CN220758317U - Multilayer deoiling device for solution - Google Patents
Multilayer deoiling device for solution Download PDFInfo
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- CN220758317U CN220758317U CN202321834604.7U CN202321834604U CN220758317U CN 220758317 U CN220758317 U CN 220758317U CN 202321834604 U CN202321834604 U CN 202321834604U CN 220758317 U CN220758317 U CN 220758317U
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000000945 filler Substances 0.000 claims abstract description 8
- 230000003014 reinforcing effect Effects 0.000 claims abstract description 8
- 238000001914 filtration Methods 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 10
- 239000011148 porous material Substances 0.000 claims description 10
- 239000000835 fiber Substances 0.000 claims description 9
- 238000011049 filling Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 3
- 238000005238 degreasing Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 9
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 230000035425 carbon utilization Effects 0.000 abstract description 3
- 239000011120 plywood Substances 0.000 abstract description 3
- 229910017053 inorganic salt Inorganic materials 0.000 abstract description 2
- 239000010410 layer Substances 0.000 description 51
- 239000000243 solution Substances 0.000 description 27
- 238000000605 extraction Methods 0.000 description 7
- 239000012071 phase Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000004804 winding Methods 0.000 description 6
- 238000001179 sorption measurement Methods 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 4
- -1 polypropylene Polymers 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 3
- 239000012074 organic phase Substances 0.000 description 3
- 229920000742 Cotton Polymers 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- 239000013354 porous framework Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
Abstract
The utility model discloses a multilayer oil removing device for a solution, and relates to the technical field of inorganic salt oil removing. The utility model comprises an outer structure and an inner structure, wherein the inner part of the outer structure is provided with the inner structure; the external structure comprises a tank body, a liquid inlet valve, a liquid outlet valve, a fine filter, a filler port, a discharge port and a fixed plate; the internal structure comprises a filter screen, a porous laminate and a reinforcing bolt. The inside of the shell is connected with the filter screen, the porous laminate and the reinforcing bolt through the fixing plate. According to the utility model, through the external structure and the internal structure, the problem of insufficient equipment space in the factory field is solved, and the field space is saved; through the additional plywood of inner structure, two-layer deoiling material (including but not limited to active carbon, can be other suitable materials) need not change simultaneously, have promoted equipment utilization efficiency, have promoted active carbon utilization ratio simultaneously, save the material, reduce material loss.
Description
Technical Field
The utility model belongs to the technical field of inorganic salt oil removal, and particularly relates to a device in the field of solution oil removal.
Background
The common noble metal purification and multipurpose extraction method is that noble metals are rare in nature and need to be recovered for reuse. Precipitation, extraction, ion exchange, electrolysis, etc. are often used in the art in extraction and repeated recovery processes. Extraction methods are often used to extract valuable metals from aqueous solutions or as an important means of solution purification. Compared with other separation methods such as precipitation methods, the extraction method has the advantages of high extraction and separation efficiency, less reagent consumption, high recovery rate, large production capacity, simple equipment, easy realization of automation and continuity and the like, and is increasingly widely applied in the departments of hydrometallurgy, petrochemical industry, environmental protection and the like in recent years. When the organic phase and the water phase are fully contacted in the extraction process, certain metals in the water phase can be selectively transferred to the organic phase to achieve the aim of removing impurities, the solution after the impurities are discharged as the water phase, but the water phase discharged during the two-phase separation can be inevitably brought into part of the organic phase, so that the oil index in the water phase is higher, an oil removing device is needed to be arranged for purifying the water phase, the existing equipment mostly adopts an active carbon tank for removing the oil, but in the practical use, the equipment has the following defects: the device occupies large space, has high replacement frequency and low efficiency.
The device solves the problem of insufficient equipment space in the factory field by arranging the oil removing device from a single layer to a plurality of layers, thereby saving the field space; through the inside subassembly increase plywood, promoted equipment utilization efficiency, promoted active carbon utilization ratio simultaneously, saved the material, reduce the loss.
Disclosure of Invention
The utility model aims to provide a multilayer oil removing device for solution, which solves the problem of insufficient equipment space in a factory field and saves the field space through an external structure and an internal component; through the inside subassembly increase plywood, promoted equipment utilization efficiency, promoted active carbon utilization ratio simultaneously, saved the material, reduce the loss.
In order to solve the technical problems, the utility model is realized by the following technical scheme:
the utility model relates to a solution multilayer oil removing device, which comprises an external structure and an internal component, wherein the external structure is as follows: the tank body, the inlet, the drain valve, the fine filter, the filler mouth, the bin outlet, fixed plate.
The tank body is divided into three layers in the middle, a liquid inlet is formed in the right side of the first layer at the lowest part, a discharge valve is arranged at the bottom of the other side, a filling port is formed in the middle upper part of the same side of the discharge valve, the middle of the second layer of the first layer is separated from the middle of the second layer through a filter screen and a multi-layer pore plate, and the filter screen and the multi-layer pore plate are fixed on a fixed plate through 4 reinforcing bolts. The solution enters the first layer through the feed inlet, and the impurity overflows to the second layer through the filter screen and the porous laminate filter by the active carbon preliminary filtration.
The second layer inside the tank body can be filled with activated carbon through the filler opening, and when activated carbon adsorption saturation needs to be replaced, the activated carbon can be discharged through the discharge opening of the second layer. The sulfate is filtered for the first time through the first layer, filtered again through the second layer, and the two layers of activated carbon adsorption saturation time is different, so that the first layer and the second layer can be replaced separately by using the device.
And a third layer in the tank body can be filled with a proper amount of fiber balls through a third layer filling port, and the fiber balls are utilized to carry out third filtration, so that large particulate matters carried by the solution passing through the first layer and the second layer or filtered out are trapped, and the solution is purified.
The uppermost part of the tank body is connected with a solution discharge pipeline, solution enters through the lower part of the tank body, is subjected to three-stage filtration, a liquid outlet valve is opened, and the solution passes through a precision filter to obtain clear oil-free solution without large-particle impurities, and is discharged through the pipeline to enter the next working procedure. The square fine filter arranged at the outlet of the pipeline is internally provided with a group of winding filter cores, the winding filter cores are deep-layer filter cores and are used for filtering with low viscosity and low impurity amount, and the square fine filter is made by winding textile fiber wires (polypropylene wires, cotton wool wires and the like) on a porous framework (polypropylene or stainless steel) precisely according to a specific process.
The utility model has the following beneficial effects:
1. according to the utility model, through arranging an external structure and an internal component, through activated carbon adsorption and fiber ball filtration, the treatment is carried out step by step aiming at the difference of the existence form and physical properties of oil in the solution, and the device is used without adding an oil removing agent, so that the solution after oil removal is not introduced with new impurities and suspended matters, the solution is not changed in the oil removal process, the replacement amount of the activated carbon is reduced, and the generation of three wastes is reduced.
2. According to the utility model, by arranging the external structure and the internal components, the multi-layer composite structure of the device is utilized to replace the saturated materials with high loads on each layer in a segmented manner, so that the utilization efficiency of the materials is improved, the loss is reduced, and the materials are saved.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
in the drawings, the list of components represented by the various numbers is as follows:
1. external structure: the liquid inlet valve (1), the tank body (2), the liquid outlet valve (3), the fine filter (4), the filler port (5), the discharge port (6) and the fixed plate (7);
2. the inner assembly comprises a filter screen (8), a multi-layer pore plate (9) and a reinforcing bolt (10).
Detailed Description
The technical solutions in the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model.
Referring to fig. 1, the present utility model is a solution multi-layer degreasing device, which includes an outer structure and an inner component, wherein the inner component is disposed inside the outer structure;
1. the external structure comprises a liquid inlet valve (1), a tank body (2), a liquid outlet valve (3), a fine filter (4), a filler port (5), a discharge port (6) and a fixed plate (7);
2. the inner assembly comprises a filter screen (8), a multi-layer pore plate (9) and a reinforcing bolt (10).
The tank body is divided equally into three layers in the inside, the first layer is arranged at the bottom, a liquid inlet (1) is formed in the right side of the tank body, a discharging valve (6) is arranged at the bottom of the other side of the tank body, a filler opening (5) is formed in the middle upper part of the same side of the discharging valve (6), the middle of the first layer and the middle of the second layer are separated by a filter screen (8) and a multi-layer pore plate (9), and the filter screen (8) and the multi-layer pore plate (9) are reinforced on a fixed plate (7) through 4 reinforcing bolts (10). The solution enters the first layer through a feed valve, and overflows to the second layer through a filter screen (8) and a porous layer plate (9) through active carbon (the deoiling substance used for the second layer of the first layer comprises but is not limited to active carbon and can be any applicable deoiling substance).
The second layer inside the tank body can be filled with activated carbon through a filler port of the second layer, and when the activated carbon is saturated in adsorption and needs to be replaced, the activated carbon can be discharged through a discharge port of the second layer. The sulfate is filtered for the first time through the first layer, filtered again through the second layer, and the two layers of activated carbon adsorption saturation time is different, so that the first layer and the second layer can be replaced separately by using the device.
And a third layer in the tank body can be filled with a proper amount of fiber balls through a third layer filling port, and the fiber balls are utilized to carry out third filtration, so that large particulate matters carried by the solution passing through the first layer and the second layer or filtered out are trapped, and the solution is purified.
The solution discharge pipeline is connected to the uppermost part of the tank body, solution enters through the lower part of the tank body, is subjected to three-stage filtration, and is opened to the liquid outlet valve (3), and the solution passes through the precision filter (4) to obtain clear oil-free solution without large-particle impurities. The square fine filter arranged at the outlet of the pipeline is internally provided with a group of winding filter cores, the winding filter cores are deep-layer filter cores and are used for filtering with low viscosity and low impurity amount, and the square fine filter is made by winding textile fiber wires (polypropylene wires, cotton wool wires and the like) on a porous framework (polypropylene or stainless steel) precisely according to a specific process.
The foregoing is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, and any modification, equivalent replacement, and improvement of some of the technical features described in the foregoing embodiments are all within the scope of the present utility model. The multilayer oil removing device is not limited to deep oil removal of sulfate solution, and can be used for solution oil removal of any system.
Claims (2)
1. A solution multilayer deoiling device comprises an external structure and an internal component, and is characterized in that: the inside of the external structure is provided with an internal component, and the external structure comprises a tank body (2), a liquid inlet (1), a liquid outlet valve (3), a fine filter (4), a filler opening (5) and a discharge opening (6); the internal space of the tank body is equally divided into three layers, and the three layers are divided by an internal component, wherein the internal component comprises a fixed plate (7), a filter screen (8), a multi-layer pore plate (9) and a reinforcing bolt (10).
2. The solution multilayer degreasing device according to claim 1, characterized in that: the inside of the tank body is divided into three layers, each layer is provided with a discharge opening and a filling opening, the lowest layer is a first layer, the right side of the tank body is provided with a liquid inlet (1), the bottom of the other side of the tank body is provided with a discharge opening (6), and the middle upper part of the same side of the discharge opening (6) is provided with a filling opening (5); a filter screen (8) and a multi-layer pore plate (9) are arranged in the middle of the second layer of the first layer, the filter screen (8) and the multi-layer pore plate (9) are fixed on the fixed plate (7) through 4 reinforcing bolts (10), a solution enters the first layer through the liquid inlet (1), and impurities are filtered through the filter screen (8) and the multi-layer pore plate (9) by preliminary filtration of activated carbon and overflowed to the second layer; a third layer in the tank body can be filled with a proper amount of fiber balls through a filling port of the third layer, and the fiber balls are utilized for third filtering; the uppermost end of the device is provided with a liquid outlet valve (3), the liquid outlet valve (3) is opened, the solution passes through a fine filter (4) to obtain oil-free clear solution without large-particle impurities, and the clear solution is discharged through a pipeline to enter the next working procedure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321834604.7U CN220758317U (en) | 2023-07-13 | 2023-07-13 | Multilayer deoiling device for solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321834604.7U CN220758317U (en) | 2023-07-13 | 2023-07-13 | Multilayer deoiling device for solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220758317U true CN220758317U (en) | 2024-04-12 |
Family
ID=90618870
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321834604.7U Active CN220758317U (en) | 2023-07-13 | 2023-07-13 | Multilayer deoiling device for solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220758317U (en) |
-
2023
- 2023-07-13 CN CN202321834604.7U patent/CN220758317U/en active Active
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