Low-temperature CO-SCR denitration Cu-Ni/AC catalyst and preparation method thereof

A CO-SCR and catalyst technology, which is applied in the field of low-temperature CO-SCR denitrification Cu-Ni/AC catalyst and its preparation, can solve the problems of corrosion reducing agent, low denitrification performance, toxicity, etc., and achieve the improvement of active functional groups and nitrogen selection Good performance and increase the specific surface area

Inactive Publication Date: 2021-02-05
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

"Carbon-based catalyst multi-pollutant synergistic removal and resource utilization technology" can achieve desulfurization and denitrification and multi-pollutant synergistic treatment under the condition of sintering flue gas temperature, but there are problems of low denitrification performance and limited denitrification rate, and traditional carbon The reducing agent for the denitrification of the base catalyst is NH 3 , is a toxic and corrosive reducing agent, and NH 3 itself is easy to interact with SO in the flue gas 2 、H 2 O, etc. generate ammonium salts, which cause blockage and poisoning of the internal pores of the catalyst
[0004] Therefore, it is necessary to provide a denitrification catalyst to solve the problems of the existing denitrification catalysts such as low denitrification rate at low temperature, easy blockage of pores, and narrow denitrification temperature range.

Method used

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  • Low-temperature CO-SCR denitration Cu-Ni/AC catalyst and preparation method thereof
  • Low-temperature CO-SCR denitration Cu-Ni/AC catalyst and preparation method thereof
  • Low-temperature CO-SCR denitration Cu-Ni/AC catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Embodiment 1: preparation carrier coconut shell activated carbon (AC)

[0046] 1: Take coconut shell activated carbon, impregnate according to the material-liquid ratio of 1g (coconut shell activated carbon): 5ml (deionized water), shake and wash in an ultrasonic water bath at 60°C for 60min, and dry at 110°C for 12h after suction filtration. Get clean activated carbon.

[0047] 2: Activate the cleaned activated carbon under air atmosphere at 350°C for 2 hours to obtain carrier activated carbon.

Embodiment 2

[0048] Example 2: Preparation of a low-temperature CO-SCR denitrification Cu-Ni / AC catalyst

[0049] 1: Dissolve an appropriate amount of copper nitrate and nickel acetate in deionized water, make it into a modified solution of 0.04-0.2g / ml, and then impregnate it with a material-to-liquid ratio of 1g (AC): 2.5ml (modified solution) , and then shaken in an ultrasonic water bath for 60 minutes, and then dried at 110° C. for 12 hours after suction filtration to obtain the initial product.

[0050] 2: The initial product was roasted at 450°C for 4h under the protection of nitrogen to prepare a low-temperature CO-SCR denitrification Cu-Ni / AC catalyst.

Embodiment 3

[0051] Example 3: Evaluation of fixed bed reactors.

[0052] The low-temperature CO-SCR denitrification Cu-Ni / AC catalyst and coconut shell activated carbon (purchased from Henan Gongyi Blue Sky Water Purification Technology Co., Ltd.) prepared in Example 2 were used as denitration reaction materials, and the denitration reaction experiments were carried out at 100-190 ° C, respectively. The loading amount of the catalyst is 10 g.

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Abstract

The invention discloses a low-temperature CO-SCR denitration Cu-Ni/AC catalyst which comprises a carrier and active components, the carrier is coconut shell activated carbon (AC), and the active components are copper and nickel oxides. The mass ratio of the copper element to the nickel element to the AC in the low-temperature CO-SCR denitration Cu-Ni/AC catalyst is (0.02-0.1): (0.01-0.05): 1. Theinvention also discloses a preparation method of the catalyst. The preparation method comprises the following steps of: respectively dissolving copper nitrate and a nickel acetate reagent with deionized water to obtain a mixed precursor solution, impregnating the coconut shell activated carbon in a formula ratio, and carrying out loading and drying to obtain a primary product; and roasting the dried primary product for 4 hours under the protection of nitrogen at 450 DEG C to obtain the low-temperature CO-SCR denitration Cu-Ni/AC catalyst. The low-temperature CO-SCR denitration Cu-Ni/AC catalyst disclosed by the invention has the characteristics of high denitration activity, good nitrogen selectivity and wide denitration temperature range. The Cu-Ni/AC catalyst provided by the invention hasthe advantages of simplified preparation process, low energy consumption, good dispersity of active components, environment-friendliness and no pollution.

Description

technical field [0001] The invention belongs to the field of catalyst preparation and sintering flue gas purification, and specifically relates to a low-temperature CO-SCR denitrification Cu-Ni / AC catalyst and a preparation method thereof. Background technique [0002] With the increasing demand for steel in my country's economic development, the steel industry has become the material basis and an important pillar industry for the development of the national economy and national defense construction. The NOx produced by it is one of the important reasons for the formation of photochemical smog and acid rain. With the full implementation and enforcement of ultra-low emission standards, it is imperative and imminent to increase the coordinated treatment of multi-pollutants in sintering flue gas! [0003] At present, the mature denitrification terminal treatment technologies for sintering flue gas mainly include SCR denitrification and carbon material (activated carbon or activ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J37/34B01J37/14B01J37/02B01J37/08B01D53/86B01D53/56
CPCB01D53/8628B01D2258/0283B01J23/755B01J37/0203B01J37/08B01J37/14B01J37/343
Inventor 黄帮福汪德富施哲张桂芳李露代蒙杨征宇文桢晶李婉君周晓雷阴树标漆鑫
Owner KUNMING UNIV OF SCI & TECH
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