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Porous support, preparation method and application thereof, catalyst, and hydrocracking method

A technology of porous carrier and catalyst, applied in the direction of catalyst carrier, molecular sieve catalyst, physical/chemical process catalyst, etc., can solve the problems to be further improved, and achieve high catalytic activity and effect.

Active Publication Date: 2013-04-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although CN101757929A discloses that the pore concentration of the carrier can be more than 7, but from the examples disclosed in CN101757929A, the highest pore concentration of the carrier is 21.4, which needs to be further improved

Method used

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  • Porous support, preparation method and application thereof, catalyst, and hydrocracking method
  • Porous support, preparation method and application thereof, catalyst, and hydrocracking method

Examples

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preparation example Construction

[0033]The present invention also provides a method for preparing a porous carrier, the method comprising: mixing a precursor capable of forming a heat-resistant inorganic oxide under calcination conditions, a Beta molecular sieve, a peptizer, and water to provide raw materials; fed into an extruder, and extruded after kneading in the extruder to obtain a molded body; the molded body is roasted to obtain the porous carrier, wherein the molded body is in the The temperature at the outlet of the extruder is 40 to 150°C.

[0034] In the process of extruding raw materials with an extruder to obtain a molded body, the cooling conditions of the extruder are generally controlled so that the temperature of the extruded molded body is around room temperature (less than 40° C.), but this The inventors of the invention found in the course of research that the temperature of the molded body at the outlet of the extruder is 40-150° C. to make the most probable pore diameter and pore diamete...

Embodiment 1

[0109] This example is used to illustrate the porous carrier and its preparation method according to the present invention.

[0110] Get SB powder (commercially purchased from sasol company, is a kind of pseudo-boehmite, relative crystallinity is 95.4%, grain size is 49.0nm, dry basis content is 75% by weight) 85.3g, SIRAL 40 powder (commercially purchased From sasol company, silicon oxide content is 40% by weight, aluminum oxide content is 60% by weight, dry basis content is 77.5% by weight, average particle diameter is 55nm) 45.1g, Beta molecular sieve (commercially purchased from Hunan Jianchang Petrochemical Co., Ltd. , the silicon-aluminum ratio is 63.4, and the dry basis content is 83% by weight) 1.2 grams, and 3 g of safflower powder are dry-mixed evenly to obtain a dry powder. Add 2 mL of concentrated nitric acid (concentration: 65% by weight, the same below) into a beaker filled with 92 mL of deionized water, and mix well to obtain an acid solution. Mix the acid liqu...

Embodiment 2

[0112] This example is used to illustrate the porous carrier and its preparation method according to the present invention.

[0113] Get CL powder (commercially purchased from Changling Catalyst Factory, it is a kind of pseudo-boehmite, the relative crystallinity is 98.1%, the grain size is 33.0nm, and the dry basis content is 71% by weight) 84.5g, SIRAL 20 powder ( Commercially purchased from sasol company, silicon oxide content is 20% by weight, aluminum oxide content is 80% by weight, dry basis content is 75% by weight, average particle diameter is 53nm) 46.7g, Beta molecular sieve (commercially purchased from Hunan Jianchang Petrochemical Co., Ltd. Co., Ltd., the silicon-aluminum ratio is 28.6, and the dry basis content is 81% by weight) 6.2 grams, and 2.5 g of safflower powder is dry-mixed evenly to obtain a dry powder. Add 3 mL of concentrated nitric acid into a beaker filled with 93 mL of hot deionized water, and mix well to obtain an acid solution. The acid liquid and...

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Abstract

The invention provides a porous support, a preparation method and application thereof. The porous support contains heat-resisting inorganic oxides and a Beta molecular sieve, wherein the most probable pore diameter of the Beta molecular sieve is 1-30nm, and the pore diameter concentration ratio is 22-48. The method comprises the following steps of: mixing a precursor capable of forming the heat-resisting inorganic oxides under a roasting condition, the Beta molecular sieve, peptizing agent and water to obtain a raw material; and feeding the raw material into an extruder for extruding, and roasting an obtained forming body to obtain the porous support, wherein the temperature of the forming body at an outlet of the extruder is 40-150 DEG C. The invention also provides a catalyst of the porous support, and application thereof. The invention also provides a hydrocracking method. The porous support not only has a larger pore diameter and pore volume, but also has a higher pore diameter concentration ratio. The catalyst has high catalytic activity and middle distillate selectivity when being used for hydrocracking hydrocarbon oil.

Description

technical field [0001] The invention relates to a porous carrier, its preparation method and application, and also relates to a catalyst containing the porous carrier and a hydrocracking method using the catalyst. Background technique [0002] In recent years, the trend of heavy and inferior crude oil has become increasingly obvious worldwide. At the same time, the demand for middle distillates, reforming and steam cracking raw materials has continued to increase. This promotes the rapid development of heavy distillate processing technology, and catalyst is the most important and key factor. [0003] Catalysts used for the conversion of heavy oil or macromolecules require not only a large pore size and sufficient pore volume, but also a concentrated pore size distribution of the pores in the catalyst (that is, a high pore size concentration). [0004] Since catalysts used for the conversion of heavy oil or macromolecules are generally obtained by loading catalytically activ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J32/00B01J35/10B01J29/70B01J29/78C10G47/20
Inventor 董松涛李明丰聂红石亚华李大东
Owner CHINA PETROLEUM & CHEM CORP