CN210367935U - Electrolytic cell system and miniature multipole type ion membrane electrolytic cell set thereof - Google Patents
Electrolytic cell system and miniature multipole type ion membrane electrolytic cell set thereof Download PDFInfo
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- CN210367935U CN210367935U CN201921095945.0U CN201921095945U CN210367935U CN 210367935 U CN210367935 U CN 210367935U CN 201921095945 U CN201921095945 U CN 201921095945U CN 210367935 U CN210367935 U CN 210367935U
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Abstract
The utility model relates to a micro multi-pole type ion membrane electrolytic cell group, the edges of an anode end plate and a cathode end plate are respectively provided with a through hole correspondingly, the two ends of a stud bolt are respectively arranged in the through holes of the anode end plate and the cathode end plate in a penetrating way, and a first nut and a second nut are respectively arranged at the two ends of the stud bolt in a rotating way; the anode liquid inlet and the anode liquid outlet are provided with anode connectors, the cathode liquid inlet and the cathode liquid outlet are provided with cathode connectors, and titanium layers are coated inside the anode connectors. The composite electrode tank frames with different numbers are arranged between the single-electrode anode tank frame and the single-electrode cathode tank frame, so that the yield is adjusted, the anode joints or the cathode joints are arranged at the liquid inlet and outlet ports of the single-electrode anode tank frame, the single-electrode cathode tank frame and the composite electrode tank frame, the effect of convenient and adjustable assembly is realized, and the miniature multi-electrode type ion membrane electrolytic cell group also has the advantages of simple integral structure and small processing difficulty.
Description
Technical Field
The utility model relates to an electrolysis equipment field of chlor-alkali industry especially relates to an electrolysis trough system and miniature multipole formula ion membrane electrolysis cell group thereof.
Background
Along with the improvement of the living standard of people, people pay attention to the safety problem and the sewage discharge problem of the domestic drinking water gradually, and the high-concentration sodium hypochlorite is generally applied as the domestic drinking water disinfection and the domestic sewage treatment. However, the multipole type ion membrane electrolytic cell is widely applied in the caustic soda production industry, the annual capacity of a single set of multipole type ion membrane electrolytic cell is 100 tons at least, and the high-concentration sodium hypochlorite produced by the existing large-scale multipole type ion membrane electrolytic cell is used in remote areas, is influenced by the transportation of dangerous chemicals, and has too high cost for disinfecting drinking water and treating domestic sewage. However, the bipolar type ion membrane electrolyzer is difficult to be manufactured in a miniaturized manner due to the complex structure, the high difficulty in processing and manufacturing and the high cost. Therefore, the design of a micro bipolar type ion membrane electrolyzer for self production in remote areas is a problem to be solved by the technical personnel in the field at present.
SUMMERY OF THE UTILITY MODEL
Therefore, it is necessary to provide an electrolytic cell system and a micro-bipolar type ion membrane electrolytic cell set thereof to solve the problem of high cost of the conventional large-scale bipolar type ion membrane electrolytic cell product used in remote areas.
In order to achieve the above object, the inventor provides a micro multi-electrode type ion membrane electrolytic cell set, comprising an anode end plate, a cathode end plate, a single-electrode anode tank frame, a single-electrode cathode tank frame and a composite electrode tank frame, wherein the single-electrode anode tank frame is connected with the anode end plate, the single-electrode cathode tank frame is connected with the cathode end plate, the composite electrode tank frame is arranged between the single-electrode anode tank frame and the single-electrode cathode tank frame, an anode chamber is arranged in the single-electrode anode tank frame, a cathode chamber is arranged in the single-electrode cathode tank frame, an anode chamber and a cathode chamber are arranged in the composite electrode tank frame,
the double-end plate structure comprises an anode end plate, a cathode end plate and a double-end bolt, and is characterized by further comprising a double-end bolt, a first nut and a second nut, wherein through holes are correspondingly formed in the edges of the anode end plate and the cathode end plate, two ends of the double-end bolt respectively penetrate through the through holes of the anode end plate and the cathode end plate, a polytetrafluoroethylene insulating material is arranged at the contact part of the double-end bolt with the anode end plate and the cathode end plate, and the first nut and the second nut are respectively screwed at two;
an anode liquid inlet and an anode liquid outlet are respectively formed in two sides of the single-electrode anode tank frame; a cathode liquid inlet and a cathode liquid outlet are respectively arranged on two sides of the single-electrode cathode tank frame; an anode liquid inlet and a cathode liquid inlet are formed in one side of the composite electrode tank frame, and an anode liquid outlet and a cathode liquid outlet are formed in the other side of the composite electrode tank frame; the anode liquid inlet and the anode liquid outlet are provided with anode connectors, the cathode liquid inlet and the cathode liquid outlet are provided with cathode connectors, and the anode connectors are coated with anti-electrochemical corrosion layers.
The anode liquid disc and the cathode liquid disc are both disc-shaped structures and are respectively arranged in the anode chamber and the cathode chamber;
the utility model discloses a compound electrode of a fuel cell, including positive pole liquid dish, negative pole liquid dish, compound electrode tank frame, positive pole liquid dish and negative pole liquid dish in the compound electrode tank frame set up with each other mutually, and through compound rib welded connection between the two dish bottoms, positive pole liquid dish bottom in the single pole positive pole tank frame is connected towards the positive pole end plate and is connected with the welding of positive pole end plate through compound rib, negative pole liquid dish bottom in the single pole negative pole tank frame is connected with the welding of negative pole end plate towards the negative pole end plate and through compound rib.
Furthermore, the composite ribs are formed by compounding titanium-nickel materials, and the number of the composite ribs is more than two.
Further, still include positive pole rib, negative pole rib, anode mesh and negative pole net, the number of positive pole rib and negative pole rib is more than two, positive pole rib and anode mesh set up in the positive pole indoor, negative pole rib and negative pole net set up in the negative pole indoor, the cross-section of positive pole rib and negative pole rib is L font structure, a terminal surface of positive pole rib is towards positive pole liquid dish and welds on positive pole liquid dish, another terminal surface of positive pole rib sets up the direction and is used for fixed anode mesh with positive pole terminal plate is perpendicular just this terminal surface end, a terminal surface of negative pole rib is towards negative pole liquid dish and is fixed in on the negative pole liquid dish, another terminal surface of negative pole rib sets up the direction and is perpendicular just this terminal surface end is used for fixed cathode mesh with negative pole terminal plate.
Further, the anode liquid disc and the anode ribs are made of titanium, and the cathode liquid disc and the cathode ribs are made of nickel.
Further, the electrochemical corrosion prevention layer is ruthenium, iridium or titanium.
Furthermore, the number of the composite electrode tank frames is more than two, and the composite electrode tank frames are arranged between the single-electrode anode tank frame and the single-electrode cathode tank frame in parallel.
The inventor also provides an electrolytic cell system, which comprises a first input pipeline, a second input pipeline, a first output pipeline, a second output pipeline and an electrolytic cell group, wherein the electrolytic cell group is the miniature multi-pole ionic membrane electrolytic cell group in any technical scheme, the first input pipeline is provided with more than two anolyte output ports, the second input pipeline is provided with more than two catholyte output ports, the first output pipeline is provided with more than two anolyte input ports, and the second output pipeline is provided with more than two catholyte input ports;
the anolyte delivery outlet is connected with the positive pole joint of positive pole inlet department through anolyte feed liquor pipe, the catholyte delivery outlet is connected with the negative pole joint of negative pole inlet department through catholyte feed liquor pipe, the anolyte input port is connected with the positive pole joint of positive pole outlet department through the anolyte drain pipe, the catholyte input port is connected with the negative pole joint of negative pole outlet department through the catholyte drain pipe.
Further, anolyte delivery outlet and anolyte input are provided with the positive pole and connect, catholyte delivery outlet and catholyte input are provided with the negative pole and connect.
Furthermore, the inner walls of the anolyte liquid inlet pipe and the anolyte liquid outlet pipe are coated with an anti-electrochemical corrosion layer.
Different from the prior art, the technical scheme has the following advantages: the composite electrode tank frames with different numbers are arranged between the single-electrode anode tank frame and the single-electrode cathode tank frame, so that the yield is adjusted, the anode joints or the cathode joints are arranged at the liquid inlet and outlet ports of the single-electrode anode tank frame, the single-electrode cathode tank frame and the composite electrode tank frame, the effect of convenient and adjustable assembly is realized, and the miniature multi-electrode type ion membrane electrolytic cell group also has the advantages of simple integral structure and small processing difficulty.
Drawings
FIG. 1 is a schematic view of an electrolytic cell system according to the present embodiment;
FIG. 2 is a schematic view of the internal structure of the composite electrode frame of the micro multi-electrode type ion-exchange membrane electrolyzer set according to the present embodiment;
FIG. 3 is a schematic diagram illustrating an internal structure of a single-electrode anode frame of a micro multi-electrode type ion-exchange membrane electrolyzer set according to the present embodiment;
fig. 4 is a schematic diagram of the internal structure of the single-electrode cathode frame of the micro bipolar ionic membrane electrolyzer of the present embodiment.
Description of reference numerals:
1. an anode end plate;
2. a cathode end plate;
3. a single electrode anode cell frame;
4. a single electrode cathode bezel;
5. a composite electrode slot frame;
61. a stud bolt;
62. a first nut;
63. a second nut;
71. an anode tap;
72. a cathode terminal;
81. an anolyte pan;
82. a cathode liquid pan;
83. compounding ribs;
91. anode ribs;
92. cathode ribs;
93. an anode mesh;
94. a cathode mesh;
01. a first input conduit;
02. a second input conduit;
03. a first output conduit;
04. a second output conduit;
011. an anolyte feed pipe;
012. a catholyte inlet pipe;
013. an anolyte outlet pipe;
014. and a catholyte outlet pipe.
Detailed Description
To explain technical contents, structural features, and objects and effects of the technical solutions in detail, the following detailed description is given with reference to the accompanying drawings in conjunction with the embodiments.
Referring to fig. 2 to 4, the utility model provides a miniature multi-electrode type ion membrane electrolytic cell group, including anode end plate 1, negative pole end plate 2, single electrode anode tank frame 3, single electrode cathode tank frame 4 and composite electrode tank frame 5, anode end plate and cathode end plate are connected with the positive negative pole of power respectively, anode end plate and the relative parallel arrangement of negative pole end plate, single electrode anode tank frame is connected with the anode end plate, single electrode cathode tank frame is connected with the negative pole end plate, and composite electrode tank frame sets up between single electrode anode tank frame and single electrode cathode tank frame. The single-electrode anode tank frame and the single-electrode cathode tank frame have the beneficial effects that the width values of the tank frames are half of the width value of the composite electrode tank frame, and the single-electrode anode tank frame and the single-electrode cathode tank frame respectively have the same size as an anode chamber and a cathode chamber which are formed in the single-electrode anode tank frame and the composite electrode tank frame, so that the electrolytic work efficiency in each unit electrolytic cell in the multi-electrode type ion membrane electrolytic cell is the same, and the controllability of the whole electrolytic work efficiency is higher.
The micro multi-pole type ion membrane electrolytic cell unit further comprises a stud 61, a first nut 62 and a second nut 63, and through holes are formed in the edges of the anode end plate and the cathode end plate correspondingly. In this embodiment, the anode end plate and the cathode end plate have similar shapes and sizes, and the anode end plate and the cathode end plate are of a square plate structure, and the through holes formed in the anode end plate and the cathode end plate are formed along the edge of the square end plate.
During anode end plate and cathode end plate's through-hole was worn to locate respectively at stud's both ends, stud's both ends are outstanding positive pole end plate and cathode end plate respectively, stud's both ends are located soon respectively to first nut and second nut, and first nut and second nut lock are pressed from both sides tightly between positive pole end plate and cathode end plate with single electrode anode tank frame, single electrode cathode tank frame and combined electrode tank frame behind stud both ends. The stud is provided with tetrafluoro insulating material with the contact site of positive pole end plate, negative pole end plate, specifically, stud's both ends cover is equipped with the insulating cover that tetrafluoro insulating material made, and the through-hole of positive pole end plate and negative pole end plate still is provided with tetrafluoro insulating gasket. The adjacent composite electrode tank frames are sealed by sealing rubber gaskets, and the composite electrode tank frames, the single-electrode anode tank frame and the single-electrode cathode tank frame are also sealed by sealing rubber gaskets.
The single-electrode anode tank frame is characterized in that an anode liquid inlet and an anode liquid outlet are respectively formed in two sides of the single-electrode anode tank frame, and the anode liquid inlet and the anode liquid outlet are formed in diagonal positions of the single-electrode anode tank frame. The cathode liquid inlet and the cathode liquid outlet are respectively arranged on two sides of the single-electrode cathode tank frame, and the cathode liquid inlet and the cathode liquid outlet are also arranged at the diagonal positions of the single-electrode cathode tank frame. The composite electrode tank comprises an electrolytic tank, an anode liquid inlet, a cathode liquid inlet, an anode liquid outlet, a cathode liquid outlet, an anode liquid inlet, a cathode liquid outlet, a cathode liquid inlet, a cathode liquid outlet, an anode liquid inlet, a cathode liquid outlet.
And the anode liquid inlet and the anode liquid outlet are provided with anode connectors 71 which are communicated with an external anode input and output liquid pipeline. And the cathode liquid inlet and the cathode liquid outlet are provided with cathode joints 72 which are communicated with external cathode input and output liquid pipelines. The anode joint is internally coated with an electrochemical corrosion prevention layer, so that the anode liquid tray of the electrolytic cell can be effectively prevented from being subjected to electrochemical corrosion by the stray current of the anode liquid. Specifically, the material of the electrochemical corrosion prevention layer is ruthenium, iridium, or titanium.
The micro multi-pole ionic membrane electrolytic cell unit further comprises an anode liquid disc 81, a cathode liquid disc 82 and composite ribs 83, wherein the anode liquid disc and the cathode liquid disc are of disc-shaped structures, the middle of the anode liquid disc and the middle of the cathode liquid disc are low, and the four sides of the anode liquid disc and the cathode liquid disc are high. The anode liquid disc and the cathode liquid disc are respectively arranged in the anode chamber and the cathode chamber, and the anode liquid disc and the cathode liquid disc are used as fixing discs of an anode net and a cathode net and places for electrochemical reaction of the anode liquid and the cathode liquid.
The positive pole liquid dish and negative pole liquid dish are the disc structure, the dish mouth of positive pole liquid dish and negative pole liquid dish in the combined electrode cell frame sets up back to the back, and the dish mouth of positive pole liquid dish and negative pole liquid dish is connected through compound rib between the dish bottom of positive pole liquid dish and negative pole liquid dish promptly, is the stable in structure and the electric conductivity in order to strengthen positive pole liquid dish and negative pole liquid dish through compound rib connection. The bottom of the anode liquid disc in the single-electrode anode tank frame faces the anode end plate and is connected with the anode end plate through the composite ribs, the composite ribs are used for enhancing the structural stability and the electric conductivity between the anode liquid disc and the anode end plate, the bottom of the cathode liquid disc in the single-electrode cathode tank frame faces the cathode end plate and is connected with the cathode end plate through the composite ribs, and the composite ribs are used for enhancing the structural stability and the electric conductivity between the cathode liquid disc and the cathode end plate.
In some preferred embodiments, the number of the composite ribs is more than two, which has the beneficial effects that the structural stability and the electrical conductivity between the anode liquid disc and the cathode liquid disc, between the anode liquid disc and the anode end plate, and between the cathode liquid disc and the cathode end plate are further enhanced.
The micro multi-electrode type ion-exchange membrane electrolytic cell unit further comprises anode ribs 91, cathode ribs 92, an anode mesh 93 and a cathode mesh 94, wherein the number of the anode ribs and the number of the cathode ribs are more than two, the anode ribs and the anode mesh are arranged in the anode chamber, the cathode ribs and the cathode mesh are arranged in the cathode chamber, the cross sections of the anode ribs and the cathode ribs are L-shaped structures, one end surface of each anode rib faces the anode liquid disc and is welded on the anode liquid disc, the other end surface of each anode rib is perpendicular to the anode end plate in the direction, the end surface of each anode rib is used for fixing the anode mesh, more than two through holes are formed in one end surface of the anode rib used for fixing the anode mesh, one end surface of each cathode rib faces the cathode liquid disc and is fixed on the cathode liquid disc, the other end surface of each cathode rib is perpendicular to the cathode end plate in the direction, and the end surface of each cathode rib is used for fixing the, and more than two through holes are formed in one end face of the cathode rib for fixing the cathode mesh. After the anode ribs are fixed on the anode liquid disc, channels are formed between the through holes on the anode ribs and the anode liquid disc, more than two anode ribs are linearly arrayed along the surface of the anode liquid disc, and the array direction is vertical to the liquid inlet direction of the anode liquid; after the cathode ribs are fixed on the cathode liquid disc, channels are formed between the through holes in the cathode ribs and the cathode liquid disc, more than two cathode ribs are linearly arrayed along the surface of the cathode liquid disc, and the array direction is perpendicular to the liquid inlet direction of cathode liquid. The anode ribs and the cathode ribs are arranged and have the effect that flow channels are constructed for anolyte or catholyte through holes formed in the anode ribs and the cathode ribs, so that the anolyte and the catholyte are distributed in the electrolytic bath in a balanced manner at an accelerated speed.
The material of positive pole liquid dish and positive pole rib is titanium, the material of negative pole liquid dish and negative pole rib is nickel.
In some preferred embodiments, the number of the composite electrode frames is two or more, and the composite electrode frames are arranged between the single-electrode anode frame and the single-electrode cathode frame in parallel. The number of the composite electrode cell frames can be adjusted according to the actual capacity demand, and the chlorine capacity of the miniature multi-electrode type ion membrane electrolytic cell set can be adjusted at will between 5 and 100 tons per year.
As shown in fig. 1 (for clarity, the connection structure between the composite electrode cell frame and the first input pipeline, the second input pipeline, the first output pipeline and the second output pipeline is omitted in fig. 1), the inventor also provides an electrolytic cell system, which comprises a first input pipeline 01, a second input pipeline 02, a first output pipeline 03, a second output pipeline 04 and an electrolytic cell group, wherein the electrolytic cell group is the micro bipolar type ionic membrane electrolytic cell group in any technical scheme. The first input pipeline is used for conveying sodium chloride brine to the electrolytic cell group, the second input pipeline is used for conveying dilute sodium hydroxide (adding pure water) to the electrolytic cell group, the first output pipeline is used for outputting the dilute brine and chlorine, and the second output pipeline is used for outputting concentrated sodium hydroxide and hydrogen. The micro multi-pole ion membrane electrolytic cell group has low yield, and directly outputs chlorine generated in the anode chamber of the electrolytic cell group to the first output pipeline.
The first input pipeline is provided with more than two anolyte output ports, the second input pipeline is provided with more than two catholyte output ports, the first output pipeline is provided with more than two anolyte input ports, and the second output pipeline is provided with more than two catholyte input ports;
the anolyte delivery outlet is connected with the anode joint of positive pole inlet department through anolyte feed liquor pipe 011, the catholyte delivery outlet is connected with the cathode joint of negative pole inlet department through catholyte feed liquor pipe 012, the anolyte input port is connected with the anode joint of positive pole outlet department through anolyte drain pipe 013, the catholyte input port is connected with the cathode joint of negative pole outlet department through catholyte drain pipe 014.
In some preferred embodiments, the anolyte output port and the anolyte input port are provided with an anode joint, and the catholyte output port and the catholyte input port are provided with a cathode joint and an anolyte drain pipe. The beneficial effects of the utility model reside in that, through anolyte feed liquor pipe, catholyte feed liquor pipe and catholyte drain pipe of different length and shape, can adjust the walking pipe position of first input pipeline, second input pipeline, first output pipeline and second output pipeline in a flexible way.
The anolyte liquid inlet pipe and the anolyte liquid outlet pipe are made of titanium materials, and the catholyte liquid inlet pipe and the catholyte liquid outlet pipe are made of nickel materials.
In some preferred embodiments, the inner walls of the anolyte inlet pipe and the anolyte outlet pipe are coated with an electrochemical corrosion prevention layer, the electrochemical corrosion prevention layer is ruthenium, iridium or titanium, and the electrochemical corrosion prevention layer can effectively prevent the anolyte stray current from generating electrochemical corrosion on an anolyte plate of the electrolytic cell.
It should be noted that, although the above embodiments have been described herein, the scope of the present invention is not limited thereby. Therefore, based on the innovative concept of the present invention, the changes and modifications of the embodiments described herein, or the equivalent structure or equivalent process changes made by the contents of the specification and the drawings of the present invention, directly or indirectly apply the above technical solutions to other related technical fields, all included in the protection scope of the present invention.
Claims (10)
1. The utility model provides a miniature multi-electrode formula ionic membrane electrolytic cell group, includes anode end plate, cathode end plate, single electrode anode tank frame, single electrode cathode tank frame and combined electrode tank frame, single electrode anode tank frame is connected with the anode end plate, single electrode cathode tank frame is connected with the cathode end plate, combined electrode tank frame sets up between single electrode anode tank frame and single electrode cathode tank frame, be provided with the anode chamber in the single electrode anode tank frame, be provided with the cathode chamber in the single electrode cathode tank frame, be provided with anode chamber and cathode chamber in the combined electrode tank frame, its characterized in that:
the double-end plate structure comprises an anode end plate, a cathode end plate and a double-end bolt, and is characterized by further comprising a double-end bolt, a first nut and a second nut, wherein through holes are correspondingly formed in the edges of the anode end plate and the cathode end plate, two ends of the double-end bolt respectively penetrate through the through holes of the anode end plate and the cathode end plate, a polytetrafluoroethylene insulating material is arranged at the contact part of the double-end bolt with the anode end plate and the cathode end plate, and the first nut and the second nut are respectively screwed at two;
an anode liquid inlet and an anode liquid outlet are respectively formed in two sides of the single-electrode anode tank frame; a cathode liquid inlet and a cathode liquid outlet are respectively arranged on two sides of the single-electrode cathode tank frame; an anode liquid inlet and a cathode liquid inlet are formed in one side of the composite electrode tank frame, and an anode liquid outlet and a cathode liquid outlet are formed in the other side of the composite electrode tank frame; the anode liquid inlet and the anode liquid outlet are provided with anode connectors, the cathode liquid inlet and the cathode liquid outlet are provided with cathode connectors, and the anode connectors are coated with anti-electrochemical corrosion layers.
2. The miniature multipole ion membrane electrolyzer of claim 1, characterized in that: the anode liquid disc and the cathode liquid disc are both of disc-shaped structures and are respectively arranged in the anode chamber and the cathode chamber;
the utility model discloses a compound electrode of a fuel cell, including positive pole liquid dish, negative pole liquid dish, compound electrode tank frame, positive pole liquid dish and negative pole liquid dish in the compound electrode tank frame set up with each other mutually, and through compound rib welded connection between the two dish bottoms, positive pole liquid dish bottom in the single pole positive pole tank frame is connected towards the positive pole end plate and is connected with the welding of positive pole end plate through compound rib, negative pole liquid dish bottom in the single pole negative pole tank frame is connected with the welding of negative pole end plate towards the negative pole end plate and through compound rib.
3. The miniature multipole ion membrane electrolyzer of claim 2, characterized in that: the composite ribs are formed by compounding titanium-nickel materials, and the number of the composite ribs is more than two.
4. The miniature multipole ion membrane electrolyzer of claim 2, characterized in that: the anode and cathode structure is characterized by further comprising anode ribs, cathode ribs, an anode net and a cathode net, wherein the number of the anode ribs and the number of the cathode ribs are more than two, the anode ribs and the anode net are arranged in the anode chamber, the cathode ribs and the cathode net are arranged in the cathode chamber, the cross sections of the anode ribs and the cathode ribs are of L-shaped structures, one end face of each anode rib faces the anode liquid disc and is welded on the anode liquid disc, the other end face of each anode rib is perpendicular to the anode end plate, the tail end of the end face is used for fixing the anode net, more than two through holes are formed in one end face of the anode rib used for fixing the anode net, one end face of each cathode rib faces the cathode liquid disc and is fixed on the cathode liquid disc, the other end face of each cathode rib is perpendicular to the cathode end plate, and the tail end of the end face is used for fixing the cathode net, and more than two through holes are formed in one end face of the cathode rib for fixing the cathode mesh.
5. The miniature multipole ion membrane electrolyzer unit of claim 4, characterized in that: the material of positive pole liquid dish and positive pole rib is titanium, the material of negative pole liquid dish and negative pole rib is nickel.
6. The miniature multipole ion membrane electrolyzer of claim 1, characterized in that: the electrochemical corrosion prevention layer is ruthenium, iridium or titanium.
7. The miniature multipole ion membrane electrolyzer of claim 1, characterized in that: the number of the composite electrode tank frames is more than two, and the composite electrode tank frames are arranged between the single-electrode anode tank frame and the single-electrode cathode tank frame in parallel.
8. An electrolytic cell system characterized by: the micro multi-polar ion membrane electrolyzer comprises a first input pipeline, a second input pipeline, a first output pipeline, a second output pipeline and an electrolyzer set, wherein the electrolyzer set is the micro multi-polar ion membrane electrolyzer set of any claim from 1 to 6, more than two anolyte output ports are arranged on the first input pipeline, more than two catholyte output ports are arranged on the second input pipeline, more than two anolyte input ports are arranged on the first output pipeline, and more than two catholyte input ports are arranged on the second output pipeline;
the anolyte delivery outlet is connected with the positive pole joint of positive pole inlet department through anolyte feed liquor pipe, the catholyte delivery outlet is connected with the negative pole joint of negative pole inlet department through catholyte feed liquor pipe, the anolyte input port is connected with the positive pole joint of positive pole outlet department through the anolyte drain pipe, the catholyte input port is connected with the negative pole joint of negative pole outlet department through the catholyte drain pipe.
9. An electrolysis cell system according to claim 8, wherein: the anolyte delivery outlet and anolyte delivery inlet are provided with the positive pole and connect, catholyte delivery outlet and catholyte delivery inlet are provided with the negative pole and connect.
10. An electrolysis cell system according to claim 8, wherein: and the inner walls of the anolyte liquid inlet pipe and the anolyte liquid outlet pipe are coated with an anti-electrochemical corrosion layer.
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| CN201921095945.0U CN210367935U (en) | 2019-07-12 | 2019-07-12 | Electrolytic cell system and miniature multipole type ion membrane electrolytic cell set thereof |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110184618A (en) * | 2019-07-12 | 2019-08-30 | 福建浩达智能科技股份有限公司 | A kind of electrolyzer system and its miniature a bipolar type ion-exchange membrane electrolyzer group |
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2019
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110184618A (en) * | 2019-07-12 | 2019-08-30 | 福建浩达智能科技股份有限公司 | A kind of electrolyzer system and its miniature a bipolar type ion-exchange membrane electrolyzer group |
| CN110184618B (en) * | 2019-07-12 | 2024-08-09 | 福建浩达智能科技股份有限公司 | Electrolytic tank system and miniature bipolar type ionic membrane electrolytic tank group thereof |
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| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: Floor 20, Building 20, Phase II, Innovation Park, No.7 Wulongjiang Middle Avenue, High tech Zone, Fuzhou City, 350000, Fujian Province Patentee after: FUJIAN HADA INTELLIGENCE TECHNOLOGY CO.,LTD. Address before: Building 62, Juyuanzhou Garden, Jinshan Industrial Zone, No. 618, Jinshan Avenue, Jianxin Town, Cangshan District, Fuzhou City, 350000, Fujian Province Patentee before: FUJIAN HADA INTELLIGENCE TECHNOLOGY CO.,LTD. |