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Deoxidating catalyst with core-shell structure, and preparation method and application of deoxidating catalyst

A technology of deoxidation catalyst and core-shell structure, which is applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. High temperature and other problems, to achieve high stability, simple preparation process, large gas treatment effect

Active Publication Date: 2017-02-01
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0016] At present, the main catalytic combustion deoxidation catalysts can be divided into the following categories: as disclosed in CN1495247A and CN101664679A, precious metal catalytic combustion deoxidation catalysts such as Pt and Pd have high catalytic activity, low reaction temperature, and the oxygen in the gas after deoxidation can be basically removed. The disadvantages of these deoxidation catalysts are that noble metals are easy to sinter at high temperatures, have poor high temperature resistance, and have low deoxidation activity at low temperatures. CN101139239A discloses a catalyst with strong sulfur resistance Co-based catalysts have the characteristics of strong sulfur resistance, but their reaction temperature is high, which has great limitations

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  • Deoxidating catalyst with core-shell structure, and preparation method and application of deoxidating catalyst
  • Deoxidating catalyst with core-shell structure, and preparation method and application of deoxidating catalyst

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preparation example Construction

[0043] The present invention provides a method for preparing a deoxidation catalyst with a core-shell structure described in the above technical solution, comprising the following steps:

[0044] (1) Mixing a copper oxide precursor, a cerium oxide precursor, a templating agent and hydrogen peroxide, and performing a hydrothermal reaction to obtain a hydrothermal product;

[0045] (2) mixing the hydrothermal product obtained in the step (1) with a titanium dioxide precursor, and hydrothermally reacting to obtain a deoxidation catalyst precursor;

[0046] (3) Calcining the deoxidation catalyst precursor obtained in the step (2) to obtain a deoxidation catalyst with a core-shell structure.

[0047] In the invention, copper oxide precursor, cerium oxide precursor, template agent and hydrogen peroxide are mixed, and hydrothermal reaction is carried out to obtain a hydrothermal product. In the present invention, the copper oxide precursor is preferably a soluble copper salt, more p...

Embodiment 1

[0072] The core part of the core-shell catalyst of the present embodiment is made of 5.0wt% CuO, 20.0wt% CeO 2 Composition, the rest of the mass is the core-shell part of TiO 2 the quality of. Named Catalyst-1.

[0073] The preparation method of this embodiment is:

[0074](1) the copper nitrate ethanolic solution of 50ml molar concentration 0.6mol / L, the cupric chloride copper ethanolic solution of 50ml molar concentration 0.6mol / L and the cerous nitrate ethanolic solution of 370ml molar concentration 3.0mol / L are mixed in proportion, Add 20ml of 0.1mol / L cetyltrimethylammonium bromide aqueous solution and 40ml of 5wt% hydrogen peroxide aqueous solution, stir at 60°C for 8h at 500rpm, and set aside;

[0075] (2) Then add 304g of tetrabutyl titanate ethanol solution dropwise into (1) the above solution, stir evenly at 25°C for 2-6 hours at a high speed of 1000rpm, then put it into a stainless steel reactor, and heat it at 110°C Stir for 6h. Filtration and washing, drying ...

Embodiment 2

[0078] The core part of the core-shell catalyst of the present embodiment is made of 10.0wt% CuO, 10.0wt% CeO 2 Composition, the rest of the mass is the core-shell part of TiO 2 the quality of. Named Catalyst-2.

[0079] The preparation method of this embodiment is:

[0080] (1) Mix 100ml of copper chloride ethanol solution with molar concentration of 0.3mol / L and 70ml of cerous nitrate ethanol solution with molar concentration of 0.2mol / L in proportion, and add 10ml of 0.05mol / L hexadecyltrimethyl bromide Aqueous ammonium chloride solution, 10ml of 0.05mol / L hexamethyleneimine and 30ml of aqueous hydrogen peroxide solution with a mass fraction of 10wt% were stirred at 200rpm at a stirring speed of 60°C for 6h and set aside;

[0081] (2) Then add 81g of tetrabutyl titanate ethanol solution dropwise to (1) above solution, stir evenly at 25°C for 2h at 800rpm high speed, then put it into a stainless steel reaction kettle, stir for 6h under 120°C hydrothermal condition , the ...

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Abstract

The invention provides a deoxidating catalyst with a core-shell structure, and belongs to the technical field of catalysis of oxygen-bearing coal bed gas. A core portion of the deoxidating catalyst comprises CuO and CeO2, and a shell portion of the deoxidating catalyst comprises TiO2. A shell is used for protecting active ingredients of metal Cu in an inner layer, and sintering of the active ingredients can be prevented effectively; the probability of collision between reaction molecules and active centers is increased through confinement effect of the shell, and low-temperature catalytic deoxidation activity and high-temperature performance of the catalyst are improved; the catalyst has the advantages of high heat stability, high low-temperature activity, ignition temperature being 400 DEG C, wide deoxidation temperature window (400-800 DEG C), high wear strength and service life as long as 1000h; the deoxidating catalyst has high stability to impurity ingredients such as water, carbon dioxide, sulfide and nitration products and high mechanical strength, can meet application requirements of fluidized beds, and has the advantages of high gas treatment quantity, high heat transfer performance and easiness in operation after being combined with a deoxidation process of the fluidized beds.

Description

technical field [0001] The invention relates to the technical field of oxygen-containing coal bed gas catalysis, in particular to an oxygen-containing coal bed gas deoxidation catalyst with a core-shell structure. Background technique [0002] my country is rich in coalbed methane resources, ranking third in the world. The national shallow coalbed methane resources are 36.8 trillion cubic meters, and the calorific value is equivalent to 52 billion tons of standard coal. In today's increasingly tight energy environment, coalbed methane, as a high-quality, efficient and clean energy, can be used for power generation, heating, residential life, and vehicle fuel, etc., and its large-scale utilization has huge economic value. [0003] Oxygen-containing coalbed methane is an important part of coalbed methane resources. It mainly refers to the coalbed methane extracted from coal bodies and surrounding rocks during the coal mining process. This kind of coalbed methane is diluted by ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/00B01J35/02C10L3/10B01J35/00
CPCC10L3/101B01J23/002B01J23/83C10L2290/12B01J35/397B01J35/40
Inventor 王建国令狐建设吴志伟秦张峰朱华青王冬平李淑敏翁震坤樊卫斌赵建涛
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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