CN206887236U - A kind of salt water electrolytic cell - Google Patents

A kind of salt water electrolytic cell Download PDF

Info

Publication number
CN206887236U
CN206887236U CN201720699805.9U CN201720699805U CN206887236U CN 206887236 U CN206887236 U CN 206887236U CN 201720699805 U CN201720699805 U CN 201720699805U CN 206887236 U CN206887236 U CN 206887236U
Authority
CN
China
Prior art keywords
anode chamber
chamber
cathode chamber
anode
cathode
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.)
Expired - Fee Related
Application number
CN201720699805.9U
Other languages
Chinese (zh)
Inventor
王波
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.)
Jiangsu Xingdi Chlor-Alkali Equipment Co Ltd
Original Assignee
Jiangsu Xingdi Chlor-Alkali Equipment 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 Jiangsu Xingdi Chlor-Alkali Equipment Co Ltd filed Critical Jiangsu Xingdi Chlor-Alkali Equipment Co Ltd
Priority to CN201720699805.9U priority Critical patent/CN206887236U/en
Application granted granted Critical
Publication of CN206887236U publication Critical patent/CN206887236U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The utility model discloses a kind of salt water electrolytic cell, including base, anode chamber and cathode chamber are installed above the base, cation-exchange membrane is installed by inlaying card between the anode chamber and cathode chamber, Hydrogen collection groove is installed on second appendix, saline solution is installed at the top of the anode chamber and cathode chamber and adds mouth, the saline solution adds above mouth and is provided with closure, circulation pipe is installed between the closure and anode chamber, the pump housing is installed on the circulation pipe, exhaust outlet is mounted at the top of the chlorine collecting tank and Hydrogen collection groove.The utility model is separated into anode chamber and cathode chamber by cation-exchange membrane, circulation pipe is installed by and the side of anode chamber, and the pump housing is installed on circulation pipe, pass through such a design, the sodium chloride not being electrolysed in anode chamber is set to make the electrolysis of saline solution more thorough easily by continued electrolysis.

Description

A kind of salt water electrolytic cell
Technical field
Electrolytic cell field is the utility model is related to, specifically a kind of salt water electrolytic cell.
Background technology
Chlor-alkali, i.e. chlorine industry, also refer to the method using saturated aqueous common salt preparing chlorine gas hydrogen caustic soda.Industrial electricity consumption is satisfied hunger Method with NaCl solution produces a series of chemical products, referred to as chlor-alkali to produce NaOH, Cl2 and H2 using them as raw material Industry.Chlorine industry is one of most basic chemical industry, its product except applied to chemical industry in itself in addition to, also extensive use In light industry, textile industry, metallurgical industry, petro chemical industry and public utilities by electrolytic aqueous solution of salt produce caustic soda, The industrial production of chlorine and hydrogen, it is one of important Essential Chemistry industry.The chlorine industry in China is mainly using two kinds of productions Technique,.
A kind of appearance of salt water electrolytic cell greatly facilitates the electrolysis of saline solution, but the salt water electrolysis of current stage There is many weak points in groove, for example, electrolysis is not thorough enough, gas collection is inconvenient.
Utility model content
The purpose of this utility model is to provide a kind of salt water electrolytic cell, not thorough enough to solve electrolysis of the prior art Bottom, the problem of gas collection inconvenience.
To achieve the above object, the utility model provides following technical scheme:A kind of salt water electrolytic cell, including base, Anode chamber and cathode chamber are installed above the base, between the anode chamber and cathode chamber by inlay card be provided with sun from Proton exchange, anode tap being installed at the side upper position of the anode chamber, the side of the cathode chamber is provided with cathode terminal, The bottom of the cathode chamber is provided with alkali lye inlet port, and the first appendix is provided with the top of the anode chamber, and described first is defeated Chlorine collecting tank is installed, the bottom of the chlorine collecting tank is provided with support frame, the top installation of the cathode chamber on tracheae There is the second appendix, Hydrogen collection groove is installed on second appendix, is provided with the top of the anode chamber and cathode chamber Saline solution adds mouth, and the saline solution adds above mouth and is provided with closure, is provided between the closure and anode chamber Circulation pipe, the pump housing is installed on the circulation pipe, exhaust outlet is mounted at the top of the chlorine collecting tank and Hydrogen collection groove.
Preferably, the chlorine collecting tank and Hydrogen collection groove are separately mounted to anode chamber and cathode chamber by support frame Top side.
Preferably, the base is hollow-core construction, and base is connected with alkali lye inlet port.
Preferably, the circulation pipe adds mouth through saline solution and connected with anode chamber and cathode chamber.
Compared with prior art, the beneficial effects of the utility model are:The utility model by cation-exchange membrane by its Anode chamber and cathode chamber are separated into, circulation pipe is installed by and the side of anode chamber, and the pump housing is installed on circulation pipe, is led to Such a design is crossed, makes the sodium chloride not being electrolysed in anode chamber make the electrolysis of saline solution more thorough easily by continued electrolysis, And chlorine collecting tank and Hydrogen collection groove are separately installed with the top of the top of anode chamber and cathode chamber, significantly facilitated by it Gas collection.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the top view of cation-exchange membrane of the present utility model.
In figure:1- chlorine collecting tank, the appendixs of 2- first, 3- support frames, 4- anode taps, the 5- pump housings, 6- circulation pipes, 7- are close Capping, 8- saline solutions add mouth, the appendixs of 9- second, 10- Hydrogen collections groove, 11- exhaust outlets, 12- cathode terminals, 13- anode chambers, 14- cation-exchange membranes, 15- inlay card, 16- bases, 17- alkali lye inlet port, 18- cathode chambers.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out Clearly and completely describing, it is clear that described embodiment is only the utility model part of the embodiment, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belong to the scope of the utility model protection.
Refer to Fig. 1~2, in the utility model embodiment, a kind of salt water electrolytic cell, including base 16, base 16 Top is provided with anode chamber 13 and cathode chamber 18, and base 16 is used for collecting sodium hydroxide mixed solution, and is concentrated solidification, sun Pole room 13 and cathode chamber 18 are respectively intended to manufacture chlorine and hydrogen, are installed between anode chamber 13 and cathode chamber 18 by inlaying card 15 There is cation-exchange membrane 14, cation-exchange membrane 14 allows the amberplex that hydrogen ion and sodium ion pass through, anode chamber 13 Anode tap 4 is installed, anode tap 4 and cathode terminal 12 are the same as connecting electric current, the side peace of cathode chamber 18 at the upper position of side Equipped with cathode terminal 12, the bottom of cathode chamber 18 is provided with alkali lye inlet port 17, and the top of anode chamber 13 is provided with the first appendix 2, the first appendix 2 is used for conveying chlorine, and chlorine collecting tank 1 is provided with the first appendix 2, and chlorine collecting tank 1 is used for collecting Chlorine, the bottom of chlorine collecting tank 1 are provided with support frame 3, and the top of cathode chamber 18 is provided with the second appendix 9, the second gas transmission Pipe 9 is used for conveying hydrogen, and Hydrogen collection groove 10 is provided with the second appendix 9, and Hydrogen collection groove 10 is used for collecting hydrogen, anode Room 13 and the top of cathode chamber 18 are provided with saline solution and add mouth 8, and saline solution adds mouth 8 and is used for anode chamber 13 and cathode chamber 18 Saline solution is added, the top that saline solution adds mouth 8 is provided with closure 7, circulation pipe is provided between closure 7 and anode chamber 13 6, circulation pipe 6 is used for reassigning to the sodium chloride solution after dilution in anode chamber 13 and cathode chamber 18, is electrolysed again, The pump housing 5 is installed, the top of chlorine collecting tank 1 and Hydrogen collection groove 10 is mounted on exhaust outlet 11, and chlorine is collected on circulation pipe 6 Groove 1 and Hydrogen collection groove 10 are separately mounted to the side on anode chamber 13 and the top of cathode chamber 18, base 16 by support frame 3 For hollow-core construction, and base 16 is connected with alkali lye inlet port 17, and circulation pipe 6 adds mouth 8 and anode chamber 13 and the moon through saline solution Pole room 18 connects.
Operation principle of the present utility model is:The equipment adds mouth 8 to anode chamber 13 and the moon when in use, by saline solution Common salt aqueous solution is added in pole room 18, is then powered by anode tap 4 and cathode terminal 12, makes common salt aqueous solution electric Solution, electrolytic process, can produce substantial amounts of chlorion and hydrogen ion, and chlorion is gathered in anode chamber 13, and generation chlorine passes through the One appendix 2 enters in chlorine collecting tank 1, and hydrogen ion is gathered in cathode chamber 18, and generation hydrogen is entered by the second appendix 9 Collected in Hydrogen collection groove 10, sodium ion is gathered in cathode chamber 18 by cation-exchange membrane 14, and sodium ion is with water power from production Raw hydroxyl ion reaction generation sodium hydroxide, sodium hydroxide solution enter water inlet concentration in base 16 by alkali lye inlet port 17 Reaction, makes its processing that is cured, by the pump housing 5 that the dilute sodium chloride solution in anode chamber 13 is close in the effect suction of circulation pipe 6 In capping 7, then it is conveyed and returns in anode chamber 13.
It is obvious to a person skilled in the art that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and And in the case of without departing substantially from spirit or essential attributes of the present utility model, it can realize that this practicality is new in other specific forms Type.Therefore, no matter from the point of view of which point, embodiment all should be regarded as exemplary, and is nonrestrictive, this practicality is new The scope of type limits by appended claims rather than described above, it is intended that the equivalency fallen in claim is contained All changes in justice and scope are included in the utility model.Any reference in claim should not be considered as limitation Involved claim.

Claims (4)

1. a kind of salt water electrolytic cell, including base (16), it is characterised in that:Anode chamber is installed above the base (16) (13) cation exchange and cathode chamber (18), is installed by inlaying card (15) between the anode chamber (13) and cathode chamber (18) Film (14), anode tap (4), the side installation of the cathode chamber (18) are installed at the side upper position of the anode chamber (13) There is cathode terminal (12), the bottom of the cathode chamber (18) is provided with alkali lye inlet port (17), the top peace of the anode chamber (13) Equipped with the first appendix (2), chlorine collecting tank (1) is installed on first appendix (2), the chlorine collecting tank (1) Bottom is provided with support frame (3), and the second appendix (9), second appendix (9) are provided with the top of the cathode chamber (18) On Hydrogen collection groove (10) is installed, be provided with the top of the anode chamber (13) and cathode chamber (18) saline solution add mouth (8), The saline solution adds above mouth (8) and is provided with closure (7), is provided between the closure (7) and anode chamber (13) Circulation pipe (6), the top of the pump housing (5), the chlorine collecting tank (1) and Hydrogen collection groove (10) is installed on the circulation pipe (6) Portion is mounted on exhaust outlet (11).
A kind of 2. salt water electrolytic cell according to claim 1, it is characterised in that:The chlorine collecting tank (1) and hydrogen Collecting tank (10) is separately mounted to the side on anode chamber (13) and the top of cathode chamber (18) by support frame (3).
A kind of 3. salt water electrolytic cell according to claim 1, it is characterised in that:The base (16) is hollow-core construction, And base (16) is connected with alkali lye inlet port (17).
A kind of 4. salt water electrolytic cell according to claim 1, it is characterised in that:The circulation pipe (6) passes through saline solution Mouth (8) is added to connect with anode chamber (13) and cathode chamber (18).
CN201720699805.9U 2017-06-16 2017-06-16 A kind of salt water electrolytic cell Expired - Fee Related CN206887236U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720699805.9U CN206887236U (en) 2017-06-16 2017-06-16 A kind of salt water electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720699805.9U CN206887236U (en) 2017-06-16 2017-06-16 A kind of salt water electrolytic cell

Publications (1)

Publication Number Publication Date
CN206887236U true CN206887236U (en) 2018-01-16

Family

ID=61318767

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720699805.9U Expired - Fee Related CN206887236U (en) 2017-06-16 2017-06-16 A kind of salt water electrolytic cell

Country Status (1)

Country Link
CN (1) CN206887236U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113293398A (en) * 2021-07-27 2021-08-24 东营市赫邦化工有限公司 Clean efficient ionic membrane caustic soda apparatus for producing
CN116024590A (en) * 2023-02-01 2023-04-28 山东和创智云环保装备有限公司 High-concentration sodium hypochlorite generator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113293398A (en) * 2021-07-27 2021-08-24 东营市赫邦化工有限公司 Clean efficient ionic membrane caustic soda apparatus for producing
CN116024590A (en) * 2023-02-01 2023-04-28 山东和创智云环保装备有限公司 High-concentration sodium hypochlorite generator
CN116024590B (en) * 2023-02-01 2023-05-30 山东和创智云环保装备有限公司 High-concentration sodium hypochlorite generator

Similar Documents

Publication Publication Date Title
US7955490B2 (en) Process for preparing sodium hydroxide, chlorine and hydrogen from aqueous salt solution using solar energy
CN106492639B (en) To adsorb the method for mentioning the obtained eluent of lithium and preparing lithium chloride concentrate as raw material
CN206887236U (en) A kind of salt water electrolytic cell
CN106222690A (en) A kind of three film four Room aqueous solution plate and frame electrolysis bath and application thereof
CN102134725B (en) Experimental ion-exchange membrane electrolyzer for chlor-alkali production
CN102304723A (en) Three-membrane four-chamber chlorine-free alkali-producing electrolytic tank consisting of anion and cation exchange membranes and bipolar membrane
CN109267087B (en) Multipole type ionic membrane electrolytic tank
CN1369576A (en) Reverse electrolyzer with dual membranes and three chambers
CN113481521B (en) Continuous chlor-alkali industrial electrolysis alkali preparation device and method
CN202297801U (en) Three-membrane four-chamber electrolytic cell with high ion conductivity
CN102605383B (en) Method and device for hydrogen-circulating electrolysis and application of the method and device in production of aluminum oxide
CN205347592U (en) Processing apparatus is decomposed with light salt aquatic chlorate to electrolysis
CN104630818B (en) The method that the film continuous electrolysis of three Room two prepares high-purity benzyltrimethylammonium hydroxide
Venkatesh et al. Chlor-alkali technology
CN201999996U (en) Experimental chlor-alkali ionic membrane electrolytic cell
CN109082680A (en) A kind of preparation method of bipyridines ionic liquid
CN212895007U (en) Synthesis system for preparing hydrogen, chlorine, caustic soda and hydrochloric acid by utilizing wind power electric energy
CN205258621U (en) Novel high -efficient hypochlorite generator
CN208562548U (en) A kind of efficient chlor-alkali equipment
CN209307495U (en) A kind of environmental protection and energy saving perchlorate electrolyzer
CN104073837B (en) Method for reducing anions in quaternary ammonium base by virtue of continuous electrolysis
CN202865351U (en) Conductive unit of oxygen cathode electrobath
CN205974688U (en) BiTAC type ion membrane electrolytic cell feed liquor pipe
CN206580886U (en) A kind of intelligent acid copper-containing etching waste solution indirect regeneration
CN202730250U (en) Oxygen passageway of oxygen cathode electrolytic tank and oxygen cathode electrolytic tank

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180116

Termination date: 20210616

CF01 Termination of patent right due to non-payment of annual fee