Method for preparing low-carbon olefine catalyst by loading iron-based synthetic gas

A technology of low-carbon olefins and catalysts, which is applied in the field of preparation of supported iron-based syngas-based low-carbon olefin catalysts, can solve the problems of difficult to achieve reaction activity, low CO conversion rate, high catalyst cost, etc., and achieve high mechanical strength, The effect of improving activity and simple preparation method

Active Publication Date: 2012-05-09
CHINA PETROLEUM & CHEM CORP +1
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  • 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, on

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  • Method for preparing low-carbon olefine catalyst by loading iron-based synthetic gas
  • Method for preparing low-carbon olefine catalyst by loading iron-based synthetic gas

Examples

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example 1

[0018] Weigh commercially available silica gel (pore volume is 1.06ml / g, specific surface area is 386.81m 2 / g, the following examples all use the silica gel) 30g, distilled water is added dropwise to initial moistening, the volume of consumed water is 48ml, 48ml concentration is 20% pyridine solution, add in silica gel at 50 ℃, process 10 hours. Dry at 60°C for 24 hours, then bake at 280°C for 15 hours. Based on the final catalyst K content of 0.023wt%, weigh 0.0179g of potassium nitrate and add distilled water to 48g, add the above-mentioned modified carrier silica gel for impregnation, dry at 60°C for 24 hours, and bake at 350°C for 10 hours. Based on the final catalyst Fe content of 3wt%, weigh 6.6303g of ferric nitrate and add distilled water to 48g, add to the above-mentioned sample impregnated with potassium, dry at 60°C for 24 hours, and bake at 350°C for 10 hours in vacuum or nitrogen atmosphere. Based on the final catalyst manganese content of 1.06wt%, weigh 2.0716g...

example 2

[0021] Weigh 30g of commercially available silica gel, add distilled water dropwise until initial moistening, the volume of consumed water is 48ml, add 48ml of 15% diethanolamine solution into the silica gel at 80°C, and stir. Treat for 30 hours and dry at 90°C for 16 hours. According to the final catalyst K content of 0.39wt%, weigh 0.3042g of potassium nitrate, add distilled water to 48g, add the above-mentioned modified carrier silica gel to impregnate, dry at 100°C for 16 hours, and roast in vacuum or nitrogen atmosphere at 550°C for 4 Hour. Based on the final catalyst Fe content of 9wt%, weigh 19.8909g of ferric nitrate, add distilled water to 48g, add to the above-mentioned sample impregnated with potassium, dry at 100°C for 16 hours, and bake in vacuum or nitrogen atmosphere at 550°C for 4 hours. Based on the final catalyst manganese content of 3.6wt%, weigh 7.0355g of 50% manganese nitrate solution, add distilled water to 48g, add the above sample impregnated with pot...

example 3

[0023]Weigh 30g of commercially available silica gel, add distilled water dropwise until initial moistening, the volume of consumed water is 48ml, add 48ml of 5% ethanolamine solution to the silica gel at 95°C, stir for 100 hours, and dry at 100°C for 8 hours. Based on the final catalyst K content of 0.8wt%, 0.624g of potassium nitrate was weighed and dissolved in 48ml, added to the modified carrier silica gel for impregnation, dried at 150°C for 8 hours, and roasted at 700°C for 2 hours in vacuum or nitrogen atmosphere. Based on the final catalyst Fe content of 12wt%, 26.5212g of iron nitrate was weighed and dissolved in 48ml, added to the above-mentioned sample impregnated with potassium, dried at 150°C for 8 hours, and roasted in vacuum or nitrogen atmosphere at 700°C for 2 hours. Based on the final catalyst manganese content of 5.44wt%, weigh 10.6315g of 50% manganese nitrate solution, add water to 48g, add the above sample impregnated with potassium and iron, age for 3 hou...

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Abstract

The invention discloses a method for preparing a low-carbon olefine catalyst by a loading iron-based synthetic gas, which comprises the following steps of: firstly carrying out surface modification on a silica gel carrier by using silica gel as a carrier, and then loading a metal auxiliary agent and an active component Fe by using an immersion method, wherein the surface modification method of the silica gel carrier comprises the following step of carrying out immersion treatment by using the acidic solution of sugar. After the silica gel carrier adopted is modified, the strong interaction between the carrier and the active component is overcome, and the activity and the selectivity of the catalyst are improved. The catalyst prepared by using the method is suitable for a reaction process of producing low-carbon olefines of ethylene, propylene, butane and the like by the synthetic gas.

Description

technical field [0001] The invention relates to a preparation method of a loaded iron-based synthesis gas catalyst for producing low-carbon olefins, in particular to a low-cost and easy-to-industrial-apply high-activity iron-based catalyst modified with modified silica gel and added with metal additives. A preparation method of a catalyst for producing low-carbon olefins from syngas. 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 petroleum 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 pro...

Claims

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Application Information

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IPC IPC(8): B01J23/745B01J23/889C07C1/04C07C11/02
CPCY02P20/52
Inventor 李杰张舒冬张喜文宋喜军
Owner CHINA PETROLEUM & CHEM CORP
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