Hydrocracking after-treatment catalyst and preparing method thereof

A hydrocracking and catalyst technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of different processing conditions, low hydrogen-to-oil ratio, incompatibility, etc., and achieve simplified preparation process , Improve hydrogenation performance and low cost

Inactive Publication Date: 2004-06-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN 1229838A improves on this basis, so that the hydrorefining of dedistillation alcohol can not only be carried out at a relatively low reaction temperature of 150-260 ° C, but also has a low hydrogen-to-oil ratio (5-30). This method Although the reaction conditions are milder and the mercaptan removal effect is better, the hydrofinishing process used is different from the usual hydrocracking post-treatment conditions, and cannot be directly matched with the hydrocracking process
Usually, in order to achieve a higher Ni / (Mo+Ni) ratio, several steps of impregnation are used, which increases the process and complicates the process.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1~4

[0035] The properties of various macroporous and small porous aluminas used in Examples 1-4 are shown in Table 1.

[0036] Table 1 Properties of alumina

[0037] raw material

Embodiment 1

[0039] Preparation of the catalyst carrier DT-1 provided by the invention.

[0040] Get 111 grams of macroporous alumina A, 100 grams of pseudoboehmite, 6.6 grams of macroporous alumina B, 16.7 grams of basic nickel carbonate (Ni content is 40wt%) and mix for 15 minutes, add 200 grams of binder (Germany SB 47.2 grams of alumina, prepared by beating with 6.46 grams of 65% nitric acid with a volume concentration of 65%, the solid content of the binder is 17wt%, and 2 grams of squash powder are mixed and rolled for 30 minutes, and the diameter of the extruded rod is 1.6 mm clover strips, dried at 120°C for 2 hours, and calcined at 500°C for 4 hours to obtain carrier DT-1. The specific surface area and pore volume of carrier DT-1 are listed in Table 2. The specific surface area and pore volume were measured by low-temperature nitrogen adsorption BET method (the same below).

Embodiment 2

[0042] Preparation of the catalyst carrier DT-2 provided by the invention.

[0043] Get 150 grams of macroporous alumina A, 67.5 grams of pseudoboehmite, 80.8 grams of German SB alumina, nickel nitrate (Ni(NO 3 ) 2 ·6H 2 (0) 44.33 grams were mixed for 15 minutes, adding 317.6 grams of binder (69.2 grams of German SB alumina and 8.4 grams of volume concentration were prepared by beating nitric acid of 65%, and the solid content of binder was 17wt%), and 3 grams of citric acid Knead and roll for 30 minutes, extrude to obtain clover strips with a diameter of 1.6mm, then dry at 110°C for 4 hours, and bake at 550°C for 4 hours to obtain carrier DT-2. The specific surface area and pore volume of carrier DT-2 are listed in Table 2.

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Abstract

The invention discloses a processing catalyzer after hydrogenated cracking and preparing method, adopting alumina as carrier, Mo and/or Wu as well as Ni and Co as active components, and P as catalyst promoting component. Firstly, it carries a part of Ni on the carrier by mixed kneading, and then uses Ni-Mo-Co-P mixed solution for dipping to make the catalyzer. It has higher NiO content, higher Ni/Ni+Mo atomic ratio, especially applied to processing the course of producing low-mercaptan product after hydrogenated cracking.

Description

technical field [0001] The invention relates to a hydroprocessing catalyst and a preparation method thereof, in particular to a hydrocracking post-treatment catalyst and a preparation method thereof. Background technique [0002] Hydrocracking is a petroleum refining process that breaks high-boiling hydrocarbons through C-C bonds to form small molecules and low-boiling target products. In the process of hydrocracking, raw materials are cracked to produce a small amount of olefins that react with H2S in the system to form mercaptans. Generally, too high a reaction temperature will be unfavorable for olefin saturation and more likely to form mercaptans. The presence of mercaptan in the product can not only cause the product to produce stench and reduce the quality and stability of the oil product, but also the mercaptan itself is corrosive. With the increase of high-sulfur crude oil refining volume and the strengthening of environmental protection regulations, the problem of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J21/04B01J27/14C10G45/08
Inventor 刘雪玲梁相程姚颂东王继锋温德荣喻正南
Owner CHINA PETROLEUM & CHEM CORP
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