Optimization Design and Engineering Application of Gas Turbine SCR Denitrification System

Youhua HUANG; Shanwei MA; Ji LIU; Zhenghua WU

doi:10.12096/j.2096-4528.pgt.21029

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Optimization Design and Engineering Application of Gas Turbine SCR Denitrification System

Power Generation and Enviromental Protection | 更新时间：2025-07-04

- Optimization Design and Engineering Application of Gas Turbine SCR Denitrification System
- Power Generation Technology Vol. 42, Issue 3, Pages: 350-356(2021)
- 作者机构：
  
  1.龙净科杰环保技术(上海)有限公司, 上海市闵行区 201106
  2.生物质发电成套设备国家工程实验室(华北电力大学), 北京市昌平区 102206
- 作者简介：
- 基金信息：
  
  National Natural Science Foundation of China(52006069)
- DOI：10.12096/j.2096-4528.pgt.21029
  CLC： TK47
- Received：06 January 2021，
  
  Published：30 June 2021
- 稿件说明：
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Youhua HUANG, Shanwei MA, Ji LIU, et al. Optimization Design and Engineering Application of Gas Turbine SCR Denitrification System[J]. Power Generation Technology, 2021, 42(3): 350-356.
DOI：

Youhua HUANG, Shanwei MA, Ji LIU, et al. Optimization Design and Engineering Application of Gas Turbine SCR Denitrification System[J]. Power Generation Technology, 2021, 42(3): 350-356. DOI： 10.12096/j.2096-4528.pgt.21029.

摘要

以东莞某电厂F级燃气轮机卧式布置余热锅炉脱硝系统为例，针对氨气与烟气混合不均导致脱硝效率不达标的问题，采用数值计算、模型实验和工程实践研究了在喷氨栅格前增加导流板对脱硝系统的影响。数值模拟结果表明：增加导流板后，喷氨入口截面烟气速度梯度明显下降，催化剂床层入口截面烟气速度分布均匀。小试模型实验结果显示，增加导流板后，催化剂入口烟气速度偏差为10.7%，氨气浓度偏差为6.06%，表明烟气与氨气混合良好，流场均匀，满足设计要求。工程实践结果进一步证明，增加导流板后，催化剂床层出口截面NO

浓度分布均匀，所有测点NO

质量浓度小于30mg/Nm

，NO

浓度偏差值小于15%，完全满足排放要求，表明优化方法具有较高实际应用价值。

Abstract

In order to solve the problem of low denitrification efficiency caused by the uneven mixing of ammonia and flue gas with an F-class gas turbine horizontal arranged waste heat boiler denitrification system

numerical simulations

lab-scale model experiments and engineering tests were carried out to study the effects of the approach of ammonia injection optimization. The numerical simulation results show that with adding a guide plate

the flue gas velocity gradient at the inlet plane of the ammonia injection decreases significantly

and the flue gas velocity distribution at the inlet plane of catalyst-bed is nearly uniform.

The model experiment results show that the standard deviation of flue gas velocity at the catalyst-bed inlet plane decreases to 10.7%

and the standard deviation of ammonia concentration decreases to 6.06%. It indicates that the flue gas and ammonia are mixed well

and the flue gas velocity field is uniform. The engineering test results show that with the addition of the guide plate

the NO

concentration in the outlet plane of the catalyst-bed is uniformly distributed

all the measured NO

concentrations are less than 30mg/Nm

and the NO

concentration deviation is less than 15%

indicating that this method could effectively improve the denitrification system.

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references

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