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A kind of hydrocracking catalyst composition and preparation method thereof

A hydrocracking and catalyst technology, which is applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem of increased secondary cracking, increased secondary cracking in the process of temperature increase, and the sensitivity of hydrocracking catalyst to temperature increase. It can improve the acid center, improve the sensitivity of temperature increase, and improve the liquid recovery and chemical hydrogen consumption of the device.

Active Publication Date: 2017-12-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, modified Y molecular sieve is the most widely used in hydrocracking process. The conventional treatment method has uniform distribution of silicon and aluminum inside and outside the molecular sieve, and uniform distribution of acid centers. When the silicon aluminum ratio of Y molecular sieve is reduced, the acid center density of Y molecular sieve is increased, and the The temperature sensitivity is improved, but at the same time, the secondary cracking is also greatly increased, and the hydrogen consumption is greatly increased
However, when the Y molecular sieve is subjected to advanced treatment and the acid density is too low, the temperature-raising sensitivity of the catalyst is poor.
[0004] 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 temperature-raising sensitivity of the prepared catalyst is Higher, but at the same time, the secondary cracking during the heating process increases significantly, and the hydrogen consumption increases significantly, which is not conducive to the stable operation of the industrial hydrocracking unit during the heating process
[0005] CN200810012212.6 discloses a hydrocracking catalyst carrier and its preparation method. The hydrocracking catalyst prepared by the invention has poor temperature raising sensitivity

Method used

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  • A kind of hydrocracking catalyst composition and preparation method thereof
  • A kind of hydrocracking catalyst composition and preparation method thereof
  • A kind of hydrocracking catalyst composition and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] Molecular sieve modification process:

[0040] (1) Take 200g of NaY molecular sieve raw powder prepared in the laboratory, mix it with ammonium nitrate with a concentration of 0.5mol / L according to the liquid-solid ratio of 3:1, exchange at 70°C for 3 hours, repeat this process 3 times, and the exchanged Y molecular sieve Na content in Na 2 O is calculated as 2.5%;

[0041] (2) The molecular sieve obtained in step (1) was mixed with distilled water according to the liquid-solid ratio of 5:1, then, 200ml of ammonium fluorosilicate solution with a concentration of 0.9mol / L was added, and treated at 80°C for 2 hours;

[0042] (3) Hydrothermally treat the Y molecular sieve obtained in step (2) at 540°C and 0.1MPa for 1.5 hours;

[0043] (4) The molecular sieve obtained in step (3) was stirred and mixed with distilled water according to the liquid-solid ratio of 7:1, and then the temperature was raised to 80°C. During the stirring process, 400ml of 0.5mol / L aluminum sulfat...

Embodiment 2

[0055] Molecular sieve modification process:

[0056] (1) Take the NaY molecular sieve raw powder prepared in the laboratory, mix it with ammonium nitrate with a concentration of 0.8mol / L according to the liquid-solid ratio of 3:1, exchange at 70°C for 3 hours, repeat this process 3 times, and the Y molecular sieve after exchange Na content in Na 2 O is calculated as 2.0%.

[0057] (2) Mix the molecular sieve obtained in step (1) with distilled water according to the liquid-solid ratio of 5:1, then add 300ml of ammonium fluorosilicate solution with a concentration of 1.5mol / L, and treat at 90°C for 2 hours;

[0058] (3) Hydrothermally treat the Y molecular sieve obtained in step (2) at 550°C and 0.1MPa for 2 hours;

[0059] (4) The molecular sieve obtained in step (3) was stirred and mixed with distilled water according to the liquid-solid ratio of 6:1, and then the temperature was raised to 90°C. During the stirring process, 600ml of 0.8mol / L aluminum sulfate solution was a...

Embodiment 3

[0071] Molecular sieve modification process:

[0072] (1) Take the NaY molecular sieve raw powder prepared in the laboratory, mix it with ammonium nitrate with a concentration of 0.8mol / L according to the liquid-solid ratio of 3:1, exchange at 70°C for 3 hours, repeat this process 3 times, and the Y molecular sieve after exchange Na content in Na 2 O is calculated as 2.0%.

[0073] (2) The molecular sieve obtained in step (1) was mixed with distilled water according to the liquid-solid ratio of 5:1, then, 250ml of ammonium fluorosilicate solution with a concentration of 1.0mol / L was added, and treated at 95°C for 2 hours;

[0074] (3) Hydrothermally treat the Y molecular sieve obtained in step (2) at 540°C and 0.1MPa for 1.5 hours;

[0075] (4) The molecular sieve obtained in step (3) was stirred and mixed with distilled water according to the liquid-solid ratio of 6:1, and then the temperature was raised to 90°C. During the stirring process, 600ml of 0.8mol / L aluminum sulfa...

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Abstract

The invention discloses a hydrocracking catalyst composition and a preparation method thereof. The catalyst composition comprises the following components: 55%-85% of a silicon-alumina carrier containing modified Y molecular sieve, and 15%-45% of an active metal; wherein The mass percentage of the modified Y molecular sieve in the silica-alumina carrier is 15%-90%, and the balance is amorphous silica-alumina and / or alumina; the bulk phase silica-alumina ratio of the modified Y molecular sieve is 10-90, and the surface The silicon-aluminum ratio of the layer is 6~30, the specific surface area is 650~900m2 / g, and the pore volume is 0.30~0.50ml / g. The preparation method is as follows: 1. Mix the modified Y molecular sieve, amorphous silica-alumina and / or alumina evenly, add dilute nitric acid to form a slurry, extrude, dry and roast to obtain the silica-alumina carrier containing the modified Y molecular sieve; 2. The carrier is impregnated with an impregnating liquid containing active metal, dried and calcined to obtain a hydrocracking catalyst. The hydrocracking catalyst prepared by the method of the invention has good temperature raising sensitivity and operational flexibility, and has broad application prospects in the hydrocracking reaction process.

Description

technical field [0001] The invention relates to a hydrocracking catalyst composition and a preparation method thereof. Background technique [0002] Hydrocracking technology has the characteristics of strong adaptability to raw materials, great flexibility in production operations and product plans, and good product quality. It can directly convert various heavy and low-quality feedstocks into high-quality jet fuel, diesel, and lubricating oil base materials that are urgently needed by the market. As well as chemical naphtha and tail oil steam cracking raw materials for ethylene production, it has become one of the most important heavy oil deep processing processes in modern oil refining and petrochemical industries, and has been increasingly widely used at home and abroad. The heart of the hydrocracking process is the hydrocracking catalyst. Hydrocracking catalyst is a typical dual-function catalyst, which has dual functions of hydrogenation and cracking. Among them, the ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16C10G47/20
Inventor 柳伟关明华杜艳泽王凤来刘昶秦波张晓萍
Owner CHINA PETROLEUM & CHEM CORP