CN217450524U - Automatic de-ironing separator of low viscosity thick liquids - Google Patents
Automatic de-ironing separator of low viscosity thick liquids Download PDFInfo
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- CN217450524U CN217450524U CN202221180305.1U CN202221180305U CN217450524U CN 217450524 U CN217450524 U CN 217450524U CN 202221180305 U CN202221180305 U CN 202221180305U CN 217450524 U CN217450524 U CN 217450524U
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Abstract
The utility model discloses an automatic de-ironing separator for low viscosity slurry, which relates to a ferromagnetic waste filter, and further comprises an inlet three-way pipe and an outlet three-way pipe, wherein the inlet three-way pipe comprises a filtrate inlet, a cleaning liquid outlet, a magnetic filter tank inlet and an inlet three-way valve, the outlet three-way pipe comprises a filtrate outlet, a cleaning liquid inlet, a magnetic filter tank outlet and an outlet three-way valve, and the magnetic filter tank is connected with the filtrate inlet and the filtrate outlet; the cleaning device also comprises a detachable and cleaning filter, and the cleaning filter is connected with the cleaning liquid outlet and the cleaning liquid inlet; compared with the prior art, the utility model discloses integrated as an organic whole with magnetic filtration system and clean system, have filtration circuit and clearance return circuit simultaneously, solved and need unpack magnetic filtration system apart just abluent problem in the past to still solved even filtration circuit and clearance return circuit part collineation, filtration circuit can not be by the problem that the clearance return circuit pollutes yet.
Description
Technical Field
The utility model relates to a ferromagnetism waste material filter especially relates to the filtration of small ferromagnetism waste material among the fluid medium.
Background
In industrial production processes, ferromagnetic filtration of liquid or slurry is required, such as new energy industry, chemical industry, metal processing industry and the like. The deironing ware among the prior art can not be fine carries out the automatically cleaning, and most of deironing wares need shut down the clearance after reaching the absorption extreme value, sneak into impurity in order to avoid polluting, need take out the bar magnet this moment, use the clearance liquid to clear up the deironing ware is inside, then pour out the clearance liquid, dry at last, the ferromagnetic stick just can continue to use is put into to the stoving end. This cleaning process is not only complex and time consuming, but requires multiple sets of iron removal equipment to be run intermittently for continuous production. And the cleaning method does not completely avoid the pollution problem, and the cleaning liquid is easy to pollute the filter body if the drying is not thorough or the cleaning liquid is not thoroughly poured out.
SUMMERY OF THE UTILITY MODEL
The utility model provides an it is not enough among the prior art to provide an automatic de-ironing separator of low viscosity thick liquids, this application is integrated as an organic whole with magnetic filtration system and clean system, has filter circuit and clearance return circuit simultaneously, has solved and need unpack magnetic filtration system apart just abluent problem in the past to even still solved filter circuit and clearance return circuit part collineation, filter circuit can not be by the problem that clearance return circuit pollutes yet.
In order to solve the technical problem, the utility model discloses a following technical scheme can solve: the automatic iron remover for the low-viscosity slurry comprises a magnetic filtering tank, an inlet three-way pipe and an outlet three-way pipe, wherein the inlet three-way pipe comprises a filtrate inlet, a cleaning solution outlet, a magnetic filtering tank inlet and an inlet three-way valve; the cleaning device also comprises a detachable cleaning filter, and the cleaning filter is connected with the cleaning liquid outlet and the cleaning liquid inlet; during filtering, the circulation of filtrate is as follows: a filtrate inlet, a magnetic filtration tank outlet and a filtrate outlet; during cleaning, the circulation of the cleaning liquid is as follows: a cleaning liquid inlet, a magnetic filter tank outlet, a magnetic filter tank inlet, a cleaning liquid outlet and a cleaning filter.
In the above technical solution, preferably, the filtrate outlet is located above the filtrate inlet.
In the above technical solution, preferably, the filter medium and the cleaning medium are the same medium.
In the above technical solution, preferably, a cleaning liquid tank and a circulation pump are arranged between the cleaning liquid outlet and the cleaning filter.
In the above technical solution, preferably, the apparatus further comprises a controller, and the controller controls the conversion between the filtrate circulation and the cleaning solution circulation.
In the above technical solution, preferably, the magnetic filter tank is provided with a plurality of movable magnetic rods therein, and the movable magnetic filter tank through the magnetic rods is provided with a magnetic area and a non-magnetic area which are changed therein.
In the above technical solution, preferably, the filter mode of the cleaning filter may be a filter screen filter type or a magnetic filter type.
The circulation of the filtrate is as follows: a filtrate inlet, a magnetic filtration tank outlet and a filtrate outlet; the filtrate has iron impurities at the section of the filtrate inlet-the inlet of the magnetic filter tank, and the filtrate has no iron impurities at the section of the outlet of the magnetic filter tank-the outlet of the filtrate. The circulation of the cleaning liquid is as follows: a cleaning liquid inlet, a magnetic filter tank outlet, a magnetic filter tank inlet, a cleaning liquid outlet and a cleaning filter; when the cleaning solution is at the inlet of the magnetic filter tank and at the outlet of the magnetic filter tank, the cleaning solution has no iron impurities. And in the section of the inlet of the magnetic filter tank and the outlet of the cleaning liquid, the cleaning liquid contains iron impurities. As can be seen from the above, iron impurities exist in the sections of the filtrate inlet, the inlet of the magnetic filter tank and the inlet of the magnetic filter tank, the inlet of the cleaning solution and the outlet of the cleaning solution, and the sections are partially collinear. The sections of the outlet of the magnetic filtration tank, the outlet of the filtrate and the inlet of the cleaning solution, the outlet of the magnetic filtration tank are free from iron impurities, and the sections are partially collinear. Both when filtering and when clearing up, the pipeline that has impurity and the pipeline that does not have impurity are unanimous, and both sides can not pollute each other no matter how the operation, if appear polluting just to show that magnetic filter jar and clearance filter damage. Simultaneously with the very big clearance degree of difficulty that has reduced magnetic filtration system in filtration return circuit and clearance return circuit, need not to demolish the bar magnet again, only need to wash the cleaning solution repeatedly and just can clear up the iron impurity in the magnetic filtration system.
Compared with the prior art, the utility model discloses with magnetic filtration system and with clean system integration as an organic whole, have filtration circuit and clearance return circuit simultaneously, solved and need unpack magnetic filtration system apart just can abluent problem in the past to even still solved filtration circuit and clearance return circuit part collineation, filtration circuit can not be by the problem that clearance return circuit pollutes yet.
Drawings
Fig. 1 is a perspective view of the main structure of the utility model with a part of pipelines removed.
Fig. 2 is a perspective view of the main structure of the present invention.
Fig. 3 is a schematic side view of the main structure of the present invention.
Fig. 4 is a front schematic view of the main structure of the present invention.
Fig. 5 is a schematic top view of the main structure of the present invention.
Detailed Description
Example 1: as shown in fig. 1 to 5, the automatic iron remover for low-viscosity slurry comprises a magnetic filter tank 1, a cleaning filter, an inlet three-way pipe 3, an outlet three-way pipe 4 and a controller 5. The inlet three-way pipe 3 comprises a filtrate inlet 31, a cleaning solution outlet 33, a magnetic filter tank inlet 32 and an inlet three-way valve 34, and the outlet three-way pipe 4 comprises a filtrate outlet 41, a cleaning solution inlet 43, a magnetic filter tank outlet 42 and an outlet three-way valve 44. The magnetic filter tank 1 is connected with a filtrate inlet 32 and a filtrate outlet 42, and the filtrate outlet 42 is positioned above the filtrate inlet 32. Be provided with a plurality of mobilizable bars magnet in the magnetism filter tank 1, through reciprocating of bar magnet make the magnetism filter tank in have the magnetic domain that changes and do not have the magnetic domain, the up-down motion of filtrating from the bottom when the magnetism filter tank 1 filters. The filtering mode of the cleaning filter adopts a filter screen filtering type or a magnetic adsorption type.
In general, the filter inlet 23 is connected to the cleaning solution outlet 33, the filter outlet 24 is connected to the cleaning solution inlet 43, and the magnetic filter tank 1 is connected to the cleaning filter and then can be used directly. For better cleaning effect, a cleaning liquid tank and a circulating pump 2 can be additionally arranged between the filter inlet 23 and the cleaning liquid outlet 33 for increasing the amount of the cleaning liquid and increasing the flow rate of the cleaning liquid. There is no special case where the filter medium and the cleaning medium are the same medium, but the cleaning liquid is a pure filtrate.
In the filtering state, the inlet three-way valve 34 controls the passage between the filtering liquid inlet 31 and the inlet 32 of the magnetic filter tank, and the cleaning liquid outlet 33 is disconnected. The outlet three-way valve 44 controls the passage of the filtrate outlet 41 and the outlet 42 of the magnetic filter tank and the disconnection of the cleaning liquid inlet 43. The filtrate enters the magnetic filtration tank 1 through the filtrate inlet 31 and then exits the filtrate outlet 41 through the filtrate outlet 41, completing a filtration cycle.
The controller 5 switches the filtration cycle and the cleaning cycle according to the filtration time. Or the magnetic filter tank 1 is provided with a photoelectric detector, the adsorption degree of the magnetic rod is determined according to the light transmission change of the surface of the magnetic rod in the magnetic filter tank 1 monitored by the photoelectric detector, and then the adsorption degree is fed back to the controller 5, so that the controller 5 performs cycle switching.
When in a cleaning state, the inlet three-way valve 34 controls the passage of the cleaning liquid outlet 33 and the inlet 32 of the magnetic filter tank, and the filter liquid inlet 31 is disconnected. The outlet three-way valve 44 controls the passage of the cleaning liquid inlet 43 and the magnetic filter tank outlet 42, and the filtering liquid outlet 41 is disconnected. Cleaning solution enters the magnetic filtration tank 1 from the cleaning solution inlet 43, then enters the cleaning filter from the cleaning solution outlet 33, the cleaning solution removes impurities in the cleaning filter, the cleaning solution with the purified impurities continuously enters the magnetic filtration tank 1, and the cleaning solution brings all iron impurities in the magnetic filtration tank 1 into the cleaning filter for treatment through one-time washing. The cleaning circulation loop and the filtering circulation loop run in completely opposite directions.
Claims (7)
1. The automatic iron remover for the low-viscosity slurry comprises a magnetic filtering tank and is characterized by further comprising an inlet three-way pipe and an outlet three-way pipe, wherein the inlet three-way pipe comprises a filtering liquid inlet, a cleaning liquid outlet, a magnetic filtering tank inlet and an inlet three-way valve;
the cleaning device also comprises a detachable cleaning filter, and the cleaning filter is connected with the cleaning liquid outlet and the cleaning liquid inlet;
during filtering, the circulation of filtrate is as follows: a filtrate inlet, a magnetic filtration tank outlet and a filtrate outlet;
during cleaning, the circulation of the cleaning liquid is as follows: a cleaning liquid inlet, a magnetic filter tank outlet, a magnetic filter tank inlet, a cleaning liquid outlet and a cleaning filter.
2. An automatic de-ironing separator for low viscosity slurry according to claim 1, wherein said filtrate outlet is located above said filtrate inlet.
3. An automatic de-ironing separator for low viscosity slurry according to claim 1, wherein the filter medium and the cleaning medium are the same medium.
4. The automatic iron remover for low viscosity slurry as claimed in claim 1, wherein a cleaning liquid tank and a circulation pump are provided between said cleaning liquid outlet and said cleaning filter.
5. The automatic de-ironing separator for low viscosity slurry as claimed in claim 1, further comprising a controller for controlling the switching between the circulation of the filtering liquid and the circulation of the cleaning liquid.
6. The automatic de-ironing separator for low viscosity slurry as claimed in claim 1, wherein the magnetic filter tank is provided with a plurality of movable magnetic bars, and the movable magnetic filter tank passing through the magnetic bars is provided with a magnetic area and a non-magnetic area which are changed.
7. The automatic iron remover for low-viscosity slurry as claimed in claim 1, wherein the cleaning filter is a screen filter type or a magnetic filter type.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221180305.1U CN217450524U (en) | 2022-05-17 | 2022-05-17 | Automatic de-ironing separator of low viscosity thick liquids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221180305.1U CN217450524U (en) | 2022-05-17 | 2022-05-17 | Automatic de-ironing separator of low viscosity thick liquids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217450524U true CN217450524U (en) | 2022-09-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221180305.1U Active CN217450524U (en) | 2022-05-17 | 2022-05-17 | Automatic de-ironing separator of low viscosity thick liquids |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217450524U (en) |
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2022
- 2022-05-17 CN CN202221180305.1U patent/CN217450524U/en active Active
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