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Porous carbon materials loaded with zero-valent fe-fe 3 The denitrification catalyst of c and its preparation and use method

A denitrification catalyst, fe-fe3c technology, applied in physical/chemical process catalysts, chemical instruments and methods, separation methods, etc., can solve the problems that are difficult to apply to coke oven flue gas denitrification, so as to avoid catalyst deactivation and reduce carrier carbon The loss and the effect of avoiding pollution

Active Publication Date: 2021-06-11
UNIV OF SCI & TECH LIAONING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, the medium and low temperature SCR denitrification technology is also difficult to apply to the coke oven flue gas denitrification industry

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0022] Porous carbon material load zero price Fe-Fe 3 A method of preparation of the denitrifination catalyst, including the following steps:

[0023] 1) The sawdust is drying in a hem drying tank at 100 to 110 ° C for 12h, and the seal is stored;

[0024] 2) 5 ~ 10g solid Fe (NO 3 ) 3 · 9h 2 O is added to 50 to 100 ml of deionized water for mixing, stirring to form a transparent solution, and the concentration of the solution is 0.1 to 0.4 mol / L;

[0025] 3) Slowly adding step 1 in step 1) to step 2), then dry the sawdust, uniformly stirred 10 min or more, and the slurry is allowed to stand at room temperature;

[0026] 4) The slurry obtained by step 3) is dried in 100 to 110 ° C in the blower drying tank, and then placed in a tubular reactor, placing a tubular reactor with a slurry into a crucible furnace. The temperature is heated to 600 ~ 800 ° C under a nitrogen atmosphere, and the Fe-Fe is produced by holding from 30 min. 3 C / C denitrifination catalyst.

[0027] Porous c...

Embodiment 1

[0031] In this embodiment, Fe-Fe 3 The preparation step of the C / C denitrifination catalyst is as follows:

[0032] Step 1), dry the sawdust in a 105 ° C blast drying tank 12h, and the seal is stored;

[0033] Step 2) At 7.214 g Solid Fe (NO 3 ) 3 · 9h 2 O. 75 ml of deionized water was added to mix, stirring and formed a transparent solution, the concentration of the solution was 0.239 mol / L;

[0034] Step 3), slowly add the sawdust in step 2 in the transparent solution obtained from step 2), and stirred evenly for 10 min, and stand at room temperature for 12 h.

[0035] Step 4), the slurry obtained by step 3) is dried in a 105 ° C blower drying tank, and then the tube reactor is placed in a crucible furnace, and the nitrogen atmosphere is warmed to 750 ° C, heat the temperature for 30 min, and produce Fe -Fe 3 C / C denitrifination catalyst.

[0036] The simulated flue gas denitration test shows that in the air speed of 6000h -1 The NO volume concentration is 300 ppm, the oxy...

Embodiment 2

[0038] In this embodiment, Fe-Fe 3 The preparation step of the C / C denitrifination catalyst is as follows:

[0039] Step 1), dry the sawdust in a 105 ° C blast drying tank 12h, and the seal is stored;

[0040] Step 2), at 8.514G Solid Fe (NO 3 ) 3 · 9h 2 O. 75 ml of deionized water is added to mix, stirring to form a transparent solution, the concentration of the solution is 0.319 mol / L;

[0041] Step 3), slowly add the sawdust in step 2 in the transparent solution obtained from step 2), and stirred evenly for 10 min, and stand at room temperature for 12 h.

[0042] Step 4), the slurry obtained by step 3) is dried in a 105 ° C blast drying tank, and then the tube reactor is placed in a crucible furnace, and the nitrogen atmosphere is warmed to 650 ° C, heat insulation for 30 min, and produce Fe -Fe 3 C / C denitrifination catalyst.

[0043] Simulated flue gas denitration test showed that in a speed of 6000h -1 Under the conditions of the NO volume concentration of 300 ppm, the...

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PUM

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Abstract

The invention relates to a porous carbon material loaded with zero-valent Fe-Fe 3 The denitration catalyst of C and its preparation, use method, described denitration catalyst is Fe-Fe 3 C / C denitration catalyst, its components are zero-valent Fe 5-15% by mass percentage, Fe 3 C 5~10%, C 75~90%; of which zero-valent Fe and Fe 3 C is used as an active component; C is porous carbon, which is used as a carrier and a reducing agent. Fe-Fe described in the present invention 3 The preparation process of C / C denitration catalyst is simple and low in cost; Fe‑Fe 3 The C / C denitrification catalyst has high low-temperature activity, which matches the temperature window of the coke oven flue exhaust gas, and uses low-valence Fe to directly catalyze the reduction of NO, avoiding the escape of ammonia and the presence of toxic vanadium in conventional denitrification catalysts Harm to the human body and the environment, and solve the problem of carbon loss in the process of direct denitrification of carbonaceous solids.

Description

Technical field [0001] The present invention relates to the field of coke oven flue gas catalytic purification techniques, and more particularly to a porous carbon material load zero price Fe-Fe 3 C The denitrifination catalyst and its preparation, method of use. Background technique [0002] Nitrogen oxide (NO X ), Forming acid rain, destroying ozone layers, causing important causes of photochemical smoke, causing serious harm to human health and ecological environment, has become the main factor in restricting the sustainable development of my country's economic and social development. my country is the world's largest coal production and consumer, NO emissions to the atmosphere every year. X Waiting for pollutants to reach the forefront of the world. Especially in recent years, with the development and spread of the whole country, how to effectively manage the NO formed during coal utilization X Waiting for pollutants have been attracted by the government and the public. [00...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/22B01D53/56B01D53/86
CPCB01D53/8628B01D2258/0283B01J27/22
Inventor 李先春李艳鹰何超
Owner UNIV OF SCI & TECH LIAONING