CN116590074B - Anti-micro pitting wind driven generator gear oil and preparation method thereof - Google Patents
Anti-micro pitting wind driven generator gear oil and preparation method thereof Download PDFInfo
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- CN116590074B CN116590074B CN202310353685.7A CN202310353685A CN116590074B CN 116590074 B CN116590074 B CN 116590074B CN 202310353685 A CN202310353685 A CN 202310353685A CN 116590074 B CN116590074 B CN 116590074B
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- 239000012208 gear oil Substances 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 9
- 230000007797 corrosion Effects 0.000 claims abstract description 13
- 238000005260 corrosion Methods 0.000 claims abstract description 13
- 229920013639 polyalphaolefin Polymers 0.000 claims description 34
- 239000002199 base oil Substances 0.000 claims description 32
- 150000001336 alkenes Chemical class 0.000 claims description 16
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 16
- -1 vulcanized lard Substances 0.000 claims description 11
- 239000004711 α-olefin Substances 0.000 claims description 10
- 239000003963 antioxidant agent Substances 0.000 claims description 9
- 238000005984 hydrogenation reaction Methods 0.000 claims description 9
- 230000003078 antioxidant effect Effects 0.000 claims description 8
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 claims description 8
- 238000006384 oligomerization reaction Methods 0.000 claims description 8
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 229920001296 polysiloxane Polymers 0.000 claims description 7
- 239000012188 paraffin wax Substances 0.000 claims description 6
- 239000013556 antirust agent Substances 0.000 claims description 5
- 239000003208 petroleum Substances 0.000 claims description 5
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 5
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 5
- 239000002518 antifoaming agent Substances 0.000 claims description 4
- 239000013530 defoamer Substances 0.000 claims description 3
- 230000000994 depressogenic effect Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 claims description 2
- 229910019142 PO4 Inorganic materials 0.000 claims description 2
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 2
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims description 2
- 150000001412 amines Chemical class 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 239000002530 phenolic antioxidant Substances 0.000 claims description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 2
- 239000010452 phosphate Substances 0.000 claims description 2
- 229920000058 polyacrylate Polymers 0.000 claims description 2
- 229920000570 polyether Polymers 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000001384 succinic acid Substances 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 description 15
- 238000006243 chemical reaction Methods 0.000 description 12
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 12
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 8
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- 239000010935 stainless steel Substances 0.000 description 8
- QVXGKJYMVLJYCL-UHFFFAOYSA-N 2,3-di(nonyl)-N-phenylaniline Chemical compound C(CCCCCCCC)C=1C(=C(C=CC1)NC1=CC=CC=C1)CCCCCCCCC QVXGKJYMVLJYCL-UHFFFAOYSA-N 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- QDCPNGVVOWVKJG-VAWYXSNFSA-N 2-[(e)-dodec-1-enyl]butanedioic acid Chemical compound CCCCCCCCCC\C=C\C(C(O)=O)CC(O)=O QDCPNGVVOWVKJG-VAWYXSNFSA-N 0.000 description 5
- 229910017318 Mo—Ni Inorganic materials 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 239000000539 dimer Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 229910052788 barium Inorganic materials 0.000 description 3
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 3
- 239000010687 lubricating oil Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- WJUMWVJBOZKPPU-UHFFFAOYSA-N 2,3-bis(6-methylheptyl)-N-phenylaniline Chemical compound C(CCCCC(C)C)C=1C(=C(C=CC1)NC1=CC=CC=C1)CCCCCC(C)C WJUMWVJBOZKPPU-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- JVUYWILPYBCNNG-UHFFFAOYSA-N potassium;oxido(oxo)borane Chemical compound [K+].[O-]B=O JVUYWILPYBCNNG-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000010722 industrial gear oil Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 125000004469 siloxy group Chemical group [SiH3]O* 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Abstract
The invention discloses a micro-pitting corrosion resistant gear oil for a wind driven generator and a preparation method thereof, and relates to the technical field of gear oil.
Description
Technical field:
The invention relates to the technical field of gear oil, in particular to anti-micro pitting wind driven generator gear oil and a preparation method thereof.
The background technology is as follows:
with the continuous development and maturity of technology, wind power generation has become a hotspot in the world new energy industry. In the working process of the fan, the bearing is often influenced by various running conditions such as high rotation speed, low rotation speed, high load and low load interconversion and the like, and the contact pressure and friction force of the gear and the bearing can be changed. With the increase of the output power of the unit, the contact pressure of the gear and the bearing is increased when the running condition is changed, the friction is increased, and the running temperature is increased. At the same time, harsh environmental conditions can also create a challenging lubrication environment.
The gear oil of the wind driven generator is generally composed of poly alpha-olefin base oil and high-performance composite additives, can be used under extreme environment temperature and severe working conditions, can effectively prevent micro pitting corrosion of gears in operation, has extreme pressure resistance and heavy load industrial gear oil resistance, forms an extremely strong oil film on tooth surfaces, and prolongs the service life of the gears.
The phenomenon of micro pitting exists in the gear of the wind driven generator generally, so that the tooth surface generates micro cracks and pits, noise and vibration are caused, the meshing precision of the gear is influenced, and even tooth breakage is caused, thereby influencing the service life of the gear of the wind driven generator. Therefore, the improvement of the micro pitting corrosion resistance of the gear oil is of great importance.
The invention comprises the following steps:
The technical problem to be solved by the invention is to provide the gear oil for the wind driven generator and the preparation method thereof, wherein the gear oil can form a dense lubricating oil film with a certain thickness on the surface of the gear, reduce contact between metals and between air and metals, effectively inhibit formation of micro pitting corrosion, and simultaneously has excellent service performances such as temperature sticking, wear resistance, bubbling resistance, low-temperature fluidity, thermal oxidation stability and the like, and prolongs the service life of the gear of the wind driven generator.
The technical problems to be solved by the invention are realized by adopting the following technical scheme:
The invention aims to provide micro-pitting corrosion resistant gear oil for a wind driven generator, which comprises the following raw materials in parts by weight:
The poly-a olefin is a common synthetic base oil, which is prepared by firstly preparing alpha olefin from olefin through polymerization reaction, and then further preparing the alpha olefin through polymerization and hydrogenation reaction. The poly alpha olefin synthetic oil (PAO for short) has good viscosity-temperature performance and low-temperature fluidity, and is ideal base oil for preparing high-grade special lubricating oil.
The preparation method of the high-viscosity poly-alpha-olefin base oil comprises the following steps: the C8-C10 alpha-olefin and vinyl triethoxysilane are subjected to oligomerization reaction to obtain an olefin oligomer, and then the olefin oligomer is subjected to hydrogenation reaction to obtain the high-viscosity poly alpha-olefin base oil. While linear alpha-olefins are commonly used in the art as feedstock to prepare polyalphaolefin base oils, the present invention is directed to the preparation of polyalphaolefin base oils using linear alpha-olefins and branched alpha-olefins containing siloxy groups as feedstock.
Preferably, the mass ratio of the C8-C10 alpha-olefin to the vinyltriethoxysilane is (90-95): 5-10. According to the invention, a small amount of vinyl triethoxysilane is added into C8-C10 alpha-olefin, and the poly alpha-olefin with a novel structure is prepared through oligomerization and hydrogenation, so that the poly alpha-olefin is used as base oil to effectively improve the application performance of gear oil.
The high-viscosity poly alpha-olefin base oil has a kinematic viscosity of 42.8-50.4 mm 2/s at 100 ℃, a viscosity index of 152-168 and a pour point of-42-36 ℃. The high-viscosity poly-alpha-olefin base oil prepared by the invention can keep good viscosity index in a wide temperature range, so that the wind power generator can be started safely in cold weather.
Preferably, the extreme pressure antiwear agent is at least one of chlorinated paraffin, vulcanized lard, phosphate, borate and vulcanized olefin. The extreme pressure antiwear agent has the functions of improving the load resistance of gear oil and preventing the gear surface from being worn under high load conditions.
Preferably, the antioxidant is at least one of a phenolic antioxidant and an amine antioxidant. The antioxidant has the function of preventing the gear oil from oxidative deterioration, and especially improving the high-temperature oxidation resistance of the gear oil.
Preferably, the defoamer is at least one of polysiloxane, methyl silicone oil, polyacrylate and polyether. The defoaming agent has the functions of reducing the foaming amount of the gear oil, reducing the contact between air in bubbles and the surface of the gear, and improving the micro pitting corrosion resistance of the gear.
Preferably, the rust inhibitor is at least one of alkenyl succinic acid and petroleum sulfonate. The polar groups in the rust inhibitor molecules have strong adsorption force on the metal surface, and a tight single-molecule or multi-molecule protective layer is formed on the metal surface to prevent the corrosive medium from contacting with the metal, thereby playing a role in rust prevention.
The second purpose of the invention is to provide a preparation method of the anti-micro pitting wind driven generator gear oil, which is characterized in that the high-viscosity poly alpha-olefin base oil, the extreme pressure antiwear agent, the antioxidant, the pour point depressant, the antirust agent and the defoaming agent are uniformly stirred and mixed according to the proportion, so that the anti-micro pitting wind driven generator gear oil is obtained. The stirring and mixing can be carried out at room temperature or under heating condition, and the heating temperature is not more than 55 ℃.
The beneficial effects of the invention are as follows: the invention prepares the high-viscosity poly-alpha-olefin base oil, and mixes the high-viscosity poly-alpha-olefin base oil with the extreme pressure antiwear agent, the antioxidant, the pour point depressant, the antirust agent and the defoamer to prepare the gear oil of the wind driven generator, and the gear oil can form a dense lubricating oil film with a certain thickness on the surface of the gear, so that the formation of micro pitting corrosion can be effectively inhibited, and meanwhile, the gear oil has excellent viscosity-temperature property, wear resistance, foam resistance, low-temperature fluidity, thermal oxidation stability and the like, thereby ensuring the normal operation of the gear of the wind driven generator and prolonging the service life of the gear of the wind driven generator.
The specific embodiment is as follows:
The invention is further described in connection with the following embodiments in order to make the technical means, the creation features, the achievement of the purpose and the effect of the invention easy to understand.
The invention tests the kinematic viscosity at 100 ℃ according to the standard GB/T265-1988; GB/T2541-1981 test viscosity index, GB/T3535-2006 test pour point, GB/T5096-2017 test copper corrosion, GB/T11143-2008 test liquid phase corrosion.
The following method of example 1 in patent CN 111019734a was used to prepare supported catalysts for oligomerization when preparing high viscosity poly-alpha-olefin base oils, using commercially available Mo-Ni/gamma-Al 2O3 catalysts (bar, 3mm diameter, 5-8 mm length, specific surface area 150-200 m 2/g, total pore volume greater than or equal to 0.65cm 3/g) as hydrogenation catalysts.
500ML of n-hexane, 95g of 1-decene, 5g of vinyl triethoxysilane and 20g of supported catalyst are added into a reaction kettle, and oligomerization reaction is carried out for 3 hours at the temperature of 50 ℃ and the pressure of 1 MPa; stopping the reaction, filtering to remove the catalyst, distilling at normal pressure to remove normal hexane, and distilling at reduced pressure to remove unreacted monomers and dimers to obtain the olefin oligomer. 50g of olefin oligomer and 5g of Mo-Ni/gamma-Al 2O3 catalyst are added into another reaction kettle, and hydrogenation reaction is carried out for 2 hours at the temperature of 210 ℃, the pressure of 3MPa and the space velocity of 0.5h -1 and the hydrogen-oil ratio of 550:1, so that the high-viscosity poly alpha-olefin base oil V-1 is obtained. The kinematic viscosity at 100 ℃ is 42.8mm 2/s, the viscosity index is 159, and the pour point is-36 ℃.
500ML of n-hexane, 90g of 1-decene, 10g of vinyl triethoxysilane and 20g of supported catalyst are added into a reaction kettle, and oligomerization reaction is carried out for 3 hours at the temperature of 60 ℃ and the pressure of 0.8 MPa; stopping the reaction, filtering to remove the catalyst, distilling at normal pressure to remove normal hexane, and distilling at reduced pressure to remove unreacted monomers and dimers to obtain the olefin oligomer. 50g of olefin oligomer and 5g of Mo-Ni/gamma-Al 2O3 catalyst are added into another reaction kettle, and hydrogenation reaction is carried out for 3 hours at the temperature of 220 ℃, the pressure of 2.5MPa, the space velocity of 1h -1 and the hydrogen-oil ratio of 500:1, so as to obtain the high-viscosity poly alpha-olefin base oil V-2. Kinematic viscosity at 100℃of 46.5mm 2/s, viscosity index of 168, pour point of-42 ℃.
500ML of n-hexane, 95g of 1-decene, 5g of vinyl triethoxysilane and 15g of supported catalyst are added into a reaction kettle, and oligomerization reaction is carried out for 3 hours at the temperature of 80 ℃ and the pressure of 0.6 MPa; stopping the reaction, filtering to remove the catalyst, distilling at normal pressure to remove normal hexane, and distilling at reduced pressure to remove unreacted monomers and dimers to obtain the olefin oligomer. 50g of olefin oligomer and 5g of Mo-Ni/gamma-Al 2O3 catalyst are added into another reaction kettle, and hydrogenation reaction is carried out for 2 hours at the temperature of 230 ℃, the pressure of 2MPa and the space velocity of 0.5h -1 and the hydrogen-oil ratio of 600:1, so that the high-viscosity poly alpha-olefin base oil V-3 is obtained. The kinematic viscosity at 100 ℃ is 50.4mm 2/s, the viscosity index is 152, and the pour point is-40 ℃.
500ML of n-hexane, 100g of 1-decene and 20g of supported catalyst are added into a reaction kettle, and oligomerization reaction is carried out for 3 hours at the temperature of 50 ℃ and the pressure of 1 MPa; stopping the reaction, filtering to remove the catalyst, distilling at normal pressure to remove normal hexane, and distilling at reduced pressure to remove unreacted monomers and dimers to obtain the olefin oligomer. 50g of olefin oligomer and 5g of Mo-Ni/gamma-Al 2O3 catalyst are added into another reaction kettle, and hydrogenation reaction is carried out for 2 hours at the temperature of 210 ℃, the pressure of 3MPa and the space velocity of 0.5h -1 and the hydrogen-oil ratio of 550:1, so that the high-viscosity poly alpha-olefin base oil V-0 is obtained. Kinematic viscosity at 100℃of 33.2mm 2/s, viscosity index 155, pour point of-32 ℃.
Example 1
100 Parts of high-viscosity poly alpha-olefin base oil V-1, 5 parts of chlorinated paraffin, 2 parts of dinonyl diphenylamine, 1 part of dodecenyl succinic acid and 0.5 part of polysiloxane are stirred and mixed uniformly to obtain gear oil.
Example 2
100 Parts of high-viscosity poly alpha-olefin base oil V-1, 4 parts of vulcanized lard, 2 parts of dinonyl diphenylamine, 1 part of dodecenyl succinic acid and 0.5 part of methyl silicone oil are uniformly stirred and mixed to obtain gear oil.
Example 3
100 Parts of high-viscosity poly alpha-olefin base oil V-2, 3 parts of potassium metaborate, 1 part of diisooctyl diphenylamine, 0.5 part of barium petroleum sulfonate and 0.5 part of polysiloxane are uniformly stirred and mixed to obtain gear oil.
Example 4
100 Parts of high-viscosity poly alpha-olefin base oil V-2, 5 parts of chlorinated paraffin, 1 part of diisooctyl diphenylamine, 0.5 part of barium petroleum sulfonate and 0.4 part of polysiloxane are stirred and mixed uniformly to obtain gear oil.
Example 5
100 Parts of high-viscosity poly alpha-olefin base oil V-3, 4 parts of vulcanized lard, 2 parts of dinonyl diphenylamine, 0.5 part of dodecenyl succinic acid and 0.4 part of methyl silicone oil are uniformly stirred and mixed to obtain gear oil.
Example 6
100 Parts of high-viscosity poly alpha-olefin base oil V-3, 3 parts of potassium metaborate, 2 parts of dinonyl diphenylamine, 1 part of barium petroleum sulfonate and 0.5 part of methyl silicone oil are uniformly stirred and mixed to obtain gear oil.
Comparative example 1
100 Parts of high-viscosity poly alpha-olefin base oil V-0, 5 parts of chlorinated paraffin, 2 parts of dinonyl diphenylamine, 1 part of dodecenyl succinic acid and 0.5 part of polysiloxane are stirred and mixed uniformly to obtain gear oil.
Comparative example 2
100 Parts of high-viscosity poly-alpha-olefin base oil (Inlet poly-alpha-olefin 174I), 5 parts of chlorinated paraffin, 2 parts of dinonyl diphenylamine, 1 part of dodecenyl succinic acid and 0.5 part of polysiloxane are stirred and mixed uniformly to obtain gear oil.
The gear oils prepared in the above examples and comparative examples were subjected to the micro pitting corrosion resistance test, and the results are shown in table 1.
TABLE 1
| Copper sheet corrosion (100 ℃,3 h) | Liquid phase rust (artificial sea water) | |
| Example 1 | 1a | Stainless steel |
| Example 2 | 1a | Stainless steel |
| Example 3 | 1a | Stainless steel |
| Example 4 | 1a | Stainless steel |
| Example 5 | 1a | Stainless steel |
| Example 6 | 1a | Stainless steel |
| Comparative example 1 | 1b | Stainless steel |
| Comparative example 2 | 1b | Stainless steel |
As can be seen from Table 1, the high viscosity polyalphaolefin base oils prepared according to the present invention provide gear oils with excellent micropitting properties.
The foregoing has shown and described the basic principles and main features of the present invention and the advantages of the present invention. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present invention, and various changes and modifications may be made without departing from the spirit and scope of the invention, which is defined in the appended claims. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (7)
1. The anti-micro pitting wind driven generator gear oil is characterized by comprising the following raw materials in parts by weight:
100 parts of high viscosity poly alpha-olefin base oil
Extreme pressure antiwear agent 1-5 parts
0.5-3 Parts of antioxidant
0.1-2 Parts of antirust agent
0.05-1 Part of defoaming agent;
The preparation method of the high-viscosity poly-alpha-olefin base oil comprises the following steps: oligomerization of C8-C10 alpha-olefin and vinyl triethoxysilane to obtain olefin oligomer, and hydrogenation of the olefin oligomer to obtain high viscosity poly alpha-olefin base oil;
The mass ratio of the C8-C10 alpha-olefin to the vinyl triethoxysilane is (90-95) to (5-10).
2. The anti-micro pitting wind turbine gear oil of claim 1, wherein: the high-viscosity poly-alpha-olefin base oil has a kinematic viscosity of 42.8-50.4 mm 2/s at 100 ℃, a viscosity index of 152-168 and a pour point of-42-36 ℃.
3. The anti-micro pitting wind turbine gear oil of claim 1, wherein: the extreme pressure antiwear agent is at least one of chlorinated paraffin, vulcanized lard, phosphate, borate and vulcanized olefin.
4. The anti-micro pitting wind turbine gear oil of claim 1, wherein: the antioxidant is at least one of phenolic antioxidants and amine antioxidants.
5. The anti-micro pitting wind turbine gear oil of claim 1, wherein: the defoaming agent is at least one of polysiloxane, methyl silicone oil, polyacrylate and polyether.
6. The anti-micro pitting wind turbine gear oil of claim 1, wherein: the antirust agent is at least one of alkenyl succinic acid and petroleum sulfonate.
7. The method for preparing the gear oil of the micro-pitting corrosion-resistant wind driven generator as set forth in any one of claims 1 to 6, which is characterized in that: and uniformly stirring and mixing the high-viscosity poly alpha-olefin base oil, the extreme pressure antiwear agent, the antioxidant, the pour point depressant, the antirust agent and the defoamer according to the proportion to obtain the micro pitting corrosion resistant gear oil for the wind driven generator.
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| CN202310353685.7A CN116590074B (en) | 2023-04-05 | Anti-micro pitting wind driven generator gear oil and preparation method thereof |
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| CN109536248A (en) * | 2018-10-30 | 2019-03-29 | 新疆金雪驰科技股份有限公司 | Fully synthetic anti-microdot erosion Wind-turbine gear oil composition of one kind and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109536248A (en) * | 2018-10-30 | 2019-03-29 | 新疆金雪驰科技股份有限公司 | Fully synthetic anti-microdot erosion Wind-turbine gear oil composition of one kind and preparation method thereof |
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Effective date of registration: 20240517 Address after: 233000 Huaiyuan Economic Development Zone, Bengbu, Anhui Applicant after: ANHUI JINDE LUBRICATION TECHNOLOGY Co.,Ltd. Country or region after: China Applicant after: Three Gorges new energy offshore wind power operation and maintenance Jiangsu Co.,Ltd. Address before: 233400 Huaiyuan Economic Development Zone, Bengbu City, Anhui Province Applicant before: ANHUI JINDE LUBRICATION TECHNOLOGY Co.,Ltd. Country or region before: China |
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