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Supported catalyst for coal gasification and preparation method thereof

A supported catalyst and catalyst technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, granular/powdered fuel gasification, etc., can solve the problems of catalyst activity reduction, alkali metal loss, deposition, adhesion, etc., to achieve Increase the chance of interaction, enhance catalytic activity, and enhance the effect of dispersion

Inactive Publication Date: 2013-09-18
河北中科能源有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, all kinds of catalysts have certain disadvantages in application: alkaline earth metal catalysts require a relatively high gasification temperature; Fe and Ni commonly used in transition metal catalysts are easily poisoned and deactivated by sulfur; alkali metals are used in catalytic gasification applications. also have losses
When coal is used as the raw material for gasification, the amount of tar generated during the low-temperature gasification process is relatively large, which makes it possible for tar to deposit and adhere to the surface of the catalyst, resulting in reduced or deactivated catalyst activity; due to the gasification agent H 2 the presence of O, K 2 CO 3 Agglomeration will occur during the reaction process, so when the single-component catalyst is used for catalytic gasification, the contact between the catalyst and coal is greatly affected by the addition method, and the active components of the catalyst are easily lost due to volatilization into the gas phase during the reaction process, and K 2 CO 3 It will react with the acidic clay mineral components in coal to form insoluble salts, which increases the difficulty of catalyst reuse and the amount of ash to be processed.

Method used

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  • Supported catalyst for coal gasification and preparation method thereof
  • Supported catalyst for coal gasification and preparation method thereof
  • Supported catalyst for coal gasification and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Preparation of embodiment 1 supported catalyst

[0035] 3.12g La(NO3 ) 3 , 1.48g Mn(NO 3 ) 2 , 0.35g Cu(NO 3 ) 2 Dissolve in 100ml of water respectively, and mix well after dissolving; then add citric acid with a ratio of 1:1 to the total number of metal ions in the solution, and continue to stir until fully dissolved; put the solution in a rotary evaporator at 45°C to evaporate and dehydrate until Form a gel-like substance; put the gel-like substance in a vacuum drying oven at 100°C and dry for 8 hours to form a porous solid; then bake and activate it in a muffle furnace at 750°C for 5 hours to obtain a composite oxide LaMn 0.8 Cu 0.2 o 3 ; Use the solution impregnation method to load the oxide on γ-Al 2 o 3 On the support, the oxide mass concentration is 20%, γ-Al 2 o 3 The mass concentration of the carrier is 75%, and it is dried and pretreated at 100°C, and roasted at 750°C; then, using the equal-volume impregnation method, K 2 CO 3 impregnated in γ-Al l...

Embodiment 2

[0036] Preparation of embodiment 2 supported catalyst

[0037] 3.12g La(NO 3 ) 3 , 0.93g Mn(NO 3 ) 2 , 0.87g Cu(NO 3 ) 2 Dissolve in 100ml of water respectively, and mix well after dissolving; then add citric acid with a ratio of 1:1 to the total number of metal ions in the solution, and continue to stir until fully dissolved; put the solution in a rotary evaporator at 45°C to evaporate and dehydrate until Form a gel-like substance; put the gel-like substance in a vacuum drying oven at 100°C and dry for 8 hours to form a porous solid; then bake and activate it in a muffle furnace at 700°C for 5 hours to obtain a composite oxide LaMn 0.6 Cu 0.4 o 3 ; Use the solution impregnation method to load the oxide on γ-Al 2 o 3 On the carrier, the oxide mass concentration is 30%, γ-Al 2 o 3 The mass concentration of the carrier is 60%, and it is dried and pretreated at 100°C, and roasted at 700°C; then, using the equal volume impregnation method, K 2 CO 3 impregnated in γ-Al...

Embodiment 3

[0038] Preparation of embodiment 3 supported catalyst

[0039] 3.12g La(NO 3 ) 3 , 1.85g Mn(NO 3 ) 2 Dissolve in 100ml of water respectively, and mix well after dissolving; then add citric acid with a total molar number of metal ions in the solution of 0.8:1, and continue to stir until fully dissolved; put the solution in a rotary evaporator to evaporate and dehydrate at 40°C until Form a gel-like substance; put the gel-like substance in a vacuum drying oven at 80°C and dry for 8 hours to form a porous solid; then bake and activate it in a muffle furnace at 500°C for 5 hours to obtain a composite oxide LaMnO 3 ; Use the solution impregnation method to load the oxide on γ-Al 2 o 3 On the carrier, the oxide mass concentration is 30%, γ-Al 2 o 3 The mass concentration of the carrier is 60%, and it is dried and pretreated at 80°C, and roasted at 500°C; then, using the equal-volume impregnation method, K 2 CO 3 impregnated in γ-Al loaded with composite oxide 2 o 3 and dr...

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PUM

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Abstract

The invention discloses a supported catalyst for coal gasification. The catalyst comprises a catalyst active component, a catalyst promoter and a carrier, wherein the catalyst active component refers to alkali metal carbonate, and accounts for 5-20% of the total weight of the catalyst; the catalyst promoter refers to a composite oxide, and accounts for 20-40% of the total weight of the catalyst, and the structure of the catalyst promoter is AxA'1- xByB'1-yO3; the carrier refers to silica or gamma-Al2O3, and accounts for 40-75% of the total weight of the catalyst. According to the invention, in a mode of adding the catalyst promoter, the catalytic activity of the active component for coal gasification is promoted, and the volatilization loss of the active component is suppressed, and meanwhile, the catalyst promoter is supported on the carrier with a higher specific surface and an enough strength, so that the original structure and catalytic activity of the catalyst after being reacted are still kept, and then the catalyst can be recycled so as to achieve the purpose of reutilization.

Description

technical field [0001] The invention relates to the field of catalysts, in particular to a supported catalyst for coal gasification and a preparation method thereof. Background technique [0002] As a clean energy, hydrogen energy is expected to become the main energy carrier in the future sustainable energy system, and large-scale and efficient hydrogen production depends on coal gasification technology. Therefore, gasification technology is the basis for clean, efficient and comprehensive utilization of coal and key technologies. Although the coal gasification technologies that have been industrialized at present have their own advantages, their shortcomings and shortcomings are also quite obvious, such as the ubiquitous high reaction temperature, difficulty in purifying the generated gas, high energy consumption, high requirements for equipment, and environmental pollution. serious adverse factors. This directly promotes the research of coal gasification technology unde...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/232C10J3/54
CPCY02P20/52Y02P20/584
Inventor 郝丽芳宋文立李俊峰林伟刚李松庚杨崇广
Owner 河北中科能源有限公司
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