Method for lowering lubricating oil fraction pour point and turbidity point
A technology for lubricating oil and distillate oil, applied in the production field of lubricating base oil, can solve the problems of low liquid yield and poor activity, and achieve the effects of reducing pour point and cloud point, and improving activity and selectivity
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preparation example Construction
[0017] In the preparation method of the catalyst, the introduction of the hydrogenation active metal component in a carrier containing ZSM-5 molecular sieve and matrix means that the effective amount of the hydrogenation active metal component is deposited Under the conditions on the carrier, the carrier is contacted with a solution containing the hydrogenation active metal component, such as by ion exchange, impregnation, co-precipitation and other methods, preferably impregnation. The impregnation method is a conventional impregnation method, through the adjustment and control of the concentration, dosage or carrier dosage of the compound solution containing the hydrogenation active metal component, the method of preparing a catalyst with a specified content of the hydrogenation active metal component is based on well known to those skilled in the art. When the impregnation is completed, it also includes the step of drying, roasting or not roasting, the conditions of the dry...
Embodiment 1
[0029] With 60 grams (dry basis weight) ZSM-5 molecular sieve (Changling Oil Refinery Catalyst Factory product, average grain size is about 80 nanometers, the mol ratio of silicon oxide and aluminum oxide is 32) and 189.2 grams of alumina powder (Changling Refinery catalyst factory products, dry basis 74% by weight) mixed, then extruded into cylindrical bars of Φ1.4 mm, wet bars were dried in air at 120°C for 4 hours, and roasted at 560°C for 4 hours to make catalyst carrier Z1.
[0030] Get 150 grams of carrier Z1, contact it with a mixed medium containing an aqueous solution of 1.0% by weight of tri-n-butylamine and air at 450°C for 8 hours, the ratio of the aqueous solution to the carrier is 1.0 g / g, and the ratio of the air to the carrier is 1.0 L / g·hour. The contact is carried out in a 150 ml reaction device, wherein the aqueous solution containing 1.0% by weight of tri-n-butylamine is introduced into the reactor by a metering pump; the air is compressed air, which is met...
Embodiment 2
[0033] With 150 grams (dry basis weight) ZSM-5 molecular sieve (Changling Oil Refinery Catalyst Factory product, average grain size is about 90 nanometers, the mol ratio of silicon oxide and aluminum oxide is 118) and 64.1 grams of alumina powder (Changling Refinery catalyst factory products, dry basis 70% by weight) mixed, then extruded into cylindrical bars of Φ1.4 mm, wet bars were dried in air at 120 ° for 4 hours, and roasted at 500 ° C for 6 hours to make catalyst carrier Z2.
[0034] Get 150 grams of carrier Z2, and contact it with a mixed medium containing an aqueous solution of 2.5% by weight of tetraethylammonium hydroxide and air at 480°C for 4 hours, the ratio of the aqueous solution to the carrier is 0.5 g / g·hour, and the ratio of the air to the carrier The ratio is 2.0 liters / gram·hour.
[0035] Get the carrier Z2 after 98.8 grams of treatment, with nickel nitrate [Wi(NO 3 ) 2 ·6H 2 O] 56 milliliters of aqueous solutions containing 1.2 grams of nickel oxide pr...
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Abstract
Description
Claims
Application Information
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