Low-temperature methanation catalyst and preparation method thereof

A low-temperature methanation and catalyst technology, applied in the field of low-temperature methanation catalyst and its preparation, can solve the problems of immature low-temperature methanation technology, high cost of mesoporous molecular sieve, high cost of polymer carrier, etc., to achieve improved catalytic activity and difficult operation Small, Inexpensive Effects

Pending Publication Date: 2020-09-22
BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, domestic low-temperature methanation technology is not mature enough, so it is necessary to develop a low-temperature methanation catalyst
Chinese patent application CN108479844A discloses a nickel-based catalyst for CO low-temperature selective methanation and its preparation method and application. The catalyst uses metal Ni as the active component and Zr-doped mesoporous molecular sieve Zr#SBA#16 as the carrier Supported catalyst, although the invented nickel-based catalyst can deeply remove CO in hydrogen-rich reformed gas to below 10ppm at a relatively low temperature (180-230°C), and at the same time, the selectivity of CO methanation reaction is higher than 50% , but the cost of mesoporous molecular sieves is high, the stability is insufficient, and the catalyst activity is slightly low
Chinese patent application CN107376925B provides a low-temperature high-activity carbon dioxide methanation catalyst and its preparation method, using CO(NH 2 ) 2 instead of NaOH and Na 2 CO, through slow hydrolysis at 90-120°C, provides OH needed for precipitation - and CO 2- Generate a uniform [Ni 1-x 2+ Al x 3+ (OH) 2 ] x+ (CO 3 ) x/2 2- Precipitation, the cataly

Method used

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preparation example Construction

[0032]Specifically, the preparation method of the low-temperature methanation catalyst may comprise the following steps:

[0033] Step 1: Preparation of the precipitation solution: dissolving the soluble Ni salt, the soluble Al salt and the soluble salt of the cocatalyst metal element in deionized water, and adding N-vinylamide nonionic polymer to prepare the concentration of Ni element as 0.5~2mol / L of the solution to be precipitated. Wherein, the promoter metal element is one or two of La, Mg, Cu, Mn; the N-vinylamide nonionic polymer is polyvinylpyrrolidone (polyvinyl pyrrolidone, PVP for short), and the poly The amount of vinylpyrrolidone accounts for 0.01%-0.8% of the total mass of the low-temperature methanation catalyst, preferably 0.6% of the total mass of the low-temperature methanation catalyst.

[0034] Step 2: Preparation of precipitant: dissolving soluble Na salt in deionized water to prepare a precipitant with a concentration of Na element of 1-3 mol / L. The vol...

Embodiment 1

[0045] A kind of low-temperature methanation catalyst, its preparation method can comprise the following steps:

[0046] Step A1: Preparation of the precipitation solution: 86.70g of Ni(NO 3 ) 2 ·6H 2 O, 3.449g of Al(NO 3 ) 3 9H 2 O, 0.48g of La(NO 3 ) 3 ·6H 2 The polyvinylpyrrolidone of 0,0.12g is dissolved in deionized water, is mixed with the liquid to be precipitated containing Ni element.

[0047] Step A2: Preparation of precipitating agent: several milliliters of Na 2 CO 3 Dissolve in deionized water to prepare a precipitant with a Na element concentration of 2mol / L. The volumetric dosage of the precipitant is twice that of the solution to be precipitated.

[0048] Step A3: Mix 6.562g of diatomaceous earth with 50mL of deionized water and place it in a water bath at 80°C, then add the solution to be precipitated and the precipitating agent for mixed precipitation, and maintain the pH value during the mixed precipitation process =9, thus obtaining the precipit...

Embodiment 2

[0050] A kind of low-temperature methanation catalyst, its preparation method can comprise the following steps:

[0051] Step B1: Preparation of the precipitation solution: 86.70g of Ni(NO 3 ) 2 ·6H 2 O, 9.198g of Al(NO 3 ) 3 9H 2 O, 0.48g of La(NO 3 ) 3 ·6H 2 The polyvinylpyrrolidone of 0,0.12g is dissolved in deionized water, is mixed with the liquid to be precipitated containing Ni element.

[0052] Step B2: Preparation of precipitating agent: several milliliters of Na 2 CO 3 Dissolve in deionized water to prepare a precipitant with a Na element concentration of 2mol / L. The volumetric dosage of the precipitant is twice that of the solution to be precipitated.

[0053] Step B3: Mix 5g of diatomaceous earth with 50mL of deionized water and place it in a water bath at 80°C, then add the liquid to be precipitated and the precipitating agent for mixed precipitation, and maintain the pH value during the mixed precipitation = 9, so as to obtain a precipitation solution...

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PUM

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Abstract

The invention discloses a low-temperature methanation catalyst and a preparation method thereof. The low-temperature methanation catalyst comprises an active component, a surfactant, a structural auxiliary agent and a cocatalyst, wherein the active component is Ni; the structure auxiliary agent is a composite structure auxiliary agent composed of Al2O3 and diatomite; the cocatalyst is one or two of La2O3, MgO, CuO and MnO; the content of the active component accounts for 50%-75% of the total mass of the low-temperature methanation catalyst, and the content of the cocatalyst accounts for 0.4%-0.8% of the total mass of the low-temperature methanation catalyst. The method is lower in reaction temperature, lower in energy consumption and simple to operate, has high catalytic activity and longservice life in a low-temperature environment, and can realize efficient catalytic conversion of CO and CO2.

Description

technical field [0001] The invention relates to the field of methanation catalysts, in particular to a low-temperature methanation catalyst and a preparation method thereof. Background technique [0002] Crude hydrogen gas in ethylene industrial plants and ammonia plants inevitably contains CO and CO 2 Components whose presence can be toxic to downstream devices must be cleaned. At present, the most economical and efficient method of purifying hydrogen is methanation, that is, through CO, CO 2 React with a small amount of hydrogen to form inert CH 4 to remove CO and CO from the gas 2 . [0003] CO and CO are inevitably contained in the hydrogen-rich gas separated from the hydrogen / methane separation tank in the hydrogen / methane separation tank of the ethylene production plant by cracking naphtha and light hydrocarbons 2 , and this part H 2 It is the raw material for the downstream hydrogenation process, and if the CO is not removed, it will cause catalyst poisoning and...

Claims

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Application Information

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IPC IPC(8): B01J23/83B01J23/889B01J31/28B01J31/32B01J37/03B01J37/08C07C1/04C07C1/12C07C9/04
CPCB01J23/83B01J23/8892B01J23/002B01J31/28B01J31/32B01J37/031B01J37/088C07C1/044C07C1/12C07C9/04B01J2523/00C07C2523/83C07C2523/889C07C2531/28C07C2531/32B01J2523/31B01J2523/3706B01J2523/847B01J2523/72
Inventor 张谦温孙锦昌刘先知
Owner BEIJING INSTITUTE OF PETROCHEMICAL TECHNOLOGY
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