CN202173840U - Negative-pressure penetration and static adsorption oil purifier - Google Patents
Negative-pressure penetration and static adsorption oil purifier Download PDFInfo
- Publication number
- CN202173840U CN202173840U CN2011202348660U CN201120234866U CN202173840U CN 202173840 U CN202173840 U CN 202173840U CN 2011202348660 U CN2011202348660 U CN 2011202348660U CN 201120234866 U CN201120234866 U CN 201120234866U CN 202173840 U CN202173840 U CN 202173840U
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- static adsorption
- oil purifier
- oil
- negative pressure
- purifier according
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Abstract
The utility model discloses a negative-pressure penetration and static adsorption oil purifier, which mainly comprises a streaming system, a negative-pressure static adsorption system, an atomizing vacuum flash vaporization system, an electrical control system and a filtering system. The streaming system, the negative-pressure static adsorption system, the atomizing vacuum flash vaporization system, the electrical control system and an automatic control element are mutually connected through valves and pipelines. The oil purifier overcomes the shortcoming that oil can only be purified by means of repeated filtration and frequent replacement of filtering elements in other traditional technology. Simultaneously, as the oil can be filtered and purified once and replacement of the filtering elements is decreased, the nominal oil purifying quantity of the oil purifier can be decreased greatly while the same quantity of oil is purified within unit time, and the manufacturing cost and the operating cost of the oil purifier are reduced greatly. The oil purifier is high in oil screening precision, and required purifying effect can be achieved after the oil passes through the oil purifier once.
Description
Technical field
The utility model relates to a kind of negative pressure infiltration Static Adsorption oil purifier that can realize liquid-solid separation.
Background technology
Negative pressure infiltration Static Adsorption is the successful appearance of absolute oil technology, and having at separation technology field has increased the newcomer, and traditional liquid-solid isolation technics is pressure filtration separation and the centrifugation through being power source with the oil transfer pump.
Pressure filtration separates the main pressure of oil transfer pump that relies on and leaves to realize fluid and solids through filter element; Reach the filtration, purification of fluid; Because the big or small uniformity (being precision) of filter element micropore is difficult to control during fabrication, during filtration, need improve filtering accuracy through circulating filtration on the one hand with the accumulation and the obstruction of dirt; But along with dirt adheres to gradually and stops up filter element; Filter pressure will increase, and the filter element micropore will raise and is out of shape along with pressure, make small dirt be prone to reduce its interception efficient through filter element.
The main centrifugal force of rotation at a high speed that leans on of centrifugation is realized liquid-solid separation; But it is just less or contain the small pollution fluid of a large amount of particle diameters and adopt centrifugation then not have effect in the unconspicuous fiber-like impurity of fluid difference in specific gravity for itself containing impurity particle; Particularly under " Water-In-Oil " or " oil-in-water " state, centrifugation can't separate removal with granulometric impurity in the fluid and the suspension in the fluid at all.
The utility model content
The purpose of the utility model just is to provide a kind of negative pressure infiltration Static Adsorption oil purifier, and it can be realized that fluid is disposable and passes through, and can reach needed clean-up effect.
To achieve these goals; The technical scheme that the utility model adopts is such: a kind of negative pressure infiltration Static Adsorption oil purifier; Mainly form, stream between system, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and the Automatic Control Component and interconnect through valve and pipeline by the system of streaming, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and filtration system.
As preferably, stream system, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and filtration system collection and be contained on the travelling car.
As preferably, the said system of streaming mainly is made up of heater, exhaust apparatus, by-pass means.
As preferably, heater is for streaming heating cabinet.
As preferably, the said heating cabinet that streams adopts the tube heater heating.
As preferably, said valve is mainly screw thread ball valve, fuel inlet ball check valve, electrical ball valve and magnetic valve.
As preferably, said negatively pressurized static adsorption system is mainly vacuum oil suction knockout drum.
As preferably, the atomizing vacuum flash system is mainly the twin-stage rotary-vane vaccum pump.
As preferably, said filtration system is mainly board-like no press filtering device.
As preferably, contain capillary in the said board-like no press filtering device.
Compared with prior art, the advantage of the utility model is:
1, the utility model has overcome other conventional arts and must could accomplish the lube purification process through multiple times of filtration and frequent change filter element; Simultaneously; Purify the replacing of fluid and minimizing and filter element owing to realized disposable filtering; Purify identical oil mass in unit interval the nominal net fuel of reconditioner can be reduced greatly, reduced device fabrication cost and operating cost greatly.
2, the utility model fluid screening precision is high, has realized that the fluid single pass just can reach needed clean-up effect.
Description of drawings
The utility model will explain through example and with reference to the mode of accompanying drawing, wherein:
Fig. 1 is the front view of the utility model;
Fig. 2 is the side view of the utility model;
Fig. 3 is the vertical view of the utility model.
The specific embodiment
To combine accompanying drawing and practical implementation that the utility model is described further below.
For the purpose, technical scheme and the advantage that make the utility model is clearer,, the utility model is further elaborated below in conjunction with accompanying drawing and embodiment.Should be appreciated that specific embodiment described herein only in order to explanation the utility model, and be not used in qualification the utility model.
Referring to Fig. 1 to Fig. 3; A kind of negative pressure infiltration Static Adsorption oil purifier; Mainly form by the system of streaming, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and filtration system, stream system, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system 1 and and filtration system between interconnect through valve and pipeline; Press Static Adsorption system, atomizing vacuum flash system, electric control system 1 and filtration system collection to be contained on the travelling car 8; The said system of streaming mainly is made up of heater, exhaust apparatus, by-pass means; Wherein, heater is for streaming heating cabinet 4, and this streams heating cabinet 4 and adopts tube heater 6 heating; The by-pass means that streams the plate composition is adopted in the inside of streaming heating cabinet 4; Stream heating cabinet 4 above be provided with four pipe tunnels arranged side by side; Four pipelines arranged side by side couple together through a horizontal pipeline; And be provided with screw thread ball valve 5 at the middle part of this horizontal pipeline, also be provided with fuel inlet ball check valve 7 on the end of horizontal pipeline.Stream between heating cabinet 4 and the vacuum oil suction knockout drum 2 and be provided with an electrical ball valve 3; The negatively pressurized static adsorption system is mainly vacuum oil suction knockout drum 2; The atomizing vacuum flash system is mainly twin-stage rotary-vane vaccum pump 11; Said filtration system is mainly board-like no press filtering device 12; Contain capillary in the said board-like no press filtering device 12.Below dolly, also be provided with a cyclic water tank 9, the water in the cyclic water tank 9 returns cyclic water tank 9 after through cooling water pump 10 cooling water being injected twin-stage rotary-vane vaccum pump 11; Twin-stage rotary-vane vaccum pump 11 can produce great amount of heat in running; This water tank 9 is provided with purpose and is through cooling water pump 10 chuck that cooling water passes through vavuum pump 11 to be injected twin-stage rotary-vane vaccum pump 11, and twin-stage rotary-vane vaccum pump 11 is played cooling purpose.
Fluid flows in the horizontal pipeline through oil-feed DN25, and the size through fuel inlet ball check valve 7 control oil inlet quantities, fluid and then enter into and stream heating cabinet 4; Stream deposition through heating; Produce " suction effect " through advection again, the larger particles contamination precipitation is fallen be able to further sink clearly, filter through board-like no press filtering device 12 then; Board-like no press filtering device 12 mainly utilizes negative pressure of vacuum to make the fluid filter element of slowly flowing through; When fluid passed through the filter element of micropore size inequality in the negative pressure infiltration, the dirt particulate impurity of greater particle size was tackled in the oil, and less granulometric impurity and suspension then are filtered the capillary absorption of element; Dirt impurity and filter element micropore by interception and absorption form more high-precision screening structure naturally, have realized that the fluid single pass just can reach needed clean-up effect.Deviate from W/O part and gas through the twin-stage rotary-vane vaccum pump at last.Filtration, purification fluid is stored in out in the oil tank 14, and circulates on oil tank 14 through magnetic valve 13 and magnetic valve 15 controlled filters purification fluid.Moisture content and gas overflow through the exhaust apparatus in the system of streaming.
The utility model has overcome other conventional arts must could accomplish the lube purification process through multiple times of filtration and frequent change filter element; Simultaneously; Purify the replacing of fluid and minimizing and filter element owing to realized disposable filtering; Purify identical oil mass in unit interval the nominal net fuel of reconditioner can be reduced greatly, reduced device fabrication cost and operating cost greatly.
The above is merely the preferred embodiment of the utility model; Not in order to restriction the utility model; Any modification of being done within all spirit and principles at the utility model, be equal to replacement and improvement etc., all should be included within the protection domain of the utility model.
Claims (10)
1. a negative pressure is permeated the Static Adsorption oil purifier; It is characterized in that: mainly form, stream between system, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and the Automatic Control Component and interconnect through valve and pipeline by the system of streaming, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and filtration system.
2. negative pressure infiltration Static Adsorption oil purifier according to claim 1 is characterized in that: stream system, negatively pressurized static adsorption system, atomizing vacuum flash system, electric control system and filtration system collection and be contained on the travelling car.
3. negative pressure infiltration Static Adsorption oil purifier according to claim 1, it is characterized in that: the said system of streaming mainly is made up of heater, exhaust apparatus, by-pass means.
4. negative pressure infiltration Static Adsorption oil purifier according to claim 3, it is characterized in that: heater is for streaming heating cabinet.
5. negative pressure infiltration Static Adsorption oil purifier according to claim 4 is characterized in that: the said heating cabinet that streams adopts the tube heater heating.
6. negative pressure infiltration Static Adsorption oil purifier according to claim 1, it is characterized in that: said valve is mainly screw thread ball valve, fuel inlet ball check valve, electrical ball valve and magnetic valve.
7. negative pressure infiltration Static Adsorption oil purifier according to claim 1, it is characterized in that: said negatively pressurized static adsorption system is mainly vacuum oil suction knockout drum.
8. negative pressure infiltration Static Adsorption oil purifier according to claim 1, it is characterized in that: the atomizing vacuum flash system is mainly the twin-stage rotary-vane vaccum pump.
9. negative pressure infiltration Static Adsorption oil purifier according to claim 1, it is characterized in that: said filtration system is mainly board-like no press filtering device.
10. negative pressure infiltration Static Adsorption oil purifier according to claim 9 is characterized in that: contain capillary in the said board-like no press filtering device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202348660U CN202173840U (en) | 2011-07-06 | 2011-07-06 | Negative-pressure penetration and static adsorption oil purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011202348660U CN202173840U (en) | 2011-07-06 | 2011-07-06 | Negative-pressure penetration and static adsorption oil purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202173840U true CN202173840U (en) | 2012-03-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011202348660U Expired - Lifetime CN202173840U (en) | 2011-07-06 | 2011-07-06 | Negative-pressure penetration and static adsorption oil purifier |
Country Status (1)
| Country | Link |
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| CN (1) | CN202173840U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103727004A (en) * | 2014-01-17 | 2014-04-16 | 吉首大学 | Automatic drying vacuum pump for lubricating oil |
-
2011
- 2011-07-06 CN CN2011202348660U patent/CN202173840U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103727004A (en) * | 2014-01-17 | 2014-04-16 | 吉首大学 | Automatic drying vacuum pump for lubricating oil |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120328 |
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| CX01 | Expiry of patent term |