SU472684A1 - Installation for electrochemical fluorination - Google Patents
Installation for electrochemical fluorinationInfo
- Publication number
- SU472684A1 SU472684A1 SU1932487A SU1932487A SU472684A1 SU 472684 A1 SU472684 A1 SU 472684A1 SU 1932487 A SU1932487 A SU 1932487A SU 1932487 A SU1932487 A SU 1932487A SU 472684 A1 SU472684 A1 SU 472684A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- installation
- heat exchangers
- electrolysis chamber
- electrochemical fluorination
- electrolyte
- Prior art date
Links
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
1one
Изобретение относитс к технологии процесса электрохимического получени различных фторорганических продуктов и может найти применение в электрохимических процессах, сопровождающихс большими тепло- и газовыделени ми .The invention relates to a process for the process of electrochemical production of various organofluorine products and may find application in electrochemical processes accompanied by large heat and gas emissions.
Известна установка дл электрохимического фторировани , состо ща из электролизной камеры и циркул ционных теплообменников, расположенных в одном корпусе.A device for electrochemical fluorination is known, consisting of an electrolysis chamber and circulation heat exchangers arranged in a single housing.
Иедостатками такой установки вл ютс мала поверхность газоотделени , не позвол юща интенсифицировать процесс, и отсутствие направленной циркул ции при посто нном объеме электролита.The drawbacks of such an installation are the small surface of the gas separation, which does not allow to intensify the process, and the absence of directional circulation with a constant volume of electrolyte.
С целью устранени указанных недостатков предлагаетс установка дл электрохимического фторировани веществ при электролизе расплавленных электролитов на основе безводного фтористого водорода, котора в верхней части электролизной камеры на пути потока электролита в циркул ционные теплообменники снабжеиа наклонными полками. При этом наклонные полки закреплены между верхней частью электролизной камеры и верхпей частью циркул ционных теплообменников и могут быть выполнены в виде теплообменников .In order to eliminate these drawbacks, an installation is proposed for electrochemical fluorination of substances during the electrolysis of molten electrolytes based on anhydrous hydrogen fluoride, which in the upper part of the electrolysis chamber is in the path of electrolyte flow into circulation heat exchangers supplied with inclined shelves. In this case, inclined shelves are fixed between the upper part of the electrolysis chamber and the upper part of the circulation heat exchangers and can be made in the form of heat exchangers.
Па фиг. 1 изображена установка дл электрохимического фторировани веществ с наклонными полками; на фиг. 2 - то же, с наклонными полками, закрепленными между верхней частью электролизной камеры и верхней частью циркул ционных теплообменников.Pa figs. 1 shows an apparatus for the electrochemical fluorination of substances with inclined shelves; in fig. 2 - the same, with inclined shelves fixed between the upper part of the electrolysis chamber and the upper part of the circulation heat exchangers.
Установка состоит из корпуса электролизера 1, нижней крыщки 2, циркул ционных теплообменников 3, наклонных полок 4, верхней крышки 5, пакета электродов 6, трубок дл слива электролита 7 и выхода электролизных газов 8.The installation consists of the electrolyzer housing 1, the bottom cover 2, circulation heat exchangers 3, inclined shelves 4, the top cover 5, the package of electrodes 6, tubes for draining the electrolyte 7 and the output of electrolysis gases 8.
Предложенна установка позвол ет увеличить поверхность газоотделени и интенсифицпровать процесс без увеличени объема электролита , что достигаетс за счет стекани газонаполненного электролита тонким слоем с наклонных полок по циркул ционным теплообменникам .The proposed installation allows to increase the gas separation surface and to intensify the process without increasing the electrolyte volume, which is achieved by draining the gas-filled electrolyte with a thin layer from the inclined shelves along the circulation heat exchangers.
Предмет изобретени Subject invention
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1932487A SU472684A1 (en) | 1973-06-06 | 1973-06-06 | Installation for electrochemical fluorination |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU1932487A SU472684A1 (en) | 1973-06-06 | 1973-06-06 | Installation for electrochemical fluorination |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU472684A1 true SU472684A1 (en) | 1975-06-05 |
Family
ID=20556697
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU1932487A SU472684A1 (en) | 1973-06-06 | 1973-06-06 | Installation for electrochemical fluorination |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU472684A1 (en) |
-
1973
- 1973-06-06 SU SU1932487A patent/SU472684A1/en active
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