PAO4 base oil and lubricating oil used for jet engine
A jet engine and lubricating oil technology, applied in the field of lubricating oil, can solve problems such as poor oxidation stability, and achieve stable lubrication effect and excellent oxidation stability.
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Embodiment 1
[0035] A. Synthesis of PAO4:
[0036] Put 1400g of 1-decene (>99%) into the polymerization kettle, add 300g of aluminum trichloride in batches, heat the reaction temperature to 90°C, and polymerize for 3 hours to obtain a crude polydecene product.
[0037] Part of the catalyst was removed by filtration, washed with 40% sodium hydroxide aqueous solution, and the aluminum trichloride was neutralized until the pH of the solution was neutral, and the remaining was put into a rotary evaporator for vacuum distillation.
[0038] The gas-liquid separation obtains oligomers and unreacted 1-decene compound monomers, and the unreacted 1-decene compound monomers re-enter the polymerization tank for polymerization. The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 160°C, the hydrogen partial pressure is 9MPa, and the volume space velocity is about 0.5h -1 , The volume ratio...
Embodiment 2
[0042] A. Synthesis of PAO4:
[0043] Put 1600g of 1-decene (>99%) into the polymerization kettle, add 300g of aluminum trichloride in batches, heat the reaction temperature to 100°C, and polymerize for 4 hours to obtain a crude polydecene product.
[0044] Part of the catalyst was removed by filtration, washed with 40% sodium hydroxide aqueous solution, and the aluminum trichloride was neutralized until the pH of the solution was neutral, and the remaining was put into a rotary evaporator for vacuum distillation.
[0045] The gas-liquid separation obtains oligomers and unreacted 1-decene compound monomers, and the unreacted 1-decene compound monomers re-enter the polymerization tank for polymerization. The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 160°C, the hydrogen partial pressure is 9MPa, and the volume space velocity is about 0.5h -1 , The volume rati...
Embodiment 3
[0049] A. Synthesis of PAO base oil:
[0050]Put 1200g of 1-decene (>99%) into the polymerization kettle, add 300g of aluminum trichloride in batches, heat the reaction temperature to 90°C, and polymerize for 3 hours to obtain a crude polydecene product.
[0051] Part of the catalyst was removed by filtration, washed with 40% sodium hydroxide aqueous solution, and the aluminum trichloride was neutralized until the pH of the solution was neutral, and the remaining was put into a rotary evaporator for vacuum distillation.
[0052] The gas-liquid separation obtains oligomers and unreacted 1-decene compound monomers, and the unreacted 1-decene compound monomers re-enter the polymerization tank for polymerization. The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 160°C, the hydrogen partial pressure is 9MPa, and the volume space velocity is about 0.5h -1 , The volum...
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