CN204073639U - Binary channels electrolysis infiltration Auto-drainage cleaning system - Google Patents
Binary channels electrolysis infiltration Auto-drainage cleaning system Download PDFInfo
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- CN204073639U CN204073639U CN201420594593.4U CN201420594593U CN204073639U CN 204073639 U CN204073639 U CN 204073639U CN 201420594593 U CN201420594593 U CN 201420594593U CN 204073639 U CN204073639 U CN 204073639U
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Abstract
The utility model provides a kind of binary channels electrolysis to permeate Auto-drainage cleaning system, comprises the first y-type filter, the second y-type filter, heating system, vacuum separation system, sheet frame pressure filtration system, electric charge electrolytic separation system, breaking emulsion and dewatering piece-rate system, counter-infiltration system.Owing to have employed technique scheme, the utility model can be applicable to the process of various industrial oil, complete pure physico decontamination process, ensure that industry oil key property, industry oil after purified treatment Reusability capable of circulation, and extend the replacement cycle of industry oil, at utmost economize energy, utilize the energy, reduce energy resource consumption.
Description
Technical field
The utility model belongs to oil filter field, particularly a kind of binary channels electrolysis infiltration Auto-drainage cleaning system.
Background technology
Lubricating oil is in the three large processes such as use, storage, transport, due to the continuous change of ambient temperature, cause the molecular structure of the reservoir vessel such as oil tank, fuel tank material in continuous motion, easily cause intermolecular gap to strengthen, the moisture in air, dust, metal ion and metal oxide etc. certainly will be embedded.The existence of Moisture in Lube Oil & can impel oil oxidation to go bad, and accelerates organic acid to corrosion of metal effect corrosion equipment, produces precipitation and hinders lubricating oil to lower the temperature normally and lubrication; The existence of these impurity, the normal wear of acceleration mechanical equipment, destroys normal lubricating system often, causes lubricating system cisco unity malfunction, and then shortens the service life of oil-using units.Traditional filter method needs heating in filter process, and energy consumption is high, maybe needs to add adsorbent and additive, causes secondary pollution.
Utility model content
The utility model provides a kind of binary channels electrolysis to permeate Auto-drainage cleaning system, this system is applicable to the process of various industrial oil, utilize pure physico decontamination process, ensure that industry oil key property, industry oil after purified treatment Reusability capable of circulation, and extend the replacement cycle of industry oil, at utmost economize energy, utilize the energy, reduce energy resource consumption.
The purpose of this utility model is realized by such technical scheme, and it comprises the first y-type filter, the second y-type filter, heating system, vacuum separation system, sheet frame pressure filtration system, electric charge electrolytic separation system, breaking emulsion and dewatering piece-rate system, counter-infiltration system; Wherein,
Described first y-type filter and the second y-type filter filter for the first time to the large granular impurity in fluid, the input of described first y-type filter is connected to the dirty oily inlet valve in one number service road, and the input of described second y-type filter is connected to No. two dirty oily inlet valves of passage;
Described heating system heats the fluid after first filtration, reduces the viscosity of fluid;
The water vapour evaporated in dirty oil and other mist are effectively extracted out by described vacuum separation system, the steam being separated and volatilizing and other pernicious gas are got rid of fast in fluid;
Described sheet frame pressure filtration system is used for filtering the suspension in fluid and impurity;
Described electric charge electrolytic separation system thoroughly can remove the harm compositions such as dissolved water, free water, metal ion, metallic particles, impurity, greasy filth and colloid in fluid fast;
Described breaking emulsion and dewatering piece-rate system carries out water-oil separating to comparatively droplet and fluid, and is stored by the water separated;
Described counter-infiltration system is for purifying the harmful substance such as mechanical admixture, greasy filth, carbide, colloid, metallic particles in fluid.
The utility model adopts exclusive spiral heating technology, mist body flash vacuum isolation technics, sheet frame pressure filtration technology, electric charge electrolytic separation technology, breaking emulsion and dewatering technology, infiltration purification techniques etc. integrally combines, the dissolved water in industry oil can be removed fast, free water, light hydrocarbon, dissolved gas, free gas and impurity, acid matter, colloid, soap class, the harmful components such as pigment, utilize pure physico decontamination process, ensure that industry oil key property, industry oil after purified treatment Reusability capable of circulation, and extend the replacement cycle of industry oil, at utmost economize energy, utilize the energy, reduce energy resource consumption.System adopts binary channels design, has the industry oil of simultaneously purified treatment two kinds of different qualities, non-interference, be independent of each other, and achieves the object of enterprise's a tractor serves several purposes.
Further, described breaking emulsion and dewatering piece-rate system comprises breaking emulsion and dewatering collector, dehydration collector is provided with in described breaking emulsion and dewatering collector, top is provided with the first Pressure gauge, bottom is provided with the first water receiver, outer wall corresponding to described first water receiver is provided with the second liquid level gauge, and the bottom of described breaking emulsion and dewatering collector is provided with the first row water valve be communicated with described first water receiver.
Further, described breaking emulsion and dewatering piece-rate system comprises breaking emulsion and dewatering separator, dehydration separator is provided with in described breaking emulsion and dewatering separator, top is provided with the second Pressure gauge, bottom is provided with the second water receiver, outer wall corresponding to described second water receiver is provided with the 3rd liquid level gauge, and the bottom of described breaking emulsion and dewatering separator is provided with the second row water valve be communicated with described second water receiver.
Further, the intelligent temperature controller that described heating system comprises heater and is connected with this heater, heating tube is provided with in described heater, top is provided with the power interface of powering to described heating tube, outer wall is provided with the first liquid level gauge, described first liquid level gauge is arranged with fluid level controller and lower fluid level controller, described heater base is connected with the second blowoff valve.
Further, described electric charge electrolytic separation system comprises electric charge electrolytic separation device, described electric charge electrolytic separation device comprises electric charge electrolytic separation device housing, positive and negative ion transmitter and high pressure atomized spray device, the bottom of described housing is provided with the first blowoff valve, described positive and negative ion transmitter is all fixed in housing, described positive and negative ion transmitter is separated by dividing plate, and described high pressure atomized spray device is fixed on described housing inner top.
Further, described counter-infiltration system comprises counter-infiltration clarifier and imports oil cup, described counter-infiltration clarifier comprises counter-infiltration purifier shell, described housing is provided with crude oil oil inlet pipe, absolute oil flowline, import oily oil inlet pipe and importing oil flowline, filter chamber is comprised in described housing, blowdown chamber, the reverse osmosis membrane core importing oil pocket and be located in filter chamber, described blowdown chamber is between described filter chamber and described importing oil pocket, described crude oil oil inlet pipe is communicated with filter chamber, the oily oil inlet pipe of described importing is connected with the importing oil-in of described reverse osmosis membrane core, the oily flowline of described importing is connected with described importing oil pocket, the oil export of pouring into of described reverse osmosis membrane core is connected with described importing oil pocket by pipeline, the sewage draining exit of described reverse osmosis membrane core is communicated with described blowdown chamber, described blowdown chamber is provided with the 3rd blowoff valve, described absolute oil flowline to export with the absolute oil of described reverse osmosis membrane core be connected through importing oil pocket and blowdown chamber.
Owing to have employed technique scheme, the utility model can be applicable to the process of various industrial oil, utilize pure physico decontamination process, ensure that industry oil key property, industry oil after purified treatment Reusability capable of circulation, and extend the replacement cycle of industry oil, at utmost economize energy, utilize the energy, reduce energy resource consumption.
Accompanying drawing explanation
Fig. 1 is structural framing figure of the present utility model.
Fig. 2 be in the utility model heating system structural representation.
Fig. 3 is the structural representation of breaking emulsion and dewatering piece-rate system in the utility model.
Fig. 4 is the structural representation of electric charge electrolytic separation system in the utility model.
Fig. 5 is the structural representation of counter-infiltration system in the utility model.
In figure, the 1, first y-type filter; 2, the second y-type filter; 3, heating system; 31, intelligent temperature controller; 32, heating tube; 33, the first liquid level gauge; 34, power interface; 341, upper fluid level controller; 342, lower fluid level controller; 35, the second blowoff valve; 4, vacuum separation system; 5, sheet frame pressure filtration system; 6, electric charge electrolytic separation system; 61, electric charge electrolytic separation device; 62, electric charge electrolytic separation device housing; 63, cation launcher; 64, anion launcher; 65, high pressure atomized spray device; 66, the first blowoff valve; 67, dividing plate; 7, breaking emulsion and dewatering piece-rate system; 71, breaking emulsion and dewatering collector; 711, dewater collector; 712, the first Pressure gauge; 713, the first water receiver; 714, the second liquid level gauge; 715, first row water valve; 72, breaking emulsion and dewatering separator; 721, dewater separator; 722, the second Pressure gauge; 723, the second water receiver; 724, the 3rd liquid level gauge; 725, second row water valve; 8, counter-infiltration system; 81, counter-infiltration clarifier; 82, oil cup is imported; 83, counter-infiltration system housing; 84, crude oil oil inlet pipe; 85, absolute oil flowline; 861, oily oil inlet pipe is imported; 862, oily flowline is imported; 871, filter chamber; 872, blowdown chamber; 873, oil pocket is imported; 88, reverse osmosis membrane core; 891, oil-in is imported; 892, oil export is imported; 893, sewage draining exit; 894, the 3rd blowoff valve; 895, absolute oil outlet.9, the dirty oily inlet valve in one number service road; 10, No. two dirty oily inlet valves of passage.
In figure, " → " represents that fluid flows to,
represent waste stream to,
represent that clean oil flows to,
represent that importing oil flows to.
Detailed description of the invention
The technological means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the utility model further.
As shown in Figure 1, the utility model comprises the first y-type filter 1, second y-type filter 2, heating system 3, vacuum separation system 4, sheet frame pressure filtration system 5, electric charge electrolytic separation system 6, breaking emulsion and dewatering piece-rate system 7, counter-infiltration system 8; Wherein,
Large granular impurity in described first y-type filter 1 and the second y-type filter 2 pairs of fluid filters for the first time, the input of described first y-type filter 1 is connected to the dirty oily inlet valve 9 in one number service road, and the input of described second y-type filter 1 is connected to No. two dirty oily inlet valves 10 of passage;
Described heating system 3 heats the fluid after first filtration, reduces the viscosity of fluid;
The water vapour evaporated in dirty oil and other mist are effectively extracted out by described vacuum separation system 4, the steam being separated and volatilizing and other pernicious gas are got rid of fast in fluid;
Described sheet frame pressure filtration system 5 is used for filtering the suspension in fluid and impurity;
Described electric charge electrolytic separation system 6 thoroughly can remove the harm compositions such as dissolved water, free water, metal ion, metallic particles, impurity, greasy filth and colloid in fluid fast;
Described breaking emulsion and dewatering piece-rate system 7 carries out water-oil separating to comparatively droplet and fluid, and is stored by the water separated;
Described counter-infiltration system 8 is for purifying the harmful substance such as mechanical admixture, greasy filth, carbide, colloid, metallic particles in fluid.
The utility model adopts exclusive spiral heating technology, mist body flash vacuum isolation technics, sheet frame pressure filtration technology, electric charge electrolytic separation technology, breaking emulsion and dewatering technology, infiltration purification techniques etc. integrally combines, the dissolved water in industry oil can be removed fast, free water, light hydrocarbon, dissolved gas, free gas and impurity, acid matter, colloid, soap class, the harmful components such as pigment, utilize pure physico decontamination process, ensure that industry oil key property, industry oil after purified treatment Reusability capable of circulation, and extend the replacement cycle of industry oil, at utmost economize energy, utilize the energy, reduce energy resource consumption.System adopts binary channels design, has the industry oil of simultaneously purified treatment two kinds of different qualities, non-interference, be independent of each other, and achieves the object of enterprise's a tractor serves several purposes.
As shown in Figure 3, described breaking emulsion and dewatering piece-rate system 7 comprises breaking emulsion and dewatering collector 71, dehydration collector 711 is provided with in described breaking emulsion and dewatering collector 71, top is provided with the first Pressure gauge 712, bottom is provided with the first water receiver 713, outer wall corresponding to described first water receiver 713 is provided with the second liquid level gauge 714, and the bottom of described breaking emulsion and dewatering collector 71 is provided with the first row water valve 715 be communicated with described first water receiver 713.Particularly, described dirty liquid flows to the breaking emulsion and dewatering collector 71 in described breaking emulsion and dewatering piece-rate system 7 under oil pump dynamic action, it is the dehydration collector 711 be made by specific glass fibrous material in described breaking emulsion and dewatering collector 71, it has good hydrophily, after fluid flows through this system, unique filter material of innermost layer particulate pollutant first in filtering fluid, and promptly break the adhesion between oil molecule and hydrone, hydrone drips again and is combined into the globule by unique filter material in middle level rapidly, the larger-size globule can rely on the gravitational settling of self to water leg, the globule that size is less has little time sedimentation and will be carried under one's arms by fluid and flow to next purifier, at described breaking emulsion and dewatering collector 71 by the moisture deviate from, be stored in described first water receiver 713 under gravity, the water entered in described first water receiver 713 can be shown intuitively by described second liquid level gauge 714, when water level arrives the second liquid level gauge 714 top, open described first row water valve 715, the water separated in fluid will be left out.
As shown in Figure 3, described breaking emulsion and dewatering piece-rate system 7 comprises breaking emulsion and dewatering separator 72, dehydration separator 721 is provided with in described breaking emulsion and dewatering separator 72, top is provided with the second Pressure gauge 722, bottom is provided with the second water receiver 723, outer wall corresponding to described second water receiver 723 is provided with the 3rd liquid level gauge 724, and the bottom of described breaking emulsion and dewatering separator 72 is provided with the second row water valve 725 be communicated with described second water receiver 723.Particularly, dirty oil is after described breaking emulsion and dewatering collector 71, described breaking emulsion and dewatering separator 72 is entered at the flows by action of malleation, by unique filter material in described breaking emulsion and dewatering separator 72, through the dehydration separator 721 that specially treated macromolecular material is made, described dehydration separator 721 has good hydrophobicity, make droplet by the outside of effectively tackling at filter core, fluid is only allowed to pass through and do not allow moisture pass through, thus reach the object that water-oil separating removes moisture further, by the water that described breaking emulsion and dewatering piece-rate system 7 is separated, due to the heavy different relation of water and oil ratio, be stored in described second water receiver 723 under gravity, the water entered in described second water receiver 723 can be shown intuitively by described 3rd liquid level gauge 724, when water level arrives described 3rd liquid level gauge 724 top, open described second row water valve 725, the water separated in fluid will be left out.
Dirty oil is intuitively shown by described first Pressure gauge 712 at the pressure of described dehydration collector 711, pressure in described dehydration separator 721 is intuitively shown by described second Pressure gauge 722, when the hypertonia of described first Pressure gauge 712 and the second Pressure gauge 722, prove dirty oil viscosity excessive or dehydration collector 711 or dehydration separator 721 block, then should heat reduction viscosity in time, and cleaning and dewatering collector 711 and dehydration separator 721, otherwise further filtration work can be affected.The dehydration of dirty oil is assembled and dehydration separating treatment, is used to water free water, emulsified water and the dissolved water in fluid, make fluid water content reach the use standard of country's oil.
As shown in Figure 2, the intelligent temperature controller 31 that described heating system 3 comprises heater and is connected with this heater, heating tube 32 is provided with in described heater, top is provided with the power interface 34 of powering to described heating tube 32, outer wall is provided with the first liquid level gauge 33, described first liquid level gauge 33 is arranged with fluid level controller 341 and lower fluid level controller 342, described heater base is connected with the second blowoff valve 35.Particularly, the dirty oil of described absorption enters in described heater and heats up, dirty oil moves from lower to upper in this heater, can observe out intuitively from described first liquid level gauge 33, when dirty oil arrives described upper fluid level controller 341, described intelligent temperature controller 31 will send control instruction (its temperature can be arranged arbitrarily between 20 ~ 120 degree), make described heater in running order, by described power interface 34 transportation work power supply to described heating tube 32, its heating tube 32 starts the work of generating heat; Otherwise when dirty oil is lower than described lower fluid level controller 342, the control instruction that described heater sends according to intelligent temperature controller 31 stops transportation work power supply, and corresponding described heating tube 32 stops heating work.In the present embodiment, the viscosity reducing fluid is used to the heating of dirty oil, strengthens the mobility of fluid, shorten the purification filtering cycle.
As shown in Figure 4, described electric charge electrolytic separation system 6 comprises electric charge electrolytic separation device 61, and described electric charge electrolytic separation device 61 comprises electric charge electrolytic separation device housing 62, ion generator, positive and negative ion transmitter 63,64 and high pressure atomized spray device 65.The bottom of described electric charge electrolytic separation device housing 62 is provided with the first blowoff valve 66, described positive and negative ion transmitter 63,64 is all fixed in electric charge electrolytic separation device housing 62, described positive and negative ion transmitter 63,64 is separated by dividing plate, prevents to puncture to form two runners simultaneously; Described ion generator is fixed on described electric charge electrolytic separation device housing 62, and described ion generator is connected with described positive and negative ion transmitter 63,64, for positive and negative ion transmitter 63,64 provides corresponding ion; Described high pressure atomized spray device 65 is fixed on described electric charge electrolytic separation device housing 62 inner top, nebulizes, break intermolecular adhesion and tractive force from the fluid of high pressure atomized spray device 65 ejection.Fluid through high pressure atomized spray device 65 divides two-way to flow, one road flows into the runner at anion launcher 64 place, metal ion in fluid is transformed into "-" charged ion, another road flows into the runner at cation launcher 63 place, metal ion in fluid is transformed into "+" charged ion, final two-way fluid mixed flow again, after mixed flow, counter ion attracts each other, the quick progress of disease becomes molecule, become particle by molecule again and increase gradually, and under gravity, particles settling is at electric charge electrolytic separation device housing 62 inner bottom part.
As shown in Figure 5, described counter-infiltration system 8 comprises counter-infiltration clarifier 81 and imports oil cup 82, counter-infiltration clarifier 81 comprises counter-infiltration purifier shell 83, described counter-infiltration purifier shell 83 is provided with crude oil oil inlet pipe 84, absolute oil flowline 85, import oily oil inlet pipe 861 and import oily flowline 862, 871 filter chambers are comprised in described counter-infiltration purifier shell 83, blowdown chamber 872, the reverse osmosis membrane core 88 importing oil pocket 873 and be located in filter chamber 871, described blowdown chamber 872 is between described filter chamber 871 and described importing oil pocket 873, described crude oil oil inlet pipe is communicated with filter chamber 871, the oily oil inlet pipe of described importing 861 is connected with the importing oil-in 891 of described reverse osmosis membrane core 88, the oily flowline of described importing is connected with described importing oil pocket 873, the importing oil export 892 of described reverse osmosis membrane core 88 is connected with described importing oil pocket 873 by pipeline, the sewage draining exit 893 of described reverse osmosis membrane core 88 is communicated with described blowdown chamber 872, described blowdown chamber 872 is provided with the 3rd blowoff valve 894, described absolute oil flowline 85 exports 895 with blowdown chamber 872 with the absolute oil of described reverse osmosis membrane core 88 through importing oil pocket 873 and is connected.
Fluid need be processed under the effect of malleation, enter the stainless steel casing net of reverse osmosis membrane core 88, enter successively in runner, very thin filter course is evenly distributed at runner inner fluid, flow into successively again in impurity collection channel, the discarded object that film stops is filtered in impurity collection channel, be collected in and flow into sewage draining exit eliminating together, fluid is entering filter membrane through impurity collection channel, clean clean fluid can penetrate filter membrane, flow to center stream oil pipe under pressure, be excluded through absolute oil outlet 895; Import oil to enter under pressure and import oil-in 891, go through runner one impurity collection channel one filter membrane, filter membrane with need process fluid and to meet and after there is reverse osmosis process, import oil and flow to and import oil export 892 and be excluded.
These are only embodiment of the present utility model; not thereby the scope of the claims of the present utility model is limited; every equivalent structure utilizing the utility model description and accompanying drawing content to do; directly or indirectly be used in the technical field that other are relevant, all in like manner within scope of patent protection of the present utility model.
Claims (6)
1. binary channels electrolysis infiltration Auto-drainage cleaning system, it is characterized in that, comprise the first y-type filter, the second y-type filter, heating system, vacuum separation system, sheet frame pressure filtration system, electric charge electrolytic separation system, breaking emulsion and dewatering piece-rate system, counter-infiltration system; Wherein,
Described first y-type filter and the second y-type filter filter for the first time to the large granular impurity in fluid, the input of described first y-type filter is connected to the dirty oily inlet valve in one number service road, and the input of described second y-type filter is connected to No. two dirty oily inlet valves of passage;
Described heating system heats the fluid after first filtration, reduces the viscosity of fluid;
The water vapour evaporated in dirty oil and other mist are effectively extracted out by described vacuum separation system, the steam being separated and volatilizing and other pernicious gas are got rid of fast in fluid;
Described sheet frame pressure filtration system is used for filtering the suspension in fluid and impurity;
Described electric charge electrolytic separation system thoroughly can remove the harm compositions such as dissolved water, free water, metal ion, metallic particles, impurity, greasy filth and colloid in fluid fast;
Described breaking emulsion and dewatering piece-rate system carries out water-oil separating to comparatively droplet and fluid, and is stored by the water separated;
Described counter-infiltration system is for purifying the harmful substance such as mechanical admixture, greasy filth, carbide, colloid, metallic particles in fluid.
2. binary channels electrolysis infiltration Auto-drainage cleaning system as claimed in claim 1, it is characterized in that, described breaking emulsion and dewatering piece-rate system comprises breaking emulsion and dewatering collector, dehydration collector is provided with in described breaking emulsion and dewatering collector, top is provided with the first Pressure gauge, bottom is provided with the first water receiver, and the outer wall corresponding to described first water receiver is provided with the second liquid level gauge, and the bottom of described breaking emulsion and dewatering collector is provided with the first row water valve be communicated with described first water receiver.
3. binary channels electrolysis infiltration Auto-drainage cleaning system as claimed in claim 1, it is characterized in that, described breaking emulsion and dewatering piece-rate system comprises breaking emulsion and dewatering separator, dehydration separator is provided with in described breaking emulsion and dewatering separator, top is provided with the second Pressure gauge, bottom is provided with the second water receiver, and the outer wall corresponding to described second water receiver is provided with the 3rd liquid level gauge, and the bottom of described breaking emulsion and dewatering separator is provided with the second row water valve be communicated with described second water receiver.
4. binary channels electrolysis infiltration Auto-drainage cleaning system as claimed in claim 1, it is characterized in that, the intelligent temperature controller that described heating system comprises heater and is connected with this heater, heating tube is provided with in described heater, top is provided with the power interface of powering to described heating tube, outer wall is provided with the first liquid level gauge, and described first liquid level gauge is arranged with fluid level controller and lower fluid level controller, described heater base is connected with the second blowoff valve.
5. binary channels electrolysis infiltration Auto-drainage cleaning system as claimed in claim 1, it is characterized in that, described electric charge electrolytic separation system comprises electric charge electrolytic separation device, described electric charge electrolytic separation device comprises electric charge electrolytic separation device housing, positive and negative ion transmitter and high pressure atomized spray device, the bottom of described housing is provided with the first blowoff valve, described positive and negative ion transmitter is all fixed in housing, described positive and negative ion transmitter is separated by dividing plate, and described high pressure atomized spray device is fixed on described housing inner top.
6. binary channels electrolysis infiltration Auto-drainage cleaning system as claimed in claim 1, it is characterized in that, described counter-infiltration system comprises counter-infiltration clarifier and imports oil cup, described counter-infiltration clarifier comprises counter-infiltration purifier shell, described housing is provided with crude oil oil inlet pipe, absolute oil flowline, import oily oil inlet pipe and importing oil flowline, filter chamber is comprised in described housing, blowdown chamber, the reverse osmosis membrane core importing oil pocket and be located in filter chamber, described blowdown chamber is between described filter chamber and described importing oil pocket, described crude oil oil inlet pipe is communicated with filter chamber, the oily oil inlet pipe of described importing is connected with the importing oil-in of described reverse osmosis membrane core, the oily flowline of described importing is connected with described importing oil pocket, the oil export of pouring into of described reverse osmosis membrane core is connected with described importing oil pocket by pipeline, the sewage draining exit of described reverse osmosis membrane core is communicated with described blowdown chamber, described blowdown chamber is provided with the 3rd blowoff valve, described absolute oil flowline to export with the absolute oil of described reverse osmosis membrane core be connected through importing oil pocket and blowdown chamber.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420594593.4U CN204073639U (en) | 2014-10-14 | 2014-10-14 | Binary channels electrolysis infiltration Auto-drainage cleaning system |
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| CN201420594593.4U CN204073639U (en) | 2014-10-14 | 2014-10-14 | Binary channels electrolysis infiltration Auto-drainage cleaning system |
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| CN204073639U true CN204073639U (en) | 2015-01-07 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113275127A (en) * | 2021-06-15 | 2021-08-20 | 中国石油化工股份有限公司 | Solid particle electrostatic separation device and method |
| CN114618230A (en) * | 2022-04-11 | 2022-06-14 | 江西宝嘉生物发展有限公司 | Ultra-micro filtering equipment |
-
2014
- 2014-10-14 CN CN201420594593.4U patent/CN204073639U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113275127A (en) * | 2021-06-15 | 2021-08-20 | 中国石油化工股份有限公司 | Solid particle electrostatic separation device and method |
| CN113275127B (en) * | 2021-06-15 | 2023-11-14 | 中国石油化工股份有限公司 | Solid particle electrostatic separation device and method |
| CN114618230A (en) * | 2022-04-11 | 2022-06-14 | 江西宝嘉生物发展有限公司 | Ultra-micro filtering equipment |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20171014 |