A slurry-bed nickel-based methanation catalyst prepared by precipitation combustion method and its application

A methanation catalyst, bed nickel-based technology, applied in the field of nickel-based catalyst preparation, can solve the problems of increasing production cost, small catalyst specific surface area, less catalyst surface active sites, etc., and achieves the effect of reducing energy consumption

Active Publication Date: 2018-04-03
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, some characteristics of the precipitation method also limit its application: (1) The catalyst prepared by the precipitation method has a small specific surface area and large crystal grains, resulting in fewer active sites on the surface of the catalyst and poor dispersion; (2) The synthesis process of the precipitation method It needs to be aged, washed, dried and roasted, which has high requirements on the control process and increases the production cost.

Method used

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  • A slurry-bed nickel-based methanation catalyst prepared by precipitation combustion method and its application
  • A slurry-bed nickel-based methanation catalyst prepared by precipitation combustion method and its application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] (1) Prepare an aluminum nitrate solution with a concentration of 1.0 mol / L, an aqueous solution of lanthanum nitrate with a concentration of 1.0 mol / L and a urea solution with a concentration of 5.0 mol / L. Adjust the adding rate of aluminum nitrate aqueous solution to 58.6 mL / min, the adding rate of lanthanum nitrate aqueous solution to 0.1 mL / min, and the adding rate of urea solution to 50.0 mL / min, so that the temperature is 75 ℃, and the stirring rate is 500 rpm in the reactor The precipitation in the medium was complete, and the addition was stopped after 2 h. During this process, the pH value of the solution was monitored with precision pH test paper, and the pH value of the solution was controlled to be 8.0.

[0024] (2) Keep the stirring rate constant, and at a temperature of 60 °C, add nickel nitrate aqueous solution with a solution concentration of 1.0 mol / L and urea aqueous solution with a solution concentration of 5.0 mol / L to the above suspension at the same...

Embodiment 2

[0028] (1) Prepare aluminum nitrate solution with a solution concentration of 1.0 mol / L, dysprosium nitrate aqueous solution with a solution concentration of 1.0 mol / L and urea solution with a solution concentration of 6.0 mol / L. Adjust the adding rate of aluminum nitrate aqueous solution to 17.1 mL / min, the rate of adding dysprosium nitrate aqueous solution to 0.2 mL / min, and the rate of adding urea solution to 50.0 mL / min, so that the temperature is 75 °C and the stirring rate is 400 rpm. The precipitation in the medium was complete, and the addition was stopped after 1 h. During this process, the pH value of the solution was monitored with precision pH test paper, and the pH value of the solution was controlled to be 8.0.

[0029](2) Keep the stirring rate constant, and at a temperature of 40 °C, add nickel nitrate aqueous solution with a solution concentration of 0.5 mol / L and urea aqueous solution with a solution concentration of 2.0 mol / L to the above suspension at the s...

Embodiment 3

[0033] (1) Prepare an aluminum nitrate solution with a concentration of 2.0 mol / L, an aqueous solution of lanthanum nitrate with a concentration of 0.5 mol / L and a urea solution with a concentration of 5.0 mol / L. Adjust the adding rate of aluminum nitrate aqueous solution to 21.2 mL / min, the adding rate of lanthanum nitrate aqueous solution to 0.5 mL / min, and the adding rate of urea solution to 50.0 mL / min, so that the reaction temperature is 80 °C and the stirring rate is 700 rpm. The precipitation in the vessel was complete, and the addition was stopped after 0.5h. During this process, the pH value of the solution was monitored with precision pH test paper, and the pH value of the solution was controlled to be 10.0.

[0034] (2) Keep the stirring rate constant, and at a temperature of 30 °C, add nickel nitrate aqueous solution with a solution concentration of 2.0 mol / L and urea aqueous solution with a solution concentration of 5.0 mol / L to the above suspension at the same ti...

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Abstract

The invention relates to a slurry reactor nickel-based methanation catalyst prepared according to a sediment burning method and an application thereof. The invention relates to a methanation nickel-based catalyst prepared according to the sediment burning method and a preparation method thereof. The methanation catalyst comprises the following raw materials by mass percent: 15-50wt% of Ni, 47-80wt% of Al2O3 and 1-10wt% of auxiliaries, wherein the auxiliaries are selected from one or two of Dy2O3, La2O3, Eu2O3 and Gd2O3; the grain size of the catalyst is 60-220 meshes; the specific surface area is 150-250 m<2> / g; the Ni crystal grain size is 12-16nm. The methanation catalyst provided by the invention has the advantages that the preparation process is simple, the preparation period is short and the activity and selectivity in the slurry reactor methanation reaction are high.

Description

technical field [0001] The invention relates to a preparation method and application of a nickel-based catalyst, in particular to a nickel-based methanation catalyst applied to a slurry bed methanation reaction and a preparation method thereof. Background technique [0002] Natural gas is a clean, safe and convenient high-quality energy. In recent years, with the rapid development of economic construction, the demand for natural gas has continued to grow. In 2014, the apparent consumption of natural gas in my country was 180 billion cubic meters, a year-on-year increase of 7.4%, of which the external dependence reached 32.2%. my country is rich in coal resources, and more than 80% of coal is directly burned every year. Compared with developed countries, the level of deep utilization of coal is relatively low. The use of coal-to-gas technology to convert abundant coal resources into natural gas not only effectively increases energy utilization, but also greatly reduces green...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/83B01J37/03B01J37/08B01J37/18B01J35/10C10L3/08
CPCB01J23/002B01J23/83B01J35/006B01J35/1019B01J37/031B01J37/088B01J37/18B01J2523/00C10L3/08B01J2523/31B01J2523/3706B01J2523/375B01J2523/3762B01J2523/3743
Inventor 崔丽萍李忠高源孟凡会
Owner TAIYUAN UNIV OF TECH
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