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Catalyst for reforming methane and carbon dioxide to prepare synthetic gas as well as preparation method and application thereof

A carbon dioxide and synthesis gas technology, which is applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, hydrogen/syngas production, etc. and other problems, to achieve the effect of good catalytic activity and stability, good catalytic performance, and large specific surface area

Inactive Publication Date: 2016-08-17
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The present invention aims to provide a catalyst for methane carbon dioxide reforming to produce synthesis gas. Aiming at the problems existing in the existing methane carbon dioxide reforming catalysts: complex preparation of the carrier, high cost, easy carbon deposition and poor stability of the catalyst, lignite and Moso bamboo is carbonized, mixed and bonded, carbonized, and activated to make activated carbon, and then under certain conditions, it is activated with 1%-15% nitric acid and 5-15 wt% ammonia water to make a catalyst carrier. Nickel, cobalt, iron, potassium, cerium, copper, and zinc are loaded on the carrier. The catalyst is low in cost, and the active components are evenly distributed on the carrier. It is resistant to carbon deposition, high in activity, and long in life.

Method used

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  • Catalyst for reforming methane and carbon dioxide to prepare synthetic gas as well as preparation method and application thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0035] Lignite and moso bamboo were carbonized at 600°C in the absence of air, and the carbonization time was 5 hours. The obtained lignite material B and moso bamboo charcoal material C are crushed respectively to obtain carbon materials with particle diameters ranging from 100 mesh to 300 mesh. Take 100g of lignite material and 10g of moso bamboo charcoal material, that is, mix the two at a ratio of 1:0.1 to obtain D, and add binder asphalt. The amount of asphalt is 35% of the total mass of B and C. Carbonize again to obtain composite carbon material E, then crush the obtained mixed carbon material E, and sieve composite carbon material F with a particle size of 0.1mm-3mm. Then, water vapor was introduced for activation, the activation temperature was 800°C, and the activation time was 30 minutes, and then dilute ammonia water was used for activation, the concentration of ammonia water was 10 wt %, the activation temperature was 600°C, and the activation time was 100 minutes...

Embodiment 2

[0038] Lignite and moso bamboo were carbonized at 600°C in the absence of air, and the carbonization time was 5 hours. The obtained brown coal material B and moso bamboo charcoal material C are crushed respectively to obtain carbon materials with a particle size of 100 mesh to 300 mesh. Take lignite material 100g, moso bamboo charcoal material 100g, mix the two at a ratio of 1:1 to obtain D, and add binder asphalt, the amount of asphalt is 35% of the total mass of B and C, at 900 ° C Carbonize again to obtain composite carbon material E, then crush the obtained mixed carbon material E, and sieve composite carbon material F with a particle size of 0.1mm-3mm. Then pass through carbon dioxide to activate, the activation temperature is 800°C, the activation time is 30min, and then activated with dilute ammonia water, the concentration of ammonia water is 10 wt%, the activation temperature is 700°C, and the activation time is 100min. A composite activated carbon G consisting of li...

Embodiment 3

[0041] Lignite and moso bamboo were carbonized at 600°C in the absence of air, and the carbonization time was 5 hours. The obtained lignite material B and moso bamboo charcoal material C are crushed respectively to obtain carbon materials with particle diameters ranging from 100 mesh to 300 mesh. Take lignite material 100g, moso bamboo charcoal material 200g, mix the two according to the ratio of 1:2 to obtain D, and add binder asphalt, the amount of asphalt is 35% of the total mass of B and C, at 850 ° C Carbonize again to obtain composite carbon material E, then crush the obtained mixed carbon material E, and sieve composite carbon material F with a particle size of 0.1mm-3mm. Then pass through water vapor to activate, the activation temperature is 800°C, the activation time is 30min, and then activated with dilute ammonia water, the concentration of ammonia water is 10 wt%, the activation temperature is 700°C, and the activation time is 100min. A composite activated carbon...

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Abstract

The invention discloses a catalyst for reforming methane and carbon dioxide to prepare synthetic gas as well as a preparation method and application thereof and belongs to the technical field of preparation of catalysts. The catalyst takes compound active carbon as a carrier, takes nickel and cobalt as active components, and takes iron, potassium, cerium, copper or zinc as a cocatalyst component. The preparation method comprises the following steps: firstly, carbonizing, activating and modifying raw materials including brown coal and mao bamboos to prepare a compound carbon material; then, modifying and roasting the prepared compound active compound under the condition of 0.2MPa-10MPa by adopting an HNO3 solution to obtain a catalyst carrier; loading nickel, cobalt, iron, potassium, cerium, copper and zinc on the carrier with the help of ultrasonic waves through an excessive immersion method; and filtering, drying, roasting and reducing to obtain the catalyst. After modification, loaded active components of the catalyst are uniformly distributed and the activity is relatively high; and the carrier takes the brown coal and the mao bamboos as the raw materials so that the carrier is high in content of active oxygen functional groups, large in specific surface area and low in cost.

Description

technical field [0001] The invention relates to a catalyst for producing synthesis gas by reforming methane and carbon dioxide, a preparation method and application thereof, and belongs to the technical field of catalyst preparation. Background technique [0002] Methane is widely distributed in nature and is the main component of natural gas. It also exists in large quantities in shale gas and combustible ice, and its reserves are abundant. At the same time, methane is also one of the important greenhouse gases. [0003] Carbon dioxide gas is the main cause of the greenhouse effect, but the carbon dioxide emitted by humans into the atmosphere is increasing year by year. How to deal with these carbon dioxide and alleviate the greenhouse effect has become a common challenge for all mankind. [0004] The reforming reaction of methane and carbon dioxide consumes two greenhouse gases, methane and carbon dioxide, and produces synthesis gas H 2 The / CO ratio is low, suitable for...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/78B01J23/83B01J23/80B01J21/18C01B3/40
CPCY02P20/52B01J23/78B01J21/18B01J23/80B01J23/83C01B3/40C01B2203/1058C01B2203/1076C01B2203/1082C01B2203/1241
Inventor 张国杰孙映晖贾永徐英苏爱廷郝兰霞屈江文叶峻岭张永发张少华
Owner TAIYUAN UNIV OF TECH
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