CN219907527U - Lanolin extraction element - Google Patents
Lanolin extraction element Download PDFInfo
- Publication number
- CN219907527U CN219907527U CN202320208141.7U CN202320208141U CN219907527U CN 219907527 U CN219907527 U CN 219907527U CN 202320208141 U CN202320208141 U CN 202320208141U CN 219907527 U CN219907527 U CN 219907527U
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- China
- Prior art keywords
- centrifugal machine
- lanolin
- filter screen
- filter tank
- fixedly arranged
- Prior art date
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- 239000004166 Lanolin Substances 0.000 title claims abstract description 33
- 229940039717 lanolin Drugs 0.000 title claims abstract description 33
- 235000019388 lanolin Nutrition 0.000 title claims abstract description 33
- 238000000605 extraction Methods 0.000 title claims abstract description 21
- 239000007788 liquid Substances 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 19
- 238000000926 separation method Methods 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 6
- 210000002268 wool Anatomy 0.000 abstract description 9
- 239000002699 waste material Substances 0.000 abstract description 5
- 230000005484 gravity Effects 0.000 abstract description 3
- 238000013461 design Methods 0.000 abstract description 2
- 238000009987 spinning Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 11
- 239000002351 wastewater Substances 0.000 description 8
- 239000007787 solid Substances 0.000 description 6
- 238000010411 cooking Methods 0.000 description 5
- 238000005406 washing Methods 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- Centrifugal Separators (AREA)
Abstract
The utility model relates to the field of wool spinning and discloses a lanolin extraction device, which comprises a filter tank, a first centrifugal machine and a second centrifugal machine, wherein the first centrifugal machine is fixedly arranged at the bottom of the filter tank; according to the utility model, through the integral structure of vertical design, lanolin waste in the extraction process is reduced, and meanwhile, the whole lanolin extraction process is not required to be driven by extra power under the influence of gravity, so that the waste of resources is saved.
Description
Technical Field
The utility model relates to the field of lanolin recovery in the wool washing industry, in particular to a lanolin extraction device.
Background
The wool washing industry is a sub-industry of the wool spinning industry, the industry scale is relatively small, but the problem of high concentration pollution of wool washing wastewater is felt by the industry personnel. After long-term technical and economic feasibility analysis and research, the applicant finds that the pollution of lanolin in high-concentration pollutants is the most serious, but is the resource with the highest recovery value, and the method has very high economic value and also has very high social value.
Chinese patent discloses a high efficiency lanolin recovery device, patent application number: CN201864713U, this high-efficiency lanolin recovery device utility model technology includes: comprises a multifunctional cooking box, a catching separator, a primary concentration separator and a high-grade concentration separator; the inlet of the multifunctional cooking box is connected with the outlet of the wool washing wastewater production line, a demulsifier feeding port is arranged on the inlet pipeline of the multifunctional cooking box, the outlet of the multifunctional cooking box is connected with the inlet of the catching separator, the outlet of the catching separator is connected with the inlet of the primary concentration separator, the outlet of the primary concentration separator is connected with the inlet of the high-grade concentration separator, and the outlet of the high-grade concentration separator is connected with the oil barrel; the waste water outlets of the multifunctional cooking box, the catching separator, the primary concentration separator and the high-grade concentration separator are all connected with a sewage treatment station through pipelines. The utility model extracts lanolin from wool washing wastewater, thereby changing waste into valuables, greatly reducing the loss of lanolin, greatly improving the extraction rate of lanolin and reducing the discharge requirement of high pollutants in wastewater.
In the prior art, the following disadvantages still exist: all structures are transversely arranged, the process is connected by a pipeline, the lanolin residues in the pipeline are easy to generate, and meanwhile, kinetic energy transmission is required in the transmission process, so that the resource consumption is increased. To this end, we propose a lanolin extraction device.
Disclosure of Invention
The utility model mainly solves the technical problems in the prior art, so that the lanolin extracting device is provided, the lanolin waste in the extracting process is reduced through the integral structure of vertical design, and meanwhile, the whole lanolin extracting process is not required to be driven by extra power under the influence of gravity, so that the waste of resources is saved.
In order to achieve the above purpose, the utility model adopts the following technical scheme that the lanolin extraction device comprises a filter tank, a first centrifugal machine and a second centrifugal machine, wherein the first centrifugal machine is fixedly arranged at the bottom of the filter tank, the second centrifugal machine is fixedly arranged at the bottom of the first centrifugal machine, the bottom of the filter tank is fixedly provided with the first centrifugal machine, and the bottom of the first centrifugal machine is fixedly provided with the second centrifugal machine;
preferably, a coarse filter screen and a fine filter screen are fixedly arranged in the filter tank, the coarse filter screen is positioned in the middle of the filter tank, the fine filter screen is fixedly arranged in the filter tank and is arranged in the lower middle of the filter tank, and the coarse filter screen and the fine filter screen are independently arranged and are fixed in position;
preferably, a discharge hole is fixedly formed in one side of the second centrifugal machine, a water pump and a water pipe are fixedly arranged on the other side of the second centrifugal machine, the other end of the water pipe is fixedly connected to the top of the second centrifugal machine, a water outlet is fixedly formed in the bottom of the second centrifugal machine, a first movable valve is movably arranged at the top of the inside of the second centrifugal machine, and the second movable valve is movably arranged at the bottom of the second centrifugal machine.
Preferably, the filter tank is funnel-shaped.
Preferably, the coarse filter screen is fixedly arranged at the middle position inside the filter tank, and the density is low.
Preferably, the fine filter screen is fixedly arranged at the middle position of the lower half part in the filter tank, and the density is high.
Preferably, the first centrifuge is a solid-liquid separation centrifuge.
Preferably, the second centrifuge is a water-fat separator centrifuge.
Preferably, the water pump is fixedly connected with the second centrifugal machine.
Advantageous effects
The utility model provides a lanolin extraction device. The beneficial effects are as follows:
(1) This lanolin extraction device, a plurality of equipment subassemblies are horizontal arrangement in traditional equipment, all are connected through the pipeline between every equipment, and the lanolin can be at the pipeline in the middle of the in-process from one equipment to another equipment, and how much can cause certain wasting of resources, this equipment is vertical arrangement equipment, all sets up perpendicularly between the equipment, has reduced the transmission process in handling process, has reduced the possibility of remaining and loss.
(2) According to the lanolin extraction device, the liquid to be treated can freely fall to the next process under the action of gravity through the vertical arrangement, no electric power is needed for driving in the whole treatment process, energy conservation and environmental protection are truly achieved, and the environmental protection of the device is improved.
(3) According to the lanolin extraction device, the circulating device is arranged at the bottom of the second centrifugal machine, centrifuged liquid is reflowed again and separated again, separation efficiency and cleanliness of discharged wastewater are ensured, and environmental pollution caused by insufficient separation is avoided.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present utility model;
FIG. 2 is a schematic diagram of the internal structure of the present utility model;
FIG. 3 is a schematic elevational view of the structure of the present utility model;
FIG. 4 is a schematic side view of the structure of the present utility model;
legend description: 1. a filtering tank; 2. a first centrifuge; 3. a second centrifuge; 4. a discharge port; 5. a water outlet; 6. a water pump; 7. a water pipe; 8. a first movable valve; 9. a coarse filter screen; 10. fine filter screen; 11. and a second movable valve.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Examples: the lanolin extraction device comprises a filter tank 1, a first centrifugal machine 2 and a second centrifugal machine 3, wherein the first centrifugal machine 2 is fixedly arranged at the bottom of the filter tank 1, the second centrifugal machine 3 is fixedly arranged at the bottom of the first centrifugal machine 2, and the whole device is vertically arranged, so that liquid retention and residue caused by transmission in a treatment process can be avoided;
the inside of the filter tank 1 is fixedly provided with a coarse filter screen 9 and a fine filter screen 10, the coarse filter screen 9 is positioned in the middle of the inside of the filter tank 1, the fine filter screen 10 is fixedly arranged in the lower middle of the inside of the filter tank 1, the coarse filter screen 9 and the fine filter screen 10 are respectively arranged independently, and the positions are fixed, so that the passing liquid can sufficiently filter out some larger solid impurities in the first working procedure, and the pressure is relieved for the subsequent separation;
the fixed discharge gate 4 that is provided with in 3 one sides of second centrifuge, the fixed water pump 6 and the water pipe 7 of being provided with of 3 opposite sides of second centrifuge, and 7 other end fixed connection of water pipe are at 3 tops of second centrifuge, and 3 bottoms of second centrifuge are fixed to be provided with delivery port 5, and the inside top activity of second centrifuge is provided with first movable valve 8 simultaneously, and the activity of second movable valve 11 is set up in the bottom of 3 centrifuges of second.
The filter tank 1 is of a funnel type for facilitating the transfer of the mixed liquor to the first centrifuge 2.
The coarse filter screen 9 is fixedly arranged at the middle position inside the filter tank 1, has lower density and is used for filtering larger solid impurities, and meanwhile, the liquid flow rate is not influenced.
The fine filter screen 10 is fixedly arranged at the middle position of the lower half part in the filter tank 1, has higher density and is used for filtering slightly smaller solid impurities and relieving pressure for the subsequent centrifuge.
The first centrifugal machine 2 is a solid-liquid separation centrifugal machine, and performs final solid-liquid separation on the liquid after the completion of a filtering procedure to separate out fine solid impurities, thereby providing conditions for the subsequent separation of lanolin.
The second centrifuge 3 is a water-fat separator centrifuge for final separation and purification, separating and extracting lanolin from the mixed liquor.
The water pump 6 is fixedly connected with the second centrifugal machine 3, and is used for fixedly pumping the liquid which is separated once back to the inlet of the second centrifugal machine 3 for secondary separation, further purifying and completing essence of water quality, so that the pollution of wastewater is reduced, and the environment is protected.
The working principle of the utility model is as follows:
when the wool-washed water-fat mixed liquid is used, the wool-washed water-fat mixed liquid is poured into the filter tank 1, when the liquid passes through the filter tank 1, the mixed liquid from which larger solid foreign matters are screened out is obtained after the liquid passes through the filter tank 1 and is filtered by the coarse filter screen 9 and the fine filter screen 10, the pressure is relieved for the subsequent separation work of the centrifugal machine, the mixed liquid enters the first centrifugal machine 2, the first centrifugal machine 2 works to centrifugally separate the fine solid foreign matters which cannot be processed by the filter screen in the mixed liquid, pure water-fat mixed liquid is obtained after the separation of the first centrifugal machine 2, the pure water-fat mixed liquid enters the second centrifugal machine 3 to carry out water-fat separation, pure wool fat can be obtained from the discharge port 4, and the separated liquid is pumped back to the second centrifugal machine 3 by the water pump 6 after separation and is extracted again to remove waste water, so that the wool fat extraction efficiency is improved.
The foregoing has shown and described the basic principles and main features of the present utility model and the advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (6)
1. The utility model provides a lanolin extraction element, includes filtering ponds (1), first centrifuge (2) and second centrifuge (3), first centrifuge (2) are fixed to be set up in filtering ponds (1) bottom, and second centrifuge (3) are fixed to be set up in first centrifuge (2) bottom, its characterized in that: a first centrifugal machine (2) is fixedly arranged at the bottom of the filter tank (1), and a second centrifugal machine (3) is fixedly arranged at the bottom of the first centrifugal machine (2);
the filter tank (1) is internally and fixedly provided with a coarse filter screen (9) and a fine filter screen (10), the coarse filter screen (9) is positioned in the middle of the filter tank (1), the fine filter screen (10) is fixedly arranged in the middle of the filter tank (1) and is arranged in a lower position, and the coarse filter screen (9) and the fine filter screen (10) are independently arranged and are fixed in position;
a discharge hole (4) is fixedly arranged on one side of the second centrifugal machine (3), a water pump (6) and a water pipe (7) are fixedly arranged on the other side of the second centrifugal machine (3), the other end of the water pipe (7) is fixedly connected to the top of the second centrifugal machine (3), the water outlet (5) is fixedly arranged at the bottom of the second centrifugal machine (3), the first movable valve (8) is movably arranged at the top of the inside of the second centrifugal machine (3), the second movable valve (11) is movably arranged at the bottom of the second centrifugal machine (3), and the filter tank (1) is in a funnel type.
2. A lanolin extraction device according to claim 1, wherein: the coarse filter screen (9) is fixedly arranged at the middle position inside the filter tank (1), and the density is low.
3. A lanolin extraction device according to claim 1, wherein: the fine filter screen (10) is fixedly arranged at the center of the lower half part in the filter tank (1), and the density is high.
4. A lanolin extraction device according to claim 1, wherein: the first centrifugal machine (2) is a solid-liquid separation centrifugal machine.
5. A lanolin extraction device according to claim 1, wherein: the second centrifugal machine (3) is a water-fat separation centrifugal machine.
6. A lanolin extraction device according to claim 1, wherein: the water pump (6) is fixedly connected with the second centrifugal machine (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320208141.7U CN219907527U (en) | 2023-02-14 | 2023-02-14 | Lanolin extraction element |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320208141.7U CN219907527U (en) | 2023-02-14 | 2023-02-14 | Lanolin extraction element |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219907527U true CN219907527U (en) | 2023-10-27 |
Family
ID=88434534
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320208141.7U Active CN219907527U (en) | 2023-02-14 | 2023-02-14 | Lanolin extraction element |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219907527U (en) |
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2023
- 2023-02-14 CN CN202320208141.7U patent/CN219907527U/en active Active
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