Method for preparing methanation catalyst with low temperature, high activity and high thermal conductivity

A methanation catalyst, a high-activity technology, applied in catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of small catalyst specific surface area, difficult control of active components, uneven mixing of raw materials, etc. Achieve the effect of avoiding heat accumulation, reducing equipment investment and operating costs, and high heat transfer efficiency

Active Publication Date: 2022-06-28
WUHUAN ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This extrusion process will lead to uneven mixing of raw materials, resulting in uneven heat conduction and difficult control of active components; there are also literatures disclosing the use of silicon carbide for direct loading, but the specific surface area of ​​the catalyst is small and the low-temperature activity is not good. Problem, the catalyst is only suitable for high temperature methanation process, and it is an adiabatic reactor

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Disperse 67.68g of nano-powder material silicon carbide (size>500 mesh) in a sodium nitrate solution at high speed (the mass concentration of the sodium nitrate solution is 5%, the control ultrasonic frequency is 40kHz, and the power is 800kW) to form a suspension ( The solid-liquid mass ratio of the suspension is 1:20); then the suspension is heated to 50°C. 155.6 g of nickel nitrate, 6.5 g of yttrium nitrate, 431.8 g of aluminum nitrate, and 82.9 g of magnesium nitrate were configured as a precursor solution, and sodium carbonate was configured as a precipitant solution (the molar ratio of precursor salt and sodium carbonate was 0.1:1), It was preheated to 80°C by electric heating, and then added dropwise to the suspension (the dropping speed was selected to be completed within 50 min, and the stirring speed was 600 rpm) to start the precipitation reaction and continue to stir and age for 3 hours. The precipitate is subjected to multiple cycles of pressure filtration,...

Embodiment 2

[0030]Disperse 6.77g of nano-powder material carbon nanotubes (size>500 mesh) in a sodium nitrate salt solution (the mass concentration of the sodium nitrate salt solution is 0.5%, the control ultrasonic frequency is 80kHz, and the power is 200kW) to form a suspension. liquid (the solid-liquid mass ratio of the suspension is 1:50), and the temperature is raised to 80°C. 155.6 g of nickel nitrate, 6.5 g of yttrium nitrate, 431.8 g of aluminum nitrate, and 82.9 g of magnesium nitrate were configured as a precursor solution, and a precipitant solution (taking the molar ratio of precursor salt to sodium carbonate) was configured with sodium carbonate and sodium bicarbonate solution. is 0.1:10), preheated to 50 ° C by electric heating, and then added dropwise to the suspension in parallel to start the precipitation reaction (the dropping speed is selected as the dropwise addition within 80 min, and the stirring speed is 100 rpm), and the stirring is continued. Aging for 8h. The pr...

Embodiment 3

[0032] The catalyst powder was prepared similarly to Example 1. Among them, silicon carbide (size>500 mesh) 113.25g, the solid-liquid mass ratio of the suspension is 1:50, the mass concentration of the sodium nitrate solution used is 1%, the control ultrasonic frequency is 60kHz, and the power is 400kW. Heating mode Preheat to 70°C. Potassium carbonate and potassium bicarbonate solution are prepared as precipitant solution, the molar ratio of precursor salt and precipitant is 0.1:3, the temperature of precursor salt solution and precipitant are respectively heated to 70 ℃, and then added dropwise to the suspension liquid During the process, the precipitation reaction was started, the completion time of the dropwise addition was 80 minutes, and the stirring was continued for 5 hours, and the stirring speed was 600 rpm. In the catalyst powder obtained by roasting, add silicone resin, succulent powder (5% of the mass of the catalyst powder), cement, and polyvinyl alcohol (4% of ...

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Abstract

The invention discloses a method for preparing a methanation catalyst with low temperature, high activity and high thermal conductivity, which comprises the following steps: high-speed stirring and ultrasonic dispersion of nano heat-conducting materials in a salt solution to form a suspension, and raising the temperature to 50-80°C for heat preservation and standby Disperse the precursor salt in deionized water to form a precursor salt solution, raise the temperature of the precursor salt solution and the precipitant solution to 50-80°C respectively, and add them dropwise to the suspension for precipitation reaction and continue Stirring; after the dropwise addition, aging is carried out, and the precipitate obtained after aging is press-filtered, beaten, washed, dried, and roasted to obtain catalyst powder; adding lubricant and forming aids to the catalyst powder, ball milling and sieving, and then passing through The molded catalyst is obtained after granulation, sieving, tableting, curing and roasting. The process is simple, easy to operate, low in production cost, and the prepared catalyst has good thermal conductivity, high heat transfer efficiency, good low-temperature reactivity and good high-temperature thermal stability.

Description

technical field [0001] The invention relates to a method for preparing a catalyst, in particular to a method for preparing a methanation catalyst with low temperature, high activity and high thermal conductivity. Background technique [0002] In the process of coal-to-natural gas production, the domestic commercial operation of Datang Keqi, Xinjiang Qinghua, and Inner Mongolia Huineng all adopt imported technologies. The key technology is methanation catalyst. Because the methanation reaction is characterized by strong exothermicity, the reaction generates water. , the high concentration of carbon monoxide increases the adiabatic temperature in the reactor, which requires the catalyst to have strong anti-sintering performance and hydrothermal resistance. In addition, the adiabatic temperature rise caused by the reaction of high concentration carbon monoxide in the adiabatic reactor is large. If no effective measures are taken, the equipment will be overheated and the catalys...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/83B01J27/224B01J35/00B01J37/03C07C1/04C10L3/08C07C9/04
CPCB01J27/224B01J23/83B01J35/006B01J35/0066B01J37/031C10L3/08C07C1/0435C07C1/0445C07C9/04
Inventor 张大洲卢文新刘佳胡媛吕庆元夏吴
Owner WUHUAN ENG
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