CN103691256A - Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production - Google Patents

Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production Download PDF

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Publication number
CN103691256A
CN103691256A CN201310693771.9A CN201310693771A CN103691256A CN 103691256 A CN103691256 A CN 103691256A CN 201310693771 A CN201310693771 A CN 201310693771A CN 103691256 A CN103691256 A CN 103691256A
Authority
CN
China
Prior art keywords
hydrogen chloride
carbon tetrachloride
chlorine
chlorine gas
tetrachloride liquid
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
CN201310693771.9A
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Chinese (zh)
Inventor
徐建林
邹建良
宗建青
仇峰
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.)
CHANGSHU ZHENFU NEW MATERIAL Co Ltd
Original Assignee
CHANGSHU ZHENFU NEW MATERIAL 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 CHANGSHU ZHENFU NEW MATERIAL Co Ltd filed Critical CHANGSHU ZHENFU NEW MATERIAL Co Ltd
Priority to CN201310693771.9A priority Critical patent/CN103691256A/en
Publication of CN103691256A publication Critical patent/CN103691256A/en
Pending legal-status Critical Current

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Abstract

The invention discloses a method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production. The method comprises the following steps: introducing a mixed gas of chlorine gas and hydrogen chloride into an absorption tower utilizing carbon tetrachloride liquid as an absorbent; driving the carbon tetrachloride liquid in the absorption tower to circularly flow between the top and the bottom of the absorption tower through a pump; separating the chlorine gas from the hydrogen chloride by dissolving the chlorine gas through the carbon tetrachloride liquid; discharging the separated hydrogen chloride from the absorption tower, and absorbing the hydrogen chloride through a hydrogen chloride absorber; and pumping part of carbon tetrachloride liquid with dissolved chlorine gas into a heating device for heating so as to evaporate the chlorine gas dissolved in the carbon tetrachloride liquid. The method disclosed by the invention can be used for effectively separating the chlorine gas from the hydrogen chloride in a trifluoroacetic acid production process.

Description

The separation method of chlorine and hydrogen chloride in trifluoroacetic acid production
Technical field
The present invention relates to trifluoroacetic acid produce in the separation method of chlorine and hydrogen chloride.
Background technology
The chlorine and the hydrogen chloride that in trifluoroacetic acid production process, produce need extraction and application.
Summary of the invention
The object of the present invention is to provide a kind of trifluoroacetic acid produce in the separation method of chlorine and hydrogen chloride, it can be effectively separated with hydrogen chloride to chlorine in trifluoroacetic acid production process.
For achieving the above object, technical scheme of the present invention is the separation method of chlorine and hydrogen chloride during a kind of trifluoroacetic acid of design is produced, and comprises the steps:
The mist of chlorine and hydrogen chloride is introduced and be take in the absorption tower that carbon tetrachloride liquid is absorbent;
Carbon tetrachloride liquid in absorption tower circulates between at the bottom of absorption tower tower top and tower by pump;
By carbon tetrachloride liquid, dissolve chlorine with by chlorine and HCl separation;
Isolated hydrogen chloride is discharged from absorption tower, by hydrogen chloride absorption device, absorbs;
By pump, the carbon tetrachloride liquid that has been partly dissolved chlorine is pumped into heater and heat, make to be dissolved in the chlorine evaporation in carbon tetrachloride liquid.
Advantage of the present invention and beneficial effect are: provide a kind of trifluoroacetic acid produce in the separation method of chlorine and hydrogen chloride, it can be effectively separated with hydrogen chloride to chlorine in trifluoroacetic acid production process.
The specific embodiment
Below in conjunction with embodiment, the specific embodiment of the present invention is further described.Following examples are only for technical scheme of the present invention is more clearly described, and can not limit the scope of the invention with this.
The concrete technical scheme of implementing of the present invention is:
In trifluoroacetic acid production, a separation method for chlorine and hydrogen chloride, comprises the steps:
The mist of chlorine and hydrogen chloride is introduced and be take in the absorption tower that carbon tetrachloride liquid is absorbent;
Carbon tetrachloride liquid in absorption tower circulates between at the bottom of absorption tower tower top and tower by pump;
By carbon tetrachloride liquid, dissolve chlorine with by chlorine and HCl separation;
Isolated hydrogen chloride is discharged from absorption tower, by hydrogen chloride absorption device, absorbs;
By pump, the carbon tetrachloride liquid that has been partly dissolved chlorine is pumped into heater and heat, make to be dissolved in the chlorine evaporation in carbon tetrachloride liquid.
The above is only the preferred embodiment of the present invention; it should be pointed out that for those skilled in the art, do not departing under the prerequisite of the technology of the present invention principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection scope of the present invention.

Claims (1)

1. the separation method of chlorine and hydrogen chloride in trifluoroacetic acid production, is characterized in that, comprises the steps:
The mist of chlorine and hydrogen chloride is introduced and be take in the absorption tower that carbon tetrachloride liquid is absorbent;
Carbon tetrachloride liquid in absorption tower circulates between at the bottom of absorption tower tower top and tower by pump;
By carbon tetrachloride liquid, dissolve chlorine with by chlorine and HCl separation;
Isolated hydrogen chloride is discharged from absorption tower, by hydrogen chloride absorption device, absorbs;
By pump, the carbon tetrachloride liquid that has been partly dissolved chlorine is pumped into heater and heat, make to be dissolved in the chlorine evaporation in carbon tetrachloride liquid.
CN201310693771.9A 2013-12-18 2013-12-18 Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production Pending CN103691256A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310693771.9A CN103691256A (en) 2013-12-18 2013-12-18 Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310693771.9A CN103691256A (en) 2013-12-18 2013-12-18 Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production

Publications (1)

Publication Number Publication Date
CN103691256A true CN103691256A (en) 2014-04-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310693771.9A Pending CN103691256A (en) 2013-12-18 2013-12-18 Method for separating chlorine gas from hydrogen chloride in trifluoroacetic acid production

Country Status (1)

Country Link
CN (1) CN103691256A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104311383A (en) * 2014-10-15 2015-01-28 山东东岳氟硅材料有限公司 Method for producing methane chloride through byproduct hydrogen chloride in production process of tetrachloroethylene
CN105363318A (en) * 2015-10-20 2016-03-02 安徽广信农化股份有限公司 Diuron intermediate body production tail gas processing technology
CN108726483A (en) * 2018-08-10 2018-11-02 重庆天原化工有限公司 The processing method of tail gas recycle containing chlorine

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104311383A (en) * 2014-10-15 2015-01-28 山东东岳氟硅材料有限公司 Method for producing methane chloride through byproduct hydrogen chloride in production process of tetrachloroethylene
CN104311383B (en) * 2014-10-15 2016-05-04 山东东岳氟硅材料有限公司 A kind of method of the hydrogen chloride production monochloro methane that utilizes by-product in tetrachloro-ethylene production process
CN105363318A (en) * 2015-10-20 2016-03-02 安徽广信农化股份有限公司 Diuron intermediate body production tail gas processing technology
CN108726483A (en) * 2018-08-10 2018-11-02 重庆天原化工有限公司 The processing method of tail gas recycle containing chlorine

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Application publication date: 20140402