• Title/Summary/Keyword: 탈질설비

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Study on the Inlet Shape of a Selective Catalyst Reduction System with an Integrated Bypass Unit for Ships (Bypass 일체형 선박용 탈질설비의 입구형태에 대한 연구)

  • Ha, Soo-Hyeon;Lee, Jae-Chul;Lee, Sang-Beom;Kang, Donghoon
    • Journal of the Korean Society of Marine Environment & Safety
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    • v.27 no.5
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    • pp.666-674
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    • 2021
  • A selective catalyst reduction system (SCR) with an integrated bypass unit is proposed. Through simulations of the SCR, variations in flow to the catalyst due to the particular shape of the bypass shutting device in the SCR are also studied. The commercial software Ansys Fluent is used to develop the simulations. For the simulations, the catalyst of the SCR is modeled using the porous media method to reduce the calculation time and number of meshes, which is necessary because of the detailed modeling of the catalyst. Simulations are performed based on changes to the entrance angle to the catalyst and the size of the bypass shutting device. Finally, simulation results are used to compare and analyze the average velocity and uniformity of the flow to the catalyst.

Effect of addition of a catalystic layer on Denitrification System efficiency in a 500 MW Coal-fired Power Plant (500 MW 석탄화력발전소 촉매단추가에 따른 탈질설비 효율에 미치는 영향)

  • Lee, Sang Soo;Moon, Seung-Jae
    • Plant Journal
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    • v.17 no.1
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    • pp.58-66
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    • 2021
  • The government has recently come up with a policy to tighten regulations on air pollutant emissions due to public concerns over the emission of pollutants such as fine dust. The coal-fired power plant is speeding up the improvement of the performance of environmental facilities, and this paper deals with the cases of performance improvement by adding a catalyst to the 500 MW standard coal-fired power DeNox system, and examines the change in the performance factors according to the addition of catalysts and the efficiency of NOx removal. The DeNOx efficiency before and after improvement increased from 80% to 88%, and the conversion rate of SO2/SO3, ammonia slip which are performance factors satisfied the design assurance value, but exceeded the design assurance value for differential pressure. At the same time, the ammonia slip concentration and differential pressure items increased as the NOx removal efficiency increased, resulting in the need for management and improvement.

Change of Ammonia Consumption with Gas Turbine Output in DeNOx System for a 580 MW Combined Cycle Power Plant (580 MW급 복합발전소 탈질설비에서 가스터빈 출력에 따른 암모니아 소모량 변화)

  • Jang, Yong-Woo;Yoo, Ho-Seon
    • Plant Journal
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    • v.15 no.3
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    • pp.23-28
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    • 2019
  • In this study, ammonia consumption by gas turbine output was adjusted to find out the amount of ammonia consumption that complies with the enhanced Air Quality Preservation Act and internal regulation emission standards in SCR type DeNOx System for a 580 MW Sejong Combined Cycle Power Plant. For measurements, the gas turbine output was varied to 50, 99, 149, 198 MW and ammonia consumption was adjusted with the combustion gas and ammonia supply conditions fixed at each stage. When the emission limit were change from 10 ppm to 8 ppm, ammonia consumption was increased from 78, 93, 105, 133 kg/h to 89, 113, 132, 176 kg/h. The increase rate of ammonia consumption was 14, 22, 26, 32% per output category compared to the 10 ppm emission limit, which was shown to increase as output increased.

A Study for Optimal Design of the AIG to Improve the Performance of DeNOx Facilities Installed in Combined Cycle Plant (복합화력 탈질설비 성능향상을 위한 암모니아 주입 그리드의 최적설계 방안에 관한 연구)

  • Kim, Kwang-Chu;Park, Man-Heung;Yoon, Jun-Kyu;Lim, Jong-Han
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.19 no.12
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    • pp.811-820
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    • 2007
  • A Study on the optimal design of the AIG(Ammonia Injection Grid) to improve the performance of DeNOx facilities in the HRSG(Heat Recovery Steam Generator) was performed using the CFD analysis. On the basis of the flow analysis results in the case that the AIG in the HRSG was not installed, the numerical analyses according to the positions of AIG, injection angles of nozzle and the control of ammonia injection quantity were carried out. The standard deviation according to factors was calculated for quantitative comparison. As the results, the AIG in the HRSG should be installed in the position that the uniform flow field shows through the exact flow analysis in the previous of the AIG design and installation. In the case the AIG has already been installed and non uniform flow distribution shows, it is recommended that flow correction device or KoNOx catalyst should be used. Otherwise, the control of ammonia injection angle or the ammonia injection quantity using the velocity profile analysis is demanded to accomplish the optimal performance.

Comparison of Ammonia Mass Flow Rate between Two Ammonia Injection Positions in DeNOx system of a Horizontal HRSG (수평형 HRSG의 탈질설비에서 암모니아 분사위치 변동에 따른 암모니아 유량비교)

  • Park, Jae-Hyun;Yoo, Hoseon
    • Plant Journal
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    • v.14 no.4
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    • pp.48-54
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    • 2018
  • As the emission limits for NOx in power generation facilities were strengthened, HRSGs installed in the 1990s became necessary to install additional DeNOx system. However, since there is no space in the HRSG for installing the entire the catalyst and ammonia injection grid, as an alternative, the catalyst was installed inside of the HRSG and the ammonia injection device was installed in the exhaust duct of the gas turbine. Experiments were conducted in horizontal HRSG of Incheon combined cycle power plant. Experimental results show that the ammonia injection method in the gas turbine exhaust duct is 1.2 times higher than the HRSG internal ammonia injection method. However when operating a HRSG for 30 years as its life span, ammonia injection method in the gas turbine exhaust duct is more economical than the cost of new HRSG construction.

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