CN204661634U - A kind of Mobile lubrication oil three combined dehydration devices - Google Patents
A kind of Mobile lubrication oil three combined dehydration devices Download PDFInfo
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- CN204661634U CN204661634U CN201520360197.XU CN201520360197U CN204661634U CN 204661634 U CN204661634 U CN 204661634U CN 201520360197 U CN201520360197 U CN 201520360197U CN 204661634 U CN204661634 U CN 204661634U
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- vacuum tank
- swirler
- pipeline
- buffer container
- oil
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Abstract
The utility model discloses a kind of Mobile lubrication oil three combined dehydration devices, comprise vehicle frame, vehicle frame is provided with and all presses feed divider and several swirler, described swirler is connected with all pressing feed divider simultaneously; In the eddy flow chamber of swirler, be provided with pulsed electrode, be connected bottom described swirler with underflow buffer container, its top is connected with overflow buffer container; Described overflow buffer container is connected with vacuum tank with strainer, well heater successively, and described vacuum tank is connected with a vacuum pump, also comprises a nitrogen gas generator, and described nitrogen gas generator is connected with the bottom of vacuum tank after nitrogen intake valve.The utility model can not only remove mechanical impurity, moisture, gas etc. in lubricating oil, also has good adaptation to third phase milk sap complicated in lubricating oil, makes it recover oil quality, be applicable to the purification of contaminated lubricating oil on various engineering mechanical device.
Description
Technical field
The utility model relates to a kind of oily dewatering purifying equipment, particularly relates to a kind of Mobile lubrication oil three combined dehydration devices.
Background technology
Along with the fast development of global industry economy, with the increase of oil mass, technical oils particularly lubricating oil, hydraulic efficiency oil is widely used in the fields such as machinery, electric power, transport and chemical industry, is described as " blood " of modern industry, in the national economic development, occupies critical role.Lubricating oil is very easily polluted in storage, transport, filling and use procedure, forms oil in water emulsion, affects oil product physico-chemical property, causes oil decay, causes lubrication trouble.If do not processed this part oil in water emulsion, will waste be brought to resource environment and pollute.Therefore, exploitation lubricant oil dewatered clean device, improves the processing condition of sump oil breakdown of emulsion purifying regeneration, the waste oil regeneration reuse of emulsification, nervous for alleviation petroleum resources, reduces environmental pollution significant; For with oily rich and influential family being also the approach reducing consumption, reduce costs; For state policies and principles, set up the strategy of sustainable development, promote the exploitation of new forms of energy and the renewable energy resources, meet the requirement of national recycling economy.
Conventional lubricant oil dewatered clean method has settling process, centrifuging etc., but Shortcomings: (1) settling process, breaking emulsion and dewatering efficiency is low; (2) centrifuging, easily causes additive losses in oil too much; (3) vaccum heating method, process high-moisture fluid energy consumption is high; (4) filtration method, processing power is limited; (5) chemical method, fluid is easily polluted by chemical demulsifier.
What developed just adopts single dewatered clean mechanism for lubricant oil dewatered clean device majority, so there is energy consumption greatly in the dewatering purifying equipment on market, and the problems such as the breakdown of emulsion time is long, and efficiency is low.Therefore, need to be improved existing lubricant oil dewatered clean device, develop a kind of lubricant oil dewatered clean device of new and effective, energy-conserving and environment-protective.
Utility model content
For prior art above shortcomings, the purpose of this utility model is how to solve the problem that existing lubricant oil dewatered clean plant efficiency is low, energy consumption is large, there is provided a kind of Mobile lubrication oil three combined dehydration devices, the mechanical impurity in lubricating oil, moisture, gas etc. can not only be removed, also there is good adaptation to third phase milk sap complicated in lubricating oil, make it recover oil quality, be applicable to the purification of contaminated lubricating oil on various engineering mechanical device.
In order to solve the problems of the technologies described above, the technical solution adopted in the utility model is such: a kind of Mobile lubrication oil three combined dehydration devices, it is characterized in that: comprise vehicle frame, vehicle frame is provided with and all presses feed divider and several swirler, described swirler is connected with all pressing all extrusion mouth of feed divider simultaneously; In the eddy flow chamber of swirler, be provided with pulsed electrode, described pulsed electrode is connected with high-voltage pulse power source;
Underflow opening bottom described swirler is connected with underflow buffer container by pipeline, and the overflow port on its top is connected with overflow buffer container by pipeline; The outlet of described overflow buffer container is connected with vacuum tank with strainer, well heater successively by pipeline after fuel charging valve, and the pipeline be connected with vacuum tank stretches in vacuum tank, and the one end stretching into vacuum tank at pipeline is provided with a spray thrower; The top of described vacuum tank is connected with a vacuum pump by pipeline, and the pipeline between vacuum pump and vacuum tank is provided with condenser, and the outlet bottom described condenser is connected with water discharge valve;
The bottom of described vacuum tank is connected with oil drain pump by pipeline, and described oil drain pump is connected with a secondary filter by pipeline, and the outlet of this secondary filter is provided with draining valve;
Also comprise a nitrogen gas generator, described nitrogen gas generator is connected with the bottom of vacuum tank after nitrogen intake valve.
Further, also comprise a housing, can be controlled swirler, fuel charging valve, well heater, condenser, vacuum pump, draining valve, water discharge valve, nitrogen gas generator, nitrogen intake valve and high-voltage pulse power source by this housing.
Further, tensimeter is provided with all pressing on feed divider.
Further, described vehicle frame has four castors.
Compared with prior art, the utility model tool has the following advantages:
1. adopt three uniting array dehydration techniques, namely the centrifuge field part be made up of swirler, the pulsed electric field part be made up of high-voltage pulse electrode and high-voltage pulse power source and the vacuum field part combination be made up of vacuum tank and vacuum pump dewater, thus make dehydration degasifying effect better.
2. adopt and all press feed divider simultaneously to several swirler feed, to process more oil plant simultaneously, thus improve the dewatering efficiency of whole device.
3. equipment is simple, easy handling, and easily, maintenance workload is less in mounting or dismounting.Filter element adopts magnetic filter, can meet the requirement of various operating mode filtering accuracy;
Accompanying drawing explanation
Fig. 1 is schematic perspective view of the present utility model.
Fig. 2 is front view of the present utility model.
Fig. 3 is vertical view of the present utility model.
In figure: 1-vehicle frame, 2-all press feed divider, 3-swirler, 4-underflow buffer container, 5-overflow buffer container, 6-fuel charging valve, 7-strainer, 8-well heater, 9-vacuum tank, 10-vacuum pump, 11-condenser, 12-oil drain pump, 13-secondary filter, 14-draining valve, 15-nitrogen gas generator, 16-nitrogen intake valve, 17-housing, 18-tensimeter, 19-castor.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
Embodiment: see Fig. 1, Fig. 2 and Fig. 3, a kind of Mobile lubrication oil three combined dehydration devices, comprise vehicle frame 1, described vehicle frame 1 has four castors 19, thus makes the movement of whole device convenient, quick.Vehicle frame 1 is provided with and all presses feed divider 2 and several swirler 3, described swirler 3 is connected with all pressing all extrusion mouth of feed divider 2 simultaneously; To process more oil plant simultaneously, thus improve the dewatering efficiency of whole device.During concrete enforcement, be provided with tensimeter 18 all pressing on feed divider 2, with real-time monitors oil hydraulic coupling situation, ensure the operating pressure of swirler 3, to reach best separating effect.Described swirler 3 number is 4, and adopts the distributing style of inclination installation curve type in parallel.During use, be connected all pressing the import of feed divider 2 with chemical pump by pipeline, all feed divider 2 is pressed to be sent into certain pressure by pending lubricating oil, by divider, pending lubricating oil is all assigned to each swirler 3 of swirler 3 groups again, can ensure that swirler 3 intake pressure is steady, to reach best separating effect like this.Lubricating oil tangentially enters swirler 3, produce the strong rotational shear turbulent motion of strong Three-Dimensional Elliptic, owing to there is granularity difference (or density difference) between coarse particles (or heavy phase) with fine particle (or light phase), its centrifugal force be subject to, centripetal buoyancy, fluid drag etc. vary in size, by centrifugal settling effect, the component that mixture Midst density is large moves downward under the effect of eddy flow field simultaneously vertically, radially move, move downward along wall in arrival cone segments, and discharged by underflow opening, material is thus formed outer swirling flow field; The component that density is little is moved to central axial direction, and forms an inside vortex moved upward in axis centre, is then discharged by overflow port.Small portion coarse particles (or heavy phase) is discharged through swirler 3 underflow opening, and most of fine particle (or light phase) is discharged by upflow tube, thus reaches the object being separated classification.
In the eddy flow chamber of swirler 3, be provided with pulsed electrode, described pulsed electrode is connected with high-voltage pulse power source.Form pulsed electric field by pulsed electrode and high-voltage pulse power source, thus complete tensile deformation, the polarization polymerization of the little water droplet of milk sap at short notice, small droplets is agglomerated into large drop the most at last, installs copper electrode additional in swirler 3 entrance parallel-segment.During concrete enforcement, in swirler 3, required pulse voltage is about 5KV, and according to the pulsed voltage selected, design thickness of electrode is 2.5mm, selects the aluminium oxide copper of wear-resisting, corrosion-resistant, long service life as electrode, and in each swirler 3, electrode employing is connected in parallel.
Underflow opening bottom described swirler 3 is connected with underflow buffer container 4 by pipeline, and the overflow port on its top is connected with overflow buffer container 5 by pipeline.The outlet of described overflow buffer container 5 is connected with vacuum tank 9 with strainer 7, well heater 8 successively by pipeline after fuel charging valve 6, and the pipeline be connected with vacuum tank 9 stretches in vacuum tank 9, and the one end stretching into vacuum tank 9 at pipeline is provided with a spray thrower; In vacuum tank 9, be also provided with a mesh plate, thus in spray process, enable the water in the oil-water mixture of spray form water vapour better.In working process, lubricating oil enters strainer 7, filtering mechanical impurity, then enters vacuum tank 9 after being heated to 65 ~ 75 DEG C by well heater 8.During making, coarse filter filter core adopts magnetic filter, can meet the requirement of various operating mode filtering accuracy.
The top of described vacuum tank 9 is connected with a vacuum pump 10 by pipeline, thus form vacuum treatment field, under negative pressure of vacuum condition, a large amount of diameter can be formed bottom vacuum tank 9 generally at the bubble of about 1 ~ 5mm, move upward bottom vacuum tank 9, fluid is constantly seethed, bubble constantly breaks in the process arriving vacuum tank 9 top, add the contact area of fluid and air, and make moisture become water vapor, the gas that loss goes out liquid level is taken away by vacuum pump 10.Pipeline between vacuum pump 10 and vacuum tank 9 is provided with condenser 11, the outlet bottom described condenser 11 is connected with water discharge valve; Thus discharge forming water after water vapor condensation.And do not have the bubble of loss to be mixed in fluid to be again with oil return box by oil drain pump 12.Also comprise a nitrogen gas generator 15, described nitrogen gas generator 15 is connected with the bottom of vacuum tank 9 after nitrogen intake valve 16, under the effect that nitrogen is advertised, W/O steam is fully discharged, and simultaneously nitrogen protection fluid is not oxidized; Thus make degasifying effect better.
The bottom of described vacuum tank 9 is connected with oil drain pump 12 by pipeline, and described oil drain pump 12 is connected with a secondary filter 13 by pipeline, and the outlet of this secondary filter 13 is provided with draining valve 14; Fluid in vacuum tank 9, through dehydration, after degassed, be deposited in bottom, and by oil drain pump 12, fluid be sent to secondary filter 13, filter oil extraction, complete whole dewatered clean process by secondary filter 13.
During actual fabrication, also comprise a housing 17, can be controlled swirler 3, fuel charging valve 6, well heater 8, condenser 11, vacuum pump 10, draining valve 14, water discharge valve, nitrogen gas generator 15, nitrogen intake valve 16 and high-voltage pulse power source etc. by this housing 17, thus control the running of whole dewatering unit.
Finally it should be noted that, above embodiment is only in order to illustrate the technical solution of the utility model but not restriction technologies scheme, those of ordinary skill in the art is to be understood that, those are modified to the technical solution of the utility model or equivalent replacement, and do not depart from aim and the scope of the technical program, all should be encompassed in the middle of right of the present utility model.
Claims (4)
1. Mobile lubrication oil three combined dehydration devices, is characterized in that: comprise vehicle frame, vehicle frame is provided with and all presses feed divider and several swirler, and described swirler is connected with all pressing all extrusion mouth of feed divider simultaneously; In the eddy flow chamber of swirler, be provided with pulsed electrode, described pulsed electrode is connected with high-voltage pulse power source;
Underflow opening bottom described swirler is connected with underflow buffer container by pipeline, and the overflow port on its top is connected with overflow buffer container by pipeline; The outlet of described overflow buffer container is connected with vacuum tank with strainer, well heater successively by pipeline after fuel charging valve, and the pipeline be connected with vacuum tank stretches in vacuum tank, and the one end stretching into vacuum tank at pipeline is provided with a spray thrower; The top of described vacuum tank is connected with a vacuum pump by pipeline, and the pipeline between vacuum pump and vacuum tank is provided with condenser, and the outlet bottom described condenser is connected with water discharge valve;
The bottom of described vacuum tank is connected with oil drain pump by pipeline, and described oil drain pump is connected with a secondary filter by pipeline, and the outlet of this secondary filter is provided with draining valve;
Also comprise a nitrogen gas generator, described nitrogen gas generator is connected with the bottom of vacuum tank after nitrogen intake valve.
2. a kind of Mobile lubrication oil according to claim 1 three combined dehydration devices, it is characterized in that: also comprise a housing, can be controlled swirler, fuel charging valve, well heater, condenser, vacuum pump, draining valve, water discharge valve, nitrogen gas generator, nitrogen intake valve and high-voltage pulse power source by this housing.
3. a kind of Mobile lubrication oil according to claim 1 three combined dehydration devices, is characterized in that: be provided with tensimeter all pressing on feed divider.
4. a kind of Mobile lubrication oil according to claim 1 three combined dehydration devices, is characterized in that: described vehicle frame has four castors.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520360197.XU CN204661634U (en) | 2015-05-29 | 2015-05-29 | A kind of Mobile lubrication oil three combined dehydration devices |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520360197.XU CN204661634U (en) | 2015-05-29 | 2015-05-29 | A kind of Mobile lubrication oil three combined dehydration devices |
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| Publication Number | Publication Date |
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| CN204661634U true CN204661634U (en) | 2015-09-23 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520360197.XU Expired - Fee Related CN204661634U (en) | 2015-05-29 | 2015-05-29 | A kind of Mobile lubrication oil three combined dehydration devices |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109868157A (en) * | 2019-03-15 | 2019-06-11 | 重庆工商大学 | A kind of double-field coupled dehydration device and parameter optimization method |
| CN109913263A (en) * | 2019-04-03 | 2019-06-21 | 重庆工商大学 | Gu a kind of liquid-liquid-three-phase separating device of waste oil |
-
2015
- 2015-05-29 CN CN201520360197.XU patent/CN204661634U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109868157A (en) * | 2019-03-15 | 2019-06-11 | 重庆工商大学 | A kind of double-field coupled dehydration device and parameter optimization method |
| CN109868157B (en) * | 2019-03-15 | 2021-05-25 | 重庆工商大学 | Double-field coupling dehydration device and parameter optimization method |
| US11135529B1 (en) | 2019-03-15 | 2021-10-05 | Chongqing Technology And Business University | Parameter optimization method for double-field coupling dehydrator |
| CN109913263A (en) * | 2019-04-03 | 2019-06-21 | 重庆工商大学 | Gu a kind of liquid-liquid-three-phase separating device of waste oil |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150923 Termination date: 20180529 |
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| CF01 | Termination of patent right due to non-payment of annual fee |