Sulfur-resisting and nitrogen-removed oxide compound metallic oxide SCR (Selective Catalytic Reduction) catalyst and preparation method thereof

A technology of SCR catalyst and nitrogen oxides, which is applied in the field of heterogeneous catalyst preparation, can solve the problems of increasing energy consumption and operating costs, and achieve the advantages of sulfur resistance performance, low temperature performance and simple preparation

Inactive Publication Date: 2011-02-16
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the temperature of the flue gas after passing through the FGD device is only 60°C. In order to make the flue gas reach the catalyst reaction temperature before entering the denitrification reaction device, it is necessary to add fuel or natural gas burners or steam heat exchangers in the flue to increase energy. Consumption and running costs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] (1) Dissolve cobalt nitrate, chromium nitrate and manganese nitrate with a metal molar ratio of 0.5:4:6 into 2mol / L citric acid solution at a ratio of 1:1 to citric acid molar ratio, and let stand for 1 hour Afterwards, obtain cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese nitrate citric acid solution respectively;

[0028] (2) Mix cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese nitrate citric acid solution at 5mL min -1 The total flow rate of the mixture was evenly added dropwise to the beaker and kept stirring continuously, and continued to stir for 2 hours after the dropwise addition to obtain a mixed solution;

[0029] (3) The mixed solution was dried in an oven at 150°C for 15 hours, and then calcined in a muffle furnace at a temperature of 650°C for 350 minutes;

[0030] (4) After the calcined product is pressed into tablets under a pressure of 6Kpa, it is ground into particles thr...

Embodiment 2

[0035] (1) Cobalt nitrate, chromium nitrate and manganese nitrate with a metal molar ratio of 2:5:5 were dissolved in 3mol / L citric acid solution at a ratio of 1:1.5 to citric acid molar ratio, and left to stand for 3 hours Afterwards, obtain cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese nitrate citric acid solution respectively;

[0036] (2) Mix cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese nitrate citric acid solution at 10mL min -1 The total flow rate is evenly added dropwise to the beaker and kept stirring continuously, after the dropwise addition, continue to stir for 0.5 hours to obtain a mixed solution;

[0037] (3) The mixed solution was dried in an oven at 90°C for 8 hours, and then calcined in a muffle furnace at a temperature of 600°C for 100 minutes;

[0038] (4) After the calcined product is pressed into tablets under a pressure of 15Kpa, it is ground into particles through a 60-m...

Embodiment 3

[0043] (1) Cobalt nitrate, chromium nitrate and manganese acetate with a metal molar ratio of 2:3:7 are dissolved in 2mol / L citric acid solution in a ratio of 1:2 to citric acid molar ratio, and left to stand for 2 hours Afterwards, obtain cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese acetate citric acid solution respectively;

[0044] (2) Mix cobalt nitrate citric acid solution, chromium nitrate citric acid solution and manganese acetate citric acid solution at 8mL·min -1 The total flow rate is evenly added dropwise to the beaker and kept stirring continuously, after the dropwise addition, continue to stir for 3 hours to obtain a mixed solution;

[0045] (3) The mixed solution was dried in an oven at 130°C for 15 hours, and then calcined in a muffle furnace at a temperature of 700°C for 200 minutes;

[0046] (4) After the calcined product is pressed into tablets under a pressure of 8Kpa, it is ground into particles through an 80-mes...

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PUM

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Abstract

The invention discloses a sulfur-resisting and nitrogen-removed oxide compound metallic oxide SCR catalyst and a preparation method and applications thereof. The catalyst contains the following elements in the molar ratio: 0.2-2 percent of structural auxiliary element M, 2-4 percent of chromium element and 5-8 percent of manganese element. The preparation method comprises the following steps of: (1) respectively dissolving metal precursors into a citric acid, and evenly stirring and standing for 1-5 hours to respectively obtain an M metal citric acid solution, a chromium metal citric acid solution and a manganese metal citric acid solution; (2) simultaneously and evenly dropwise adding all the metal citric acid solutions to a container and stirring without stop, and continuing to stir for 0.5-3 hours after all the metal citric acid solutions are dropwise added completely; (3) placing the container in a drying oven for drying for 8-15 hours at the temperature of 90-150 DEG C, and then calcining in a muffle furnace for 100-350 min; and (4) tabletting calcined products and then grinding and sieving. The catalyst can be applied to automobile exhaust NOx treatment devices or the denitrification devices of stationary source coal fired power plants.

Description

technical field [0001] The invention belongs to the field of preparation of heterogeneous catalysts, in particular to a composite metal oxide SCR catalyst resistant to sulfur and nitrogen oxide removal and its preparation method and application. Background technique [0002] Flue gas emission is an important source of air pollution, so purifying flue gas is an important means of controlling air pollution. Greenhouse gases mainly start from the perspective of energy saving and emission reduction and new energy development. Flue gas desulfurization technology has become increasingly mature and stable. For denitrification technology, selective catalytic reduction (SCR) is the most effective and most widely used technology. Currently, the NH 3 Selective catalytic reduction (NH 3 -SCR)NO x Catalysts are mainly divided into four categories: metal catalysts, molecular sieve catalysts, carbon-based catalysts and metal oxide catalysts. Compared with the high cost of metal catalyst...

Claims

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Application Information

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IPC IPC(8): B01D53/56B01J23/889B01J37/00B01D53/86
Inventor 李雪辉李华于英豪王芙蓉陈志航
Owner SOUTH CHINA UNIV OF TECH
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