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Multi-component compound catalyst and preparation method thereof

A composite and multi-component technology, applied in the direction of molecular sieve catalysts, preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, etc., can solve the problems of poor catalyst stability, poor product selectivity, cumbersome catalyst preparation steps, etc., and achieve structural stability , increase the pore content, and the effect of large interaction force

Inactive Publication Date: 2020-05-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is the cumbersome catalyst preparation steps in the prior art, poor product selectivity and poor catalyst stability when used in Fischer-Tropsch synthesis, synthesis gas methanation and alkane reforming reactions; Component composite catalyst, which has the advantages of high product selectivity and good catalyst stability when used in Fischer-Tropsch synthesis, syngas methanation and alkane reforming reactions

Method used

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  • Multi-component compound catalyst and preparation method thereof
  • Multi-component compound catalyst and preparation method thereof
  • Multi-component compound catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0049] After uniformly mixing 100 grams of boehmite and 25 grams of polyethylene glycol in 200 grams of water, aging treatment was performed at a temperature of 120° C. for 15 hours to obtain a precursor A;

[0050] After uniformly mixing the above-mentioned precursor A with 13.6 grams of platinum chloride (equivalent to 10 g of platinum) and 5 grams of molecular sieve, aging treatment was performed again at a temperature of 160° C. for 20 hours to obtain a precursor B;

[0051] The above precursor B is dried at a temperature of 120°C for 20 hours; then calcined at a temperature of 550°C for 10 hours to obtain a precursor C;

[0052] The above precursor C is subjected to reduction treatment at a temperature of 600°C for 5 hours to obtain a multi-component composite catalyst. The preparation process conditions are shown in Table 1. The catalyst grain size is 500nm and the average pore size is 84nm. More specifically The physical characteristics are shown in Table 2.

[0053] T...

Embodiment 2~8

[0057] According to the synthesis steps described in Example 1, changing the type and quality of the inert component precursor, the active component precursor and the surfactant, and adjusting the preparation conditions, the multi-component composite catalyst of the present invention can be synthesized, and the preparation process The conditions are shown in Table 1, and the physical properties of the catalyst are shown in Table 2.

[0058] The catalysts were used for Fischer-Tropsch synthesis, synthesis gas methanation and alkane reforming reactions respectively, the reaction conditions were the same as in Example 1, and the catalytic performance was shown in Table 2.

Embodiment 9

[0060] After uniformly mixing 98 grams of boehmite, 2 grams of magnesium oxide and 25 grams of polyethylene glycol in 200 grams of water, aging treatment was carried out at a temperature of 120° C. for 15 hours to obtain a precursor A;

[0061] After mixing the above precursor A with 13.6 grams of platinum chloride (equivalent to 10 g of platinum), 13.7 grams of ZSM-5 molecular sieve and uniformly, aging treatment was carried out again at a temperature of 160 ° C for 20 hours to obtain a precursor B;

[0062] The above precursor B is dried at a temperature of 120°C for 20 hours; then calcined at a temperature of 550°C for 10 hours to obtain a precursor C;

[0063] The above precursor C was subjected to reduction treatment at a temperature of 600°C for 5 hours to obtain a multi-component composite catalyst. The preparation process conditions are shown in Table 1, and the physical properties of the catalyst are shown in Table 2.

[0064] The catalyst is used for Fischer-Tropsch ...

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Abstract

The invention relates to a multi-component compound catalyst and a preparation method thereof, and mainly solves the problems of low activity, poor product selectivity and poor stability in the existing compound catalyst. According to the technical scheme, the multi-component compound catalyst comprises the following components in parts by weight: a) 50-100 parts of at least one selected from aluminum oxide, zirconium oxide, magnesium oxide, cerium oxide and silicon oxide; b) 1-20 parts of a metal or an oxide thereof; and c) 1-30 parts of a molecular sieve. The multi-component compound catalyst is a porous compound, the specific surface area is greater than 5m < 2 > / g, and the pore volume is greater than 0.01cm<2> / g; according to the technical scheme, the problems of low catalyst activity,poor catalyst stability, poor sintering resistance, and easily caused carbon deposition and the like are well solved, and the multi-component compound catalyst can be used in the catalytic industrialproduction process of Fischer-Tropsch synthesis, synthesis gas methanation and alkane reforming.

Description

technical field [0001] The invention relates to a multi-component composite catalyst, its preparation method and application, in particular to a multi-component composite catalyst and its preparation method which can be used for Fischer-Tropsch synthesis, synthesis gas methanation and alkane reforming. Background technique [0002] The conversion and utilization of syngas is of great significance in the context of China's energy rich in coal and lack of oil and gas. Both Fischer-Tropsch synthesis and syngas methanation are processes in which syngas is used as raw material to synthesize liquid fuel or methane under catalyst and appropriate reaction conditions. On the other hand, with the exploitation and development of unconventional natural gas in China, especially coalbed methane and shale gas, the chemical utilization of natural gas has attracted increasing attention. Whole refers to the process of using water vapor, carbon dioxide or oxygen to make alkanes into synthesis...

Claims

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Application Information

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IPC IPC(8): B01J29/44B01J29/74B01J29/76B01J29/85B01J35/10C10G3/00C01B3/26
CPCB01J29/44B01J29/7476B01J29/7484B01J29/7646B01J29/85B01J29/74C10G3/49C01B3/26B01J35/635B01J35/633B01J35/651B01J35/615Y02P30/20
Inventor 周健刘志成李丽媛高焕新
Owner CHINA PETROLEUM & CHEM CORP
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