CN201280596Y - Multifunctional electro-chemical electrolytic tank for laboratory - Google Patents

Multifunctional electro-chemical electrolytic tank for laboratory Download PDF

Info

Publication number
CN201280596Y
CN201280596Y CNU2008201647555U CN200820164755U CN201280596Y CN 201280596 Y CN201280596 Y CN 201280596Y CN U2008201647555 U CNU2008201647555 U CN U2008201647555U CN 200820164755 U CN200820164755 U CN 200820164755U CN 201280596 Y CN201280596 Y CN 201280596Y
Authority
CN
China
Prior art keywords
laboratory
unit groove
exchange membrane
plate
chemical cell
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
CNU2008201647555U
Other languages
Chinese (zh)
Inventor
胡正良
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.)
HANGZHOU ZHEDA PANACO CHEMICAL ENGINEERING Co Ltd
Original Assignee
HANGZHOU ZHEDA PANACO CHEMICAL ENGINEERING 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 HANGZHOU ZHEDA PANACO CHEMICAL ENGINEERING Co Ltd filed Critical HANGZHOU ZHEDA PANACO CHEMICAL ENGINEERING Co Ltd
Priority to CNU2008201647555U priority Critical patent/CN201280596Y/en
Application granted granted Critical
Publication of CN201280596Y publication Critical patent/CN201280596Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

The utility model discloses a multifunctional electrochemical electrolytic bath used in a laboratory, which mainly consists of an anode unit cell, a cathode unit cell, an ion exchange membrane, an anode plate and a cathode plate. The ion exchange membrane is sealed between the anode unit cell and the cathode unit cell by a sheet gasket. The lab-used multifunctional electrochemical electrolytic bath has advanced electrochemical performance, high electrolytic efficiency, and is stable; liquid can be circulated well inside the electrolytic bath. In addition, instruments are compact and the fabrication process is simple; the cost is low. The electrolytic bath is easily controllable, which is in particular applicable to the laboratory.

Description

A kind of laboratory multifunction electric chemical cell
Technical field
The utility model relates to a kind of laboratory equipment that is applied to the electrochemistry industry, especially, relates to a kind of laboratory multifunction electric chemical cell.
Background technology
Current experiments chamber electrolyzer, general volume is comparatively huge, and institute takes up space bigger, moves also inconvenient.And there have its diaphragm frame of a lot of electrolyzers, the false end to be to be wooden or made of iron, and its acid resistance is poor, and intensity is low, is difficult to satisfy the retrofit requirement.Also exist the problem of electric current distribution inequality simultaneously.Therefore, develop a kind of chemical property advanced person, good stability, and instrument is small and exquisite, and manufacture craft is simple, and cost is lower, and the electrolyzer that is easy to control seems extremely important.
The utility model content
With long-pending comparatively huge, the deficiencies such as electrolytic efficiency is low, poor stability of cell body, provide a kind of laboratory multifunction electric chemical cell at existing laboratory.
The purpose of this utility model is achieved through the following technical solutions: a kind of laboratory multifunction electric chemical cell is characterized in that it mainly is made up of anode unit groove, cathode electrode unit groove, ion-exchange membrane, positive plate and negative plate; Described ion-exchange membrane is sealed between anode unit groove and the cathode electrode unit groove by gasket seal.
Further, described ion-exchange membrane is homogeneous phase cation film, heterogeneous cationic membrane, homogeneous-phase anion film or heterogeneous anionic membrane.Described anode unit groove (1) and positive plate (4) are made by the titanium plate, and cathode electrode unit groove (2) is made by stereotype, and negative plate (5) is made by stereotype, silver plate or copper coin.Described gasket seal (6) is made by Reinforced Polypropylene.
The beneficial effects of the utility model are: the utility model chemical property advanced person, and internal recycling is good, electrolytic efficiency height, good stability, and instrument is small and exquisite, and manufacture craft is simple, and cost is lower, be easy to control, simple to operate, be that the ideal of under lab carrying out electrochemistry experiment is selected.
Description of drawings
Fig. 1 is the electrolysis cells structural representation of the utility model laboratory with the multifunction electric chemical cell;
Fig. 2 is the user mode reference drawing of the utility model laboratory with the multifunction electric chemical cell.
Embodiment
Describe the utility model below with reference to the accompanying drawings in detail, it is more obvious that the purpose of this utility model and effect will become.
As depicted in figs. 1 and 2, laboratory of the present utility model mainly is made up of anode unit groove 1, cathode electrode unit groove 2, ion-exchange membrane 3, positive plate 4 and negative plate 5 with the multifunction electric chemical cell.Ion-exchange membrane 3 is sealed between anode unit groove 1 and the cathode electrode unit groove 2 by gasket seal 6.
Ion-exchange membrane 3 can be homogeneous phase cation film, heterogeneous cationic membrane, homogeneous-phase anion film and heterogeneous anionic membrane.
Anode unit groove 1 and positive plate 4 are made by the titanium plate, and cathode electrode unit groove 2 is made by stereotype.Negative plate 5 is made by stereotype, silver plate or copper coin.
Gasket seal 6 is by Reinforced Polypropylene preparation, acid-fast alkali-proof.
The utility model is in groping the electrochemical electrolysis technological process, can be conveniently with changing different electrolytic films, because cathode and anode unit groove strong alkali-acid resistance can low-costly be changed electrolyte ratio and concentration, simultaneously can conveniently change anode and cathode structure and coating, find out electrochemical process with least cost.

Claims (4)

1. a laboratory multifunction electric chemical cell is characterized in that, it mainly is made up of anode unit groove (1), cathode electrode unit groove (2), ion-exchange membrane (3), positive plate (4) and negative plate (5); Described ion-exchange membrane (3) is sealed between anode unit groove (1) and the cathode electrode unit groove (2) by gasket seal (6).
2. laboratory according to claim 1 multifunction electric chemical cell is characterized in that, described ion-exchange membrane (3) is homogeneous phase cation film, heterogeneous cationic membrane, homogeneous-phase anion film or heterogeneous anionic membrane.
3. laboratory according to claim 1 multifunction electric chemical cell is characterized in that, described anode unit groove (1) and positive plate (4) are made by the titanium plate, and cathode electrode unit groove (2) is made by stereotype, and negative plate (5) is made by stereotype, silver plate or copper coin.
4. laboratory according to claim 1 multifunction electric chemical cell is characterized in that described gasket seal (6) is made by Reinforced Polypropylene.
CNU2008201647555U 2008-09-25 2008-09-25 Multifunctional electro-chemical electrolytic tank for laboratory Expired - Fee Related CN201280596Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201647555U CN201280596Y (en) 2008-09-25 2008-09-25 Multifunctional electro-chemical electrolytic tank for laboratory

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201647555U CN201280596Y (en) 2008-09-25 2008-09-25 Multifunctional electro-chemical electrolytic tank for laboratory

Publications (1)

Publication Number Publication Date
CN201280596Y true CN201280596Y (en) 2009-07-29

Family

ID=40927476

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201647555U Expired - Fee Related CN201280596Y (en) 2008-09-25 2008-09-25 Multifunctional electro-chemical electrolytic tank for laboratory

Country Status (1)

Country Link
CN (1) CN201280596Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105755502A (en) * 2016-05-10 2016-07-13 东莞市升瑞资环保科技有限公司 Multi-variable combined multifunctional electrolytic bath
CN109868368A (en) * 2019-04-11 2019-06-11 东北大学 Extraction and recovery Cr(III in a kind of high acid solution) method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105755502A (en) * 2016-05-10 2016-07-13 东莞市升瑞资环保科技有限公司 Multi-variable combined multifunctional electrolytic bath
CN109868368A (en) * 2019-04-11 2019-06-11 东北大学 Extraction and recovery Cr(III in a kind of high acid solution) method

Similar Documents

Publication Publication Date Title
CN101634035B (en) Electrochemical method and electrochemical device for synergistically generating ozone and hydrogen peroxide in neutral medium
CN101267045B (en) A microbe fuel battery and its application
Gajda et al. Water formation at the cathode and sodium recovery using microbial fuel cells (MFCs)
Nam et al. Optimization of catholyte concentration and anolyte pHs in two chamber microbial electrolysis cells
Bae* et al. All-chromium redox flow battery for renewable energy storage
CN103603005B (en) Continuous way weakly alkaline high-concentration hydrogen-rich water electrolysis device
FR2969179B1 (en) HYDROGEN PRODUCTION CELL COMPRISING A HIGH TEMPERATURE WATER VAPOR ELECTROLYSER CELL
CN103820807A (en) Device and method for producing hydrogen and generating electricity
CA2509696A1 (en) Process for the production of hydrogen
Nagasawa et al. The effect of flow-field structure in toluene hydrogenation electrolyzer for energy carrier synthesis system
CN102206832A (en) Method for preparing electronic-grade tetramethylammonium hydroxide (TMAH)
CN105908210B (en) A kind of solid polymer electrolyte electrolytic bath
CN200958119Y (en) Cylindrical double-diaphragm and cathode electrolytic bath
CN113862690A (en) Water electrolysis hydrogen production device based on bipolar electrode system
CN102121113A (en) Electrolyte tank and three-tank combined electrolytic tank using same
CN205088310U (en) A electrolytic bath device that is used for cloudy anode chamber of partition of electrolytic preparation ozone water
CN201280596Y (en) Multifunctional electro-chemical electrolytic tank for laboratory
CN101901881A (en) The fuel cell of the shell that fuel cell is used and this shell of use
CN205069768U (en) Preparation facilities of full vanadium electrolyte of high concentration
Chen et al. Cr-methanol fuel cell for efficient Cr (VI) removal and high power production
Zerrouki et al. An investigation on polymer ion exchange membranes used as separators in low-energy microbial fuel cells
CN106929875B (en) A method of ferrate is prepared based on carbon plate plating iron
CN201793761U (en) Membrane electrolytic tank for electrolyzing gold in cyanide pregnant solution
CN205077154U (en) Electrolytic device of preparation high concentration vanadium electrolyte
CN211420329U (en) Be applied to electrolysis trough in electrochemistry laboratory

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090729

Termination date: 20091026