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Catalyst for one-step conversion of synthesis gas to aromatics and preparation method thereof

A synthesis gas and catalyst technology, which is applied in the field of catalyst and its preparation for one-step conversion of synthesis gas to aromatics, can solve the problems of complex reactor process, difficulty in maintaining life, and insufficient competitiveness, and achieve improved conversion efficiency, low cost, and stability sex good effect

Active Publication Date: 2018-09-04
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Aromatics can be obtained on these catalysts, but often not more than 45% (such as Pd-modified Fe-HZSM-5 catalysts), and it is difficult to maintain a good life
Some studies report that methanol synthesis and methanol-to-aromatics dual-stage catalysts are used in synthesis gas to aromatics, such as Chinese patents CN 200710061506.3, CN200810079957.4, CN 200980149207.2, etc. These research reports can obtain certain aromatics selectivity, but the two-stage reactor process Complexity, high cost, and insufficient competitiveness; and from the reported results, the selectivity of heavy aromatics accounts for more than 50% of the proportion of aromatics, and heavy aromatics need subsequent treatment to obtain basic chemical raw materials of benzene, toluene, and xylene

Method used

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  • Catalyst for one-step conversion of synthesis gas to aromatics and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Weigh 1.34g KNO 3 , add 60ml of deionized water and stir for 5h to form a solution, then weigh 5.0g of hierarchical zeolite molecular sieve H-ZSM-11 and add it to the above solution, and stir at room temperature for 6h. After suction filtration and washing, the resulting filter cake was moved to a vacuum drying oven and dried at 70° C. for 24 hours. The dried solid powder was mixed with 6.25g BaZrO 3 The perovskite was mixed, and after being ground, the sample was moved to a muffle furnace, and the temperature was raised to 500°C at a rate of 2°C / min for 10 hours of roasting. The calcined samples were placed in a tube furnace, fed with hydrogen gas at a rate of 2 °C / min to 400 °C for reduction, and the reduction time was 10 h. The reduced solid sample was pressed into tablets to obtain the catalyst.

[0034] The catalytic reaction is carried out in a fixed-bed high-pressure microreactor, and the H in the syngas 2 The volume ratio to CO is 2, the reaction pressure is...

Embodiment 2

[0036] Weigh 2.29g Mg(NO 3 ) 2, add 50ml of deionized water and stir for 5h to form a solution, then weigh 5.0g of hierarchical zeolite molecular sieve H-ZSM-5 and add to the above solution, and stir at room temperature for 6h. After suction filtration and washing, the resulting filter cake was moved to a vacuum drying oven and dried at 70° C. for 24 hours. The dried solid powder was mixed with 5.0g BaZrO 3 The perovskite was mixed, and after being ground, the sample was moved to a muffle furnace, and the temperature was raised to 500°C at a rate of 2°C / min for 10 hours of roasting. The calcined samples were placed in a tube furnace, fed with hydrogen gas at a rate of 2 °C / min to 450 °C for reduction, and the reduction time was 10 h. The reduced solid sample was pressed into tablets to obtain the catalyst.

[0037] The catalytic reaction was carried out in a fixed-bed high-pressure microreactor. The reaction conditions and product analysis were the same as in Example 1. Th...

Embodiment 3

[0039] Weigh 0.51g Mn(CH 3 COO) 2 , add 50ml of absolute ethanol and stir for 5h to form a solution, then weigh 5.0g of hierarchical zeolite molecular sieve H-X and add it to the above solution, and stir at room temperature for 6h. After suction filtration and washing, the resulting filter cake was moved to a vacuum drying oven and dried at 70° C. for 24 hours. The dried solid powder was mixed with 5.0g CaZrO 3 The perovskite was mixed, and after being ground, the sample was moved to a muffle furnace, and the temperature was raised to 500°C at a rate of 2°C / min for 10 hours of roasting. The calcined samples were placed in a tube furnace, fed with hydrogen gas at a rate of 2 °C / min to 450 °C for reduction, and the reduction time was 10 h. The reduced solid sample was pressed into tablets to obtain the catalyst.

[0040] The catalytic reaction was carried out in a fixed-bed high-pressure microreactor. The reaction conditions and product analysis were the same as in Example 1...

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Abstract

A catalyst for one-step conversion of synthesis gas to aromatic hydrocarbons and a preparation method thereof, involving a catalyst. The catalyst is composed of zirconium-containing perovskite, multi-stage pore zeolite molecular sieve and oxide additives. Calculated in mass percentage, the content of zirconium-containing perovskite is 30% to 70%, and the content of multi-stage pore zeolite molecular sieve is 30%. % ~ 60%, and the content of oxide additives is 0.1% ~ 10%. Preparation method: 1) According to the components of the catalyst, weigh the salt compound of at least one element of IA, IIA, VB, VIB, VIIB, IIB, IVA group elements and rare earth elements, and add it to water or alcohol to prepare the mixture. Form solution A; weigh the multi-stage pore zeolite molecular sieve and add it to solution A, filter and wash with suction, and dry the filter cake to obtain a solid powder, which is then mixed with zirconium-containing perovskite, ground, roasted, and passed into hydrogen or hydrogen and inert gas. The mixed gas is heated and reduced, and the reduced solid sample is pressed into tablets to obtain.

Description

technical field [0001] The invention relates to a catalyst, in particular to a catalyst for one-step conversion of synthesis gas to aromatics and a preparation method thereof. Background technique [0002] Syngas conversion is CO hydrogenation reaction, which can produce fuel products such as gasoline, naphtha, diesel, and aviation fuel, as well as important chemical raw materials such as low-carbon olefins and aromatics. At present, the industrial production of fuel oil based on coal or natural gas has been realized at home and abroad. For example, South African Sasol Company, Anglo-Dutch Shell Company, Synfuels, and Yankuang Group all have coal-to-oil technology based on coal or natural gas. However, the technology for producing aromatics from syngas has not yet been industrialized. The main technical difficulties lie in the low selectivity of aromatics and poor catalyst stability. [0003] The research focus of one-step conversion of synthesis gas to aromatics mainly foc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40B01J29/08B01J29/70B01J29/85B01J35/10C07C1/04C07C15/04C07C15/06C07C15/08
CPCC07C1/04C07C1/043C07C1/0445B01J29/087B01J29/405B01J29/7049B01J29/7057B01J29/7088B01J29/85B01J35/60C07C15/04C07C15/06C07C15/08Y02P20/52
Inventor 王野康金灿成康张庆红周伟
Owner XIAMEN UNIV