Preparation method for single segment hydro-cracking catalyst

Abstract

The invention discloses a preparation method for a single segment hydro-cracking catalyst. The method comprises the following steps: 1) uniformly mixing modified Y molecular sieve, amorphous form aluminum silicon and / or aluminum oxide, adding dilute nitric acid, pulping and then extruding a strip and forming, drying and roasting, thereby acquiring an aluminum silicon carrier containing the modified Y molecular sieve, wherein the mass percent of the modified Y molecular sieve in the aluminum silicon carrier is 1%-13%, preferably, 2%-10%, and the balance is amorphous form aluminum silicon and / or aluminum oxide; 2) adopting a steeping liquor containing active metal for steeping the carrier acquired in the step (1), drying and roasting the steeped carrier, thereby acquiring the hydro-cracking catalyst. The single segment hydro-cracking catalyst prepared according to the method disclosed by the invention has excellent reaction activity and nitrogen resistance in a single segment hydro-cracking process.

Description

technical field [0001] The invention relates to a preparation method of a single-stage hydrocracking catalyst. Background technique [0002] Hydrocracking technology has the characteristics of strong adaptability of raw materials, flexible product plan, high selectivity of target products, good product quality and high added value, and can directly produce a variety of high-quality petroleum products and chemical raw materials. Therefore, this technology has become the most suitable refining technology for rational utilization of limited crude oil resources, maximum production of clean petroleum products and high-quality chemical raw materials. Hydrocracking technology can be mainly divided into three types according to the processing flow: one-stage series hydrocracking process, single-stage hydrocracking process and two-stage hydrocracking process. One of the serial process flow sets up two reactors, refining and cracking. In the refining reactor, a hydrotreating catalyst...

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Problems solved by technology

In this way, although the catalyst has strong nitrogen tolerance, the catalyst activity is poor, and the reaction temperature usually exceeds 400 ° C.

Due to the high reaction temperature, limited by the thermodynamic equilibrium of hydrogenation saturation of aromatic hydrocarbons, too high reaction temperature is unfavorable to the hydrogenation saturation reaction of aromatic hydrocarbons, and the product properties are poor

The higher reaction temperature also accelerates the carbon deposition and deactivation of the catalyst, which affects the operation cycle of the hydrocracking unit.

[0005] CN200710158784.0 discloses a hydrocracking catalyst containing Y molecular sieve and its preparation method. In this invention, Y-type molecular sieve is obtained after hydrothermal treatment with a mixed aqueous solution of aluminum salt and acid, and the obtained catalyst has high activity. But nitrogen tolerance is poor

[0006] CN98114489.6 discloses a nitrogen-resistant hydrocracking catalyst for high-yielding middle oil, which is used for one-stage serial hydrocracking of heavy distillate oil to produce a large amount of middle distillate oil. The nitrogen content of the feed in the cracking section can reach 100 μg / g, but the Catalyst activity is poor

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