CN215234190U - Reactor for hydrofining of lubricating oil - Google Patents
Reactor for hydrofining of lubricating oil Download PDFInfo
- Publication number
- CN215234190U CN215234190U CN202121442520.XU CN202121442520U CN215234190U CN 215234190 U CN215234190 U CN 215234190U CN 202121442520 U CN202121442520 U CN 202121442520U CN 215234190 U CN215234190 U CN 215234190U
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- Prior art keywords
- device body
- pipe
- reactor
- heating
- lubricating oil
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- 239000010687 lubricating oil Substances 0.000 title claims abstract description 44
- 238000010438 heat treatment Methods 0.000 claims abstract description 38
- 239000003921 oil Substances 0.000 claims abstract description 22
- 238000003756 stirring Methods 0.000 claims abstract description 14
- 238000007599 discharging Methods 0.000 claims abstract description 10
- 229920002545 silicone oil Polymers 0.000 claims description 8
- 238000003466 welding Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 18
- 239000001257 hydrogen Substances 0.000 abstract description 11
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000007670 refining Methods 0.000 description 5
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 4
- 229910052710 silicon Inorganic materials 0.000 description 4
- 239000010703 silicon Substances 0.000 description 4
- 239000004927 clay Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a reactor for lubricating oil hydrofining, the device comprises a device body, the inside baffle that is provided with of device body, baffle one side is provided with the reaction tank, one side that the reaction tank was kept away from to the baffle is provided with the heating tank, the top of reaction tank is provided with the inlet pipe, the top of baffle is provided with the intake pipe, the top of heating tank is provided with into oil pipe, device body bottom central point puts and is provided with the motor, motor one end is provided with the pivot, the pivot both sides are provided with stirring vane, the inside gas tank that is provided with of baffle, one side that the baffle is close to the reaction tank is provided with the venthole, device body bottom is provided with the supporting legs, device body one side is provided with the discharging pipe, discharging pipe one side is provided with the row oil pipe, device body inner wall is provided with the heating pipe. This a reactor for lubricating oil hydrofining can react lubricating oil and the abundant mixing of hydrogen, can reach the even, the stable effect of control by temperature change of heating simultaneously, has guaranteed the output quality of lubricating oil.
Description
Technical Field
The utility model relates to a lubricating oil processingequipment technical field specifically is a reactor for lubricating oil hydrofining.
Background
The lubricating oil needs to be refined in the production process to improve the quality of the lubricating oil, the refining of the lubricating oil comprises clay refining and hydrorefining, the clay refining step is complicated and consumes a large amount of time, and the clay refining step is slowly abandoned by lubricating oil manufacturers, and the color, stability and smell of the hydrorefined oil are improved, and the sensitivity to an antioxidant is obviously improved.
The existing lubricating oil hydrorefining reactor can not well control the temperature in the lubricating oil processing process, has the conditions of uneven heating and sudden temperature rise and drop, can affect the quality of the lubricating oil, leads the lubricating oil to fail to reach the use standard, and affects the production efficiency, and the existing reactor does not have the capacity of fully mixing the lubricating oil with hydrogen, so that the lubricating oil does not react completely, and the quality of the lubricating oil can be affected.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a reactor for lubricating oil hydrofining aiming at the defects in the prior art so as to solve the problems in the prior art.
In order to achieve the above object, the utility model provides a following technical scheme: the utility model provides a reactor for lubricating oil hydrofining, includes the device body, the inside baffle that is provided with of device body, baffle one side is provided with the reaction tank, one side that the reaction tank was kept away from to the baffle is provided with the heating tank, the top of reaction tank is provided with the inlet pipe, the top of baffle is provided with the intake pipe, the top of heating tank is provided with the inlet pipe, device body bottom central point puts and is provided with the motor, motor one end is provided with the pivot, the pivot both sides are provided with stirring vane, the inside gas tank that is provided with of baffle, one side that the baffle is close to the reaction tank is provided with the venthole, device body bottom is provided with the supporting legs, device body one side is provided with the discharging pipe, discharging pipe one side is provided with the oil extraction pipe, device body inner wall is provided with the heating pipe.
As the utility model discloses an optimized technical scheme, inlet pipe, discharging pipe all are connected with the reaction tank, advance oil pipe, arrange oil pipe and all be connected with the heating bath.
As the utility model discloses a preferred technical scheme, device body bottom sets up the inclined plane into certain angle.
As the utility model discloses an optimal technical scheme, the motor is connected with the equal fixed connection of device body, pivot, stirring vane and pivot welding, stirring vane rotates through pivot and motor to be connected.
As the utility model discloses an optimized technical scheme, intake pipe, venthole all are connected with the gas tank, the quantity of venthole is a plurality of groups.
As the utility model discloses a preferred technical scheme, heating pipe and device body fixed connection, the quantity of heating pipe is a plurality of groups, pour into silicone oil in the heating tank.
As an optimal technical scheme of the utility model, the quantity of supporting legs is four groups, the supporting legs uses rectangular array to distribute in device body bottom.
Compared with the prior art, the utility model provides a reactor for lubricating oil hydrofining possesses following beneficial effect:
1. according to the reactor for hydrorefining of the lubricating oil, the gas tank is arranged to connect the gas inlet pipe and the gas outlet holes, hydrogen can be injected from the gas inlet pipe, the hydrogen enters the reaction tank from the plurality of groups of gas outlet holes through the gas tank, the lubricating oil and the hydrogen can be fully mixed, the rotation of the rotating shaft and the stirring blades is driven by the motor, the mixing degree of the lubricating oil and the hydrogen can be further improved, the lubricating oil can be fully reacted, the reaction efficiency can be effectively improved, and the production efficiency and the product quality of the lubricating oil are improved;
2. this a reactor for lubricating oil hydrofining, through setting up heating tank and heating pipe, inject silicon oil to the heating tank through advancing oil pipe, can regard silicon oil as the hot medium, silicon oil heats the inside lubricating oil of reaction tank in the cooperation of heating pipe, ensure that lubricating oil is in suitable temperature in processing, compare in using heater direct heating lubricating oil, use silicon oil as the hot medium, can reach even heating, the stable effect of control by temperature change, can prevent that the lubricating oil quality that the abrupt temperature rise drop leads to is not up to standard, the consumption of production resource has been reduced, and the production efficiency is improved.
Drawings
FIG. 1 is a schematic view of the overall structure of the present invention;
FIG. 2 is a top view of a portion of the structure of the present invention;
FIG. 3 is a schematic view of the connection structure of the air tank of the present invention;
fig. 4 is a schematic view of the connection structure of the heating pipe of the present invention.
In the figure: 1. a device body; 2. a partition plate; 3. a reaction tank; 4. a heating tank; 5. a feed pipe; 6. an air inlet pipe; 7. an oil inlet pipe; 8. a motor; 9. a rotating shaft; 10. a stirring blade; 11. an air tank; 12. an air outlet; 13. supporting legs; 14. a discharge pipe; 15. an oil discharge pipe; 16. heating the tube.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, in this embodiment: the utility model provides a reactor for lubricating oil hydrofining, including device body 1, device body 1 is inside to be provided with baffle 2, baffle 2 one side is provided with reaction tank 3, one side that reaction tank 3 was kept away from to baffle 2 is provided with heating bath 4, reaction tank 3's top is provided with inlet pipe 5, baffle 2's top is provided with intake pipe 6, heating bath 4's top is provided with into oil pipe 7, device body 1 bottom central point puts and is provided with motor 8, motor 8 one end is provided with pivot 9, pivot 9 both sides are provided with stirring vane 10, baffle 2 is inside to be provided with gas tank 11, one side that baffle 2 is close to reaction tank 3 is provided with venthole 12, device body 1 bottom is provided with supporting legs 13, device body 1 one side is provided with discharging pipe 14, discharging pipe 14 one side is provided with row oil pipe 15, device body 1 inner wall is provided with heating pipe 16.
In the embodiment, the feeding pipe 5 and the discharging pipe 14 are both connected with the reaction tank 3, and the oil inlet pipe 7 and the oil discharging pipe 15 are both connected with the heating tank 4, so that lubricating oil and heat medium silicone oil which need to be processed can be added and discharged conveniently; the bottom of the device body 1 is provided with an inclined plane with a certain angle, so that lubricating oil and a heat medium can flow out of the device conveniently; the motor 8 is fixedly connected with the device body 1 and the rotating shaft 9, the stirring blade 10 is welded with the rotating shaft 9, and the stirring blade 10 is rotatably connected with the motor 8 through the rotating shaft 9 to stir the lubricating oil so as to fully react; the gas inlet pipe 6 and the gas outlet holes 12 are connected with the gas tank 11, and the number of the gas outlet holes 12 is a plurality of groups, so that the contact area of hydrogen and lubricating oil is increased, and the reaction efficiency is improved; the heating pipes 16 are fixedly connected with the device body 1, the number of the heating pipes 16 is a plurality of groups, silicone oil is injected into the heating groove 4, and the silicone oil is used as a heat medium to facilitate the control of the temperature in the processing process; the number of the supporting legs 13 is four, and the supporting legs 13 are distributed at the bottom of the device body 1 in a rectangular array, so that the stability of the whole structure of the device is ensured.
The utility model discloses a theory of operation and use flow: a user checks that all parts have no problem before using the device, silicone oil is injected into the heating tank 4 through the oil inlet pipe 7, lubricating oil to be processed and refined is injected into the reaction tank 3 through the inlet pipe 5, after the injection is finished, the oil inlet pipe 7 and the inlet pipe 5 are sealed, the temperature of the heating pipe 16 is controlled to rise at the moment, the temperature in the reaction tank 3 is continuously raised while the temperature of the silicone oil is raised, when the temperature in the reaction tank 3 reaches a proper temperature, the heating pipe 16 is controlled not to rise any more, a heat preservation mode is changed, hydrogen is injected into the gas tank 11 through the gas inlet pipe 6 at the moment, the hydrogen enters the reaction tank 3 from the gas outlet holes 12 through the gas tank 11, the starting motor 8 drives the rotating shaft 9 and the stirring blades 10 to rotate, the hydrogen and the lubricating oil are fully mixed, a reaction is carried out at the proper temperature, the lubricating oil is uniformly heated and stably controlled by taking the silicone oil as a heat medium, and the hydrogen and the lubricating oil are fully mixed, the output quality of the lubricating oil is ensured, and a higher refining system of the lubricating oil is ensured.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (7)
1. A reactor for hydrofinishing lubricating oil, characterized by: comprises a device body (1), a baffle plate (2) is arranged in the device body (1), a reaction tank (3) is arranged on one side of the baffle plate (2), a heating tank (4) is arranged on one side of the baffle plate (2) far away from the reaction tank (3), an inlet pipe (5) is arranged above the reaction tank (3), an inlet pipe (6) is arranged above the baffle plate (2), an inlet pipe (7) is arranged above the heating tank (4), a motor (8) is arranged at the central position of the bottom of the device body (1), a rotating shaft (9) is arranged at one end of the motor (8), stirring blades (10) are arranged on two sides of the rotating shaft (9), an air tank (11) is arranged in the baffle plate (2), an air outlet hole (12) is arranged on one side of the baffle plate (2) close to the reaction tank (3), supporting legs (13) are arranged at the bottom of the device body (1), the device is characterized in that a discharge pipe (14) is arranged on one side of the device body (1), an oil discharge pipe (15) is arranged on one side of the discharge pipe (14), and a heating pipe (16) is arranged on the inner wall of the device body (1).
2. The reactor of claim 1, wherein: the feeding pipe (5) and the discharging pipe (14) are connected with the reaction tank (3), and the oil inlet pipe (7) and the oil discharge pipe (15) are connected with the heating tank (4).
3. The reactor of claim 1, wherein: the bottom of the device body (1) is provided with an inclined plane with a certain angle.
4. The reactor of claim 1, wherein: motor (8) and device body (1), the equal fixed connection of pivot (9), stirring vane (10) and pivot (9) welding, stirring vane (10) rotate with motor (8) through pivot (9) and are connected.
5. The reactor of claim 1, wherein: the air inlet pipe (6) and the air outlet holes (12) are connected with the air groove (11), and the number of the air outlet holes (12) is a plurality of groups.
6. The reactor of claim 1, wherein: the heating pipes (16) are fixedly connected with the device body (1), the number of the heating pipes (16) is a plurality of groups, and silicone oil is injected into the heating groove (4).
7. The reactor of claim 1, wherein: the number of the supporting feet (13) is four, and the supporting feet (13) are distributed at the bottom of the device body (1) in a rectangular array.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121442520.XU CN215234190U (en) | 2021-06-28 | 2021-06-28 | Reactor for hydrofining of lubricating oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121442520.XU CN215234190U (en) | 2021-06-28 | 2021-06-28 | Reactor for hydrofining of lubricating oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215234190U true CN215234190U (en) | 2021-12-21 |
Family
ID=79484345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121442520.XU Active CN215234190U (en) | 2021-06-28 | 2021-06-28 | Reactor for hydrofining of lubricating oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215234190U (en) |
-
2021
- 2021-06-28 CN CN202121442520.XU patent/CN215234190U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240401 Address after: Room 1201, 12th Floor, Building A2, Huizhi Science and Technology Park, Hengtai Road, Nanjing Economic and Technological Development Zone, Jiangsu Province, 210000 Patentee after: Jiangsu R&D Energy Conservation and Environmental Protection Technology Co.,Ltd. Country or region after: China Address before: 300203 No. 508, building 14, innovation and entrepreneurship Park, No. 4668, Xinbei Road, Tanggu marine science and Technology Park, Binhai New Area, Tianjin (settled in No. 73 of Tianjin legal and business secretary Co., Ltd.) Patentee before: Zhongyi Jingxing (Tianjin) Technology Co.,Ltd. Country or region before: China |
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| TR01 | Transfer of patent right |