• Title/Summary/Keyword: 석탄 가스화 복합발전시스템

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A Study on the Demonstration of Yellow Plume Elimination System from Combined Cycle Power Plant Using Liquid Injection System (액상 직분사 시스템을 이용한 복합화력 황연제거 실증 연구)

  • Lee, Seung-Jae;Kim, Younghee
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.21 no.10
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    • pp.317-324
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    • 2020
  • Combined cycle power plants (CCPP) that use natural gas as fuel are easier to start and stop, and have lower pollutant emissions, so their share of domestic power generation facilities is steadily increasing. However, CCPP have a high concentration of nitrogen dioxide (NO2) emission in the initial start-up and low-load operation region, which causes yellow plume and civil complaints. As a control technology, the yellow plume reduction system was developed and operated from the mid-2000s. However, this technology was unable to control the phenomenon due to insufficient preheating of the vaporization system for 10 to 20 minutes of the initial start-up. In this study, CFD analysis and demonstration tests were performed to derive a control technology by injecting a reducing agent directly into the gas turbine exhaust duct. CFD analysis was performed by classifying into 5 cases according to the exhaust gas condition. The RMS values of all cases were less than 15%, showing a good mixing. Based on this, the installation and testing of the demonstration facilities facilitated complete control of the yellow plume phenomenon in the initial start-up.

A Study on Reaction Characteristics of Fe$_2$O$_3$High-Temperature Desulfurization Sorbents (Fe$_2$O$_3$계 고온건식탈황제의 반응특성 연구)

  • Kang, Suk-Hwan;Rhee, Young-Woo;Kang, Yong;Han, Keun-Hee;Yi, Chang-Keun;Jin, Gyoung-Tae;Son, Jae-Ek;Park, Yeong-Seong
    • Journal of Energy Engineering
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    • v.5 no.2
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    • pp.123-130
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    • 1996
  • Reduction, sulfidation, and regeneration reactions were performed using domestic and Australian iron ore in order to develop a desulfurizing sorbent for the high temperature desulfurization process that is one of major processes in the integrated coal gasification combined cycle (IGCC) system. A TGA (Thermogravimetric Analysis) reactor and a fixed-bed reactor were used. Some basic kinetic information was obtained from BET surface area measurements, SEM photos, cyclic reactions, reaction temperature changes and TGA curves of the sorbents. The rates of both desulfurization and regeneration increased with increasing reaction temperature in the range of 500-700$^{\circ}C$.

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