CN202951285U - Coalescence vacuum-type oil purification device - Google Patents
Coalescence vacuum-type oil purification device Download PDFInfo
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- CN202951285U CN202951285U CN 201220681313 CN201220681313U CN202951285U CN 202951285 U CN202951285 U CN 202951285U CN 201220681313 CN201220681313 CN 201220681313 CN 201220681313 U CN201220681313 U CN 201220681313U CN 202951285 U CN202951285 U CN 202951285U
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- transfer valve
- oil
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- vacuum
- coalescence
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Abstract
The utility model discloses a coalescence vacuum-type oil purification device, comprising an oil inlet valve, a first switchover valve, a coalescence separator, a second switchover valve and an oil outlet valve which are serially connected in a main oil way in sequence, wherein a first non-return valve is arranged between the coalescence separator and the second switchover valve; the both ends of the second switchover valve are connected with a vacuum separator assembly in parallel; the oil inlet of the vacuum separator assembly is connected with a third switchover valve in series; and the oil outlet of the vacuum separator assembly is connected with a second non-return valve in series. The coalescence vacuum-type oil purification device disclosed by the utility model has the beneficial effects of being suitable for performing purification treatment on oil which is seriously doped with water or turbidly emulsified, and effectively removing impurities such as water and metal particles in the oil, and capable of realizing staged treatment on oil with various pollution degrees and independent heating for the oil.
Description
Technical field
This utility model relates to a kind of in-line purification that is widely used in the industrial steam turbine group turbine oils such as firepower, hydroelectric generation unit to be processed, particularly a kind of coalescent vacuum type reconditioner.
Background technology
The Main Function of fluid is to be lubricated and to cool off in that equipment is in service, and its quality good or not is directly connected to reliability and the economy of equipment.Equipment can be sneaked into along with the increase of running time various moisture content and impurity in running, can make metal surface generation corrosion in various degree with long-term the contact with metal parts of the oil of water, and generation corrosion thing, add the metal impurities that component abrasion produces in the running, oil lubrication and cooling effect are reduced, thereby can cause damage to the operation parts, even cause the generation of story, therefore need to filter and purify fluid.The filter plant that part band oil-water separating function is also arranged at present, but this kind equipment oil water separator when filtering also work simultaneously, but lower for the lube purification treatment effeciency of serious water inlet or turbid emulsification, and easy cause damage of equipment.
Summary of the invention
Goal of the invention: the purpose of this utility model provides the coalescent vacuum type reconditioner that the impurity such as the moisture content in the oil, sour matter, soap class, metallic particles were processed and can effectively be sloughed to a kind of lube purification that is applicable to serious water inlet or turbid emulsification.
Technical scheme: a kind of coalescent vacuum type reconditioner, comprise the inlet valve, the first transfer valve, coalescing separator, the second transfer valve and the delivery valve that are serially connected in successively in the working connection, be provided with the first check-valves between described coalescing separator and the second transfer valve, described the second transfer valve two ends are parallel with the vacuum separator assembly, described vacuum separator assembly oil-in is in series with the 3rd transfer valve, and described vacuum separator assembly oil-out is in series with the second check-valves.The few lower needs of situation of impurity such as the moisture content in fluid, sour matter, soap class, metallic particles are opened coalescing separator and are carried out isolation of purified, open the first transfer valve and the second transfer valve this moment, close the 3rd transfer valve, fluid flows out purifier through the first transfer valve, coalescing separator, the first check-valves, the second transfer valve and delivery valve successively from inlet valve; In the more situation of the impurity such as the moisture content in the fluid, sour matter, soap class, metallic particles, need to open simultaneously coalescing separator and the vacuum separator assembly carries out isolation of purified, open the first transfer valve and the 3rd transfer valve this moment, close the second transfer valve, fluid flows out purifier through the first transfer valve, coalescing separator, the first check-valves, the 3rd transfer valve, vacuum separator assembly, the second check-valves and delivery valve successively from inlet valve.
In order to improve clean-up effect, described the first transfer valve to the first check-valves two ends are parallel with heater, described heater oil-out is respectively equipped with the 4th transfer valve and the 5th transfer valve in parallel, the oil-out of described the 4th transfer valve is connected with coalescing separator, described the 5th transfer valve is connected to the pipeline between the first check-valves and the second transfer valve, and described heater is connected with the oil-in of the 3rd transfer valve.Need to heat fluid in order further to improve clean-up effect, close the first transfer valve and the 5th transfer valve, open the second transfer valve, the 3rd transfer valve and the 4th transfer valve, fluid enters vacuum separator assembly and coalescing separator by the 3rd transfer valve and the 4th transfer valve respectively through heater successively, flows out purifier from oil-out at last; In the time only need to carrying out isolation of purified by coalescing separator, close the first transfer valve, the 3rd transfer valve and the 5th transfer valve, open the second transfer valve and the 4th transfer valve, fluid enters coalescing separator through heater by the 4th transfer valve successively, flows out purifier from oil-out at last; In the time only need to carrying out isolation of purified by the vacuum separator assembly, close the first transfer valve, the second transfer valve, the 4th transfer valve and the 5th transfer valve, open the 3rd transfer valve, fluid enters the vacuum separator assembly through heater by the 3rd transfer valve successively, flows out purifier from oil-out at last; In the time only need to heating fluid, close the first transfer valve, the 3rd transfer valve and the 4th transfer valve, open the second transfer valve and the 5th transfer valve, fluid flows out purifier through heater, the 5th transfer valve and the second transfer valve from oil-out successively.
Beneficial effect: the utility model can not only be applicable to the lube purification of serious water inlet or turbid emulsification and process, effectively slough the impurity such as moisture content in the oil, metallic particles, can also realize the classification of the fluid of various pollution levels is processed and separately to the heating of fluid.
Description of drawings
Fig. 1 is the utility model control principle drawing
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
As shown in the figure, a kind of coalescent vacuum type reconditioner, comprise the inlet valve 1, the first transfer valve 2, coalescing separator 3, the second transfer valve 4 and the delivery valve 5 that are serially connected in successively in the working connection, be provided with the first check-valves 6 between described coalescing separator 3 and the second transfer valve 4, described the second transfer valve 4 two ends are parallel with vacuum separator assembly 7, described vacuum separator assembly 7 oil-ins are in series with the 3rd transfer valve 8, and described vacuum separator assembly 7 oil-outs are in series with the second check-valves 9.Described the first transfer valve 2 to first check-valves 6 two ends are parallel with heater 10, described heater 10 oil-outs are respectively equipped with the 4th transfer valve 11 and the 5th transfer valve 12 in parallel, the oil-out of described the 4th transfer valve 11 is connected with coalescing separator 3, described the 5th transfer valve 12 is connected to the pipeline between the first check-valves 6 and the second transfer valve 4, and described heater 10 is connected with the oil-in of the 3rd transfer valve 8.Need to heat fluid in order further to improve clean-up effect, close the first transfer valve 2 and the 5th transfer valve 12, open the second transfer valve 4, the 3rd transfer valve 8 and the 4th transfer valve 11, fluid enters vacuum separator assembly 7 and coalescing separator 3 by the 3rd transfer valve 8 and the 4th transfer valve 11 respectively through heater 10 successively, flows out purifier from oil-out 5 at last; In the time only need to carrying out isolation of purified by coalescing separator 3, close the first transfer valve 2, the 3rd transfer valve 8 and the 5th transfer valve 12, open the second transfer valve 4 and the 4th transfer valve 11, fluid enters coalescing separator 3 through heater 10 by the 4th transfer valve 11 successively, flows out purifier from oil-out 5 at last; In the time only need to carrying out isolation of purified by vacuum separator assembly 7, close the first transfer valve 2, the second transfer valve 4, the 4th transfer valve 11 and the 5th transfer valve 12, open the 3rd transfer valve 8, fluid enters vacuum separator assembly 7 through heater 3 by the 3rd transfer valve 8 successively, flows out purifier from oil-out 5 at last; In the time only need to heating fluid, close the first transfer valve 2, the 3rd transfer valve 8 and the 4th transfer valve 11, open the second transfer valve 4 and the 5th transfer valve 12, fluid flows out purifier through heater 10, the 5th transfer valve 12 and the second transfer valve 4 from oil-out 5 successively.
Claims (2)
1. coalescent vacuum type reconditioner, it is characterized in that: comprise the inlet valve (1) that is serially connected in successively in the working connection, the first transfer valve (2), coalescing separator (3), the second transfer valve (4) and delivery valve (5), be provided with the first check-valves (6) between described coalescing separator (3) and the second transfer valve (4), described the second transfer valve (4) two ends are parallel with vacuum separator assembly (7), described vacuum separator assembly (7) oil-in is in series with the 3rd transfer valve (8), and described vacuum separator assembly (7) oil-out is in series with the second check-valves (9).
2. coalescent vacuum type reconditioner according to claim 1, it is characterized in that: described the first transfer valve (2) to the first check-valves (6) two ends are parallel with heater (10), described heater (10) oil-out is respectively equipped with the 4th transfer valve (11) and the 5th transfer valve (12) in parallel, the oil-out of described the 4th transfer valve (11) is connected with coalescing separator (3), described the 5th transfer valve (12) is connected to the pipeline between the first check-valves (6) and the second transfer valve (4), and described heater (3) is connected with the oil-in of the 3rd transfer valve (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220681313 CN202951285U (en) | 2012-12-12 | 2012-12-12 | Coalescence vacuum-type oil purification device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220681313 CN202951285U (en) | 2012-12-12 | 2012-12-12 | Coalescence vacuum-type oil purification device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202951285U true CN202951285U (en) | 2013-05-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220681313 Expired - Fee Related CN202951285U (en) | 2012-12-12 | 2012-12-12 | Coalescence vacuum-type oil purification device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202951285U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055544A (en) * | 2012-12-12 | 2013-04-24 | 镇江市科能电力设备有限公司 | Coalescing vacuum type oil cleaning device |
| CN104801103A (en) * | 2015-05-13 | 2015-07-29 | 重庆万美机电有限公司 | Coalescence vacuum oil purifier |
-
2012
- 2012-12-12 CN CN 201220681313 patent/CN202951285U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103055544A (en) * | 2012-12-12 | 2013-04-24 | 镇江市科能电力设备有限公司 | Coalescing vacuum type oil cleaning device |
| CN104801103A (en) * | 2015-05-13 | 2015-07-29 | 重庆万美机电有限公司 | Coalescence vacuum oil purifier |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20130529 Termination date: 20141212 |
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| EXPY | Termination of patent right or utility model |