CN211420329U - Be applied to electrolysis trough in electrochemistry laboratory - Google Patents

Be applied to electrolysis trough in electrochemistry laboratory Download PDF

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Publication number
CN211420329U
CN211420329U CN201921734851.3U CN201921734851U CN211420329U CN 211420329 U CN211420329 U CN 211420329U CN 201921734851 U CN201921734851 U CN 201921734851U CN 211420329 U CN211420329 U CN 211420329U
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China
Prior art keywords
tank
cathode
anode
electrolytic cell
plate
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Expired - Fee Related
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CN201921734851.3U
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Chinese (zh)
Inventor
付晓伟
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Yingkou Institute of Technology
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Yingkou Institute of Technology
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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

Abstract

The utility model introduces an electrolytic cell applied to an electrochemical laboratory, which belongs to the technical field of laboratory equipment and comprises an anode tank, a cathode tank and a middle separation tank positioned between the anode tank and the cathode tank, wherein an ion exchange membrane is placed in the middle separation tank, and the middle separation tank is provided with a plurality of through holes; an anode plate is arranged in the anode tank, a cathode plate is arranged in the cathode tank, and the anode plate and the cathode plate are respectively provided with a plurality of lead connecting columns; the sealing gaskets are positioned in the middle partition groove and tightly attach and fix the ion exchange membrane; the middle partition groove is composed of a first partition plate and a second partition plate; comprises an electrolytic bath main body consisting of an anode bath, a cathode bath and a middle separation bath, and is in a cuboid shape; the number of the through holes is two, and the through holes are respectively arranged at the upper positions of the first partition plate and the second partition plate. The utility model discloses an electrolysis trough transparency is high, is convenient for observe, and heat-resisting, corrosion resistance are strong, and is small, is equipped with rotatable handle, makes things convenient for the bulk motion.

Description

Be applied to electrolysis trough in electrochemistry laboratory
Technical Field
The utility model relates to an electrolytic cell especially relates to an electrolytic cell who is applied to electrochemistry laboratory, belongs to laboratory paraphernalia technical field.
Background
The electrolytic cell consists of a cell body, an anode and a cathode, and an anode chamber and a cathode chamber are mostly separated by a diaphragm. The electrolytic bath is divided into three types, namely an aqueous solution electrolytic bath, a molten salt electrolytic bath and a non-aqueous solution electrolytic bath according to the difference of the electrolyte.
In order to prevent the mixing of the products of the cathode and anode and to avoid possible harmful reactions, the cathode and anode chambers are substantially separated by a diaphragm in the cell. The membrane should have a porosity that allows ions to pass through it, but not molecules or bubbles, and the ohmic drop of the membrane should be low when a current flows through it. These properties are required to be substantially unchanged during use and to have good chemical stability and mechanical strength under the action of the electrolytes in the cathode and anode chambers. When water is electrolyzed, the electrolytes in the cathode chamber and the anode chamber are the same, and the diaphragm of the electrolytic cell only needs to separate the cathode chamber and the anode chamber to ensure the purity of hydrogen and oxygen and prevent the explosion of mixed hydrogen and oxygen.
More often than not, the more complicated situation is that the electrolyte compositions of the cathode and anode chambers in the electrolytic cell are different. In this case, the diaphragm is also required to prevent the mutual diffusion and interaction of electrolysis products in the electrolyte in the cathode chamber and the anode chamber, such as the diaphragm in the diaphragm method electrolytic cell in chlor-alkali production, and can increase the resistance of the hydroxide ions in the cathode chamber to the diffusion and migration to the anode chamber.
The existing electrolytic cell for the electrochemical laboratory is large in size, large in occupied space and inconvenient to move. Moreover, the diaphragm frame and the false bottom of the electrolytic cell are made of wood or iron, the visibility is poor, the acid resistance is poor, and the requirements of experiments, observation and the like are difficult to meet. Therefore, it is very important to develop an electrolytic cell which has stable electrochemical performance, is convenient to observe and is easy to control.
SUMMERY OF THE UTILITY MODEL
1. Technical problem to be solved
The electrolytic cell aims at the problems that the existing electrolytic cell for the electrochemical laboratory is huge in size, large in occupied space and inconvenient to move, and a plurality of electrolytic cells are provided with diaphragm frames and false bottoms which are made of wood or iron, so that the visibility is poor, the acid resistance is poor, and the requirements of experiments, observation and the like are difficult to meet. "problem, an object of the utility model is to provide an electrolysis trough for electrochemistry laboratory, it is small, be equipped with the handle and be convenient for remove, use the quartz material that the transparency is high, observe in the convenient experiment, and quartz material is heat-resisting, acid and alkali corrosion resistant.
2. Technical scheme
In order to solve the above problems, the utility model adopts the following technical proposal.
An electrolytic cell applied to an electrochemical laboratory comprises an anode cell, a cathode cell and a middle separation cell positioned between the anode cell and the cathode cell, wherein an ion exchange membrane is placed in the middle separation cell, and the middle separation cell is provided with a plurality of through holes;
an anode plate is arranged in the anode tank, a cathode plate is arranged in the cathode tank, and the anode plate and the cathode plate are respectively provided with a plurality of lead connecting columns;
the sealing gaskets are positioned in the middle partition groove and tightly attach and fix the ion exchange membrane.
In any of the above aspects, preferably, the intermediate partition groove is formed by a first partition plate and a second partition plate; comprises an electrolytic bath main body consisting of an anode tank, a cathode tank and a middle separation tank, and is in a cuboid shape.
In any of the above schemes, preferably, there are two through holes, each of which is respectively disposed at an upper position of the first partition board and an upper position of the second partition board, and a vertical distance from the through holes on the first partition board and the second partition board to the bottom is greater than an upward distance thereof; the through hole is arranged at a certain position above, when the ion exchange membrane is not needed, for example, when the hydrogen is prepared by electrolyzing water, the liquid level of the two grooves with the anode and the cathode is positioned below the through hole, and the middle separation groove is empty.
In any of the above embodiments, preferably, the first separator and the second separator are integrally formed with the electrolytic cell main body, and are made of quartz material with certain transparency;
or the first clapboard and the second clapboard are made of transparent quartz materials and are in seamless connection with the electrolytic bath main body.
In any of the above schemes, the volume ratio of the anode tank, the middle separation tank and the cathode tank is preferably 49:2: 49;
the cell body size ranges from fifteen to sixty centimeters.
The preferred is in any above scheme that the through-hole is plugged up to the sealing plug, and the sealing plug is the plug of silica gel material, and the screw thread.
In any of the above schemes, preferably, the sealing gasket is made of reinforced polypropylene, and is tightly attached to the first separator and the second separator around the ion exchange membrane; and in the middle separation groove, under the sealing action of the sealing gasket, electrolytes on two sides of the ion exchange membrane between the two through holes are isolated.
In any of the above embodiments, it is preferable that the anode tank and the cathode tank are hinged at both sides with handles, and the handles are made of insulating material and heat insulating material and can rotate in situ.
3. Advantageous effects
Compared with the prior art, the utility model has the advantages of:
(1) the handle is arranged to facilitate movement.
(2) Visual: the quartz material with high transparency is used, so that observation in an experiment is facilitated, and instantaneous change of chemical reaction is captured in time.
(3) Heat resistance, acid and alkali corrosion resistance: the main body of the electrolytic cell is made of quartz material, has high heat resistance and corrosion resistance and is suitable for electrochemical experiments.
(4) The application is various: the main body of the electrolytic cell, which consists of the anode tank, the cathode tank and the middle separation tank, comprises three chambers for storing electrolyte, and is convenient for carrying out chemical experiments with different requirements.
(5) The stability is strong, in the middle separation groove, under the sealing action of the sealing gasket, the clamping and sealing action on the ion exchange membrane is strong, the stability of the ion exchange membrane is facilitated, and the normal progress of the experiment is facilitated.
Drawings
FIG. 1 is a schematic view of the overall structure of an electrolytic cell according to a preferred embodiment of the present invention;
FIG. 2 is a schematic view showing the operation state of an electrolytic cell according to a preferred embodiment of the present invention;
fig. 3 is a schematic structural view of a "middle spacer groove" in a preferred embodiment of the present invention.
The reference numbers in the figures illustrate:
101 anode cell, 102 cathode cell, 103 middle compartment cell, 1031 ion exchange membrane, 1032 through hole, 1033 sealing plug, 104 anode plate, 105 cathode plate, 106 first separator, 107 second separator, 108 handle.
Detailed Description
The drawings in the embodiments of the present invention will be combined; the technical scheme in the embodiment of the utility model is clearly and completely described; obviously; the described embodiments are only some of the embodiments of the present invention; but not all embodiments, are based on the embodiments of the invention; all other embodiments obtained by a person skilled in the art without making any inventive step; all belong to the protection scope of the utility model.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "top/bottom", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted", "provided", "sleeved/connected", "connected", and the like are to be understood in a broad sense, such as "connected", which may be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Example 1:
referring to fig. 1 to 3, an electrolytic cell for an electrochemical laboratory according to the present embodiment includes an anode tank 101, a cathode tank 102, and a middle separation tank 103 disposed between the anode tank 101 and the cathode tank 102, wherein an ion exchange membrane 1031 is disposed in the middle separation tank 103, and the middle separation tank 103 is provided with a plurality of through holes 1032;
an anode plate 104 is arranged in the anode tank 101, a cathode plate 105 is arranged in the cathode tank 102, and the anode plate 104 and the cathode plate 105 are respectively provided with a plurality of lead connecting columns;
the sealing gaskets are positioned in the middle partition groove 103 and tightly attach and fix the ion exchange membrane 1031.
In the present embodiment, the intermediate partition groove 103 is formed by a first partition plate 106 and a second partition plate 107; comprises an electrolytic bath main body consisting of an anode bath 101, a cathode bath 102 and an intermediate bath 103, and is in a rectangular parallelepiped shape.
In the present embodiment, two through holes 1032 are provided, and each is provided at an upper position of the first partition plate 106 and the second partition plate 107.
Example 2:
referring to fig. 1 to 3, the principle of the present embodiment is similar to that of embodiment 1 and embodiment 2, except that: an electrolytic cell applied to an electrochemical laboratory is characterized in that a first partition plate 106 and a second partition plate 107 which are made of transparent quartz materials are seamlessly connected with an electrolytic cell main body; the volume ratio of the anode groove 101 to the middle separation groove 103 to the cathode groove 102 is 49:2: 49;
the size range of the main body of the electrolytic cell is 15cm-60 cm.
In this embodiment, the through hole 1032 is blocked by the sealing plug 1033, and the sealing plug 1033 is a rubber plug made of silica gel and is threaded.
In this embodiment, the sealing gasket is made of reinforced polypropylene, and is tightly attached to the first separator 106 and the second separator 107 around the ion exchange membrane 1031; in the middle separation groove 103, under the sealing action of the sealing gasket, electrolytes on both sides of the ion exchange membrane 1031 between the two through holes 1032 are isolated.
Example 3:
referring to fig. 1 to 3, the principle of the present embodiment is similar to that of embodiment 1 and embodiment 2, except that: the electrolytic bath applied to an electrochemical laboratory is characterized in that the sides of an anode tank 101 and a cathode tank 102 are respectively hinged with a handle 108, and the handles 108 are made of insulating materials and heat insulating materials and can rotate in situ.
The above is only a preferred embodiment of the present invention; the scope of the present invention is not limited thereto. Any person skilled in the art should also be able to cover the technical scope of the present invention by replacing or changing the technical solution and the improvement concept of the present invention with equivalents and modifications within the technical scope of the present invention.

Claims (8)

1. An electrolytic cell for use in an electrochemical laboratory, comprising: the ion exchange membrane ion source comprises an anode tank (101), a cathode tank (102) and a middle separation tank (103) positioned between the anode tank (101) and the cathode tank (102), wherein an ion exchange membrane (1031) is placed in the middle separation tank (103), and the middle separation tank (103) is provided with a plurality of through holes (1032);
an anode plate (104) is arranged in the anode tank (101), a cathode plate (105) is arranged in the cathode tank (102), and the anode plate (104) and the cathode plate (105) are respectively provided with a plurality of lead connecting columns;
the sealing gaskets are positioned in the middle partition groove (103) and tightly attach and fix the ion exchange membrane (1031).
2. An electrolytic cell for use in an electrochemical laboratory according to claim 1 wherein: the intermediate partition groove (103) is composed of a first partition plate (106) and a second partition plate (107); comprises an electrolytic bath main body consisting of an anode bath (101), a cathode bath (102) and an intermediate cell (103), and is in a cuboid shape.
3. An electrolytic cell for use in an electrochemical laboratory according to claim 1 wherein: the number of the through holes (1032) is two, the through holes are respectively arranged at the upper positions of the first partition plate (106) and the second partition plate (107), and the vertical distance from the through holes (1032) on the first partition plate (106) and the second partition plate (107) to the bottom is larger than the upward distance.
4. An electrolytic cell for use in an electrochemical laboratory according to claim 2 wherein: the first separator (106) and the second separator (107) are integrally formed with the electrolytic bath main body and are made of quartz materials with certain transparency;
or a first clapboard (106) and a second clapboard (107) which are made of transparent quartz materials, and both are seamlessly connected with the electrolytic bath main body.
5. An electrolytic cell for use in an electrochemical laboratory according to claim 1 wherein: the volume ratio of the anode tank (101), the middle separation tank (103) and the cathode tank (102) is 49:2: 49; the size range of the electrolytic cell main body is 15cm-60 cm.
6. An electrolytic cell for use in an electrochemical laboratory according to claim 1 wherein: the through hole (1032) is plugged by the sealing plug (1033), and the sealing plug (1033) is a rubber plug made of silica gel and is provided with threads.
7. An electrolytic cell for use in an electrochemical laboratory according to claim 2 wherein: the sealing gasket is made of reinforced polypropylene and is tightly attached to the first partition plate (106) and the second partition plate (107) around the ion exchange membrane (1031); in the middle partition groove (103), under the sealing action of the sealing gasket, electrolyte on two sides of the ion exchange membrane (1031) between the two through holes (1032) is isolated.
8. An electrolytic cell for use in an electrochemical laboratory according to any one of claims 1 to 7 wherein: the sides of the anode tank (101) and the cathode tank (102) are respectively hinged with a handle (108), and the handle (108) is made of insulating materials and heat insulating materials and can rotate in situ.
CN201921734851.3U 2019-10-16 2019-10-16 Be applied to electrolysis trough in electrochemistry laboratory Expired - Fee Related CN211420329U (en)

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CN201921734851.3U CN211420329U (en) 2019-10-16 2019-10-16 Be applied to electrolysis trough in electrochemistry laboratory

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Application Number Priority Date Filing Date Title
CN201921734851.3U CN211420329U (en) 2019-10-16 2019-10-16 Be applied to electrolysis trough in electrochemistry laboratory

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113621985A (en) * 2021-09-16 2021-11-09 李明展 Hydrogen production system employing ferronickel catalyst and hydroxide conducting polymer through hydro-electric decomposition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113621985A (en) * 2021-09-16 2021-11-09 李明展 Hydrogen production system employing ferronickel catalyst and hydroxide conducting polymer through hydro-electric decomposition

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Granted publication date: 20200904

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