CN212476908U - Novel nx-BiTAC electrolysis trough test device - Google Patents
Novel nx-BiTAC electrolysis trough test device Download PDFInfo
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- CN212476908U CN212476908U CN202020721397.4U CN202020721397U CN212476908U CN 212476908 U CN212476908 U CN 212476908U CN 202020721397 U CN202020721397 U CN 202020721397U CN 212476908 U CN212476908 U CN 212476908U
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Abstract
The utility model discloses a novel nx-BiTAC electrolytic cell testing device, which belongs to the technical field of electrolytic cell testing devices and comprises an electrolytic cell, wherein an anode tank and a cathode tank are arranged in the electrolytic cell, a pipeline at the outer wall of the electrolytic cell at one side of the anode tank is communicated with a water outlet end of an electric ball valve A, a pipeline at the water inlet end of the electric ball valve A is communicated with an anode liquid storage tank, shell cavities are arranged in the shells of the anode liquid storage tank and the cathode liquid storage tank, then an S-shaped joint plate is jointed on the inner wall of the shell cavity for reinforcing and supporting, a C-shaped support plate at the groove of the S-shaped joint plate is protruded to push against the inner wall of the shell cavity, when the anode liquid storage tank and the cathode liquid storage tank are impacted under high pressure, the S-shaped joint plate and the C-shaped support plate are arranged in the shells for reinforcing and supporting, thereby preventing the tank from being broken, and the S, easy to move and solves the problem that the shell of the liquid storage tank matched with the prior nx-BiTAC electrolytic tank has simple structure.
Description
Technical Field
The utility model relates to an electrolysis trough testing arrangement technical field especially relates to a novel nx-BiTAC electrolysis trough testing arrangement.
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. When direct current passes through the electrolytic cell, an oxidation reaction occurs at the interface of the anode and the solution, and a reduction reaction occurs at the interface of the cathode and the solution, so as to prepare the required product. The optimized design of the electrolytic cell structure and the reasonable selection of the electrode and diaphragm materials are the keys of improving the current efficiency, reducing the cell voltage and saving the energy consumption.
1. When an existing nx-BiTAC electrolytic cell is processed, the power consumption for analyzing and using the cell body is large, the corrosion resistance is low, the damage is high, the service life is short, and therefore a novel nx-BiTAC electrolytic cell testing device is provided.
2. The two sides of the conventional nx-BiTAC electrolytic tank are provided with a cathode and anode liquid storage tank for liquid distribution, the tank body of the conventional cathode and anode liquid storage tank is simple in structure, and the tank body is easy to break when being collided by high pressure to cause liquid in the tank body to leak, so that a novel nx-BiTAC electrolytic tank testing device is provided.
SUMMERY OF THE UTILITY MODEL
The utility model provides a novel nx-BiTAC electrolysis trough testing arrangement, coating negative pole coating and anode coating in the negative pole groove and the anode tank of electrolysis trough, the positive pole liquid storage pot in the chlorion secondary refine the anode tank contact anode coating that gets into the electrolysis trough through electronic ball valve A, the circulating alkali of negative pole liquid storage pot gets into the negative pole groove contact cathode coating of electrolysis trough through electronic ball valve B this moment, under the direct current effect, the chlorion is by oxidation production chlorine overflow to waste chlorine house steward in the positive pole inslot, the hydrogen that produces behind sodion and water see through the negative pole groove that the ionic membrane got into the electrolysis trough spills over to the hydrogen water seal after empting, remove waste alkali groove behind alkali lye entering waste alkali house steward, further reduced hydrogen and chlorine evolution electric potential with the help of anode coating and cathode coating, make unit cell voltage further descend. And the current density can reach 6 KA/square meter, the problem that the conventional electrolytic tank of the nx-BiTAC is large in power consumption and short in service life is solved, shell cavities are formed in the shells of the anode liquid storage tank and the cathode liquid storage tank, then the inner walls of the shell cavities are attached to the S-shaped attaching plate for reinforcing and supporting, meanwhile, the C-shaped support plate at the groove of the S-shaped attaching plate protrudes and props against the inner walls of the shell cavities, when the anode liquid storage tank and the cathode liquid storage tank are impacted by high pressure, the S-shaped attaching plate and the C-shaped support plate are arranged in the shells for reinforcing and supporting, the tank body is prevented from being broken under pressure, meanwhile, the S-shaped attaching plate and the C-shaped support plate are gap reinforcing plates in the shell cavities, the weight of the shell is lighter and easy to move relative.
The utility model provides a specific technical scheme as follows:
the utility model provides a pair of novel nx-BiTAC electrolysis trough testing arrangement, including the electrolysis trough, the inside of electrolysis trough is provided with anode tank and negative pole groove, and the electrolysis trough outer wall department pipeline intercommunication of anode tank one side has electric ball valve A's play water end, electric ball valve A's income water end pipeline intercommunication has the positive pole liquid storage pot, the electrolysis trough outer wall department pipeline intercommunication of negative pole groove one side has electric ball valve B's output, and electric ball valve B's input pipeline intercommunication has the negative pole liquid storage pot, electric ball valve A and electric ball valve B's power end electric connection external power source, the inner wall department of anode tank and negative pole groove has coated positive pole coating and cathode coating respectively, and the electrolysis trough inner wall department between anode tank and the negative pole groove installs the ionic membrane.
Optionally, the inner walls of the shells of the anode liquid storage tank and the cathode liquid storage tank are provided with shell cavities, the shells are internally laminated with S-shaped laminating plates, the sunken parts of the S-shaped laminating plates are protruded with C-shaped supporting plates, and the tops of the C-shaped supporting plates are laminated on the inner walls of the shell cavities.
Optionally, the bottom end of the electrolytic cell is fixedly connected with a base.
Optionally, the bottom ends of the cathode liquid storage tank and the anode liquid storage tank are welded with support legs.
The utility model has the advantages as follows:
1. the utility model discloses coating negative pole coating and positive pole coating in the cathode trough and the positive pole groove of electrolysis trough, the positive pole groove contact positive pole coating that gets into the electrolysis trough through electric ball valve A is refined to the chlorion secondary in the positive pole liquid storage pot, the circulation alkali of negative pole liquid storage pot gets into the negative pole groove contact negative pole coating of electrolysis trough through electric ball valve B this moment, under the direct current effect, chlorine ion is by oxidation production chlorine overflow to waste chlorine house steward in the positive pole inslot, the hydrogen that produces behind sodium ion and the water seeing through the negative pole groove that the ionic membrane got into the electrolysis trough spills over to the hydrogen water seal after and empties, alkali lye gets into and removes waste alkali groove behind the waste alkali house steward, further reduced hydrogen evolution and chlorine evolution electric potential with the help of positive pole coating and negative pole coating, make unit cell voltage. And the current density can reach 6 KA/square meter, thus solving the problem of large power consumption and low service life of the conventional nx-BiTAC electrolytic cell.
2. The utility model discloses a set up the shell chamber in the casing of positive pole liquid storage pot and negative pole liquid storage pot, then shell intracavity wall laminating S-shaped attaching plate carries out the reinforcement and supports, the C shape extension board protrusion of S-shaped attaching plate groove is pushing up shell intracavity wall simultaneously, when positive pole liquid storage pot and negative pole liquid storage pot suffer high-pressure impact, it supports with the reinforcement of C shape extension board to have S-shaped attaching plate in its casing, prevent that jar body pressurized from breaking, S-shaped attaching plate and C shape extension board are clearance reinforcement panel in the shell intracavity simultaneously, light for solid casing weight, easy to move, the supporting liquid storage pot shell simple structure' S of the electrolysis trough of current nx-BiTAC problem has been solved.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings without creative efforts.
FIG. 1 is a schematic view of the overall structure of a novel nx-BiTAC electrolytic cell testing device in an embodiment of the present invention.
FIG. 2 is a schematic view of a liquid storage tank shell structure of the novel nx-BiTAC electrolytic tank testing device of the embodiment of the utility model.
In the figure: 1. an electrolytic cell; 2. an anode tank; 3. a cathode channel; 4. an electric ball valve A; 5. an anode liquid storage tank; 6. an electric ball valve B; 7. a cathode liquid storage tank; 8. an anodic coating; 9. a cathode coating; 10. an ionic membrane; 11. a shell cavity; 12. an S-shaped attaching plate; 13. a C-shaped support plate; 14. a base; 15. and (3) a support leg.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention clearer, the present invention will be described in further detail with reference to the accompanying drawings, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
A detailed description will be given below of a novel nx-BiTAC electrolytic cell testing device according to an embodiment of the present invention with reference to FIGS. 1 to 2.
Referring to fig. 1, the embodiment of the utility model provides a novel nx-BiTAC electrolytic cell testing device, which comprises an electrolytic cell 1, an anode tank 2 and a cathode tank 3 are arranged inside the electrolytic cell 1, and the pipeline at the outer wall of the electrolytic tank 1 at one side of the anode tank 2 is communicated with the water outlet end of the electric ball valve A4, the pipeline at the water inlet end of the electric ball valve A4 is communicated with an anode liquid storage tank 5, the pipeline at the outer wall of the electrolytic bath 1 at one side of the cathode bath 3 is communicated with the output end of the electric ball valve B6, and the input end pipeline of the electric ball valve B6 is communicated with a cathode liquid storage tank 7, the power ends of the electric ball valve A4 and the electric ball valve B6 are electrically connected with an external power supply, the inner walls of the anode tank 2 and the cathode tank 3 are respectively coated with an anode coating 8 and a cathode coating 9, and the inner wall of the electrolytic tank 1 between the anode tank 2 and the cathode tank 3 is provided with an ionic membrane 10.
Illustratively, a cathode coating 9 and an anode coating 8 are coated in a cathode tank 3 and an anode tank 2 of an electrolytic tank 1, chloride ions in an anode liquid storage tank 5 are refined for the second time and enter the anode tank 2 of the electrolytic tank 1 through an electric ball valve A4 to contact with the anode coating 8, circulating alkali of a cathode liquid storage tank 7 enters the cathode tank 3 of the electrolytic tank 1 through an electric ball valve B6 to contact with the cathode coating 9, under the action of direct current, the chloride ions in the anode tank 2 are oxidized to generate chlorine gas and overflow to a waste chlorine gas header pipe, sodium ions and water penetrate through an ion membrane 10 and enter the cathode tank 3 of the electrolytic tank 1 to generate hydrogen gas, the hydrogen gas overflows to a hydrogen water seal and is discharged, alkali liquor enters the waste alkali header pipe and then enters the waste alkali tank, and the hydrogen evolution potential and the chlorine evolution potential are further reduced by means of the anode coating 8 and the cathode coating 9, so that. And the current density can reach 6 KA/square meter.
Referring to fig. 1-2, the inner walls of the shells of the anode liquid storage tank 5 and the cathode liquid storage tank 7 are provided with a shell cavity 11, an S-shaped attachment plate 12 is attached inside the shell cavity 11, a C-shaped support plate 13 protrudes from a concave part of the S-shaped attachment plate 12, and the top end of the C-shaped support plate 13 is attached to the inner wall of the shell cavity 11.
Illustratively, a shell cavity 11 is formed in the shells of the anode liquid storage tank 5 and the cathode liquid storage tank 7, then an S-shaped attachment plate 12 is attached to the inner wall of the shell cavity 11 for reinforcement and support, meanwhile, a C-shaped support plate 13 at the groove of the S-shaped attachment plate 12 is protruded to push against the inner wall of the shell cavity 11, when the anode liquid storage tank 5 and the cathode liquid storage tank 7 are impacted by high pressure, the shells of the shells are provided with the S-shaped attachment plate 12 and the C-shaped support plate 13 for reinforcement and support, so that the tank body is prevented from being broken by pressure, and meanwhile, the S-shaped attachment plate 12 and the C-shaped support plate 13 are gap reinforcement plates in the shell.
Referring to fig. 1, a base 14 is fixedly connected to the bottom end of the electrolytic cell 1.
Illustratively, the bottom of the electrolytic cell 1 has a base 14 for supporting it in contact with the ground.
Referring to fig. 2, the bottom ends of the cathode reservoir 7 and the anode reservoir 5 are welded with support legs 15.
Illustratively, the bottom ends of the cathode reservoir 7 and the anode reservoir 5 are supported in contact with the ground by support legs 15.
The utility model relates to a novel nx-BiTAC electrolytic cell testing device, a cathode coating 9 and an anode coating 8 are coated in a cathode slot 3 and an anode slot 2 of an electrolytic cell 1, chloride ions in an anode liquid storage tank 5 are refined for the second time and enter the anode slot 2 of the electrolytic cell 1 through an electric ball valve A4 to contact the anode coating 8, at the moment, circulating alkali of the cathode liquid storage tank 7 enters the cathode slot 3 of the electrolytic cell 1 through an electric ball valve B6 to contact the cathode coating 9, under the action of direct current, chlorine gas generated by oxidizing chloride ions in the anode tank 2 overflows to a waste chlorine gas main pipe, hydrogen generated by sodium ions and water after penetrating through the ion membrane 10 and entering the cathode tank 3 of the electrolytic tank 1 overflows to a hydrogen water seal and is discharged, alkali liquor enters the waste alkali main pipe and then enters the waste alkali tank, and the hydrogen evolution potential and the chlorine evolution potential are further reduced by means of the anode coating 8 and the cathode coating 9, so that the voltage of the unit tank is further reduced. And the current density can reach 6 KA/square meter, shell cavities 11 are arranged in the shell bodies of the anode liquid storage tank 5 and the cathode liquid storage tank 7, then the inner wall of each shell cavity 11 is attached with the S-shaped attaching plate 12 for reinforcing and supporting, meanwhile, the C-shaped support plate 13 at the groove of the S-shaped attaching plate 12 is protruded to push against the inner wall of each shell cavity 11, when the anode liquid storage tank 5 and the cathode liquid storage tank 7 are impacted by high pressure, the S-shaped attaching plate 12 and the C-shaped support plate 13 in the shell bodies are used for reinforcing and supporting, the tank bodies are prevented from being broken under pressure, and meanwhile, the S-shaped attaching plate 12 and the C-shaped support plate 13 are gap reinforcing plates in the shell.
It should be noted that, the utility model relates to a novel nx-BiTAC electrolysis trough testing arrangement, including electrolysis trough 1, anode tank 2, negative pole groove 3, electronic ball valve A4, positive pole liquid storage tank 5, electronic ball valve B6, negative pole liquid storage tank 7, anode coating 8, negative pole coating 9, ionic membrane 10, shell chamber 11, S-shaped rigging board 12, C shape extension board 13, base 14, stabilizer blade 15, the part is the part that general standard component or technical personnel in the field know, and its structure and principle all are that this technical personnel all can learn through the technical manual or learn through conventional experimental method.
Above electronic ball valve A4 and electronic ball valve B6 that use can select for use the electronic ball valve of Q941F46 model, can also select electronic ball valve by oneself according to user's demand, and above-mentioned electronic ball valve is the current product on the market, and its theory of operation and inner structure are known to the technical personnel of the technical field that belongs to, the utility model discloses just utilized above-mentioned main part function and did not improve its inner structure, consequently, no longer detailed description here.
It is apparent that those skilled in the art can make various changes and modifications to the embodiments of the present invention without departing from the spirit and scope of the embodiments of the present invention. Thus, if such modifications and variations of the embodiments of the present invention fall within the scope of the claims and their equivalents, the present invention is also intended to include such modifications and variations.
Claims (4)
1. A novel nx-BiTAC electrolysis trough testing arrangement, includes electrolysis trough (1), its characterized in that: an anode tank (2) and a cathode tank (3) are arranged in the electrolytic tank (1), and the pipeline at the outer wall of the electrolytic tank (1) at one side of the anode tank (2) is communicated with the water outlet end of the electric ball valve A (4), an anode liquid storage tank (5) is communicated with a water inlet end pipeline of the electric ball valve A (4), the pipeline at the outer wall of the electrolytic cell (1) at one side of the cathode cell (3) is communicated with the output end of an electric ball valve B (6), and the input end pipeline of the electric ball valve B (6) is communicated with a cathode liquid storage tank (7), the power ends of the electric ball valve A (4) and the electric ball valve B (6) are electrically connected with an external power supply, the inner walls of the anode tank (2) and the cathode tank (3) are respectively coated with an anode coating (8) and a cathode coating (9), and an ion membrane (10) is arranged on the inner wall of the electrolytic tank (1) between the anode tank (2) and the cathode tank (3).
2. The novel nx-BiTAC electrolytic cell testing device of claim 1, wherein: shell cavity (11) have been seted up to the shells inner wall of anode liquid storage pot (5) and cathode liquid storage pot (7), and the inside laminating of shell cavity (11) has S-shaped attaching plate (12), the sunken department arch of S-shaped attaching plate (12) has C shape extension board (13), and C shape extension board (13) top laminating shell cavity (11) inner wall department.
3. The novel nx-BiTAC electrolytic cell testing device of claim 1, wherein: the bottom end of the electrolytic tank (1) is fixedly connected with a base (14).
4. The novel nx-BiTAC electrolytic cell testing device of claim 2, wherein: and supporting legs (15) are welded at the bottom ends of the cathode liquid storage tank (7) and the anode liquid storage tank (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020721397.4U CN212476908U (en) | 2020-05-06 | 2020-05-06 | Novel nx-BiTAC electrolysis trough test device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020721397.4U CN212476908U (en) | 2020-05-06 | 2020-05-06 | Novel nx-BiTAC electrolysis trough test device |
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| CN212476908U true CN212476908U (en) | 2021-02-05 |
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| CN202020721397.4U Active CN212476908U (en) | 2020-05-06 | 2020-05-06 | Novel nx-BiTAC electrolysis trough test device |
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