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Catalyst for preparation of olefin from synthesis gas as well as preparation method and application of catalyst

A catalyst and synthesis gas technology, which is applied in the field of high activity and stability supported iron-based synthesis gas to low-carbon olefin catalysts and its preparation, and can solve the problems of low-carbon olefin catalyst activity and stability, low CO conversion rate, and low-carbon olefin catalysts. High cost and other problems, to achieve the effect of outstanding comprehensive performance, improved conversion rate, and improved selectivity

Active Publication Date: 2017-05-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

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 preparation of olefin from synthesis gas as well as preparation method and application of catalyst

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 1.5 mol / L and 3 mol / L respectively by unsaturated spray impregnation method. 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 dipped in morphine aqueous solution, the spray volume of morphine aq...

example 3

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

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Abstract

The invention discloses a preparation method of a catalyst for preparation of olefin from synthesis gas. The preparation method comprises the following steps: (1) dipping a nitrogen-containing organic compound aqueous solution with an aluminum oxide carrier under the isovolumetric saturation condition, and drying after dipping until the adsorption amount of the nitrogen-containing organic compound aqueous solution is 30 to 60 percent of the amount of the aluminum oxide carrier saturated absorbing solution; (2) preparing a mixed aqueous solution of nickel salt and gallium salt, and dipping the mixed aqueous solution with the modified aluminum oxide carrier prepared in the step (1) by an unsaturated dipping method; (3) dipping the carrier roasted in the step (2) without wetting liquid containing an adsorbent by an unsaturated dipping method; (4) dipping a solution containing active metal iron with the adsorbent-containing carrier in the step (3), drying, roasting, dipping with metal additives, and drying and roasting again to prepare the catalyst for preparation of low-carbon olefin by the synthesis gas. The catalyst has the characteristic of high long-period operation activity stability and is favorable for industrial application and popularization.

Description

technical field [0001] The invention relates to a catalyst for producing olefins from synthesis gas and a preparation method thereof, in particular to a high-activity and stability loaded iron-based catalyst for producing low-carbon olefins from synthesis gas and a preparation method thereof. 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 a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/889C07C1/04C07C11/04C07C11/06C07C11/08
CPCY02P20/52B01J23/002B01J23/889B01J2523/00C07C1/044C07C2523/889
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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