 1978-01-20 Purification of hydrochloric acid gas Granted JPS5497597A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP484178A JPS5497597A (en) 1978-01-20 1978-01-20 Purification of hydrochloric acid gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP484178A JPS5497597A (en) 1978-01-20 1978-01-20 Purification of hydrochloric acid gas

Publications (2)

Publication Number Publication Date
JPS5497597A true JPS5497597A (en) 1979-08-01
JPS5611643B2 JPS5611643B2 (en) 1981-03-16

Family

ID=11594901

Family Applications (1)

Application Number Title Priority Date Filing Date
JP484178A Granted JPS5497597A (en) 1978-01-20 1978-01-20 Purification of hydrochloric acid gas

Country Status (1)

Country Link
JP (1) JPS5497597A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102161474A (en) * 2010-09-08 2011-08-24 泸州北方化学工业有限公司 Method for refining hydrogen chloride gas
CN109231168A (en) * 2018-09-27 2019-01-18 河北东华舰化工有限公司 A kind of production of chloroacetic acid reduce hydrochloric acid, in acetic acid by-product sulfuric acid content method and apparatus
CN114436215A (en) * 2021-12-29 2022-05-06 安徽华塑股份有限公司 Dehydrogenation process of hydrogen chloride synthesis gas

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102161474A (en) * 2010-09-08 2011-08-24 泸州北方化学工业有限公司 Method for refining hydrogen chloride gas
CN109231168A (en) * 2018-09-27 2019-01-18 河北东华舰化工有限公司 A kind of production of chloroacetic acid reduce hydrochloric acid, in acetic acid by-product sulfuric acid content method and apparatus
CN109231168B (en) * 2018-09-27 2020-03-24 河北东华舰化工有限公司 Method and device for reducing sulfuric acid content in hydrochloric acid and acetic acid by-products in chloroacetic acid production
CN114436215A (en) * 2021-12-29 2022-05-06 安徽华塑股份有限公司 Dehydrogenation process of hydrogen chloride synthesis gas
CN114436215B (en) * 2021-12-29 2023-12-29 安徽华塑股份有限公司 Dehydrogenation process of hydrogen chloride synthesis gas

Also Published As

Publication number Publication date
JPS5611643B2 (en) 1981-03-16

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