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Hydrocracking catalyst and preparation and application thereof

A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems to be further improved, and achieve high catalytic activity, middle distillate selectivity, and high pore size. The effect of concentration

Active Publication Date: 2014-09-17
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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  • Hydrocracking catalyst and preparation and application thereof
  • Hydrocracking catalyst and preparation and application thereof
  • Hydrocracking catalyst and preparation and application thereof

Examples

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preparation example Construction

[0027]According to the catalyst preparation method provided by the present invention, the preparation method of the support includes the following steps: (1) mixing the precursor of the heat-resistant inorganic oxide, the Y-type molecular sieve and the molecular sieve with the MFI structure, the peptizer and water to provide the raw material ; (2) feeding the raw materials into an extruder and extruding after kneading in the extruder to obtain a molded body; (3) roasting the molded body to obtain the carrier , wherein, the temperature of the molded body at the outlet of the extruder is 40-150°C.

[0028] In the process of extruding raw materials with an extruder to obtain a molded body, the extrusion temperature is usually not particularly controlled (usually room temperature or lower than 40 ° C), but the inventors of the present invention have found in the course of research that Making the temperature of the molded body at the outlet of the extruder 40-150° C. can make the ...

Embodiment 1

[0089] Take SB powder (taken from Changling Catalyst Factory, produced by SASOL Company, relative crystallinity 95.4%, grain size 49.0nm, dry basis content is 75%, the same below) 84.0g, Siral40 powder (commercially purchased from SASOL Company, oxidized Silicon content is 40%, dry basis content is 77.5%) 25.8g, Y-type molecular sieve A (unit cell constant , crystallinity 81.4%, Na 2 0.02%, dry basis 86%, the preparation method is referring to ZL01118446.9, embodiment 6, molecular sieve I, the same below) 18.1g, ZRP-5 molecular sieve A (taken from Changling Catalyst Factory, containing rare earth, has MFI structure, The silicon-aluminum ratio is 60.6, the dry basis content is 83%, the same below) 2.4g, add 3g of safflower powder and dry mix evenly to obtain a dry powder. Add 3 mL of concentrated nitric acid into a beaker filled with 90 mL of deionized water, and mix well to obtain an acid solution. Mix the acid liquid and dry powder, and stir evenly to obtain the raw materi...

Embodiment 2

[0091] Take CL powder (taken from Changling Catalyst Factory, relative crystallinity 98.1%, grain size 33.0nm, dry basis content 71%, the same below) 45.1g, Siral30 powder (commercially purchased from SASOL company, silicon oxide content is 30 %, the dry basis content is 76%, the same below) 46.6g, Y-type molecular sieve C (unit cell constant , crystallinity 85.7%, Na 2 O0.032%, dry basis 85%, the preparation method sees ZL01118446.9, embodiment 3, molecular sieve C) 30.1g, ZRP-5 molecular sieve B (taken from Changling Catalyst Factory, contains rare earth, has MFI structure, silicon aluminum ratio 35.6, the dry basis content is 81%, the same below) 9.9g, add 3g of scallop powder and dry mix evenly to obtain dry powder. Add 1.5mL of concentrated nitric acid into a beaker containing 87mL of deionized water, and mix well to obtain an acid solution. Mix acid liquid and dry powder, and stir evenly to obtain the raw material mixture for extrusion, send the obtained mixture into ...

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Abstract

The invention relates to a hydrocracking catalyst and its preparation and application. The catalyst contains a matrix containing a heatproof inorganic oxide, a Y-type molecular sieve and a carrier of an MFI-structured molecular sieve, wherein the most probable pore of the carrier is 1-30 nm; and pore concentration ratio is 22-48. The most probable pore is measured by a BET method. The pore concentration ratio is the ratio of height of a peak to half-width of the peak in a distribution curve of volume of the pore measured by the BET method changing with the pore. The preparation method of the catalyst comprises preparation of matrix containing the heatproof inorganic oxide, the Y-type molecular sieve and the carrier of the MFI-structured molecular sieve. A preparation method of the carrier comprises mixing of a precursor of the heatproof inorganic oxide, the Y-type molecular sieve, the MFI-structured molecular sieve, a peptizer and water and extrusion molding, wherein temperature of a molded body at the exit of an extruder is 40-150 DEG C. In comparison with the prior art, the hydrocracking catalyst provided by the invention has high catalytic activity and middle distillate selectivity when used in hydrocarbon oil processing and has stronger ability of reducing condensation point of tail oil.

Description

technical field [0001] The invention relates to a hydrocracking catalyst and its preparation and application. 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 the catalysts used for the conversion of heavy oil or macromolecules are generally obtained by loading catalytically active components on the carrier, the preparation has larger pore size and pore volume, and has a higher ...

Claims

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Application Information

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IPC IPC(8): B01J29/80C10G47/20
Inventor 董松涛赵阳辛靖聂红石亚华李大东
Owner CHINA PETROLEUM & CHEM CORP
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