Catalyst for synthesis gas reaction, preparation method and application thereof

A catalyst and synthesis gas technology, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem that the activity stability of low-carbon olefin catalyst needs to be further improved, the CO conversion rate is low, and the catalyst cost is high. problem, to achieve the effect of outstanding comprehensive performance, improved conversion rate and improved selectivity

Active Publication Date: 2018-01-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] CN1065026A discloses a method for producing ethylene from synthesis gas, which involves the preparation of catalysts by chemical precipitation and mechanical mixing, using precious metals or rare metals, such as niobium, gallium, praseodymium, scandium, indium, cerium, lanthanum, ytterbium, etc. For other chemical elements, the selectivity of ethylene is 65%-94%, but the conversion rate of CO is very low, only about 10%, 12% and 15%. The recycling of CO will inevitably lead to energy consumption, and the catalyst cost is high
However, the activity stability of the long-term operation of the above-mentioned Fe-based silica gel-supported synthesis gas to directly prepare low-carbon olefins catalysts still needs to be further improved.

Method used

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  • Catalyst for synthesis gas reaction, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0025] Weigh commercially available alumina (pore volume is 0.96ml / g, specific surface area is 286.81m 2 / g, the saturated water absorption is 145ml / g, provided by Fushun Branch of Sinopec Catalyst Co., Ltd., the following examples and comparative examples all use this alumina), the mass concentration is 5% pyridine aqueous solution saturated spray impregnated alumina Immediately after finishing, dry at 95°C for 1 h, the adsorption amount of the dried pyridine aqueous solution is 60% of the saturated absorption solution of the alumina carrier, aging at 60°C for 7 h, drying at 100°C for 24 hours, and then calcining at 300°C for 5 The modified alumina carrier was prepared in hours. The above-mentioned modified alumina carrier is impregnated with nickel and gallium mixed aqueous solution of nickel nitrate and gallium nitrate with molar concentrations of 0.5mol / L and 1mol / L respectively by unsaturated spray impregnation method, the impregnation temperature is 50°C, the impregnation...

example 2

[0028] Weigh commercially available alumina, saturate spray and impregnate the alumina with a mass concentration of 20% diethanolamine aqueous solution, and immediately dry at 110°C for 0.5h after drying until the adsorption amount of the diethanolamine aqueous solution is the amount of the saturated absorption solution of the alumina carrier. 40%, aged at 80°C for 4 hours, dried at 120°C for 8 hours, and then calcined at 400°C for 3 hours to obtain a modified alumina carrier. The above-mentioned modified alumina carrier is impregnated with nickel nitrate and gallium nitrate mixed aqueous solutions with nickel and gallium molar concentrations of 1.5mol / L and 3mol / L respectively by unsaturated spray impregnation method. The impregnation temperature is 60°C and the impregnation time is 2h. It is 40% of the amount of the saturated absorption solution of the alumina carrier, dried at 90°C for 10h, and calcined at 900°C for 4h. The unsaturated carrier after roasting is sprayed and ...

example 3

[0030] Except that 5% ammonium thiocyanate was added to the impregnated ferric nitrate aqueous solution, the rest were the same as in Example 1, and the prepared catalyst was recorded as C-3, and the evaluation results after 300 hours were shown in Table 1.

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Abstract

The invention discloses a catalyst for synthesis gas reaction and a preparation method and application thereof. The preparation of the catalyst comprises the following steps: (1) carrying out equivalent-volume saturated impregnation on an alumina carrier with an aqueous solution of a nitrogen-containing organic compound; (2) preparing a mixed aqueous solution of nickel salt and gallium salt, and impregnating the modified alumina carrier prepared in the step (1) with the above mixed aqueous solution by an unsaturated impregnation method; (3) impregnating the carrier roasted in the step (2) with a wetting solution containing an adsorbent by an unsaturated impregnation method; (4) impregnating the adsorbent-containing carrier obtained in the step (3) with a solution containing active metal iron and a promoter manganese, drying, roasting and impregnating with a metal promoter potassium solution, drying, and roasting to produce the catalyst for preparing low-carbon olefin by catalyzing synthesis gas. The catalyst has the characteristic of high activity stability for long-term operation and is beneficial to industrial application and promotion.

Description

technical field [0001] The invention relates to a catalyst for synthesis gas reaction, its preparation method and application, in particular to a highly active and stable loaded iron-based catalyst for producing low-carbon olefins from synthesis gas and its preparation method. Background technique [0002] Low-carbon olefins such as ethylene and propylene are important basic organic chemical raw materials. With the development of the chemical industry, their demand is increasing. So far, the way to produce low-carbon olefins such as ethylene and propylene is mainly through the cracking process of light oil. With the increasing depletion of oil resources worldwide, the future energy structure will inevitably shift. Compared with oil resources, coal and natural gas resources are relatively abundant, and it is of great significance to develop low-carbon olefin production processes based on coal and natural gas. The development of direct production of ethylene and propylene tec...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/889B01J37/18
Inventor 李杰张信伟张舒冬孙晓丹尹泽群刘全杰
Owner CHINA PETROLEUM & CHEM CORP
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