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A kind of regeneration method of deactivated methanation catalyst

A methanation catalyst and catalyst technology, which are applied in the field of methanation reaction, can solve the problems of reduced methanation activity, low recovery rate of precious metals, fast deactivation speed of methane catalyst, etc. Efficient utilization, good activity and thermal stability of

Active Publication Date: 2021-03-23
CHINA HUANENG GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The methanation reaction is a strong exothermic reaction. The large amount of heat released by the high-concentration CO methanation reaction will cause the bed to overheat instantaneously, causing the catalyst to be sintered at high temperature and deactivated. In addition, the carbon deposition reaction is also accompanied by the methanation reaction. , under low temperature conditions, a large amount of filamentous carbon is generated in the micropores of the catalyst, and when sufficient pressure is generated, the catalyst particles are broken, causing the catalyst skeleton to be pulverized and deactivated; under high temperature conditions, controlled by thermodynamics, the methanation reaction is balanced The constant will gradually decrease as the temperature increases, and high-density plate-like carbon is formed at an alarming rate, covering the active neutrality of the catalyst surface and reducing the methanation activity
[0003] At present, in the industry, for the deactivated methanation catalyst after use, the metal nickel in it is generally recovered by high-temperature fire method, and the residue is discarded or paved. In fact, a large amount of nickel oxide still remains in the residue, which makes the recovery rate of precious metals low and wastes resources. , and easily cause environmental pollution
[0004] Chinese patent CN103265394 uses two methanation reactors connected in parallel to realize methanation reaction and catalyst carbon removal and regeneration reaction alternately, but the temperature of the carbon removal reaction is generally above 700°C, and the reaction process needs to consume a lot of heat to maintain the reactor bed temperature, and the catalyst cannot be fully activated; in the Chinese patent CN102451774, the regeneration of the nickel-based catalyst is realized by acid washing after alkali washing, but the surface of the catalyst after pickling is more prone to carbon deposition, resulting in the loss of methane catalyst after regeneration. The activity speed is faster, and the solution after alkali washing and pickling will form secondary pollution

Method used

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  • A kind of regeneration method of deactivated methanation catalyst

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Effect test

Embodiment 1

[0024] 1) Sieve the deactivated methanation catalyst to obtain a deactivated methanation catalyst with a regular mechanical structure, place it in an air atmosphere at 450°C for 8 hours to fully burn charcoal, weigh 200g of the methanation catalyst and impregnate it in 5 times The volume of nitric acid solution was dipped at 80°C for 12 hours, the mass percent concentration of the nitric acid solution was 0.8%, and after drying, it was soaked in 8 times the volume of sodium bicarbonate solution at 80°C for 4 hours, the mass of sodium bicarbonate solution The percentage concentration is 15%. After drying, dry at 80°C for 12 hours in an air atmosphere, and roast at 550°C for 4 hours to prepare an activated catalyst carrier. After the acid catalyst is solid in the pickling solution, a pickling metal salt solution is obtained, and the alkali washing solution is alkali After washing the catalyst solid, alkali washing metal salt solution is obtained;

[0025] 2) Filter the above-men...

Embodiment 2

[0027] 1) Sieve the deactivated methanation catalyst to obtain a deactivated methanation catalyst with a regular mechanical structure, place it in an air atmosphere at 500°C for 6 hours to fully burn charcoal, weigh 200g of the methanation catalyst and impregnate it in 5 times Immerse in a volume of oxalic acid solution at 80°C for 12 hours. The mass percent concentration of the oxalic acid solution is 1.0%. The percentage concentration is 15%. After drying, dry at 80°C for 12 hours in an air atmosphere, and roast at 550°C for 6h to prepare an activated catalyst carrier;

[0028] 2) The metal salt solution after the above-mentioned pickling and alkali cleaning is filtered respectively to remove solid impurity particles, and 990g of nickel nitrate and 360g of magnesium nitrate are dissolved in the pickling solution to make a regeneration solution, and the above-mentioned alkali cleaning solution 1.45 L. Adjust the regeneration solution to pH = 7.5, soak the above-mentioned acti...

Embodiment 3

[0030] 1) Sieve the deactivated methanation catalyst to obtain a deactivated methanation catalyst with a regular mechanical structure, place it in an air atmosphere at 500°C for 8 hours to fully burn charcoal, weigh 200g of the methanation catalyst and impregnate it in 5 times Soak in citric acid solution of 10 volumes at 80°C for 24 hours, the concentration of citric acid solution is 1.2%, after drying, soak at 80°C for 4 hours in 10 times the volume of ammonium bicarbonate solution, the concentration of ammonium bicarbonate solution is 12%, dried in the air atmosphere at 80°C for 12 hours, and roasted at 550°C for 4 hours to prepare an activated catalyst carrier. After the acid catalyst solid in the pickling solution, pickling metal salt solution was obtained. Obtain alkali washing metal salt solution;

[0031]2) Filter the above-mentioned pickling metal salt solution and alkali-washing metal salt solution respectively to remove solid impurity particles, and take 930g of nic...

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Abstract

A regeneration process for a deactivated methanation catalyst is disclosed. The process includes subjecting the deactivated methanation catalyst to a series of sieving, charring, acid washing and alkali washing to obtain an activated catalyst carrier; then preparing a regeneration solution by utilizing a solution obtained after acid washing; modifying the regeneration solution with a solution obtained after alkali washing; soaking the activated catalyst carrier in the modified regeneration solution; and performing drying, calcination and cooling to room temperature to obtain a new methanationcatalyst, thus achieving regeneration of the methanation catalyst. The process achieves recovery and utilization of waste solutions, overcomes a problem that heavy metal solutions pollute the environment. The new methanation catalyst prepared by the regeneration process has improved metal nickel utilization rate, high mechanical strength, good thermal stability and good carbon deposition resistance.

Description

technical field [0001] The invention belongs to the technical field of methanation reaction, and relates to a regeneration method of a deactivated methanation catalyst. Background technique [0002] The methanation reaction is a strong exothermic reaction. The large amount of heat released by the high-concentration CO methanation reaction will cause the bed to overheat instantaneously, causing the catalyst to be sintered at high temperature and deactivated. In addition, the carbon deposition reaction is also accompanied by the methanation reaction. , under low temperature conditions, a large amount of filamentous carbon is generated in the micropores of the catalyst, and when sufficient pressure is generated, the catalyst particles are broken, causing the catalyst skeleton to be pulverized and deactivated; under high temperature conditions, controlled by thermodynamics, the methanation reaction is balanced The constant will gradually decrease as the temperature increases, an...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J38/72B01J38/02B01J38/12B01J38/60B01J38/62B01J38/64B01J38/66C07C1/04C07C9/04
CPCB01J38/02B01J38/12B01J38/60B01J38/62B01J38/64B01J38/66B01J38/72C07C1/045C07C9/04Y02P20/584
Inventor 王晓龙何忠郜时旺肖天存
Owner CHINA HUANENG GRP CO LTD