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High-activity hydro-cracking preprocessing catalyst and preparing method and application thereof

A hydrocracking and catalyst technology, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, catalyst carrier, etc., can solve the problems of reducing catalyst reactivity, aggregation of active metal components, uneven metal distribution, etc., to achieve shortening The effect of drying activation time, reducing production cost, and improving drying activation efficiency

Inactive Publication Date: 2018-09-21
CNOOC TIANJIN CHEM RES & DESIGN INST +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional wet method loads the active components. When the amount of metal impregnation is large, the impregnation will easily cause uneven distribution of the metal inside and outside the pores of the porous material; the catalyst is activated by traditional drying in an electric oven or a rotary kiln. The heating method is heat conduction, which is low in heating efficiency and time-consuming. Long, difficult temperature control, this way of heating and drying the activated catalyst will easily cause the aggregation of active metal components and reduce the reactivity of the catalyst

Method used

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  • High-activity hydro-cracking preprocessing catalyst and preparing method and application thereof
  • High-activity hydro-cracking preprocessing catalyst and preparing method and application thereof
  • High-activity hydro-cracking preprocessing catalyst and preparing method and application thereof

Examples

Experimental program
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Effect test

Embodiment -1

[0033] Catalyst design: NiO:4.0wt%, MoO 3 :4.0wt%, WO 3 : 20.0wt%, P 2 o 5 : 2.0wt%, silicon modified alumina 28.0wt%, modified USY molecular sieve 12.0wt%, macroporous alumina 30.0wt%.

[0034] 238.0g macroporous alumina (dry basis content 72%), 222.0g silicon modified alumina (SiO 2 Content 4wt%, dry basis content 74%), 78.0g modified Y molecular sieve (SiO 2 / Al 2 o 3 =25.0, dry basis content 88%) mixed with 8.0g methyl cellulose, put into kneader and knead for 20min, add 500g of acidic solution prepared by water, acetic acid, citric acid into dry powder successively, first knead until extrudable paste The material is then extruded once through an empty plate and a cylindrical orifice plate with a diameter of 8 mm, and finally formed into a butterfly-shaped bar with a diameter of 1.5 mm; the obtained wet bar is dried in an oven at 120 ° C for 8 hours, and finally placed in a muffle furnace The temperature was programmed to rise to 500°C for 3 hours to obtain the carr...

Embodiment -2

[0037] Catalyst design: NiO:4.0wt%, MoO 3 :4.0wt%, WO 3 : 20.0wt%, P 2 o 5 : 2.0wt%, silicon-zirconium modified alumina 24.0wt%, H-Beta molecular sieve 14.0wt%, macroporous alumina 32.0wt%.

[0038] 256.0g macroporous alumina (dry basis content 72%), 183.0g silicon zirconium modified alumina (SiO 2 , ZrO 2 Total content 8wt%, dry basis content 75%), 94.0g H-Beta molecular sieve (SiO 2 / Al 2 o 3 =40.0, dry basis content 85%), 8.0g kale powder mixed with 4.0g methyl cellulose and then dropped into a kneader for 20min mixing, and 490g was added successively in the dry powder by the acidic solution prepared by water, acetic acid and citric acid. Knead until extrudable paste, then extrude through an empty plate and a cylindrical orifice plate with a diameter of 8 mm, and finally form a butterfly-shaped bar with a diameter of 1.5 mm; dry the obtained wet bar in an oven at 120 ° C for 8 hours, and finally Place in a muffle furnace and heat up to 500°C for 3 hours to obtain th...

Embodiment -3

[0041] Catalyst design: NiO:4.0wt%, MoO 3 :4.0wt%, WO 3 : 20.0wt%, P 2 o 5 : 2.0wt%, silicon phosphorus modified alumina 28.0wt%, H-SAPO-5 molecular sieve 14.0wt%, macroporous alumina 28.0wt%.

[0042] 222.0g macroporous alumina (dry basis content 72%), 222.0g silicon phosphorus modified alumina (SiO 2 ,P 2 o 5 Total content 6wt%, dry basis content 72%), 89.0g H-Beta molecular sieve (SiO 2 / Al 2 o 3 = 0.3, dry basis content 90%), 8.0g kale powder and 4.0g soluble starch are mixed and put into a kneader for 20min. The acid solution prepared by water, acetic acid and citric acid is added to the dry powder successively by 490g, and first kneaded to The extrudable paste is extruded through a toothed spherical orifice, stretched and broken by a belt transmission device, and finally pelletized to obtain a toothed spherical carrier with a particle size of 2.0mm; the obtained wet ball is dried in an oven at 120°C for 6 hours , and finally placed in a muffle furnace and progra...

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Abstract

The invention provides a high-activity hydro-cracking preprocessing catalyst and a preparing method and application thereof. The catalyst is composed of active components, carriers and aids, has the specific surface area of 160-300 m<2> / g and the pore volume of 0.38-0.60 cm<3> / g; the active components are one or more of Ni, Mo and W, the carriers are one or more of large-pore aluminum oxide, modified aluminum oxide and modified molecular sieves, and the aids are one or more of B, F and P; the hydro-cracking preprocessing catalyst is prepared through a vacuum organic complexing and dipping-microwave low-temperature activating method by placing the carriers in a dipping double cone for vacuumizing processing, loading active metal through an incipient-wetness impregnation method and finally conducting microwave heating and rapid low-temperature activating. The high-activity hydro-cracking preprocessing catalyst has the advantages of being high in activity and low in production cost.

Description

technical field [0001] The invention relates to the technical field of hydrogenation catalysts, and relates to a preparation method of a high-activity hydrocracking pretreatment catalyst. Background technique [0002] As the world's petroleum resources become increasingly heavy and inferior, and petroleum fuel products become increasingly high-quality and clean, the development of high-efficiency conversion of heavy crude oil and clean oil production technology has become the top priority of today's petroleum processing industry. Hydrocracking technology is a comprehensive processing technology that integrates the lightening of heavy oil and the production of clean oil products. It has become the core technology of future oil processing and the main trend of vigorous development of refining and chemical enterprises. The core of the hydrocracking technology lies in the hydrocracking catalyst, and the catalyst contains molecular sieves, which are easy to adsorb nitrogen compou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/16B01J29/78B01J29/85B01J29/80B01J32/00B01J37/02B01J37/34B01J37/08B01J35/10C10G47/20
CPCC10G47/20B01J29/166B01J29/7815B01J29/80B01J29/85B01J37/0018B01J37/0201B01J37/0205B01J37/0207B01J37/343B01J2229/186B01J35/617B01J35/615B01J35/635B01J35/633
Inventor 于海斌肖寒朱金剑臧甲忠张景成张国辉王帅宋国良张尚强潘月秋张玉婷陈永生李佳彭雪峰姜雪丹
Owner CNOOC TIANJIN CHEM RES & DESIGN INST
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