Device for intercepting floating gold loss of vertical noble metal electrolytic bath and vertical noble metal electrolytic bath

Abstract

The utility model provides a device for intercepting floating gold loss of a vertical noble metal electrolytic bath and the vertical noble metal electrolytic bath, and relates to the technical field of electrolytic gold recovery. The device is integrally mounted in the vertical noble metal electrolytic bath and arranged between an inner electrolytic bath and an outer electrolytic bath, and comprises a first-stage high-temperature-resistant synthetic fiber filtering interception and liquid distribution system and a second-stage high-temperature-resistant synthetic fiber filtering interception and liquid distribution system, the first-stage high-temperature-resistant synthetic fiber filtering interception and liquid distribution system is arranged below a liquid outlet of the inner tank and is used for carrying out first-stage filtering on electrolytic barren liquor containing floating gold; and the second-stage high-temperature-resistant synthetic fiber filtering interception system is communicated with the first-stage high-temperature-resistant synthetic fiber filtering interception and liquid distribution system in a staggered manner, has a staggered height difference, and is used for performing second-stage filtering on the electrolytic barren liquor containing the floating gold after the first-stage filtering. And a two-stage filtering and intercepting integrated structure is adopted, so that the gold floating loss is effectively reduced, and the electrolysis recovery rate is increased.

Description

Technical Field

[0001] The utility model relates to the technical field of electrolytic gold recovery, in particular to a device for intercepting gold loss from a vertical precious metal electrolytic cell and a vertical precious metal electrolytic cell. Background Art

[0002] The process of electrolytic gold recovery from precious metal-containing liquids may cause the electrolytically deposited gold to not adhere well to the cathode due to the presence of flotation agents, frothers, etc. in the liquid phase. Alternatively, the fine gold powder formed during the electrolysis process will flow out of the electrolytic cell in the form of "floating gold" along with the electrolytic lean liquid under water disturbance, resulting in a certain amount of gold loss. Therefore, it is necessary to effectively recover the floating gold and improve the electrolytic recovery rate.

[0003] In view of this, it is necessary to study a device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell and a vertical precious metal electrolytic cell to solve the above technical problems. Utility Model Content

[0004] In view of the technical problems existing in the background technology, the utility model provides a device for intercepting the loss of gold from bleaching in a vertical precious metal electrolytic cell and a vertical precious metal electrolytic cell. The device intercepts the electrolytic lean liquid containing "bleaching gold" once through a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system (first-level filtration) and further distributes it to two second-level high-temperature resistant synthetic fiber filtration interception systems that are staggered and connected for secondary interception (second-level filtration), reducing the filtration amount step by step to effectively separate the "bleaching gold" from the electrolytic lean liquid. The filter tank is configured as a movable structure, which can be removed and cleaned when taking out the gold mud. The filter medium is made of high-temperature resistant synthetic fiber filter cotton, which is light and has good water permeability, stable performance and strong chemical resistance. It can withstand high temperatures of 220°C for a long time without shrinking or brittleness, and can be incinerated at 400°C for subsequent incineration and recovery. It is green, environmentally friendly and highly economical.

[0005] In a first aspect, an embodiment of the present invention provides a device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell. The device is integrally installed inside the vertical precious metal electrolytic cell and disposed between the inner electrolytic cell and the outer electrolytic cell. The device comprises a first-level high-temperature resistant synthetic fiber filtration and interception system and a second-level high-temperature resistant synthetic fiber filtration and interception system.

[0006] The first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is arranged below the liquid outlet of the inner tank and is used to perform the first-level filtration of the electrolytic lean liquid containing "bleaching gold";

[0007] The secondary high-temperature resistant synthetic fiber filtration and interception system is staggered and connected to the primary high-temperature resistant synthetic fiber filtration and interception and liquid distribution system and has a staggered height difference, and is used to perform a second-stage filtration on the electrolytic lean liquid containing "bleached gold" after the first-stage filtration.

[0008] As a further improvement of the present invention, the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system includes a first-level distribution filter tank and a liquid guide tank; the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system is staggeredly connected to the second-level high-temperature resistant synthetic fiber filtration interception system through the liquid guide tank.

[0009] As a further improvement of the present invention, the side of the first-level distribution filter tank is provided with several groups of liquid outlets with a horizontal height lower than the filter cross-section; the top of the liquid guide tank is connected to the liquid guide outlet, and the bottom is connected to the top water inlet of the second-level high-temperature resistant synthetic fiber filtration interception system.

[0010] As a further improvement of the present invention, the secondary high-temperature resistant synthetic fiber filtering and intercepting system includes several groups of secondary filter tanks.

[0011] As a further improvement of the present invention, the bottom and sides of the first-level distribution filter tank and the second-level filter tank are provided with filtrate discharge holes, and an elastic high-temperature resistant synthetic fiber cotton filter filler layer is laid inside.

[0012] As a further improvement of the present invention, the device for intercepting gold loss from bleaching in a vertical precious metal electrolytic cell further includes a filter tank support system disposed between the inner electrolytic cell and the outer electrolytic cell.

[0013] As a further improvement of the present invention, the filter tank support system includes a filter tank bracket and an inner tank reinforcement frame for movably supporting the first-level high-temperature resistant synthetic fiber filter interception and liquid distribution system and the second-level high-temperature resistant synthetic fiber filter interception system.

[0014] As a further improvement of the present invention, the filtrate drainage holes are arranged with a maximum drainage area; the aperture of the filtrate drainage holes is larger than the filter particle size of the elastic high-temperature resistant synthetic fiber cotton filter filler layer.

[0015] As a further improvement of the present invention, the first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is movably installed on the outer wall of the electrolytic inner tank; the second-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is symmetrically installed on the outer wall of the electrolytic inner tank adjacent to the first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system.

[0016] In a second aspect, an embodiment of the present invention provides a vertical precious metal electrolytic cell, which includes the above-mentioned device for intercepting gold loss from bleaching in a vertical precious metal electrolytic cell;

[0017] The device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell is integrally installed inside the vertical precious metal electrolytic cell and is arranged between the inner electrolytic cell and the outer electrolytic cell, and is movably connected to the inner electrolytic cell, and is used for performing secondary filtration on the electrolytic barren liquid containing "bleaching gold" to achieve the recovery of "bleaching gold".

[0018] Beneficial effects of the utility model:

[0019] 1. The device for intercepting gold loss from vertical precious metal electrolytic cells provided by the utility model adopts a two-stage filtering and intercepting integrated structure, which realizes the effective separation of fine particles of "gold loss" lost with the barren liquid in the vertical precious metal electrolytic cell from the barren liquid and intercepts them in the two-stage filter tank, effectively reducing the loss of "gold loss" and improving the electrolysis recovery rate.

[0020] 2. The utility model provides a device for intercepting gold loss in vertical precious metal electrolytic cells. The device intercepts the electrolytic lean liquid containing "gold loss" once through a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system (first-level filtration) and further distributes it to two second-level high-temperature resistant synthetic fiber filtration interception systems that are staggered and connected for secondary interception (second-level filtration). The filtration volume is gradually reduced to effectively separate the "gold loss" from the electrolytic lean liquid. The filter tank is configured as a movable structure, which can be removed and cleaned when taking out the gold mud. The filter medium is made of high-temperature resistant synthetic fiber filter cotton, which is light and has good water permeability. It has stable performance and strong chemical resistance. It can withstand high temperatures of 220°C for a long time without shrinking or becoming brittle. It can be incinerated at 400°C for subsequent incineration and recovery. It is green, environmentally friendly and highly economical.

[0021] The above description is only an overview of the technical solution of the present invention. In order to more clearly understand the technical means of the present invention, it can be implemented in accordance with the contents of the specification. In order to make the above and other purposes, features and advantages of the present invention more obvious and easy to understand, the specific implementation methods of the present invention are listed below. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] In order to more clearly illustrate the technical solution of the present invention, the following is a brief introduction to the drawings used in the present invention. Obviously, the drawings described below are only some embodiments of the present invention. For those skilled in the art, other drawings can be derived from these drawings without inventive effort.

[0023] Figure 1 This is a side view of a device for intercepting gold loss from a vertical precious metal electrolytic cell provided by an embodiment of the utility model, installed in the vertical precious metal electrolytic cell;

[0024] Figure 2 This is a top view of a device for intercepting gold loss from a vertical precious metal electrolytic cell provided by an embodiment of the utility model, installed in the vertical precious metal electrolytic cell;

[0025] Description of reference numerals:

[0026] 1. Electrolytic inner tank; 2. Inner tank reinforcement frame; 3. Liquid inlet; 4. Pressure-bearing shell and sealing flange; 5. Plates; 6. Inner tank liquid outlet; 7. Liquid guide tank; 8. Primary distribution filter tank; 9. Filter tank bracket; 10. Secondary filter tank; 11. Filtrate discharge hole; 12. High-temperature resistant synthetic fiber filter cotton filler layer. DETAILED DESCRIPTION

[0027] The following embodiments of the technical solution of the present invention are described in detail with reference to the accompanying drawings. The following embodiments are only used to more clearly illustrate the technical solution of the present invention and are therefore only examples and are not intended to limit the scope of protection of the present invention.

[0028] Unless otherwise defined, all technical and scientific terms used herein have the same meanings as those commonly understood by those skilled in the art to which this invention pertains; the terms used herein are for the purpose of describing specific embodiments only and are not intended to limit this invention; the terms "including" and "having" and any variations thereof in the specification and claims of this invention and the above-mentioned drawings are intended to cover non-exclusive inclusions.

[0029] In the description of the embodiments of this utility model, the technical terms "first" and "second" are used only to distinguish different objects and should not be understood to indicate or imply relative importance or implicitly specify the quantity, specific order, or primary and secondary relationship of the technical features indicated. In the description of the embodiments of this utility model, the meaning of "plurality" is more than two, unless otherwise clearly and specifically defined.

[0030] References to "embodiments" herein mean that a particular feature, structure, or characteristic described in connection with the embodiments may be included in at least one embodiment of the present invention. The appearance of this phrase in various places in the specification does not necessarily refer to the same embodiment, nor does it constitute an independent or alternative embodiment that is mutually exclusive of other embodiments. It is understood, both explicitly and implicitly, by those skilled in the art that the embodiments described herein may be combined with other embodiments.

[0031] In the description of the embodiments of the present invention, the term "and / or" is simply a description of the association relationship between related objects, indicating that three relationships can exist. For example, A and / or B can represent three situations: A exists alone, A and B exist simultaneously, and B exists alone. In addition, the character " / " in this document generally indicates that the related objects are in an "or" relationship.

[0032] In the description of the embodiments of the present invention, the term "multiple" refers to more than two (including two). Similarly, "multiple groups" refers to more than two groups (including two groups), and "multiple pieces" refers to more than two pieces (including two pieces).

[0033] In the description of the embodiments of the present invention, the technical terms "center", "longitudinal", "lateral", "length", "width", "thickness", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inside", "outside", "clockwise", "counterclockwise", "axial", "radial", "circumferential", etc., indicating the orientation or position relationship, are based on the orientation or position relationship shown in the accompanying drawings, and are only for the convenience of describing the embodiments of the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operate in a specific orientation, and therefore cannot be understood as a limitation on the embodiments of the present invention.

[0034] In the description of the embodiments of the present invention, unless otherwise expressly specified or limited, technical terms such as "installed," "connected," "connect," and "fixed" should be understood in a broad sense. For example, they can refer to fixed connection, detachable connection, or integration; mechanical connection or electrical connection; direct connection or indirect connection through an intermediate medium; internal communication between two components or interaction between two components. For those skilled in the art, the specific meanings of the above terms in the embodiments of the present invention can be understood according to specific circumstances.

[0035] In order to solve the technical problem of gold loss from bleaching in precious metal electrolytic cells, the utility model provides a device for intercepting gold loss from bleaching in a vertical precious metal electrolytic cell and a vertical precious metal electrolytic cell. The device intercepts the electrolytic lean liquid containing "bleaching gold" through a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system (first-level filtration) and further distributes it to two second-level high-temperature resistant synthetic fiber filtration interception systems that are staggered and connected for secondary interception (second-level filtration), reducing the filtration volume step by step to effectively separate the "bleaching gold" from the electrolytic lean liquid. The filter tank is configured as a movable structure that can be removed and cleaned when taking out the gold mud. The filter medium, high-temperature resistant synthetic fiber filter cotton, is lightweight and has good water permeability, stable performance, and strong chemical resistance. It can withstand high temperatures of 220°C for a long time without shrinking or becoming brittle, and can be incinerated at 400°C for subsequent incineration and recovery. It is green, environmentally friendly, and highly economical.

[0036] Example 1

[0037] See also Figures 1 to 2 As shown, Example 1 of the utility model provides a device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell, which is installed as a whole inside the vertical precious metal electrolytic cell and arranged between the inner electrolytic cell 1 and the outer electrolytic cell, and includes a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system, a second-level high-temperature resistant synthetic fiber filtration interception system, and a filter cell support system.

[0038] Among them, the first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is arranged below the inner tank liquid outlet 6, and is used for the first-level filtration of the electrolytic lean liquid containing "bleaching gold".

[0039] The secondary high-temperature resistant synthetic fiber filtration and interception system is staggered and connected to the primary high-temperature resistant synthetic fiber filtration and interception and liquid distribution system and has a staggered height difference, and is used to perform a second-stage filtration on the electrolytic lean liquid containing "bleached gold" after the first-stage filtration.

[0040] The filter tank support system is arranged between the inner electrolytic tank 1 and the outer electrolytic tank, and is used to movably support the first-level high-temperature resistant synthetic fiber filtering and intercepting liquid distribution system and the second-level high-temperature resistant synthetic fiber filtering and intercepting system.

[0041] In some embodiments, the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system includes a first-level distribution filter tank 8 and a liquid guide tank 7; the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system and the second-level high-temperature resistant synthetic fiber filtration interception system are staggered and connected through the liquid guide tank 7.

[0042] The side of the first-level distribution filter tank 8 is provided with several groups of liquid outlets with a horizontal height lower than the filter cross-section; the top of the liquid guide tank 7 is connected to the liquid guide outlet, and the bottom is connected to the top water inlet of the second-level high-temperature resistant synthetic fiber filter interception system.

[0043] The first-level distribution filter tank 8 is installed below the inner tank liquid outlet 6, and filtrate discharge holes 11 are provided on the bottom and side surfaces thereof, and an elastic high-temperature resistant synthetic fiber filter cotton filler layer 12 is laid inside.

[0044] In some embodiments, the primary distribution filter 8 performs the first-stage interception of the "gold bleaching" lean liquid, which is then discharged into the lower portion of the pressure housing through the bottom filtrate discharge hole 11. Due to the limited interception area of the primary distribution filter 8, the "gold bleaching" electrolytic lean liquid is not intercepted in time. Instead, it is diverted into two liquid guide slots 7 through the horizontal outlets provided on both sides of the primary distribution filter 8 and at the bottom of the water flow section for secondary filtration and interception.

[0045] The secondary high-temperature resistant synthetic fiber filtering and intercepting system includes several groups of secondary filter tanks 10.

[0046] The secondary filter tank 10 has filtrate discharge holes 11 on the bottom and sides, and a high-temperature resistant synthetic fiber filter cotton filler layer 12 is laid inside. The difference from the primary distribution filter tank 8 is that the secondary filter tank 10 has no liquid outlet on both sides, and the upper edges of the sides are horizontal.

[0047] The filtrate discharge holes 11 should be arranged with the maximum drainage area while meeting the processing technology requirements; the aperture of the filtrate discharge holes 11 is larger than the filter particle size of the high-temperature resistant synthetic fiber filter cotton filler layer 12.

[0048] The "bleached gold" accumulated in the first-level distribution filter tank 8 and the second-level filter tank 10 is taken out together with the gold mud, and the gold is recovered after washing with water, and the high-temperature resistant synthetic fiber filter cotton filling layer 12 is reused and can be used repeatedly.

[0049] The filter tank support system includes a filter tank bracket 9 and an inner tank reinforcement frame 2 for movably supporting the first-level high-temperature resistant synthetic fiber filtering and intercepting liquid distribution system and the second-level high-temperature resistant synthetic fiber filtering and intercepting system.

[0050] The first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is movably installed on the outer wall of the electrolytic inner tank 1 through the filter tank bracket 9; the second-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is symmetrically installed on the outer wall of the electrolytic inner tank 1 adjacent to the first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system through the inner tank reinforcement frame 2.

[0051] The working process of the device for intercepting gold loss in a vertical precious metal electrolytic cell provided by the utility model is as follows:

[0052] The precious metal-containing liquid enters the electrolytic inner tank 1 through the liquid inlet 3 for electrolytic gold deposition. During the process of electrolytic gold recovery from the precious metal-containing liquid, the electrolytically deposited gold may not adhere well to the cathode due to the presence of flotation agents, foaming agents, etc. in the liquid phase, or the fine gold powder formed during the electrolysis process may flow out of the electrolytic tank in the form of "bleached gold" along with the electrolytic lean liquid under the disturbance of the water flow. Therefore, a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system is installed below the inner tank liquid outlet 6 of the vertical electrolytic inner tank 1 through several filter tank brackets 9. When the electrolytic lean liquid containing "bleached gold" passes through the first-level distribution filter tank 8, it is intercepted by the high-temperature resistant synthetic fiber filter cotton packing layer 12, and the clear liquid enters the lower part of the vertical pressure electrolytic outer tank through the filtrate discharge holes 11 set at the bottom and side, realizing the first-level filtration.

[0053] The electrolytic lean liquid containing "bleached gold" that was not filtered in time during the first stage of filtration is evenly distributed into the two liquid guide grooves 7 through the liquid outlets opened on the two sides of the first-level distribution filter tank 8, and then enters the secondary filter tanks 10 of the two secondary high-temperature resistant synthetic fiber filtration and interception systems. The electrolytic lean liquid containing "bleached gold" that was not filtered in time during the first stage of filtration passes through the high-temperature resistant synthetic fiber filter cotton filler layer 12. After the second stage of filtration, the clean lean liquid is also discharged into the lower part of the vertical pressure electrolytic outer tank through the filtrate discharge holes 11 set at the bottom and sides, thereby achieving complete interception of the "bleached gold".

[0054] The "bleached gold" accumulated in the first-level distribution filter tank 8 and the second-level filter tank 10 is taken out together with the gold mud, and the gold is recovered after washing with water. The high-temperature resistant synthetic fiber filter cotton filling layer 12 is reused and can be used repeatedly. When it needs to be finally disposed of, the gold is recovered after ashing.

[0055] Example 2

[0056] Embodiment 2 of the present invention provides a vertical precious metal electrolytic cell, which includes the above-mentioned device for intercepting gold loss in a vertical precious metal electrolytic cell;

[0057] The device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell is integrally installed inside the vertical precious metal electrolytic cell and is arranged between the inner electrolytic cell 1 and the outer electrolytic cell, and is movably connected to the inner electrolytic cell 1, and is used for performing secondary filtration on the electrolytic barren liquid containing "bleaching gold" to achieve the recovery of "bleaching gold".

[0058] In summary, the utility model provides a device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell and a vertical precious metal electrolytic cell, and relates to the technical field of electrolytic gold recovery. The device is installed as a whole inside the vertical precious metal electrolytic cell and is arranged between the inner electrolytic cell and the outer electrolytic cell, and includes a first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system and a second-level high-temperature resistant synthetic fiber filtration interception system; the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system is arranged below the liquid outlet of the inner cell, and is used for performing a first-level filtration of the electrolytic lean liquid containing "bleaching gold"; the second-level high-temperature resistant synthetic fiber filtration interception system is staggered and connected to the first-level high-temperature resistant synthetic fiber filtration interception and liquid distribution system and has a staggered height difference, and is used for performing a second-level filtration of the electrolytic lean liquid containing "bleaching gold" after the first-level filtration. The device intercepts the electrolytic lean liquid containing "bleached gold" through a first-level high-temperature resistant synthetic fiber filtration and interception and liquid distribution system (first-level filtration) and further distributes it to two second-level high-temperature resistant synthetic fiber filtration and interception systems that are staggered and connected for secondary interception (second-level filtration). The filtration volume is gradually reduced to effectively separate the "bleached gold" from the electrolytic lean liquid. The filter tank is configured as a movable structure that can be removed and cleaned when removing the gold mud. The filter medium, high-temperature resistant synthetic fiber filter cotton, is lightweight and has good water permeability, stable performance, and strong chemical resistance. It can withstand high temperatures of 220°C for a long time without shrinking or becoming brittle, and can be incinerated at 400°C for subsequent incineration and recovery. It is green, environmentally friendly, and highly economical.

[0059] It should be noted that the present invention is not limited to the above-described embodiments. The above-described embodiments are merely examples, and any embodiments having substantially the same structure and effect as the technical concept within the scope of the present invention are included within the technical scope of the present invention. Furthermore, within the scope of the present invention, various modifications that can be conceived by those skilled in the art to the embodiments, and other configurations constructed by combining some of the components of the embodiments are also included within the scope of the present invention.

Claims

1. A device for intercepting gold loss from vertical precious metal electrolytic cells, characterized in that: The whole system is installed inside the vertical precious metal electrolytic cell and is arranged between the inner electrolytic cell and the outer electrolytic cell, and includes a first-level high-temperature resistant synthetic fiber filtration and interception and liquid distribution system and a second-level high-temperature resistant synthetic fiber filtration and interception system; The first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is arranged below the liquid outlet of the inner tank and is used to perform the first-level filtration of the electrolytic lean liquid containing "bleaching gold"; The secondary high-temperature resistant synthetic fiber filtration and interception system is staggered and connected to the primary high-temperature resistant synthetic fiber filtration and interception and liquid distribution system and has a staggered height difference, and is used to perform a second-stage filtration on the electrolytic lean liquid containing "bleached gold" after the first-stage filtration.

2. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 1, characterized in that: The first-level high-temperature resistant synthetic fiber filter interception and liquid distribution system includes a first-level distribution filter tank and a liquid guide tank; the first-level high-temperature resistant synthetic fiber filter interception and liquid distribution system is staggeredly connected to the second-level high-temperature resistant synthetic fiber filter interception system through the liquid guide tank.

3. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 2, characterized in that: The side of the first-level distribution filter tank is provided with several groups of liquid outlets with a horizontal height lower than the filter section; the top of the liquid guide tank is connected to the liquid guide outlet, and the bottom is connected to the top water inlet of the second-level high-temperature resistant synthetic fiber filter interception system.

4. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 3, characterized in that: The secondary high-temperature resistant synthetic fiber filtering and intercepting system includes several groups of secondary filter tanks.

5. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 2 or 4, characterized in that: The bottom and side of the first-level distribution filter tank and the second-level filter tank are both provided with filtrate discharge holes, and elastic high-temperature resistant synthetic fiber cotton filter filler layers are laid inside.

6. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 1, characterized in that: The device for intercepting gold loss from leaching in a vertical precious metal electrolytic cell further comprises a filter cell support system arranged between the inner electrolytic cell and the outer electrolytic cell.

7. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 6, characterized in that: The filter tank support system includes a filter tank bracket and an inner tank reinforcement frame for movably supporting a first-level high-temperature resistant synthetic fiber filter interception and liquid distribution system and a second-level high-temperature resistant synthetic fiber filter interception system.

8. The device for intercepting gold loss from bleaching in a vertical precious metal electrolytic cell according to claim 5, characterized in that: The filtrate drainage holes are arranged with a maximum drainage area; the aperture of the filtrate drainage holes is larger than the filter particle diameter of the elastic high-temperature resistant synthetic fiber cotton filter filler layer.

9. The device for intercepting gold loss from vertical precious metal electrolytic cells according to claim 1, characterized in that: The first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is movably installed on the outer wall of the electrolytic inner tank; the second-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system is symmetrically installed on the outer wall of the electrolytic inner tank adjacent to the first-level high-temperature resistant synthetic fiber filtering, intercepting and liquid distribution system.

10. A vertical precious metal electrolytic cell, characterized in that: A device for intercepting gold loss in a vertical precious metal electrolytic cell according to any one of claims 1 to 9; The device for intercepting gold loss caused by bleaching in a vertical precious metal electrolytic cell is integrally installed inside the vertical precious metal electrolytic cell and is arranged between the inner electrolytic cell and the outer electrolytic cell, and is movably connected to the inner electrolytic cell to perform secondary filtration on the electrolytic barren liquid containing "bleaching gold" to achieve the recovery of "bleaching gold".

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