An electrolytic cell with a balanced liquid inlet device

Abstract

The present disclosure provides an electrolytic cell with a balanced liquid inlet device, including an electrolytic cell body and at least one cathode plate and an anode plate. The balanced liquid inlet device is arranged on the inner wall of one side of the top of the electrolytic cell body, and the inner wall of the other side of the electrolytic cell body is arranged with a diversion liquid outlet plate. The balanced liquid inlet device has a liquid flow channel and a plurality of liquid discharge ports evenly distributed along the length direction of the liquid flow channel. The diversion liquid outlet plate and the inner wall of the electrolytic cell body form a diversion liquid outlet channel. The liquid flow channel can allow electrolyte to enter the interior of the electrolytic cell body in a balanced manner through the plurality of liquid discharge ports, and flow out through the diversion liquid outlet channel. The present disclosure can ensure stable circulation of liquid inlet through the balanced liquid inlet device and the diversion liquid outlet channel. The electrolyte flows in a stable and single direction, and the possibility of flowing in other directions is small. It is not easy to cause agitation of anode mud, thereby improving the utilization rate of electrolyte and the quality of electrolytic products, and having high production efficiency, reducing power consumption, and having high stability and reliability.

Description

Technical Field

[0001] The present disclosure relates to the field of electrolysis technology, and in particular to an electrolytic cell with a balanced liquid inlet device. Background Art

[0002] The traditional electrolysis technology is to place the cathode and cathode in a tank where the electrolyte flows slowly. Under the action of the electric field, the anions move toward the anode and the cations move toward the cathode. By controlling certain technical conditions, the target metal cations are electrolytically deposited at the cathode, thereby obtaining a high-purity electrolytic product. Since the electrode reaction rate is often faster than the diffusion rate of the ions, concentration polarization is formed. In the traditional electrolytic cell, it is precisely because of the concentration polarization of the cathode that a small amount of impurity ions or hydrogen ions are precipitated on the cathode together with the target metal ions, which on the one hand leads to a decrease in the quality of the cathode product, and on the other hand, it causes a significant decrease in the cathode current efficiency, thereby increasing the energy consumption per unit product. Therefore, when using traditional electrolysis technology for metal purification or electrolytic deposition, in order to ensure a high cathode current efficiency and cathode product quality, its current density must be controlled within a low range, resulting in a large electrolysis system, high equipment investment costs, and low production efficiency.

[0003] With the development of society and science and technology, and the continuous advancement of metal refining technology, people are pursuing to increase the current density of metal electrolysis, strengthen electrolytic production, and improve the production efficiency of electrolytic cells while ensuring the quality of metals. One of the breakthrough directions is the circulation of electrolyte, increasing the circulation volume of electrolyte, increasing the migration speed of metal ions, and reducing concentration polarization in the electrolytic production process, thereby achieving high current density electrolytic production.

[0004] However, the existing electrolytic cells usually have multiple electrolyte nozzles in the electrolytic cell for liquid inlet, which easily causes uneven liquid flow distribution and uneven electrolyte dispersion. As the electrolyte circulation volume increases, it is easy to cause anode mud agitation, increase the concentration of suspended particles in the electrolyte, and be unfavorable for the sedimentation of the anode mud, seriously affecting the quality of the electrolytic product, such as reducing the recovery rate of precious metals, etc., and the electrolyte nozzle is also prone to clogging, which can easily reduce production efficiency or even clog the electrolyte outlet after long-term production, and has low stability and reliability. Summary of the invention

[0005] In view of the above problems existing in the existing electrolytic cells, the present disclosure proposes an electrolytic cell with a balanced liquid inlet device.

[0006] In order to solve at least one of the above technical problems, the present disclosure proposes the following technical solutions:

[0007] An electrolytic cell with a balanced liquid inlet device comprises an electrolytic cell body and at least one cathode plate and an anode plate, wherein the cathode plate and the anode plate are sequentially arranged in the interior of the electrolytic cell body at intervals, an balanced liquid inlet device is arranged on the inner wall on one side of the top of the electrolytic cell body, a guide liquid outlet plate is arranged on the inner wall on the other side of the electrolytic cell body, the cathode plate and the anode plate are located between the balanced liquid inlet device and the guide liquid outlet plate, the balanced liquid inlet device has a liquid flow channel and a plurality of liquid discharge ports evenly distributed along the length direction of the liquid flow channel, the guide liquid outlet plate and the inner wall of the electrolytic cell body form a guide liquid outlet channel, and the liquid flow channel can allow electrolyte to enter the interior of the electrolytic cell body in a balanced manner through the plurality of liquid discharge ports and flow out through the guide liquid outlet channel.

[0008] In some embodiments, the inlet of the diverting outlet channel is located at the bottom of the diverting outlet plate, and a liquid outlet connected to the diverting outlet channel is provided at one end of the top of the electrolytic cell body.

[0009] In some embodiments, a first bent portion is provided at one end of the top of the liquid guide plate near the liquid outlet, and the first bent portion and the inner wall of the electrolytic cell body form an outlet of the liquid guide channel connected to the liquid outlet.

[0010] In some embodiments, the cathode plate and the anode plate are respectively perpendicular to the balanced liquid inlet device and the liquid guide outlet plate in a vertical direction.

[0011] In some embodiments, the cross-section of the liquid discharge port is rectangular, and the length direction of the liquid discharge port is consistent with the vertical direction.

[0012] In some embodiments, the balanced liquid inlet device includes a liquid inlet box, and the liquid flow channel and the liquid discharge port are arranged on the liquid inlet box.

[0013] In some embodiments, the liquid inlet box is mounted on a panel, and the panel is mounted on the inner wall of the electrolytic cell body.

[0014] In some embodiments, a first tank body for accommodating a panel is disposed on the inner wall of the electrolytic tank body.

[0015] In some embodiments, the balanced liquid inlet device includes a liquid inlet plate, the liquid inlet plate and the inner wall of the electrolytic cell body form a liquid flow channel, and the liquid discharge port is arranged on the liquid inlet plate.

[0016] In some embodiments, the liquid inlet plate is provided with a first bent edge that matches the inner wall of the electrolytic cell.

[0017] The beneficial effects of the present disclosure are as follows: during use, the external circulating liquid supply system is connected to the liquid flow channel of the balanced liquid inlet device through the corresponding pipeline to supply liquid, and the electrolyte entering the liquid flow channel automatically and evenly enters the interior of the electrolytic cell body from top to bottom through multiple discharge ports, and then flows in parallel between the adjacent cathode plates and anode plates respectively, and is evenly distributed between the cathode plates and anode plates, that is, electrolysis intervals are formed between each adjacent cathode plate and anode plate, and each electrolysis interval does not affect each other, the electrolyte flows stably and single, and turbulence is not easy to occur, and finally the electrolyte enters the diversion liquid outlet channel opposite to the balanced liquid inlet device and then flows out to the external circulating liquid supply system, and stable circulating liquid inlet can be ensured by the balanced liquid inlet device and the diversion liquid outlet channel. The electrolyte enters from the balanced liquid inlet device and then exits from the diversion liquid outlet channel opposite to the balanced liquid inlet device, so that the electrolyte flow is the shortest, the electrolyte flow direction is stable and single, and the possibility of flowing in other directions is small, which improves the utilization rate of the electrolyte. Under the same current density conditions, the required circulation volume is smaller, and the power required is reduced. Even if the electrolyte circulation volume increases, the electrolyte in the electrolytic cell body has no turbulence, which is not easy to cause anode mud agitation, reduces the concentration of suspended particles in the electrolyte, facilitates the rapid sedimentation of the anode mud, and improves the quality of the electrolytic product. In addition, the electrolyte nozzle is cancelled, and the electrolyte nozzle will not be easily blocked. The electrolyte outlet is not easy to be blocked after long-term production, and the production efficiency is high, and the stability and reliability are high.

[0018] In addition, in the technical solution disclosed in the present invention, unless otherwise specified, the technical solution can be implemented by adopting conventional means in the art. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] In order to more clearly illustrate the specific embodiments of the present disclosure or the technical solutions in the prior art, the drawings required for use in the specific embodiments or the description of the prior art will be briefly introduced below. Obviously, the drawings described below are some embodiments of the present disclosure. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.

[0020] Figure 1 A first cross-sectional view of an electrolytic cell with a balanced liquid inlet device provided in an embodiment of the present disclosure.

[0021] Figure 2 A second cross-sectional view of an electrolytic cell with a balanced liquid inlet device provided in an embodiment of the present disclosure.

[0022] Figure 3 A schematic diagram of the partial structure of an electrolytic cell with a balanced liquid inlet device without cathode plates and anode plates provided in an embodiment of the present disclosure.

[0023] Figure 4Solution 1 of the balanced liquid inlet device provided in the embodiment of the present disclosure.

[0024] Figure 5 This is a second solution of the balanced liquid inlet device provided in the embodiment of the present disclosure.

[0025] Figure 6 A three-dimensional diagram of a liquid guide plate provided in an embodiment of the present disclosure.

[0026] The numbers in the accompanying drawings illustrate the electrolytic cell body 1, the liquid outlet 11, the first connecting tube 12, the first cell body 13, the supporting protrusion 14, the sewage outlet 15, the mounting block 16, the cathode plate 2, the anode plate 3, the balanced liquid inlet device 4, the liquid flow channel 401, the liquid outlet 402, the liquid inlet box 41, the reinforcing rib 411, the panel 42, the liquid inlet plate 43, the first bending edge 431, the liquid guide plate 5, the liquid guide channel 51, the bending portion 52, the second bending edge 53, the partition plate 54, and the second connecting tube 6. DETAILED DESCRIPTION

[0027] In order to make the purpose, technical solutions and advantages of the present disclosure more clearly understood, the present disclosure is further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are part of the embodiments of the present disclosure, rather than all of the embodiments, and are only used to explain the present disclosure, and are not used to limit the present disclosure. Based on the embodiments in the present disclosure, all other embodiments obtained by ordinary technicians in the field without making creative work are within the scope of protection of the present disclosure.

[0028] In the description of the present disclosure, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", "two ends", "both sides" and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the accompanying drawings, and are only for the convenience of describing the present disclosure and simplifying the description, rather than indicating or implying that the referred elements must have a specific orientation or be constructed and operated in a specific orientation, and therefore cannot be understood as limitations on the present disclosure. In addition, the terms "first", "second", "superior", "inferior", "primary", "secondary" and the like are used for descriptive purposes only, and can simply be used to more clearly distinguish different components, and cannot be understood as indicating or implying relative importance.

[0029] In the description of the present disclosure, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection, or it can be indirectly connected through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present disclosure can be understood according to specific circumstances.

[0030] Figure 1 A first cross-sectional view of an electrolytic cell with a balanced liquid inlet device provided in an embodiment of the present disclosure, Figure 2 A second cross-sectional view of an electrolytic cell with a balanced liquid inlet device provided in an embodiment of the present disclosure, Figure 3 A partial structural schematic diagram of an electrolytic cell with a balanced liquid inlet device provided in an embodiment of the present disclosure, with the cathode plate and the anode plate removed, Figure 4 The first solution of the balanced liquid inlet device provided in the embodiment of the present disclosure is: Figure 5 The second solution of the balanced liquid inlet device provided in the embodiment of the present disclosure is: Figure 6 A three-dimensional diagram of a liquid guide plate provided in an embodiment of the present disclosure.

[0031] Example:

[0032] like Figures 1 to 6As shown, an electrolytic cell with a balanced liquid inlet device can be used for electrolysis and electrolytic electrowinning of metals such as copper, zinc, nickel, and manganese, and includes an electrolytic cell body 1 and at least one cathode plate 2 and an anode plate 3. The number of cathode plates 2 and anode plates 3 depends on the specific situation, and is usually a plurality of cathode plates 2 and a plurality of anode plates 3. The cathode plates 2 and the anode plates 3 are sequentially arranged inside the electrolytic cell body 1 at intervals. A balanced liquid inlet device 4 is arranged on the inner wall on one side of the top of the electrolytic cell body 1, and a guide liquid outlet plate 5 is arranged on the inner wall on the other side of the electrolytic cell body 1, that is, the guide liquid outlet plate 5 is located opposite to the balanced liquid inlet device 4, and the cathode plate 2 and the anode plate 3 are located between the balanced liquid inlet device 4 and the guide liquid outlet plate 5. The balanced liquid inlet device 4 is usually arranged horizontally along the length direction inside the electrolytic cell body 1. The length of the balanced liquid inlet device 4 is slightly shorter than the length inside the electrolytic cell body 1 to facilitate installation and other operations. The balanced liquid inlet device 4 has a liquid flow channel 401 and a plurality of discharge ports 402 evenly distributed along the length direction of the liquid flow channel 401. The number and size of the discharge ports 402 depend on the specific situation. The liquid guide plate 5 and the inner wall of the electrolytic cell body 1 form a liquid guide channel 51, that is, the liquid guide channel 51 is located opposite the liquid flow channel 401. The external circulation liquid supply system is connected with the liquid flow channel 401 of the balanced liquid inlet device 4 through the corresponding pipeline for liquid supply. The electrolyte enters the liquid flow channel 401 and enters the interior of the electrolytic cell body 1 through multiple discharge ports 402 in a balanced manner, and then flows in parallel between the adjacent cathode plates 2 and anode plates 3, and is evenly distributed between the cathode plates 2 and anode plates 3, that is, electrolysis intervals are formed between each adjacent cathode plate 2 and anode plate 3, and each electrolysis interval does not affect each other. Finally, the electrolyte enters the diversion liquid outlet channel 51 opposite to the balanced liquid inlet device 4 and then flows out to the external circulation liquid supply system. The electrolyte flows in a stable, single and short direction, and the possibility of flowing in other directions is small. It is not easy to generate turbulence, which improves the utilization rate of the electrolyte. Under the same current density conditions, the required circulation volume is smaller, which reduces the power required to be consumed. Even if the electrolyte circulation volume is increased, the electrolyte in the electrolytic cell body 1 has no turbulence, which is not easy to cause agitation of the anode mud, reduces the concentration of suspended particles in the electrolyte, facilitates the rapid sedimentation of the anode mud, and improves the quality of the electrolysis product.

[0033] The inlet of the diversion liquid outlet channel 51 is located at the bottom of the diversion liquid outlet plate 5, and one end of the top of the electrolytic cell body 1 is provided with a liquid outlet 11 connected to the diversion liquid outlet channel 51. The inlet of the diversion liquid outlet channel 51 is usually roughly flush with the bottom of the cathode plate 2 or the anode plate 3 in the electrolytic cell body 1. The electrolyte enters the interior of the electrolytic cell body 1 from the balanced liquid inlet device 4 on the top side of the electrolytic cell body 1, and then the electrolyte flows in parallel between the adjacent cathode plates 2 and anode plates 3, and is evenly distributed between the cathode plates 2 and anode plates 3. Then the electrolyte enters the diversion liquid outlet channel 51 from the bottom of the diversion liquid outlet plate 5, and finally the electrolyte flows out to the external circulation liquid supply system through the diversion liquid outlet channel 51, that is, the circulation direction of the electrolyte is up-in and down-out, thereby ensuring that the electrolyte interacts more fully and completely with the cathode plate 2 and the anode plate 3, thereby improving the utilization rate and efficiency of the equipment. In addition, the second connecting pipe 6 connecting the external circulating liquid supply system and the balanced liquid inlet device 4 can also be set at one end of the balanced liquid inlet device 4 close to the liquid outlet 11, which makes it easier to connect the electrolytic cell to the external circulating liquid supply system and more convenient to operate.

[0034] A first bent portion 52 is provided at one end of the top of the liquid guiding plate 5 near the liquid outlet 11. The first bent portion 52 and the inner wall of the electrolytic cell body 1 form an outlet of a liquid guiding channel 51 connected to the liquid outlet 11, thereby ensuring that the electrolyte flows out more stably along the liquid guiding channel 51. The liquid guiding plate 5 usually has a second bent edge 53 connected to the inner wall of the electrolytic cell body 1, thereby facilitating the formation of the liquid guiding channel 51 and making the operation more convenient. The electrolytic cell body 1 is provided with a first connecting pipe 12 matched with the liquid outlet 11. The first connecting pipe 12 usually also has a threaded joint, thereby making it easier to connect to an external circulating liquid supply system and making the operation more convenient.

[0035] The diversion outlet plate 5 is provided with a plurality of partitions 54 along the vertical direction. The partitions 54 are located in the diversion outlet channel 51. The partitions 54 are arranged in sequence along the length direction of the diversion outlet plate 5. The top of the partition 54 is substantially flush with the bottom of the first bending portion 52, that is, the top of the partition 54 is substantially flush with the bottom of the outlet of the diversion outlet channel 51, thereby dividing the diversion outlet channel 51 into a plurality of channels. The electrolytes in different electrolysis intervals respectively enter different channels in the diversion outlet channel 51, thereby reducing mutual interference, being less likely to generate turbulence, and being more stable and reliable.

[0036] The cathode plate 2 and the anode plate 3 are respectively perpendicular to the balanced liquid inlet device 4 and the diversion liquid outlet plate 5 in the vertical direction, so that the electrolyte flows in parallel between the cathode plate 2 and the anode plate 3, and the flow direction of the electrolyte is respectively parallel to the cathode plate 2 and the anode plate 3, so that the electrolyte is more evenly distributed between the cathode plate 2 and the anode plate 3, reducing the flow of the electrolyte in other directions, without generating turbulence, and not easily causing agitation of the anode mud, so as to facilitate rapid sedimentation of the anode mud, and have higher stability and reliability.

[0037] The cross section of the drain port 402 is rectangular, the length direction of the drain port 402 is consistent with the vertical direction, the bottom of the drain port 402 is usually higher than the bottom of the liquid flow channel 401, and after the electrolyte enters the liquid flow channel 401, when the liquid level exceeds the bottom of the drain port 402, the electrolyte automatically and stably enters the interior of the electrolytic cell body 1 through the rectangular drain port 402. If the drain port 402 adopts other shapes such as V-shaped, the liquid inlet stability is relatively poor. In addition, the top of the liquid flow channel 401 and the top of the diversion and outlet channel 51 can be open or closed by corresponding cover plates.

[0038] like Figure 4 As shown, the first scheme of the balanced liquid inlet device 4, the balanced liquid inlet device 4 includes a liquid inlet box 41, a liquid flow channel 401 and a liquid discharge port 402 are arranged on the liquid inlet box 41, the liquid inlet box 41 can be directly fixed on the inner wall of the electrolytic cell body 1, the liquid inlet box 41 can also be installed on a panel 42, the panel 42 is installed on the inner wall of the electrolytic cell body 1, and the inner wall of the electrolytic cell body 1 can also be provided with a first trough 13 for placing the panel 42, which is convenient to operate and has a more stable and reliable structure. In addition, a mounting block 16 for fixing the liquid inlet box 41, such as a resin block, can be arranged on the inner wall of the electrolytic cell body 1, and the liquid inlet box 41 can also be provided with a reinforcing rib 411, so that when the liquid inlet box 41 is relatively long, the structural strength of the liquid inlet box 41 can also be ensured, which is more stable and reliable.

[0039] like Figure 5 As shown, the second scheme of the balanced liquid inlet device 4, the balanced liquid inlet device 4 includes a liquid inlet plate 43, the liquid inlet plate 43 and the inner wall of the electrolytic cell body 1 form a liquid flow channel 401, the liquid discharge port 402 is arranged on the liquid inlet plate 43, and the liquid inlet plate 43 can be fixed to the inner wall of the electrolytic cell body 1 by gluing, fastener connection, etc., the structure is simpler, more compact, and the operation is more convenient. The liquid inlet plate 43 is usually provided with a first bent edge 431 connected to the inner wall of the electrolytic cell body 1, so as to facilitate the formation of the liquid flow channel 401, and the operation is more convenient.

[0040] A sewage outlet 15 is also provided at the bottom of the electrolytic cell body 1 to facilitate the regular discharge of anode mud deposited in the electrolytic cell body 1, thereby improving the efficiency of electrolysis and making it more stable and reliable.

[0041] The outer side and the outer bottom of the electrolytic cell body 1 may also be provided with a plurality of supporting protrusions 14 , respectively. The number and position distribution of the supporting protrusions 14 are determined according to specific circumstances, so as to facilitate more stable placement of the electrolytic cell body 1 .

[0042] During use, the external circulation liquid supply system circulates and supplies liquid. The external circulation liquid supply system is connected to the liquid flow channel 401 of the balanced liquid inlet device 4 through the corresponding pipeline to supply liquid. The electrolyte entering the liquid flow channel 401 enters the interior of the electrolytic cell body 1 through multiple discharge ports 402. The rectangular discharge ports 402 facilitate the electrolyte to automatically and evenly enter the interior of the electrolytic cell body 1 from top to bottom, and then flow in parallel between the adjacent cathode plates 2 and anode plates 3, and are evenly distributed between the cathode plates 2 and anode plates 3, that is, each adjacent cathode plate 2 and anode plate 3 form an electrolysis interval, each electrolysis interval does not affect each other, the electrolyte flows stably and single, and turbulence is not easy to occur, and then the electrolyte enters the diversion outlet channel 51 from the bottom of the diversion outlet plate 5, and finally the electrolyte enters the diversion outlet channel 51 opposite the balanced liquid inlet device 4 and then flows out from the outlet 13 to the external circulation liquid supply system. Compared with the prior art, the present invention can ensure stable circulation of liquid inflow through the balanced liquid inlet device 4 and the diversion liquid outlet channel 51. The electrolyte enters the balanced liquid inlet device 4 and then exits the diversion liquid outlet channel 51 opposite to the balanced liquid inlet device 4, so that the electrolyte flow is the shortest, the electrolyte flow direction is stable and single, and the possibility of flowing in other directions is small, thereby improving the utilization rate of the electrolyte. Under the same current density conditions, the required circulation volume is smaller, and the required power consumption is reduced. Even if the electrolyte circulation volume is increased, the electrolyte in the electrolytic cell body 1 has no turbulence, and it is not easy to cause agitation of the anode mud. The concentration of suspended particles in the electrolyte is reduced, which is convenient for the rapid sedimentation of the anode mud, and the quality of the electrolytic product is improved. For example, the silver content in the cathode copper is reduced, and the recovery rate of precious metals is improved. In addition, the electrolyte nozzle is eliminated, and the electrolyte nozzle will not be easily blocked. After a long period of production, it is not easy to block the electrolyte outlet, and the production efficiency is high, and the stability and reliability are high.

[0043] The above are only some embodiments of the present disclosure, which are only used to illustrate the technical solution of the present disclosure, rather than to limit it. It should be understood that, for those skilled in the art, without departing from the creative concept of the present disclosure, it is possible to make improvements or substitutions according to the above description, and all these improvements and substitutions should fall within the scope of protection of the claims attached to the present disclosure. In this case, all details can be replaced by equivalent elements, and the materials, shapes and sizes can also be arbitrary.

Claims

1. An electrolytic cell with a balanced liquid inlet device, characterized in that: The invention comprises an electrolytic cell body (1) and at least one cathode plate (2) and an anode plate (3), wherein the cathode plate (2) and the anode plate (3) are arranged in sequence inside the electrolytic cell body (1) at intervals, a balanced liquid inlet device (4) is arranged on the inner wall of one side of the top of the electrolytic cell body (1), and a liquid guide plate (5) is arranged on the inner wall of the other side of the electrolytic cell body (1), the cathode plate (2) and the anode plate (3) are located between the balanced liquid inlet device (4) and the liquid guide plate (5), and the balanced liquid inlet device (4) is arranged on the inner wall of the other side of the electrolytic cell body (1). The liquid outlet plate (401) has a liquid flow channel (401) and a plurality of liquid discharge ports (402) evenly distributed along the length direction of the liquid flow channel (401); the liquid outlet plate (5) and the inner wall of the electrolytic cell body (1) form a liquid outlet channel (51); the liquid flow channel (401) enables electrolyte to enter the interior of the electrolytic cell body (1) in a balanced manner through the plurality of liquid discharge ports (402) and flow out through the liquid outlet channel (51); the liquid outlet plate (5) has a second bent edge (53) connected to the inner wall of the electrolytic cell body (1); The electrolyte entering the liquid flow channel automatically and evenly enters the interior of the electrolytic cell from top to bottom through multiple discharge ports, and then flows in parallel between adjacent cathode plates and anode plates, and is evenly distributed between the cathode plates and anode plates. Each adjacent cathode plate and anode plate forms an electrolysis zone, and each electrolysis zone does not affect each other. The balanced liquid inlet device (4) comprises a liquid inlet box (41), the liquid flow channel (401) and the liquid discharge port (402) are arranged on the liquid inlet box (41), or The balanced liquid inlet device (4) comprises a liquid inlet plate (43), wherein the liquid inlet plate (43) and the inner wall of the electrolytic cell body (1) enclose the liquid flow channel (401), the liquid discharge port (402) is arranged on the liquid inlet plate (43), and the liquid inlet plate (43) is provided with a first bent edge (431) that matches the inner wall of the electrolytic cell body (1).

2. The electrolytic cell with a balanced liquid inlet device according to claim 1, characterized in that: The inlet of the liquid diversion channel (51) is located at the bottom of the liquid diversion plate (5), and one end of the top of the electrolytic cell body (1) is provided with a liquid outlet (11) which is in communication with the liquid diversion channel (51).

3. The electrolytic cell with a balanced liquid inlet device according to claim 2, characterized in that: A first bent portion (52) is provided at one end of the top of the liquid guide plate (5) close to the liquid outlet (11); the first bent portion (52) and the inner wall of the electrolytic cell body (1) form an outlet of the liquid guide channel (51) that is in communication with the liquid outlet (11).

4. The electrolytic cell with a balanced liquid inlet device according to claim 1, characterized in that: The cathode plate (2) and the anode plate (3) are respectively perpendicular to the balanced liquid inlet device (4) and the liquid guide outlet plate (5) in a vertical direction.

5. An electrolytic cell with a balanced liquid inlet device according to any one of claims 1 to 4, characterized in that: The cross-section of the liquid discharge port (402) is rectangular, and the length direction of the liquid discharge port (402) is consistent with the vertical direction.

6. The electrolytic cell with a balanced liquid inlet device according to claim 1, characterized in that: The liquid inlet box (41) is mounted on a panel (42), and the panel (42) is mounted on the inner wall of the electrolytic cell body (1).

7. The electrolytic cell with a balanced liquid inlet device according to claim 6, characterized in that: A first tank body (13) for accommodating the panel (42) is provided on the inner wall of the electrolytic tank body (1).

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