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High temperature-resistant methanation catalyst preparation method

A methanation catalyst and catalyst technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of poor thermal stability and carbon deposition resistance of catalysts, Hexaaluminate carrier has low specific surface area and high catalyst reduction temperature to achieve the effect of high density, high mechanical strength and lower reduction temperature

Active Publication Date: 2015-12-09
HUANENG CLEAN ENERGY RES INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The methanation catalysts prepared in Chinese patents CN102029162 and CN102259004A all adopt the homogeneous precipitation method, and the components of the prepared methanation catalyst are uniformly dispersed, and the activity of the catalyst is good at high temperature, but the NiO and Al in the catalyst 2 o 3 The combination is tight, the catalyst reduction temperature is high, and the thermal stability and carbon deposition resistance of the catalyst are poor, so it does not use industrial production
The methanation catalyst prepared by Chinese patent CN102836718A is a methanation catalyst prepared by first preparing a high-temperature resistant and sintering-resistant hexaaluminate carrier, and then impregnating the active component NiO. Since the active component NiO is loaded on the hexaaluminate carrier In general, the prepared methanation catalyst has good thermal stability, but the specific surface area of ​​the hexaaluminate carrier is low, and the preparation process is complicated, which is not conducive to industrial production

Method used

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Experimental program
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Effect test

Embodiment 1

[0017] A preparation method of a high-temperature-resistant methanation catalyst, comprising the following steps:

[0018] Step A, catalyst semi-finished product:

[0019] 171.32g of Ni(NO 3 ) 2 ·6H 2 O, 17.58g of Ca(NO 3 ) 2 4H 2 O, 12.76g of La(NO 3 ) 3 ·6H 2 O and 89.74g of Mg(NO 3 ) 2 ·6H 2 O was dissolved in 500ml of deionized water to make mixed metal salt solution I, and then 129.83g of Na 2 CO 3 Dissolve in 500ml of deionized water to make alkaline solution II, maintain the constant temperature of alkaline solution II at 80°C, gradually add the mixed salt solution I into the alkaline solution II, and keep stirring for complete precipitation reaction, with pH = 8 as the titration end point After the precipitation, add 7ml of silica sol, stir well and age at 90°C for 2 hours, wash the precipitated precursor with deionized water three times; after suction filtration, dry the filter cake at 90°C for 8h, and roast at 400°C 4h, obtain catalyst semi-finished pro...

Embodiment 2

[0028] A preparation method of a high-temperature-resistant methanation catalyst, comprising the following steps:

[0029] Step A, catalyst semi-finished product:

[0030] 155.74g of Ni(NO 3 ) 2 ·6H 2 O, 29.30g of Ca(NO 3 ) 2 4H 2 O, 11.16g of La(NO 3 ) 3 ·6H 2 O and 76.92g of Mg(NO 3 ) 2 ·6H 2 O was dissolved in 500ml of deionized water to make mixed metal salt solution I, and then 124.54g of Na 2 CO 3 Dissolve in 500ml of deionized water to make alkaline solution II, keep the alkaline solution II at a constant temperature of 70°C, gradually add the mixed salt solution I into the alkaline solution II, and keep stirring for complete precipitation reaction, with pH = 8 as the titration end point After the precipitation, add 10ml of silica sol, stir well and age at 80°C for 2 hours, wash the precipitated precursor with deionized water three times; dry the filter cake at 100°C for 12h after suction filtration, and roast at 450°C 6h, obtain catalyst semi-finished pro...

Embodiment 3

[0039] A preparation method of a high-temperature-resistant methanation catalyst, comprising the following steps:

[0040] Step A, catalyst semi-finished product:

[0041] 147.96g of Ni(NO 3 ) 2 ·6H 2 O, 38.09g of Ca(NO 3 ) 2 4H 2 O, 9.57g of La(NO 3 ) 3 ·6H 2 O and 70.50g of Mg(NO 3 ) 2 ·6H 2 O was dissolved in 500ml of deionized water to make mixed metal salt solution I, and then 124.58g of Na 2 CO 3 Dissolve in 500ml of deionized water to make alkaline solution II, maintain the constant temperature of alkaline solution II at 80°C, gradually add the mixed salt solution I into the alkaline solution II, and keep stirring for complete precipitation reaction, with pH = 8 as the titration end point After the precipitation, add 14ml of silica sol, stir well and age at 90°C for 2 hours, wash the precipitated precursor with deionized water three times; dry the filter cake at 90°C for 12h after suction filtration, and roast at 500°C 4h, obtain catalyst semi-finished pro...

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PUM

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Abstract

The invention discloses a high temperature-resistant methanation catalyst preparation method. The preparation method comprises preparing a catalyst semi-finished product with composite functions from nickel as an active component, a rare earth metal as a cocatalyst, and alkaline earth metal and alkali metal as anti-carbon formation components by a precipitation method, adding kaliophilite, graphite and pure calcium aluminate cement into the catalyst semi-finished product, carrying out mixing to obtain a uniform mixture, carrying out granulation and tabletting molding, and carrying out steam curing to obtain the catalyst finished product. The high temperature-resistant methanation catalyst retains good methanation activity in a use temperature range of 300-700 DEG C and has good thermostability and anti-carbon formation performances.

Description

technical field [0001] The invention belongs to the technical field of coal-to-synthesis gas to natural gas, in particular to a preparation method of a high-temperature-resistant methanation catalyst. Background technique [0002] Natural gas is an efficient, safe and clean fossil energy. Methanation reaction is the core technology of coal-to-natural gas, and methanation reaction is a strong exothermic reaction. In the usual gas components, every 1% of CO methane can produce an adiabatic temperature rise of 74°C for every 1 percentage point of CO 2 Methanation can produce an adiabatic temperature rise of 60°C. The large amount of heat released by the methanation reaction will cause the reactor bed to overheat instantaneously, causing the catalyst to be sintered at high temperature and deactivated. The occurrence of carbon deposition reaction leads to the reduction of catalyst activity; therefore, high temperature sintering and carbon deposition of the catalyst are the key t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C07C1/04C07C9/04
Inventor 王晓龙何忠郜时旺肖天存冯向程
Owner HUANENG CLEAN ENERGY RES INST
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