CN205313491U - High -purity lubricating oil preparation system - Google Patents
High -purity lubricating oil preparation system Download PDFInfo
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- CN205313491U CN205313491U CN201620085706.7U CN201620085706U CN205313491U CN 205313491 U CN205313491 U CN 205313491U CN 201620085706 U CN201620085706 U CN 201620085706U CN 205313491 U CN205313491 U CN 205313491U
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- lubricating oil
- tank
- preparation system
- vacuum
- high purity
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Abstract
The utility model provides a high -purity lubricating oil preparation system, includes lubricating oil mediation subtotal storage part, and the preparation system still includes and stores the vacuum dehydration part that the part is connected, and the vacuum dehydration part includes real empty can, and very empty can connects the condensation branch road, and the condensation branch road includes the vacuum pump, the vacuum pump connection condenser, the collector is connected to the condenser, the vacuum dehydration part still includes the inert gas branch road, and the inert gas branch road includes the inert gas jar of being connected with real empty can. This system has of high quality, the low advantage of power consumption of lubricating oil of output.
Description
Technical field
The utility model relates to lubricating oil reconciliation techniques field, especially relates to a kind of high purity lubricating oil preparation system.
Background technology
Lubricating oil is used in all kinds of automobile, mechanical means to reduce friction, protection machinery and the liquid of workpiece or the lubricant of semisolid. The production stage of lubricating oil mainly comprise base oil and desired additives are added in proportion the lubricating oil carrying out being in harmonious proportion, be in harmonious proportion in Mixer pot enter to be filled in hold tank, moderate lubrication oil is filled in container, form lubricating oil finished product and enter the step of stockyard.
Finding in the use procedure of lubricating oil, adopt and there is following defect in the lubricating oil of above-mentioned explained hereafter: 1) moisture content is big, the emulsion of oil product is obvious, and oil product viscosity is poor, and then lubricant effect is deteriorated; 2) filling middle oil product and air contact, the oxygen in air accelerates oxidation of lubricating oil so that lubricating oil produces foam, can reduce the rigidity of system to be lubricated so that system response is slow.
Summary of the invention
The purpose of this utility model is to overcome in prior art the shortcoming existed, a kind of high purity lubricating oil preparation system is provided, this system one is the moisture having discharged in lubricating oil to greatest extent, two is can effectively prevent oxidation of lubricating oil, the technical scheme adopted is: a kind of high purity lubricating oil preparation system, comprise lubricating oil to be in harmonious proportion partly and storage part, it is characterized in that: described preparation system also comprises the vacuum hydro-extraction part being connected with described storage part, described vacuum dehydration part divides and comprises vacuum tank, described vacuum tank connects condensation branch road, described condensation branch road comprises vacuum pump, described vacuum pump connects condenser, described condenser connects collector, described vacuum hydro-extraction part also comprises rare gas element branch road, and described rare gas element branch road comprises the tank connected rare gas element tank with described vacuum.
Technology feature of the present utility model also has: described preparation system also comprises rapid heating pipeline, described rapid heating pipeline comprises and the warming pipeline that described storage part is connected, described warming pipeline is provided with hydro-pump and chamber of heating, described in heat chamber be provided with heating tube.
Technology feature of the present utility model also has: described heating tube is electric heating tube or steam heat exchanging tube.
Technology feature of the present utility model also has: described storage part is hold tank.
Technology feature of the present utility model also has: described hold tank comprises tank body, is provided with heating jacket described tank is external.
Technology feature of the present utility model also has: described lubricating oil mediation part comprises Mixer pot and the hay tank that pipeline connects, and described Mixer pot is placed on weighbridge, and described hay tank comprises the filtering net being positioned at tank body.
Technology feature of the present utility model also has: being provided with stir shaft in described Mixer pot, described stir shaft is equipped with three to above paddle.
Technology feature of the present utility model also has: described paddle is four right, wherein first to and the 2nd between spacing minimum, the 3rd to and the 4th between spacing maximum.
The beneficial effects of the utility model are: 1) native system reduces water ratio of lubricating oil by vacuum hydro-extraction part, and protect oil product to greatest extent, make it to avoid in filling oxidized; 2) two connection branch roads are provided between hold tank and vacuum tank, can select according to outside temperature during use, once occur that outside temperature is low, the situation of oil product mobility difference, now starting rapid heating pipeline can consume energy under minimum prerequisite, it is provided that oil product proper flow is temperature required; 3) setting of paddle that in Mixer pot, multiple spacing does not wait, ensure that the homogeneity being uniformly mixed; 4) native system has that the quality of lubrication oil of output is good, consume energy low advantage.
Accompanying drawing explanation
Accompanying drawing 1 is the utility model front view, 1 is Mixer pot, 11 is charging opening, 12 is opening for feed, 13 is stir shaft, 14 is paddle, 15 is cooling jacket, 16 is water-in, 17 is water outlet, 18 is porthole, 19 is tank mouth, 110 is control valve, 111 is discharge port, 2 is weighbridge, 3 is hay tank, 31 is filter tank, 32 is filtering net, 33 is hay tank entrance, 34 is hay tank outlet, 4 is hold tank, 41 is storage tank, 42 is heating jacket, 5 is pipeline of heating fast, 51 is warming pipeline, 52 is hydro-pump, 53 is chamber of heating, 6 is vacuum tank, 7 is vacuum pump, 8 is condenser, 9 is collector, 10 is rare gas element tank.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described. The utility model provides a kind of high purity lubricating oil preparation system, this preparation system comprises lubricating oil and is in harmonious proportion partly and storage part, also comprise the vacuum hydro-extraction part being connected with storage part, mediation part completes the mediation of lubricating oil, lubricating oil after mediation enters storage part and keeps in, it is necessary to time filling, lubricating oil is filling after vacuum dehydration part divisional processing, thus reduce the moisture in lubricating oil to greatest extent, and effectively prevent the generation of lubricating oil oxidative phenomena.
This Mixer pot 1 have employed the mode of weight proportion when adding raw material, and weigh be the actual raw material weight joined in Mixer pot 1 tank body, thus improve the accuracy of proportioning, specifically Mixer pot 1 is placed on weighbridge 2, Mixer pot 1 tank body is also provided with water-in 16, the water outlet 17 of cooling jacket 15 and correspondence thereof, opening for feed 12 is positioned at Mixer pot 1 tank body top, opening for feed 12 connects feed-pipe, is provided with control valve 110 on feed-pipe. The top of Mixer pot 1 tank body is also provided with charging opening 11 and porthole 18. The bottom of Mixer pot 1 tank body is provided with discharge port 111. In order to the object mixed, the stir shaft 13 being provided with under driven by motor in Mixer pot 1 tank body to rotate, stir shaft 13 is equipped with three to above paddle 14, and the spacing between often pair of paddle 14 is not etc.
In the present embodiment, it is right that paddle 14 amounts to four, wherein first to and the 2nd spacing between paddle is minimum, 3rd to and the 4th spacing between paddle is maximum, the 2nd to and the 3rd the spacing between paddle is greater than first to and the 2nd to spacing between paddle, be less than the 3rd to and the 4th to spacing between paddle. The reason so arranged is that raw material is upper throwing material, and along with stirring carries out, the closer to discharge port 111, it is more even that raw material is mixed.
Hay tank 3 is equipped with filtering net 32, through filtering net 32 filter after lubricating oil through Cemented filling in hold tank 4.
Hold tank 4 comprises storage tank 41, is provided with heating jacket 42 outside storage tank 41. Hold tank 4 is connected with pipeline 5 of heating fast, pipeline 5 of heating fast is connected on hold tank 4, pipeline 5 of heating fast comprises warming pipeline 51, warming pipeline 51 is provided with hydro-pump 52, also being provided with chamber 53 of heating on warming pipeline 51, chamber 53 of heating is built with heating tube (not shown), and heating tube can be electric heating tube or steam heat exchanging tube, can certainly be the heating tube of other types, as long as the requirement of lubricating oil of heating fast can be met. Like this, when in external environment temperature become low, lubricating oil mobility is poor, filling needs can not be met time, while heating jacket 42 heats, start pipeline 5 of heating fast and extract lubricating oil, under the prerequisite that so can not reach specified temperature at whole tank lubricating oil, realize the filling object of lubricating oil, and saving heat energy. Certainly also can only start heating jacket heating or only start pipeline of heating fast, select according to actual needs.
Vacuum dehydration part divides and comprises vacuum tank 6, and vacuum tank 6 connects condensation branch road, and condensation branch road comprises vacuum pump 7, and vacuum pump 7 connects condenser 8, and condenser 8 connects collector 9; Vacuum hydro-extraction part also comprises rare gas element branch road, and rare gas element branch road comprises the rare gas element tank 10 being connected with vacuum tank 6.
During use, start vacuum pump 7, under the effect of vacuum pump 7, vacuum tank 6 produces negative pressure, and then lubricating oil is sucked, enters in vacuum tank 6; In vacuum tank 6, lubricating oil is separated with the moisture content contained by it, and moisture content becomes gaseous state to enter in condenser 8, and post liquefaction enters collector 9 in condenser 8, and the lubricating oil after dewatered clean outwards exports from the oil outlet of vacuum tank 6 under protection of inert gas.
Certainly; above-mentioned explanation is not limitation of the utility model; the utility model is also not limited only to above-mentioned citing, and change, remodeling, interpolation or the replacement that those skilled in the art make in essential scope of the present utility model, also belongs to protection domain of the present utility model.
Claims (8)
1. a high purity lubricating oil preparation system, comprise lubricating oil to be in harmonious proportion partly and storage part, it is characterized in that: described preparation system also comprises the vacuum hydro-extraction part being connected with described storage part, described vacuum dehydration part divides and comprises vacuum tank, described vacuum tank connects condensation branch road, described condensation branch road comprises vacuum pump, and described vacuum pump connects condenser, and described condenser connects collector; Described vacuum hydro-extraction part also comprises rare gas element branch road, and described rare gas element branch road comprises the tank connected rare gas element tank with described vacuum.
2. according to high purity lubricating oil preparation system according to claim 1, it is characterized in that: described preparation system also comprises rapid heating pipeline, described rapid heating pipeline comprises and the warming pipeline that described storage part is connected, described warming pipeline is provided with hydro-pump and chamber of heating, described in heat chamber be provided with heating tube.
3. according to high purity lubricating oil preparation system according to claim 2, it is characterised in that: described heating tube is electric heating tube or steam heat exchanging tube.
4. according to high purity lubricating oil preparation system according to claim 2, it is characterised in that: described storage part is hold tank.
5. according to high purity lubricating oil preparation system according to claim 4, it is characterised in that: described hold tank comprises tank body, is provided with heating jacket described tank is external.
6. according to high purity lubricating oil preparation system according to claim 1, it is characterised in that: described lubricating oil mediation part comprises Mixer pot and the hay tank that pipeline connects, and described Mixer pot is placed on weighbridge, and described hay tank comprises the filtering net being positioned at tank body.
7. according to high purity lubricating oil preparation system according to claim 6, it is characterised in that: being provided with stir shaft in described Mixer pot, described stir shaft is equipped with three to above paddle.
8. according to high purity lubricating oil preparation system according to claim 7, it is characterised in that: described paddle is four right, wherein first to and the 2nd between spacing minimum, the 3rd to and the 4th between spacing maximum.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620085706.7U CN205313491U (en) | 2016-01-28 | 2016-01-28 | High -purity lubricating oil preparation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620085706.7U CN205313491U (en) | 2016-01-28 | 2016-01-28 | High -purity lubricating oil preparation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205313491U true CN205313491U (en) | 2016-06-15 |
Family
ID=56187395
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620085706.7U Expired - Fee Related CN205313491U (en) | 2016-01-28 | 2016-01-28 | High -purity lubricating oil preparation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205313491U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287183A (en) * | 2016-08-23 | 2017-01-04 | 中国科学院理化技术研究所 | Filling storage device |
| CN106350187A (en) * | 2016-08-29 | 2017-01-25 | 江苏博格东进管道设备有限公司 | Preparation method of liquid composition for processing lubrication of pipelines |
| CN107413270A (en) * | 2017-08-14 | 2017-12-01 | 周晓红 | A kind of efficient OIL IN LUBRICATING OIL PRODUCTION mediation equipment |
| CN111196941A (en) * | 2020-01-16 | 2020-05-26 | 嘉兴瑞勒新材料科技有限公司 | Production method of olefin chain extension acid lubricant |
-
2016
- 2016-01-28 CN CN201620085706.7U patent/CN205313491U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106287183A (en) * | 2016-08-23 | 2017-01-04 | 中国科学院理化技术研究所 | Filling storage device |
| CN106350187A (en) * | 2016-08-29 | 2017-01-25 | 江苏博格东进管道设备有限公司 | Preparation method of liquid composition for processing lubrication of pipelines |
| CN107413270A (en) * | 2017-08-14 | 2017-12-01 | 周晓红 | A kind of efficient OIL IN LUBRICATING OIL PRODUCTION mediation equipment |
| CN107413270B (en) * | 2017-08-14 | 2020-08-04 | 温州海蓝工业设计有限公司 | Efficient lubricating oil production mediation equipment |
| CN111196941A (en) * | 2020-01-16 | 2020-05-26 | 嘉兴瑞勒新材料科技有限公司 | Production method of olefin chain extension acid lubricant |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160615 Termination date: 20200128 |