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Shaped coal-based SO2 and NO adsorption catalyst and preparation method thereof

A catalyst, coal-based technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of high cost and increased desulfurization cost, achieve higher power, achieve economic and environmental win-win, source wide range of effects

Inactive Publication Date: 2012-05-23
OCEAN UNIV OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process uses a moving bed technology with a certain strength of shaped activated coke, and the cost of coke is relatively high; in addition, there is mechanical wear and loss of carbon during the desulfurization and regeneration process, and fresh activated carbon (coke) needs to be continuously replenished, resulting in desulfurization costs greater increase in

Method used

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  • Shaped coal-based SO2 and NO adsorption catalyst and preparation method thereof
  • Shaped coal-based SO2 and NO adsorption catalyst and preparation method thereof
  • Shaped coal-based SO2 and NO adsorption catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] The lignite is crushed, ground, and sieved to obtain 200-mesh particles, and a certain amount of lignite powder is put into a mixer, and a 20% aqueous solution of sodium nitrohumate activated by nitric acid, dextrin and graphite are added to stir, so that The lignite content is 75wt%, the binder sodium nitrohumate content is 20wt%, the pore-forming agent dextrin content is 4.5wt%, and the lubricant graphite content is 0.5wt%. Stir and mix at a constant temperature of 25°C for about 0.5 hours, then add water to adjust to an appropriate viscosity, and then extrude into strands. The extruded precursor body is dried in an oven at 120°C for 2 hours. After drying, the particle size of the precursor embryo body for extrusion molding is ∮2mm, and then it is passed through a mixture containing 20%-40%H 2 O and 2%O 2 N 2 The mixed gas is activated and modified for 1-2h. Finally, the prepared adsorption catalyst is cut into columnar particles according to the length being 2-3 t...

Embodiment 2

[0027] The powdered semi-coke is further crushed, ground, and sieved to obtain 160-mesh particles. A certain amount of powdered semi-coke powder is put into a blender, and a 30% concentration of potassium humate aqueous solution, starch and tung oil are added to stir, so that The powdery semi-coke content is 64wt%, the binder potassium humate content is 30wt%, the pore-forming agent starch content is 5.2wt%, and the lubricant tung oil content is 0.8wt%. Stir and mix at room temperature for about 0.6 hours, then add water to adjust to an appropriate viscosity, and then extrude and shape the precursor body after extrusion molding at 200° C. for 1.5 hours. After drying, the particle size of the precursor body for extrusion molding is ∮4mm, and it is passed through a mixture containing 10%-30%H 2 O and 4%O 2 N 2 The mixed gas is activated and modified for 1-1.5h. Finally, the prepared catalyst is cut into columnar particles according to the length being 2-3 times of the particl...

Embodiment 3

[0029] The lignite and powdered semi-coke (mass ratio 1:1) are crushed, ground and sieved to obtain 200-mesh particles, a certain amount of the above powder is put into a mixer, and a 20% aqueous solution of nitrohumic acid zinc is added , dextrin and graphite, so that the content of lignite and powdery semi-coke is 70wt%, the content of binder nitrohumic acid zinc is 25wt%, the content of pore-forming agent dextrin is 4.3wt%, and the content of lubricant graphite is 0.7 wt%. Stir and mix the raw material pulverized coal or powdery semi-coke at a constant temperature of 30°C for about 0.4 hours, then add water to adjust to an appropriate viscosity, and then roll into balls to shape the precursor body after rolling into a ball and dry it in an oven at 100°C for 2 hours . After drying, the particle size of the precursor embryo body for rolling ball forming is ∮3mm, and it is passed at 680°C with 15%-35%H 2 O and 3%O 2 N 2 The mixed gas is activated and modified for 1-1.5h. ...

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Abstract

The invention discloses a shaped coal-based SO2 and NO adsorption catalyst which is characterized by comprising the following components in percentage by weight: 50-85% of coal-based material, 10-40% of binder, 0.3-10.0% of pore forming agent and 0.1-0.9% of lubricating agent. The invention also discloses a preparation method of the catalyst, comprising the following steps: (1) breaking and grinding the coal-based material into a 2-250 mesh product; (2) mixing the coal-based material obtained in the step (1) with the binder, the pore forming agent and the lubricating agent according to the proportion, and then shaping; and (3) drying the shaped product obtained in the step (2) to obtain the shaped coal-based SO2 and NO adsorption catalyst. The shaped coal-based SO2 and NO adsorption catalyst disclosed by the invention has the advantages that the raw material coal or powdery semicoke is widely available, the price is low, and good adsorption performance can be obtained after activationand modification; and the shaped catalyst can be used for improving the gas flow condition in the reactor, and reducing the pressure drop of a catalyst bed layer, thus improving the combustion efficiency of a boiler and the power of a draught fan.

Description

technical field [0001] The present invention relates to an adsorption catalyst for flue gas desulfurization and denitrification in coal-fired power plants, coal-fired boilers and coal-fired kilns, etc. 2 And NO adsorption catalyst and preparation method thereof. Background technique [0002] According to statistics, in 1998 the national SO 2 The total emissions reached 20.9 million tons, ranking first in the world, NO x emissions also accounted for 10.1% of the world's total. About 87% of SO 2 , 67% NO x from coal combustion. In 2006, the national SO 2 The emissions were 25.888 million tons, the emissions of soot were 10.784 million tons, and the emissions of industrial dust were 8.075 million tons. If measures are not taken quickly, my country's SO in 2010 2 Annual emissions will be close to 30 million tons, NO x Total emissions will be close to 10 million tons. In 2006, the national environmental pollution control investment was 240.28 billion yuan, accounting fo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/20B01J27/20B01D53/02B01D53/86B01D53/60
CPCY02A50/20
Inventor 李春虎冯丽娟卞俊杰高健李子真
Owner OCEAN UNIV OF CHINA