CN212523241U - Flow dividing controller for white oil filtering system - Google Patents
Flow dividing controller for white oil filtering system Download PDFInfo
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- CN212523241U CN212523241U CN202020972407.1U CN202020972407U CN212523241U CN 212523241 U CN212523241 U CN 212523241U CN 202020972407 U CN202020972407 U CN 202020972407U CN 212523241 U CN212523241 U CN 212523241U
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Abstract
The utility model relates to a shunt controller for among white oil filtration system, including main line, lateral line, locate solenoid valve I on the lateral line, locate the interior lower level sensor II of straining jar of essence, its technical essential is: the overflow tank is characterized by further comprising overflow tanks, the number of the overflow tanks is the same as that of the fine filtration tanks, the overflow tanks are in one-to-one correspondence with the number of the fine filtration tanks, overflow pipes are connected between the overflow tanks and the fine filtration tanks, return branch pipes are arranged at the bottoms of the overflow tanks, the tail ends of the return branch pipes of the overflow tanks are connected with a confluence header pipe, the tail ends of the confluence header pipe are communicated with the top of the coarse filtration tank, electromagnetic valves II are arranged on the return branch pipes, an upper liquid level sensor I and a lower liquid level sensor I are arranged in each overflow. The problem that when filtering materials are injected into each fine filtering unit through a coarse filtering device, the flow consistency of each fine filtering unit is difficult to guarantee is solved, and the influence of the material flow rate, the fine filtering unit installation position and the like on shunt control is greatly reduced.
Description
Technical Field
The utility model relates to a chemical production technical field, concretely relates to a flow distribution controller for among white oil filtration system.
Background
In the chemical production process, the white oil is usually used as an additive, the white oil needs to be separated from the product in the later stage of the production link, and if the separated white oil is discharged into the air, the white oil is wasted, and the environmental pollution is caused, so that the separated white oil is generally recycled by enterprises. During recovery, coarse filtration is performed through a coarse filtration device, fine filtration is performed through a fine filtration device, the fine filtration device needs to be used in parallel by a plurality of fine filtration units because the fine filtration process requires small flow of the filtration materials, but when the coarse filtration device injects the filtration materials into each fine filtration unit, the flow of each fine filtration unit is difficult to ensure to be consistent, and therefore, distribution of the filtration materials is difficult to control.
CN208757079U discloses a shunt controller used in a white oil filtering system, which comprises a main pipeline, wherein one end of the main pipeline is sealed, the other end of the main pipeline is connected with an oil inlet joint, a plurality of shunt pipelines are arranged at two sides of the main pipeline, and each shunt pipeline is provided with a two-way electromagnetic valve; a fine filtration module is arranged below each shunt pipeline, and is provided with a liquid level sensing controller which is connected with a two-way electromagnetic valve. This patent comes automatic distribution flow according to the filtration condition of essence filtration module, guarantees that essence filters the normal high-efficient conduct of work. The working principle is as follows: the oil inlet joint is connected with a pre-stage coarse filtration device, and the white oil after coarse filtration enters a diversion pipeline through a main pipeline; when a liquid level sensing controller of the fine filtration module monitors that the white oil liquid level in the fine filtration module is lower than a lower limit set value, a two-way solenoid valve is opened, and the white oil in a shunt pipeline flows into the fine filtration module; when the white oil injection reaches the upper limit set value, the two-way electromagnetic valve is closed, the flow can be automatically distributed according to the filtering condition of the fine filtering module, and the normal and efficient operation of the fine filtering operation is ensured to a certain extent. However, the following problems still exist: when the liquid level sensing controller monitors that the white oil liquid level in the fine filtration module reaches an upper limit set value, the two-way solenoid valve cuts off the shunt pipeline, but materials in the section of the shunt pipeline from the solenoid valve position to the fine filtration module continuously enter the fine filtration module, under the influence of the material flow rate, the position of the fine filtration module, the length of the pipeline and the like, the quantity of the materials entering each fine filtration module is still different, so that higher requirements are provided for the installation position of each fine filtration module, and the difficulty is increased for equipment assembly. Based on this, the structure of the existing flow dividing controller used in the white oil filtering system still needs to be improved.
Disclosure of Invention
The utility model aims at providing a rational in infrastructure, use reliable a shunt controller for among white oil filtration system, when having solved and having poured into the filtration material into to each essence by coarse filter equipment, hardly guarantee the unanimous problem of flow of every essence filtration unit, the influence greatly reduced of shunt control is strained to material velocity of flow, essence filtration unit mounted position and pipeline length.
The technical scheme of the utility model is that:
the utility model provides a shunt controller for among white oil filtration system, includes the main line, connects a plurality of branch pipelines between main line and each smart canister, locates solenoid valve I on each branch pipeline, locates the lower liquid level sensor II in the smart canister, and its technical essential is: in addition including locating the overflow launder in the smart canister outside, the quantity of overflow launder is the same and the one-to-one with the quantity of smart canister, is connected with the overflow pipe between the top surface of overflow launder and the smart canister top side, and the bottom of overflow launder is equipped with the return branch pipe, and the return branch pipe end and the total union coupling of each overflow launder are connected, and total union coupling's end and coarse filter tank top intercommunication are equipped with solenoid valve II on each return branch pipe, are equipped with level sensor I and lower level sensor I in each overflow launder respectively, and each branch pipeline corresponds I feed liquor side position of solenoid valve and is equipped with manual control.
The flow distribution controller for the white oil filtering system is characterized in that one end of the main pipeline is provided with the oil inlet connector, the other end of the main pipeline is provided with the plugging head, and the inner end of the oil inlet connector is provided with the filter screen.
The aforesaid is arranged in the reposition of redundant personnel controller of white oil filtration system, the central line of collecting main is parallel with the horizontal plane, and the end utilizes the elbow to be connected with coarse filtration jar top, and collecting main is higher than the coarse filtration jar position in the vertical direction.
According to the flow distribution controller for the white oil filtering system, the bottom of the overflow groove is provided with the cone hopper, and the lower liquid level sensor I is positioned at the lower part of the cone hopper.
The utility model has the advantages that:
1. through setting up the overflow launder, the biggest essence filtration volume of every essence canister can be set for through physical structure, and when lower level sensor I in the overflow launder detected liquid, it showed that the essence canister reaches the biggest essence filtration volume, solenoid valve I cut off the branch pipeline, and the part of continuing the unloading still can get into in the overflow launder through the overflow pipe, does not influence the essence filtration volume that sets for in the essence canister, has consequently realized accurate reposition of redundant personnel control to every essence canister, has guaranteed that the flow of every essence canister is unanimous. The problem of when filling into the filtration material to each essence filtration unit by rough filter equipment, hardly guarantee the flow unanimity of each essence filtration unit is solved, the influence that material velocity of flow, essence filtration unit mounted position and pipeline length shunt control greatly reduced.
2. When the lower liquid level sensor I in the overflow groove detects liquid, the solenoid valve I cuts off the branch pipeline, the solenoid valve II is opened, the liquid in the overflow groove is discharged into the backflow branch pipe, and flows back to the coarse filtration tank through the backflow branch pipe and the confluence main pipe. When the liquid level sensor I on the overflow groove detects liquid, the electromagnetic valve I or the electromagnetic valve II is damaged, the worker is reminded, and the branch pipeline is cut off by using the manual control valve for maintenance. Convenient operation and reliable use.
Drawings
Fig. 1 is a schematic view of the usage state of the present invention;
fig. 2 is a left side view of fig. 1 (with a coarse canister portion omitted).
In the figure: 1. the system comprises an oil inlet joint, a main pipeline, a blocking head, a branch pipeline, a manual control valve, a solenoid valve I, a solenoid valve 7, an overflow pipe, an upper liquid level sensor I, an upper liquid level sensor 9, an overflow groove, a lower liquid level sensor I, an upper liquid level sensor 11, a solenoid valve II, a return branch pipe 12, a confluence main pipe 13, a coarse filtration tank 14, a lifting pump 15, a filter screen 16, a fine filtration tank 17 and a lower liquid level sensor II.
Detailed Description
As shown in fig. 1 and 2, the flow dividing controller for the white oil filtering system comprises a main pipeline 2, a plurality of branch pipelines 4 connected between the main pipeline 2 and each fine filtering tank 17, electromagnetic valves i 6 arranged on the branch pipelines 4, a lower liquid level sensor ii 18 arranged in the fine filtering tank 17, and an overflow trough 9 arranged outside the fine filtering tank 17.
The quantity of overflow launder 9 is the same and the one-to-one correspondence with the quantity of essence jar 17, be connected with overflow pipe 7 between the top surface of overflow launder 9 and the essence jar 17 top side, the bottom of overflow launder 9 is equipped with return branch pipe 12, the return branch pipe 12 end of each overflow launder 9 is connected with total manifold 13, total manifold 13's end and coarse filtration jar 14 top intercommunication converge, be equipped with solenoid valve II 11 on each return branch pipe 12, be equipped with liquid level sensor I8 and lower liquid level sensor I10 in each overflow launder 9 respectively, each branch pipeline 4 corresponds solenoid valve I6 inlet liquid side position and is equipped with manual control valve 5.
In this embodiment, an oil inlet joint 1 is arranged at one end of the main pipeline 2, a blocking head 3 is arranged at the other end of the main pipeline, and a filter screen 16 is arranged at the inner end of the oil inlet joint 1. The central line of the confluence main pipe 13 is parallel to the horizontal plane, the tail end of the confluence main pipe is connected with the top of the coarse filtration tank 14 through an elbow, and the confluence main pipe 13 is higher than the position of the coarse filtration tank 14 in the vertical direction. The bottom of the overflow groove 9 is a conical hopper, and the lower liquid level sensor I10 is positioned at the lower part of the conical hopper.
The working principle is as follows:
after white oil enters the coarse filtration tank 14 for filtration, the primarily filtered material is sent to the main pipeline 2 through the lifting pump 15 from the bottom, and then is distributed by the main pipeline 2 to enter each branch pipeline 4, so as to enter each fine filtration tank 17, the liquid in the fine filtration tank 17 can overflow to the corresponding overflow tank 9 after reaching the maximum fine filtration amount, when the liquid level sensor I10 detects the liquid, it is indicated that the fine filtration tank 17 has reached the maximum fine filtration amount, the solenoid valve I6 cuts off the branch pipeline 4, meanwhile, the solenoid valve II 11 is opened, the liquid in the overflow tank 9 is discharged into the backflow branch pipe 12, and flows back to the coarse filtration tank 14 through the backflow branch pipe 12 and the confluence main pipe 13, and when the liquid level sensor I10 cannot detect the liquid for a set time, the solenoid valve II 11 is closed.
When the lower liquid level sensor II 18 in the fine filtration tank 17 cannot detect liquid, the liquid needs to be injected into the fine filtration tank 17 again, the electromagnetic valve I6 is opened, and the steps are repeated.
When the upper liquid level sensor I8 in the overflow groove 9 detects liquid, the electromagnetic valve I6 or the electromagnetic valve II 11 is damaged, the worker is reminded, and the branch pipeline 4 is cut off by using the manual control valve 5 for maintenance.
The embodiments of the present invention have been described in detail, but the description is only for the preferred embodiments of the present invention and should not be construed as limiting the scope of the present invention. All equivalent changes and modifications made within the scope of the present invention should be covered by the present patent.
Claims (4)
1. The utility model provides a shunt controller for among white oil filtration system, includes the main line, connects a plurality of branch pipelines between main line and each smart canister, locates solenoid valve I on each branch pipeline, locates the lower liquid level sensor II in the smart canister, its characterized in that: in addition including locating the overflow launder in the smart canister outside, the quantity of overflow launder is the same and the one-to-one with the quantity of smart canister, is connected with the overflow pipe between the top surface of overflow launder and the smart canister top side, and the bottom of overflow launder is equipped with the return branch pipe, and the return branch pipe end and the total union coupling of each overflow launder are connected, and total union coupling's end and coarse filter tank top intercommunication are equipped with solenoid valve II on each return branch pipe, are equipped with level sensor I and lower level sensor I in each overflow launder respectively, and each branch pipeline corresponds I feed liquor side position of solenoid valve and is equipped with manual control.
2. The flow divider controller for use in a white oil filtration system of claim 1, wherein: an oil inlet connector is arranged at one end of the main pipeline, a blocking head is arranged at the other end of the main pipeline, and a filter screen is arranged at the inner end of the oil inlet connector.
3. The flow divider controller for use in a white oil filtration system of claim 1, wherein: the central line of the confluence main pipe is parallel to the horizontal plane, the tail end of the confluence main pipe is connected with the top of the rough filtering tank through an elbow, and the confluence main pipe is higher than the position of the rough filtering tank in the vertical direction.
4. The flow divider controller for use in a white oil filtration system of claim 1, wherein: the bottom of the overflow groove is a conical hopper, and the lower liquid level sensor I is positioned at the lower part of the conical hopper.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113023804A (en) * | 2021-03-26 | 2021-06-25 | 天津纳万源科技发展有限公司 | Multistage fine filter unit for circulating water |
CN114405104A (en) * | 2022-03-30 | 2022-04-29 | 新乡市立夏过滤技术有限公司 | Hydraulic support filter for coal mine machine |
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2020
- 2020-06-02 CN CN202020972407.1U patent/CN212523241U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113023804A (en) * | 2021-03-26 | 2021-06-25 | 天津纳万源科技发展有限公司 | Multistage fine filter unit for circulating water |
CN114405104A (en) * | 2022-03-30 | 2022-04-29 | 新乡市立夏过滤技术有限公司 | Hydraulic support filter for coal mine machine |
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