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A kind of method of methane carbon dioxide reforming to produce synthesis gas carbon-based catalyst

A technology of carbon-based catalysts and carbon dioxide, applied in the direction of metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve problems such as sulfur poisoning, carbon deposition deactivation, etc. Achieve good adsorption capacity, good catalytic activity, and overcome the effect of easy carbon deposition and deactivation

Active Publication Date: 2017-06-23
陕西荷螓能源科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The object of the present invention is to aim at the defect in the above-mentioned prior art, provide a kind of method for methane carbon dioxide reforming system synthesis gas carbon-based catalyst, this preparation method operation process is simple, the catalyst that makes has higher catalytic activity, does not need Adding additional active metals can overcome the problems of non-precious metal catalysts that are prone to carbon deposition and deactivation and sulfur poisoning

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] (1) Catalyst preparation:

[0029] Combine 60-80 mesh CLR with KOH, KNO 3 , according to CLR:KOH:KNO 3 = The mass ratio of 1:2:0.05 is mixed and ground evenly; placed in a tube furnace, the whole process is under N 2 Carry out carbonization treatment under atmosphere: raise the temperature to 450°C at a constant temperature of 0.5h at a heating rate of 10°C / min, then raise the temperature to 850°C at a heating rate of 10°C / min and keep for 1.5h, and cool naturally to room temperature after the carbonization treatment is completed; Wash with hot distilled water until neutral, and dry at 110° C. for 12 hours to obtain the carbon-based catalyst for carbon dioxide reforming of methane to synthesis gas of the present invention. After measurement, the BET specific surface area of ​​the catalyst is 1631m 2 / g.

[0030] (2) Performance test of the catalyst:

[0031] The prepared CH 4 / CO 2 Catalyst performance test conditions for reforming to synthesis gas are: the refor...

Embodiment 2

[0033] (1) Catalyst preparation:

[0034] Take 60-80 mesh CLR and KOH, KNO 3 , to CLR:KOH:KNO 3= The mass ratio of 1:3:0.05 is mixed and ground evenly; placed in a tube furnace, the whole process is under N 2 Carry out carbonization treatment under atmosphere: raise the temperature to 450°C at a constant temperature of 0.5h at a heating rate of 10°C / min, then raise the temperature to 850°C at a heating rate of 10°C / min and keep for 1.5h, and cool naturally to room temperature after the carbonization treatment is completed; Wash with hot distilled water until neutral, and dry at 110° C. for 12 hours to obtain the carbon-based catalyst for carbon dioxide reforming of methane to synthesis gas of the present invention. After measurement, the BET specific surface area of ​​the catalyst is 1689m 2 / g.

[0035] (2) Performance test of the catalyst:

[0036] The performance testing method of the catalyst is the same as in Example 1. Under these conditions, the conversion rates o...

Embodiment 3

[0038] (1) Catalyst preparation:

[0039] Combine 60-80 mesh CLR with KOH, KNO 3 , according to CLR:KOH:KNO 3 = The mass ratio of 1:3:0.05 is mixed and ground evenly; placed in a tube furnace, the whole process is under N 2 Carry out carbonization treatment under the atmosphere: heat up to 600°C at a constant temperature of 10°C / min for 0.5 hours, then raise the temperature to 850°C at a rate of 10°C / min and keep it for 1.5h, and cool naturally to room temperature after carbonization; Wash with hot distilled water until neutral, and dry at 110° C. for 12 hours to obtain the carbon-based catalyst for carbon dioxide reforming of methane to synthesis gas of the present invention. After measurement, the BET specific surface area of ​​the catalyst is 1506m 2 / g.

[0040] (2) Performance test of the catalyst:

[0041] The performance testing method of the catalyst is the same as in Example 1. Under these conditions, the conversion rates of methane and carbon dioxide were 91% a...

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Abstract

A method for producing a carbon-based catalyst for synthesis gas by reforming methane and carbon dioxide, comprising the following steps: step 1, taking the coal direct liquefaction residue with a particle size of 60-80 mesh and a composite modifier according to the mass ratio of 1: (1-3) Mix and grind evenly; the composite modifier includes 90% to 98% alkali and 2% to 10% nitrate in terms of mass fraction; step 2, heat up the obtained uniformly ground mixture under an inert atmosphere for carbonization treatment; step 3 1. Cooling the carbonized mixture and washing it to neutrality; step 4, drying the mixture washed to neutrality to obtain a carbon-based catalyst. The present invention uses Shenhua coal direct liquefaction residue CLR as a raw material to obtain a carbon-based catalyst through carbonization treatment, effectively utilizes the main by-products during direct coal liquefaction, has a simple preparation method, and the prepared catalyst has a large specific surface area and is effective for methane carbon dioxide reforming reaction better catalytic activity.

Description

technical field [0001] The invention belongs to the field of catalyst preparation, in particular to a method for preparing carbon-based catalysts for syngas by reforming methane and carbon dioxide. Background technique [0002] Shenhua Ordos Coal-to-Liquid Company has achieved the successful operation of the demonstration project of direct coal liquefaction of one million tons. It is currently the only enterprise in the world that can directly liquefy coal. Since its official commercial operation in 2011, it has always maintained a In 2014, it put coal into operation for 302 days, produced 902,000 tons of oil products, and processed 4.013 million tons of coal. With the industrial application of direct coal liquefaction technology, the by-product liquefaction residue is huge, accounting for about 30% of the coal. At the same time, the liquefaction residue has the characteristics of high sulfur and high ash. important aspects of sex. [0003] The carbon dioxide reforming rea...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J35/10B01J21/18B01J23/04C01B3/02C01B32/50
Inventor 徐龙刘鹏孙鸣马晓迅
Owner 陕西荷螓能源科技有限公司
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