• Title/Summary/Keyword: 탈질 설비

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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 on the Economic Analysis of Low-Temperature SCR Technology for NOx Reduction by Scenarios (배연탈질을 위한 저온 SCR 기술 도입에 따른 시나리오별 경제성 분석)

  • Hong, Sungjun;Lee, Youah;Jeong, Soonkwan
    • Journal of Energy Engineering
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    • v.29 no.2
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    • pp.10-22
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    • 2020
  • As the national demand for solving the fine dust problem has increased, the government has announced intensive measures to deal with fine dust. So recently, selective catalytic reduction(SCR) has attracted attention as a technology for removing nitrogen oxides from precursors of fine dust. In this study, the government's policies related to fine dust and the current status of market and R&D were investigated, and economic analysis by scenarios was conducted by dividing cases where SCR technology was applied to industries. The results of economic analysis for each scenario were calculated using NPV, and companies with no denitrification facilities(Case 1) introduced general SCR technologies(Scenario 1-1) and low-temperature SCR technologies(Scenario 1-2). In addition, companies that have already installed denitrification facilities(Case 2) analyzed the two categories, using the general SCR technology as it is(Scenario 2-1) and replacing it with low-temperature SCR technology(Scenario 2-2). Comparative analysis was performed based on the results of each NPV.