CN219701230U - Emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system - Google Patents
Emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system Download PDFInfo
- Publication number
- CN219701230U CN219701230U CN202320402682.3U CN202320402682U CN219701230U CN 219701230 U CN219701230 U CN 219701230U CN 202320402682 U CN202320402682 U CN 202320402682U CN 219701230 U CN219701230 U CN 219701230U
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- China
- Prior art keywords
- emulsifier
- filter
- tank
- pipeline
- impurity removing
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- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 89
- 239000012535 impurity Substances 0.000 title claims abstract description 86
- 238000001914 filtration Methods 0.000 title claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 239000000126 substance Substances 0.000 claims description 17
- 238000006243 chemical reaction Methods 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 5
- 230000001351 cycling effect Effects 0.000 claims description 3
- 238000005202 decontamination Methods 0.000 claims 1
- 230000003588 decontaminative effect Effects 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 26
- 229910052742 iron Inorganic materials 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 10
- 238000000034 method Methods 0.000 description 5
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 4
- 235000003891 ferrous sulphate Nutrition 0.000 description 3
- 239000011790 ferrous sulphate Substances 0.000 description 3
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 3
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 150000001491 aromatic compounds Chemical group 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007764 o/w emulsion Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000007762 w/o emulsion Substances 0.000 description 1
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
The utility model discloses an emulsifier temperature dynamic regulation circulation filtration impurity removal system, which belongs to the technical field of emulsifier impurity removal and comprises the following components: first support column, second support column, circulation filtration structure, accuse temperature storage structure, chemistry edulcoration structure, circulation filtration structure and chemistry edulcoration structure pipe connection, chemistry edulcoration structure is fixed in the second support column top, accuse temperature storage structure pipe connection is in chemistry edulcoration structure bottom, and this emulsifier temperature dynamic adjustment circulation filtration edulcoration system can adjust control emulsifier heating temperature, conveniently stores, can circulate partial impurity in the filtration emulsifier, reduces the human cost, can get rid of the iron fillings in the emulsifier manufacturing process simultaneously, improves the practicality of product.
Description
Technical Field
The utility model belongs to the technical field of emulsifier impurity removal, and particularly relates to an emulsifier temperature dynamic adjustment circulation filtration impurity removal system.
Background
In real life, various fabrics are woven into various clothes, the fabrics are required to be dyed in the process, and an emulsifying agent is added in the dyeing process to enable the dyeing to be uniform and stable. Emulsifiers are part of a broader group of compounds known as surfactants or "surfactants". Surfactants (emulsifiers) are typically amphiphilic compounds, meaning that they have a polar or hydrophilic (i.e. water-soluble) moiety and a non-polar (i.e. hydrophobic or lipophilic) moiety. Therefore, the emulsifier has certain solubility in water or oil, the emulsifier which is more soluble in water (on the contrary, is more insoluble in oil) usually forms an oil-in-water emulsion, and the emulsifier which is more soluble in oil usually forms a water-in-oil emulsion, and most of the emulsifier is manufactured by mechanical equipment in the process of manufacturing the emulsifier, so that solid particle impurities such as scrap iron and the like are easy to exist in the emulsifier, and most of the emulsifier is subjected to centrifugal filtration, so that only a small part of impurities can be removed, meanwhile, the prior art lacks a circulating filtration process, and can achieve a good impurity removal effect, the labor cost is increased, and on the other hand, the emulsifier is not regulated in structure of heating temperature after being manufactured, so that the emulsifier is unstable, the quality is not guaranteed, and is inconvenient to store.
Disclosure of Invention
The utility model aims to provide an emulsifying agent temperature dynamic regulation circulation filtering and impurity removing system, which can regulate and control the heating temperature of an emulsifying agent, is convenient to store, can circularly filter part of impurities in the emulsifying agent, reduces labor cost, can remove scrap iron in the emulsifying agent manufacturing process, and improves the practicability of products.
In order to achieve the above purpose, the present utility model provides the following technical solutions: an emulsifier temperature dynamic adjustment cycling filter impurity removal system, the emulsifier temperature dynamic adjustment cycling filter impurity removal system comprising: the chemical impurity removing device comprises a first supporting column, a second supporting column, a circulating filtering structure, a temperature control storage structure and a chemical impurity removing structure, wherein the circulating filtering structure is connected with the chemical impurity removing structure through a pipeline, the chemical impurity removing structure is fixed at the top end of the second supporting column, the temperature control storage structure is connected with the bottom end of the chemical impurity removing structure through a pipeline, and the first supporting column is arranged between the chemical impurity removing structure and the circulating filtering structure.
Further, the circulating filter structure comprises a filter tank, a filter pipeline is arranged at the bottom end of the filter tank, a circulating pipeline is arranged on the side face of the filter pipeline, the circulating pipeline penetrates through an inner pipeline of the impurity removal tank to be connected with a pressure pump, and a wire of the pressure pump is connected with a second driving motor.
Further, the filter pipeline is internally provided with a filter screen, the bottom end of the filter screen is provided with a filter element, and the top end of the filter tank is provided with a feed inlet.
Further, the temperature control storage structure comprises a storage box, the storage box is connected to the bottom end of the impurity removal tank through a pipeline, a first driving motor is arranged in the storage box, and a heating screw rod is connected with the first driving motor through a wire.
Further, the chemical impurity removing structure comprises an impurity removing tank, wherein a reaction basin body is arranged in the impurity removing tank, and the impurity removing tank is connected to the bottom end of the filtering tank through a pipeline.
Further, a separation plate is arranged in the reaction basin body.
The beneficial effects of the utility model are as follows:
1. setting up circulation filtration, pour the emulsifier of waiting to filter the edulcoration into the filter canister through the feed inlet, then the emulsifier begins to flow into filtering pipeline owing to gravity's influence, the emulsifier is firstly through the interception of filter screen with partial impurity in filtering pipeline, the emulsifier flows through the filter screen simultaneously and enters into in the filter core, make still another partial impurity in the emulsifier filter by the filter core, then filterable emulsifier enters into the edulcoration jar through the pipeline and carries out the edulcoration, simultaneously manual start second driving motor drives the pressure pump, make emulsifier circulation filtration, partial impurity in the emulsifier can be circulated filtration, reduce the human cost.
2. The chemical impurity removing structure is arranged, after the emulsifier is filtered, the emulsifier enters the impurity removing tank through the filtering pipeline, as a part of impurities are filtered out in the filtering process, a small amount of scrap iron impurities are still present in the emulsifier, a large amount of sulfurous acid solution is placed in the reaction basin body in the impurity removing tank, when the emulsifier flows into the reaction basin body, the scrap iron impurities in the emulsifier react with the sulfurous acid solution to generate ferrous sulfate precipitation and hydrogen, the emulsifier is aromatic compound with higher stability and can not react with strong acid and alkali and are not mutually compatible, when the emulsifier flows into the reaction basin body from the upper part of the impurity removing tank, the emulsifier covers the sulfurous acid solution, after the scrap iron impurities react with the sulfurous acid solution, only a small amount of scrap iron solution is left, and then, a certain amount of scrap iron impurities to be filtered and removed are manually removed through the feeding port, so that the sulfurous acid solution and the circulating reaction is complete, then the scrap iron impurities flow into the temperature control storage structure through the pipeline, and meanwhile, after the impurity removing is removed, the ferrous iron precipitates are manually removed from the separation plate, the ferrous sulfate precipitation can be cleaned, and the practicality of the product can be improved.
3. After the filtering and impurity removing are finished, the high-purity emulsifying agent flows into the storage box through the pipeline, at the moment, the first driving motor is manually started to drive the heating screw rod to operate, then the emulsifying agent is heated by manually adjusting the integral adjusting switch of the heating screw rod, and the emulsifying agent is preferably heated to be in a state of being in a solution by adjusting the temperature to be floating up and down between 50 and 70 ℃, so that the emulsifying agent is convenient to store and take, and when the temperature of the heating screw rod is adjusted, the heating screw rod cannot be used for heating the emulsifying agent to be higher than 230 ℃, otherwise, the emulsifying agent is unstable, the heating temperature of the emulsifying agent can be adjusted and controlled, and the emulsifying agent is convenient to store.
Drawings
FIG. 1 is a schematic diagram of a dynamic temperature adjustment circulating filtration and impurity removal system for an emulsifier;
FIG. 2 is a schematic cross-sectional view of an emulsifier temperature dynamic adjustment circulating filtration and impurity removal system according to the present utility model;
FIG. 3 is an enlarged schematic view of the structure of the emulsifier temperature dynamic adjustment circulating filtration and impurity removal system shown in FIG. 2A;
in the figure: 1. a first support column; 2. a second support column; 3. a canister; 4. a filter tube; 5. a circulation pipe; 6. a pressure pump; 7. a second driving motor; 8. a feed inlet; 9. a filter screen; 10. a filter element; 11. a storage tank; 12. a first driving motor; 13. heating the screw rod; 14. a impurity removing tank; 15. a reaction basin body; 16. a separation plate; 17. a circulating filtering structure; 18. a temperature-controlled storage structure; 19. chemical impurity removing structure.
Detailed Description
For a further understanding of the utility model, its features and advantages, reference is now made to the following examples, which are illustrated in the accompanying drawings.
Referring to fig. 1 to 3, a detailed description of an emulsifier temperature dynamic adjustment circulating filter impurity removal system according to an embodiment of the utility model will be provided below.
Referring to fig. 1 to 3, in the present embodiment, the emulsifier temperature dynamic adjustment cycle filter impurity removal system includes: the chemical impurity removing device comprises a first support column 1, a second support column 2, a circulating filter structure 17, a temperature control storage structure 18 and a chemical impurity removing structure 19, wherein the circulating filter structure 17 is connected with the chemical impurity removing structure 19 in a pipeline mode, the chemical impurity removing structure 19 is fixed at the top end of the second support column 2, the temperature control storage structure 18 is connected with the bottom end of the chemical impurity removing structure 19 in a pipeline mode, and the first support column 1 is arranged between the chemical impurity removing structure 19 and the circulating filter structure 17.
The emulsifier temperature dynamic adjustment circulation filtering impurity removing system can adjust and control the heating temperature of the emulsifier, is convenient to store, can circularly filter partial impurities in the emulsifier, reduces labor cost, can remove scrap iron in the manufacturing process of the emulsifier, and improves the practicability of products.
Referring to fig. 2 and 3, in this embodiment, the circulating filter structure 17 includes a filter tank 3, a filter pipe 4 is disposed at the bottom end of the filter tank 3, a circulating pipe 5 is disposed on the side surface of the filter tank 3, the circulating pipe 5 passes through a pipeline connection pressure pump 6 in a impurity removal tank 14, the pressure pump 6 is connected with a second driving motor 7 by a wire, the pressure pump 6 is connected with the second driving motor 7 by a wire, a filter screen 9 is disposed inside the filter pipe 4, a filter core 10 is disposed at the bottom end of the filter screen 9, and a feed inlet 8 is disposed at the top end of the filter tank 3.
The emulsifier to be filtered and decontaminated is poured into the filter tank 3 through the feed inlet 8, then the emulsifier starts to flow into the filter pipeline 4 due to the influence of gravity, part of impurities in the emulsifier are intercepted by the filter screen 9 in the filter pipeline 4, meanwhile, the emulsifier flows through the filter screen 9 and enters the filter element 10, so that the other part of impurities in the emulsifier are filtered by the filter element 10, then the filtered emulsifier enters the decontaminating tank 14 through the pipeline to be decontaminated, and meanwhile, the second driving motor 7 is manually started to drive the pressure pump 6, so that the emulsifier is circularly filtered, part of impurities in the emulsifier can be circularly filtered, and the labor cost is reduced.
Referring to fig. 2, in the present embodiment, the temperature-controlled storage structure 18 includes a storage tank 11, the storage tank 11 is connected to the bottom end of the impurity removal tank 14 through a pipe, a first driving motor 12 is disposed inside the storage tank 11, and the first driving motor 12 is connected to a heating screw 13 through a wire.
After the filtering and impurity removal of the emulsifier are completed, the high-purity emulsifier flows into the storage tank 11 through the pipeline, at the moment, the first driving motor 12 is manually started to drive the heating screw rod 13 to operate, then the emulsifier is heated by manually adjusting an integral adjusting switch of the heating screw rod 13, preferably, the temperature is adjusted to be between 50 and 70 ℃ to float up and down, when the heating screw rod 13 is operated, the heating screw rod 13 cannot heat the emulsifier at a temperature exceeding 230 ℃, and otherwise, the emulsifier is unstable.
Referring to fig. 2, in this embodiment, the chemical impurity removing structure 19 includes an impurity removing tank 14, the impurity removing tank 14 is connected to the bottom end of the filter tank 3 through a pipe, a reaction basin 15 is disposed in the impurity removing tank 14, and a separation plate 16 is disposed in the reaction basin 15.
When the filtering of the emulsifying agent is completed, the emulsifying agent enters the impurity removing tank 14 through the filtering pipeline 4, as a part of impurities are filtered out in the filtering process, and a small amount of scrap iron impurities are still present in the emulsifying agent, a large amount of sulfurous acid solution is placed in the reaction basin 15 in the impurity removing tank 14, when the emulsifying agent flows into the reaction basin 15, the scrap iron impurities in the emulsifying agent react with the sulfurous acid solution to generate ferrous sulfate precipitation and hydrogen, the emulsifying agent is an aromatic compound with higher stability and almost cannot react with strong acid and strong alkali and are mutually insoluble, when the emulsifying agent flows into the reaction basin 15 from above the impurity removing tank 14, the emulsifying agent covers the sulfurous acid solution, and when the scrap iron impurities react with the sulfurous acid solution, only a small amount of the high-purity emulsifying agent and the sulfurous acid solution are left, at this time, some emulsifying agent to be filtered and the impurity removed is completely reacted with the circulation through the feed inlet 8, then the ferrous iron filings to flow into the temperature control storage structure 18 through the pipeline, and after the impurity removal, the ferrous filings on the separating plate 16 are manually removed, and the ferrous filings are cleaned.
The pressure pump in the above embodiment is directly commercially available, and in this embodiment, the pressure pump is of the LST-0416 type.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. An emulsifier temperature dynamic adjustment cycling filtration decontamination system, comprising: first support column (1), second support column (2), circulation filtration structure (17), accuse temperature storage structure (18), chemistry edulcoration structure (19), circulation filtration structure (17) and chemistry edulcoration structure (19) pipe connection, chemistry edulcoration structure (19) are fixed in second support column (2) top, accuse temperature storage structure (18) pipe connection is in chemistry edulcoration structure (19) bottom, first support column (1) set up between chemistry edulcoration structure (19) and circulation filtration structure (17).
2. The emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system according to claim 1, wherein the circulation filtering structure (17) comprises a filter tank (3), a filter pipeline (4) is arranged at the bottom end of the filter tank (3), a circulation pipeline (5) is arranged on the side face of the filter tank (3), the circulation pipeline (5) penetrates through an inner pipeline of an impurity removing tank (14) to be connected with a pressure pump (6), and the pressure pump (6) is connected with a second driving motor (7) through an electric wire.
3. The emulsifying agent temperature dynamic regulation circulation filtering and impurity removing system according to claim 2, wherein a filter screen (9) is arranged in the filter pipeline (4), a filter element (10) is arranged at the bottom end of the filter screen (9), and a feed inlet (8) is arranged at the top end of the filter tank (3).
4. The dynamic temperature adjustment circulating filtration and impurity removal system of claim 1, wherein the chemical impurity removal structure (19) comprises an impurity removal tank (14), the impurity removal tank (14) is connected to the bottom end of the filter tank (3) through a pipeline, and a reaction basin (15) is arranged in the impurity removal tank (14).
5. The emulsifier temperature dynamic adjustment circulation filtering and impurity removing system according to claim 1, wherein the temperature control storage structure (18) comprises a storage box (11), the storage box (11) is connected to the bottom end of the impurity removing tank (14) through a pipeline, a first driving motor (12) is arranged inside the storage box (11), and the first driving motor (12) is connected with a heating screw rod (13) through a wire.
6. An emulsifier temperature dynamic adjustment circulation filtration and impurity removal system according to claim 4, characterized in that a separation plate (16) is arranged in the reaction basin (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320402682.3U CN219701230U (en) | 2023-03-07 | 2023-03-07 | Emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320402682.3U CN219701230U (en) | 2023-03-07 | 2023-03-07 | Emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219701230U true CN219701230U (en) | 2023-09-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320402682.3U Active CN219701230U (en) | 2023-03-07 | 2023-03-07 | Emulsifying agent temperature dynamic adjustment circulation filtering and impurity removing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219701230U (en) |
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2023
- 2023-03-07 CN CN202320402682.3U patent/CN219701230U/en active Active
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