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Magnetically separable and recyclable iron oxide SCR denitration catalyst and application method thereof

A denitration catalyst, magnetic iron oxide technology, applied in separation methods, chemical instruments and methods, dispersed particle separation and other directions, can solve the problems of difficult to control catalyst preparation conditions, serious high temperature ablation of activated carbon, and high catalytic preparation costs, and achieve savings. The effect of environmental protection investment and operation cost, low airflow resistance and low price

Inactive Publication Date: 2015-10-14
HEFEI UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

V 2 o 5 / TiO 2 The disadvantages of denitrification catalysts are: first, the cost of catalytic preparation is relatively high; second, the preparation conditions of the catalyst are relatively strict and difficult to control; third, the operating temperature is relatively high at 350-400 ° C, and the control is strict, which is not suitable for the flue gas desulfurization of existing power plants in my country. The actual situation of low temperature after dust removal
The advantage of catalysts prepared with activated carbon as a carrier is that the rich specific surface area of ​​the activated carbon carrier is conducive to the dispersion of active components and has a certain resistance to SO 2 However, during the activation and regeneration process, the high-temperature ablation of activated carbon is too serious, resulting in excessive catalyst loss

Method used

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  • Magnetically separable and recyclable iron oxide SCR denitration catalyst and application method thereof
  • Magnetically separable and recyclable iron oxide SCR denitration catalyst and application method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0032] Choose goethite content 70%, specific surface area 15m 2 / g of limonite ore as raw material;

[0033] Crush and sieve the limonite ore to obtain particles with a particle size between 0.05mm and 0.075mm;

[0034] Calcining the particles at 250°C under a hydrogen atmosphere, reducing the goethite to magnetite, and obtaining a magnetically recyclable magnetic iron oxide SCR denitrification catalyst;

[0035] Use a fixed-bed gas-solid-phase catalytic microreactor to evaluate the performance of the SCR denitrification catalyst: fill 2g of the above-mentioned denitration catalyst into the gas-solid-phase catalytic denitration reaction tube, program the temperature to a predetermined temperature, use argon as the dilution gas, and feed NH at the same time 3 / Ar, NO / Ar, SO 2 / Ar standard gas and high-purity oxygen, add water quantitatively with a syringe pump to simulate flue gas components, and investigate SO in flue gas 2 Concentrations of 800ppm and 800ppmSO 2 +5%H 2 T...

Embodiment 2

[0037] Choose goethite content greater than 80%, specific surface area greater than 20m 2 / g of limonite ore as raw material;

[0038] Crush and sieve the limonite ore to obtain 0.075-0.1mm particles;

[0039] Calcining the particles at 300°C under a hydrogen atmosphere, reducing the goethite to magnetite, and obtaining a magnetically recoverable magnetic iron oxide SCR denitrification catalyst;

[0040] Add the above-mentioned magnetite particle catalyst and ammonia into the flue gas flow at the same time, the dosage of the catalyst is 1.0g per cubic meter of flue gas volume, and the amount of ammonia gas is added according to the amount of NH 3 The molar ratio to NO in the flue gas is 0.9:1, and the flue gas component is: SO 2 800ppm, H 2 O 5%, NO 1000PPm, O 2 3%, and the SCR denitrification efficiency reaches more than 90% under the condition of flue gas temperature 300-450°C.

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Abstract

The invention discloses a magnetically separable and recyclable iron oxide SCR denitration catalyst and an application method thereof. The catalyst is prepared through the following steps: with a limonite ore as a raw material, crushing and screening to form particles, calcining the particles in an atmosphere of hydrogen or carbon monoxide, so as to reduce goethite in the particles to be magnetite to obtain the catalyst, or further calcining in an air atmosphere, so that the magnetite is oxidized to be maghemite to obtain the catalyst, wherein the goethite content of the limonite ore is not less than 60%, the limonite ore has a nano-micro hierarchical porous structure, and the specific surface area of the limonite ore is not less than 10m<2> / g. When in use, the catalyst and ammonia are simultaneously fed into a flue gas flow at the temperature of 300-450 DEG C, and the catalyst and dust are together adsorbed onto the electrode plate of an electric dust collector or the surface of a filter bag and then are collected into a dust hopper through a dust cleaning method; the SCR denitration catalyst in the material discharged from the dust hopper is separated and recycled through a magnetic separation method; if inactivated, the SCR denitration catalyst can be washed and regenerated with water or weak aqua ammonia.

Description

1. Technical field [0001] The invention relates to the field of air pollution control, in particular to a selective catalytic reduction flue gas denitrification catalyst and an application method thereof. 2. Background technology [0002] Various industrial furnaces such as thermal power plants, sintering plants, cement kilns, and motor vehicles, etc., produce a large amount of NOx during high-temperature combustion. Nitrogen oxide emissions not only cause acid rain, but also lead to regional environmental pollution problems such as photochemical smog and ozone layer depletion. Nowadays, there are two main types of technologies for reducing nitrogen oxides in flue gas: the first type is combustion process control, that is, improving the combustion method and reducing the formation of nitrogen oxides during the combustion process (including low-oxygen combustion technology, multi-stage combustion technology, etc.) The second category is terminal treatment, that is, flue gas ...

Claims

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Application Information

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IPC IPC(8): B01J23/745B01D53/90B01D53/76B01D53/96B01D53/56
Inventor 陈天虎徐彬邹雪华朱承驻刘海波陈冬
Owner HEFEI UNIV OF TECH
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