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Magnesium-titanium perovskite type nickel-based catalyst for hydrogen production by autothermal reforming of acetic acid

An autothermal reforming and catalyst technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, hydrogen, etc., can solve the problems of poor stability, low activity, catalyst deactivation, etc. The effect of stable activity, inhibition of acetone, and efficient conversion

Active Publication Date: 2022-04-05
CHENGDU UNIVERSITY OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The technical problem to be solved by the present invention is to aim at the low activity, poor stability and sintering resistance of existing catalysts in the autothermal reforming reaction of acetic acid, which lead to catalyst deactivation To solve the problem, provide a new catalyst with anti-coking, anti-oxidation and anti-sintering

Method used

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  • Magnesium-titanium perovskite type nickel-based catalyst for hydrogen production by autothermal reforming of acetic acid
  • Magnesium-titanium perovskite type nickel-based catalyst for hydrogen production by autothermal reforming of acetic acid
  • Magnesium-titanium perovskite type nickel-based catalyst for hydrogen production by autothermal reforming of acetic acid

Examples

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Effect test

example 1

[0034] Weigh 2.355g of Ni(NO 3 ) 2 ·6H 2 O, 21.666g of Mg(NO 3 ) 2 ·6H 2 O add an appropriate amount of deionized water, fully stir until dissolved to obtain 1# solution; then weigh citric acid with a total molar number of metal cations of 1:1, dissolve it in deionized water, and stir to obtain 2# solution, weigh and metal cation Ethylene glycol with a total molar number of cations of 1:1, to obtain 3# solution; slowly drop 2# solution into 3# solution, stir until the mixture is uniform, and slowly add the mixed solution dropwise under the condition of 70°C water bath Put it into the 1# solution, stir until it becomes a gel, take it out and place it in an oven at 100-110°C to dry for 10-15h to obtain a catalyst precursor; put the sample in a tube furnace, and raise the temperature to 700°C at a rate of 10°C / min ℃, and after calcination at this temperature for 4 hours, the catalyst N85M was obtained. The molar composition of the catalyst is (NiO) 0.08 (MgO) 0.85 , by we...

Embodiment 1

[0038] Weigh 2.352g of Ni (NO 3 ) 2 ·6H 2 O, 2.593g of Mg(NO 3 ) 2 ·6H 2 O add an appropriate amount of deionized water, fully stir until dissolved; then weigh 12.735g of butyl titanate solution into the beaker equipped with nitrate solution, stir evenly to obtain 1# solution; follow-up steps are the same as in reference example 1, put the sample Put it into a tube furnace, raise it to 700°C with a heating rate of 10°C / min, and obtain the catalyst N10MT of the present invention after roasting at this temperature for 4 hours, forming a (Mg, Ni)TiO 3 Perovskite-like structure and rutile phase TiO 2 The mesoporous catalyst, the phase composition is as attached figure 1 As shown, the pore size distribution is shown in the attached figure 2 shown. The molar composition of the catalyst is (NiO) 0.08 (MgO) 0.1 (TiO 2 ) 0.37 , by weight percentage of oxides: nickel oxide is 15.0%, magnesium oxide is 10.0%, and titanium oxide is 75.0%.

[0039] The activity of the N10MT c...

Embodiment 2

[0041] Weigh 2.330g of Ni(NO 3 ) 2 ·6H 2 O, 1.284g of Mg(NO 3 ) 2 ·6H 2 O add an appropriate amount of deionized water, fully stir until dissolved; then weigh 13.636g of butyl titanate solution into the beaker equipped with nitrate solution, stir evenly to obtain 1# solution; follow-up steps are the same as in reference example 1, put the sample Put it into the tube furnace, rise to 700°C with a heating rate of 10°C / min, and obtain the catalyst N5MT of the present invention after roasting at this temperature for 4 hours, and the catalyst forms (Mg, Ni)TiO 3 Perovskite-like structure, the typical structure is as attached figure 1 shown. The molar composition of the catalyst is (NiO) 0.08 (MgO) 0.05 (TiO 2 ) 0.4 , by weight percentage of oxides: nickel oxide is 15.0%, magnesium oxide is 5.0%, and titanium oxide is 80.0%.

[0042] The activity of the N5MT catalyst was investigated by the autothermal reforming reaction of acetic acid. The reduction temperature was 700°C...

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Abstract

The invention relates to a nickel-magnesium-titanium perovskite type catalyst for preparing hydrogen by autothermal reforming of acetic acid. The chemical component of the catalyst is (NiO) a (MgO) b (TiO2) c, a is 0.08, b is 0.05-0.85, c is 0-0.40, and c is not 0. A sol-gel method is adopted, Ni serves as an active component, Ti is introduced, Ni is partially replaced with Mg, the mesoporous (Mg, Ni) TiO3 perovskite-like structure catalyst is formed, the activity of the catalyst is improved, generation of by-products such as acetone in the acetic acid autothermal reforming process is inhibited, gasification of carbon-containing intermediate species such as CHx * is promoted, and the catalytic activity of the catalyst is improved. Therefore, the thermal stability, sintering resistance and carbon deposition resistance of the catalyst in the autothermal reforming reaction of acetic acid are improved.

Description

technical field [0001] The invention relates to a magnesium-titanium perovskite-type nickel-based catalyst used for producing hydrogen by autothermal reforming of acetic acid, belonging to the field of producing hydrogen by autothermal reforming of acetic acid. Background technique [0002] At present, in the global energy consumption structure, petroleum is still the primary energy with the largest total consumption, followed by coal, natural gas and other energy sources, but these energy consumption processes produce a large amount of CO 2 and other greenhouse gases. As a green energy, hydrogen energy has the characteristics of zero pollution, high calorific value, and abundant reserves compared with traditional fossil energy. [0003] Renewable biomass has the characteristics of extensive sources and carbon neutrality. The development and utilization of biomass to produce hydrogen can replace some fossil fuels and help reduce the greenhouse effect. Biomass oil can be ob...

Claims

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Application Information

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IPC IPC(8): B01J23/78B01J35/10C01B3/22
CPCY02P20/52
Inventor 黄利宏廖富霞丁晨宇黄佳舒程宏
Owner CHENGDU UNIVERSITY OF TECHNOLOGY