CN220736624U - Non-blocking high-pressure filter with automatic cleaning and deslagging functions - Google Patents
Non-blocking high-pressure filter with automatic cleaning and deslagging functions Download PDFInfo
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- CN220736624U CN220736624U CN202322364963.7U CN202322364963U CN220736624U CN 220736624 U CN220736624 U CN 220736624U CN 202322364963 U CN202322364963 U CN 202322364963U CN 220736624 U CN220736624 U CN 220736624U
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- filter
- liquid
- liquid medicine
- high pressure
- automatic cleaning
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- 238000004140 cleaning Methods 0.000 title claims abstract description 22
- 239000007788 liquid Substances 0.000 claims abstract description 85
- 239000003814 drug Substances 0.000 claims abstract description 44
- 230000001105 regulatory effect Effects 0.000 claims description 13
- 238000012806 monitoring device Methods 0.000 claims description 5
- 239000013049 sediment Substances 0.000 claims description 5
- 239000010865 sewage Substances 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 4
- 238000003860 storage Methods 0.000 abstract description 15
- 238000001914 filtration Methods 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000000903 blocking effect Effects 0.000 abstract description 2
- 101100372509 Mus musculus Vat1 gene Proteins 0.000 description 4
- 229940079593 drug Drugs 0.000 description 4
- 230000002572 peristaltic effect Effects 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 230000003670 easy-to-clean Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Abstract
The utility model discloses a non-blocking high-pressure filter with automatic cleaning and deslagging functions, and relates to the technical field of liquid medicine filtering and separating. The utility model aims to solve the problems that in the prior art, when liquid medicine is injected into a liquid storage tank, dregs in the liquid medicine can be deposited at the bottom of the liquid storage tank, so that the liquid outlet of the liquid storage tank is easy to be blocked, frequent cleaning is needed, the cleaning process is complex, dregs are not easy to be removed, and the production efficiency is seriously affected. The utility model comprises a plurality of filter barrels connected in series through pipelines, wherein a filter element is arranged in each filter barrel, each filter barrel is connected with a raw liquid tank body through a liquid medicine inlet pipeline, a liquid medicine pump is arranged on each liquid medicine inlet pipeline, and extracting solution in each raw liquid tank body is conveyed into each filter barrel through the corresponding liquid medicine pump. The utility model is used for filtering liquid medicine.
Description
Technical Field
The utility model relates to the technical field of liquid medicine filtering separation, in particular to a non-blocking high-pressure filter with automatic cleaning and deslagging functions.
Background
In the process of extracting and purifying a drug, the drug is usually subjected to steps such as filtration extraction, concentration, ion exchange chromatography and the like, and the filtration extraction of the drug is a necessary and very critical step, in the prior art, there are two general ways to inject the drug solution into a filtration device: the first is to inject the liquid medicine into the filtering device by adopting a peristaltic pump, but the pressure of the peristaltic pump is unstable, and the peristaltic pump is connected with the filtering device by adopting a hose, so that the peristaltic pump cannot bear larger pressure, and the transmission efficiency is low; the second is to inject the liquid medicine into the liquid storage tank firstly, the liquid medicine in the liquid storage tank is pressed into the filtering device communicated with the liquid storage tank by adopting air pressurization, and the existing liquid storage tank has the following defects that firstly, when the liquid medicine is injected into the liquid storage tank, the dregs in the liquid medicine can be deposited at the bottom of the liquid storage tank, the liquid outlet of the liquid storage tank is easy to be blocked, frequent cleaning is needed, the cleaning process is complex, dregs are not easy to be removed, the production efficiency is seriously affected, and the liquid storage tank is easy to damage.
Disclosure of Invention
The utility model aims to solve the problems that when liquid medicine is injected into a liquid storage tank of a high-pressure filter in the prior art, dregs in the liquid medicine can be deposited at the bottom of the liquid storage tank, so that a liquid outlet of the liquid storage tank is easy to be blocked, frequent cleaning is needed, the cleaning process is complex, dregs are not easy to be removed, the production efficiency is seriously affected, the liquid storage tank is easy to be damaged, and the like, and further the high-pressure filter with the automatic cleaning and deslagging functions is provided.
The technical scheme adopted by the utility model for solving the problems is as follows: the utility model provides a no jam area self-cleaning arranges sediment high pressure filter, includes a plurality of filter vats that establish ties through the pipeline, the inside filter vats that is provided with of filter vats, the filter vats passes through liquid medicine import pipeline connection former liquid pot body, be provided with the liquid medicine pump on the liquid medicine import pipeline, the extract in the former liquid pot body is passed through the liquid medicine pump and is carried in the filter vats.
Further, a longitudinal valve is arranged on a pipeline connecting the filter barrels.
Further, the filter vat is provided with a liquid outlet, and the liquid outlets of the filter vats are connected in series through pipelines.
Further, the filter barrels are also provided with drain outlets, and the drain outlets of the filter barrels are connected in series through pipelines.
Further, the drain outlet is connected with a drain main pipe.
Further, a pressure regulating valve is arranged on the liquid medicine pump.
Further, a pressure monitoring device is arranged on the liquid medicine inlet pipeline.
Further, the screen mesh number of the filter element 2 is 40-200 meshes.
The utility model has the following beneficial technical effects:
when the device works, materials in the raw liquid tank body are washed and filtered through the lateral liquid inlet of the filter barrel, filtered liquid medicine passes through the filter screen on the filter element to the liquid outlet, dregs can be automatically switched to wash and discharge the dregs outside the filter barrel through pressure control, when the pressure is greater than a preset value, the liquid inlet longitudinal valve is closed, the washing valve and the dregs discharge valve are opened, and the dregs are washed and discharged.
The utility model can also be manually operated, the deslagging port is provided with a pressure regulating valve, when the filtering pressure is higher than the pressure regulating valve, the deslagging port can be automatically jacked up to automatically deslagge, and when the pressure is lower than the pressure regulating valve, the liquid is normally discharged. The filter is not easy to block, easy to clean, convenient to operate, and capable of being controlled automatically and manually.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
in the figure: 1. a filter vat; 2. a filter element; 3. a longitudinal valve; 4. a liquid outlet; 5. a sewage outlet; 6. a liquid medicine inlet pipeline; 7. a liquid medicine pump; 8. a pressure regulating valve; 9. a pressure monitoring device; 10. a stock solution tank body.
Detailed Description
The present utility model will be further described in detail with reference to the drawings and examples, which are provided to illustrate the present utility model and not to limit the present utility model.
The first embodiment is as follows: referring to fig. 1, the embodiment is described with reference to the present embodiment, which is a non-clogging high-pressure filter with automatic cleaning and deslagging functions, and includes a plurality of filter barrels 1 connected in series through pipelines, wherein a filter element 2 is disposed inside the filter barrels 1, the filter barrels 1 are connected with a raw liquid tank 10 through a liquid medicine inlet pipeline 6, a liquid medicine pump 7 is disposed on the liquid medicine inlet pipeline 6, and an extracting solution in the raw liquid tank 10 is conveyed into the filter barrels 1 through the liquid medicine pump 7.
The second embodiment is as follows: the present embodiment is described with reference to fig. 1, in which a longitudinal valve 3 is provided on a pipe line connecting the plurality of filter tanks 1.
In the embodiment, the materials in the raw liquid tank 10 are washed and filtered through the lateral liquid inlet of the filter barrel 1, the filtered liquid medicine passes through a filter screen with 40-200 meshes on the filter element 2 to the liquid outlet 4, the dregs can be automatically cleaned and discharged outside the filter cartridge screen through pressure control, when the pressure is greater than the preset pressure, the liquid inlet longitudinal valve 3 is closed, the cleaning valve and the slag discharge valve are opened, and the dregs are cleaned and discharged.
Other components and connections are the same as those of the embodiment.
And a third specific embodiment: referring to fig. 1, a liquid outlet 4 is provided on the filter vat 1 according to the present embodiment, and the liquid outlets 4 of the filter vats 1 are connected in series through a pipeline.
The liquid outlets 4 on the plurality of filter barrels 1 in the filtering system of the embodiment are connected in series through pipelines, so that one filter barrel 1 can be independently controlled, or all the filter barrels 1 in the system can be simultaneously controlled.
Other components and connections are the same as those of the embodiment.
The specific embodiment IV is as follows: referring to fig. 1, the filter vat 1 of the present embodiment is further provided with a drain outlet 5, and the drain outlets 5 of the multiple filter vats 1 are connected in series through a pipeline; the sewage outlet 5 is connected with a sewage main pipe.
The filter vat 1 of the embodiment is provided with a drain outlet 5, the drain outlets 5 of the filter vats 1 are connected in series through pipelines, the drain outlet 5 is connected with a drain main pipe, and slag is discharged through the drain main pipe.
Other components and connections are the same as those of the embodiment.
Fifth embodiment: the liquid medicine pump 7 according to the present embodiment is provided with a pressure regulating valve 8, as described with reference to fig. 1.
The pressure regulating valve 8 is installed on the liquid medicine pump 7 adopted in the embodiment, and the type of the pressure regulating valve 8 adopts a general standard component or a component known by a person skilled in the art, and the structure and the principle of the pressure regulating valve are all known by the person through a technical manual.
Other components and connections are the same as those of the embodiment.
Specific embodiment six: the liquid medicine inlet line 6 according to the present embodiment is provided with a pressure monitoring device 9, as described with reference to fig. 1.
The pressure monitoring device 9 used in this embodiment is a pressure gauge, and the type of the pressure gauge adopts a general standard component or a component known to those skilled in the art, and its structure and principle are all known by those skilled in the art through a technical manual.
Other components and connections are the same as those of the embodiment.
The working principle of the utility model is as follows:
the material in the stock solution jar body 10 washes the filtration through the side direction inlet of filter vat 1 when this filter work, and the liquid medicine after the filtration passes through the filter screen of 40-200 mesh on the filter core 2 and to liquid outlet 4, and the dregs of a decoction can be through pressure control automatic switch washing sediment outside the cartridge filter screen, and when pressure was greater than the settlement, closed the vertical valve 3 of feed liquor, open and wash valve and sediment valve, wash sediment. The manual mode is also available, the slag discharging port is provided with a pressure regulating valve, when the filtering pressure is larger than the pressure regulating valve, the automatic slag discharging port can be automatically jacked up, and when the pressure is lower than the pressure regulating valve, the liquid is normally discharged. The filter is not easy to block, easy to clean, convenient to operate, and capable of being controlled automatically and manually.
The above embodiments are only preferred and exemplary, and are not intended to limit the present utility model, but any modifications, equivalent substitutions, improvements, etc. within the spirit and principle of the present utility model should be included in the scope of the present utility model.
Claims (8)
1. The utility model provides a no jam area self-cleaning arranges sediment high pressure filter which characterized in that: including a plurality of filter vat (1) that establish ties through the pipeline, filter vat (1) inside is provided with filter core (2), filter vat (1) are through liquid medicine import pipeline (6) connection former liquid pot body (10), be provided with liquid medicine pump (7) on liquid medicine import pipeline (6), extract in former liquid pot body (10) is carried in filter vat (1) through liquid medicine pump (7).
2. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: a longitudinal valve (3) is arranged on a pipeline connecting the filter barrels (1).
3. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: the filter vat (1) is provided with a liquid outlet (4), and the liquid outlets (4) of the filter vats (1) are connected in series through pipelines.
4. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: the filter vat (1) is also provided with a drain outlet (5), and the drain outlets (5) of the filter vats (1) are connected in series through pipelines.
5. The non-clogging, belt-cleaning, slag-removing high pressure filter of claim 4, wherein: the sewage outlet (5) is connected with a sewage main pipe.
6. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: the liquid medicine pump (7) is provided with a pressure regulating valve (8).
7. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: the liquid medicine inlet pipeline (6) is provided with a pressure monitoring device (9).
8. The non-clogging high pressure filter with automatic cleaning and deslagging function according to claim 1, wherein: the screen mesh number of the filter element (2) is 40-200 meshes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322364963.7U CN220736624U (en) | 2023-08-31 | 2023-08-31 | Non-blocking high-pressure filter with automatic cleaning and deslagging functions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322364963.7U CN220736624U (en) | 2023-08-31 | 2023-08-31 | Non-blocking high-pressure filter with automatic cleaning and deslagging functions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220736624U true CN220736624U (en) | 2024-04-09 |
Family
ID=90553222
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322364963.7U Active CN220736624U (en) | 2023-08-31 | 2023-08-31 | Non-blocking high-pressure filter with automatic cleaning and deslagging functions |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220736624U (en) |
-
2023
- 2023-08-31 CN CN202322364963.7U patent/CN220736624U/en active Active
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| GR01 | Patent grant |