A method for efficient preparation of pao40 base oil
A base oil and high-viscosity base oil technology, applied in the field of chemical synthesis, to achieve the effects of saving production costs, good lubrication performance, and improving production energy efficiency
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Embodiment 1
[0049] Put 150g of aluminum trichloride, 120g of 15% triisobutylaluminum hexane solution, and 5800g of refined waste lubricating oil into the polymerization kettle, adjust the reaction temperature in the kettle to 40°C, and add 35g of benzoyl peroxide; Polymerization reaction, the reaction time is 1h, and a high-viscosity crude product is obtained.
[0050] Part of the catalyst was removed by filtration, washed with 60% 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.
[0051] The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 260°C, the hydrogen partial pressure is 15MPa, and the volume space velocity is about 0.5h -1 , The volume ratio of hydrogen to oil is 500:1, and the new PAO40 base oil is obtained through hydr...
Embodiment 2
[0053] Put 150g of aluminum trichloride, 25g of triisobutylaluminum, and 6000g of refined waste lubricating oil (low viscosity PAO≈4-6) into the polymerization kettle, adjust the reaction temperature in the kettle to 60°C, and add 25g of benzene peroxide Formyl, a polymerization reaction occurs, the reaction time is 1.5h, and a high-viscosity crude product is obtained.
[0054] 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.
[0055] The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 240°C, the hydrogen partial pressure is 18MPa, and the volume space velocity is about 0.5h -1 , The volume ratio of hydrogen to oil is 400:1, and the new PAO45 base oil is ...
Embodiment 3
[0057]Put 150g of aluminum trichloride, 45g of 96% triisobutylaluminum, and 6200g of refined waste lubricating oil (medium viscosity PAO≈10-12) into the polymerization kettle, adjust the reaction temperature in the kettle to 50°C, and add 15g of over Bis(2,4-dichlorobenzoyl) was oxidized, and a polymerization reaction occurred. The reaction time was 0.5h, and a high-viscosity crude product was obtained.
[0058] Part of the catalyst was removed by filtration, washed with 60% 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.
[0059] The vacuum distillation product is pressurized and mixed with hydrogen, and directly enters the device equipped with a hydrogenation catalyst. The feed temperature is 260°C, the hydrogen partial pressure is 15MPa, and the volume space velocity is about 0.5h -1 , The volume ratio of hydrogen to oil is 50...
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