• Title/Summary/Keyword: Oxy combustion

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Operational Characteristics of a Dry Electrostatic Precipitator for Removal of Particles from Oxy Fuel Combustion (순산소 연소 배출 입자 제거용 건식 전기집진장치 운전 특성)

  • Kim, Hak-Joon;Han, Bang-Woo;Oh, Won-Seok;Hwang, Gyu-Dong;Kim, Yong-Jin;Hong, Jeong-Hee
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.34 no.1
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    • pp.27-34
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    • 2010
  • In a test duct with closed configuration, particle removal performance of an edge-plate type electrostatic precipitator (ESP) was evaluated at a high flow rate in $CO_2$ rich environments by changing gap distances between collection plates, concentrations of $CO_2$, particle sizes, types of electrodes, and types of power supplies. At the same experimental conditions, collection efficiency of particles with the mean particle size, 300 nm, decreased as the gap distance and $CO_2$ concentration increased because of low electrostatic force and low discharged current. In addition, as the particle size increased, the efficiency increased because of high charging rate of the large particles. With the electrode type which has higher surface area of a discharging plate and with the power supply which applied 25 kHz-pulsed DC voltages, the removal efficiency was high even in rich $CO_2$ condition due to high electrostatic force at the same power consumption.

Process Design of Carbon Dioxide Storage in the Marine Geological Structure: II. Effect of Thermodynamic Equations of State on Compression and Transport Process (이산화탄소 해양지중저장 처리를 위한 공정 설계: II. 열역학 상태방정식이 압축 및 수송 공정에 미치는 영향 평가)

  • Huh, Cheol;Kang, Seong-Gil
    • Journal of the Korean Society for Marine Environment & Energy
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    • v.11 no.4
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    • pp.191-198
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    • 2008
  • To design a reliable $CO_2$ marine geological storage system, it is necessary to perform numerical process simulation using thermodynamic equation of state. $CO_2$ capture process from the major point sources such as power plants, transport process from the capture sites to storage sites and storage process to inject $CO_2$ into the deep marine geological structure can be simulate with numerical modeling. The purpose of this paper is to compare and analyse the relevant equations of state including ideal, BWRS, PR, PRBM and SRK equation of state. We also studied the effect of thermodynamic equation of state in designing the compression and transport process. As a results of comparison of numerical calculations, all relevant equation of state excluding ideal equation of state showed similar compression behavior in pure $CO_2$. On the other hand, calculation results of BWRS, PR and PRBM showed totally different behavior in compression and transport process of captured $CO_2$ mixture from the oxy-fuel combustion coal-fired plants. It is recommended to use PR or PRBM in designing of compression and transport process of $CO_2$ mixture containing NO, Ar and $O_2$.

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Experimental Study of Char Oxidation and Kinetic Rate in O2/CO2 and O2/N2 Environments (O2/CO2조건과 O2/N2조건에서의 촤 연소특성 및 산화 반응성에 관한 실험적 연구)

  • Kim, Song-Gon;Lee, Cheon-Seong;Lee, Byoung-Hwa;Song, Ju-Hun;Chang, Young-June;Jeon, Chung-Hwan
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.34 no.12
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    • pp.1101-1109
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    • 2010
  • We investigated the combustion rate and kinetic rate of char when burning in oxygen-enriched atmospheres with either an $N_2$ or $CO_2$ bath gas in a drop tube furnace. The experiments were performed with sub-bituminous coal (Adaro) and bituminous coal (Coal valley) under atmospheric pressure conditions. Two different coals were investigated over 12 to 30 vol% oxygen and furnace temperatures of 900, 1100, and $1300^{\circ}C$. For both coals, the particle temperature and overall reaction rate are lower in the $CO_2$ bath gas. However, analysis of single-particle data shows that the surface-specific burning rate of char oxidation is similar in both gases. In addition, the kinetic rate and activation energy for each coal were similar for both gases. Generally, the particle temperature and overall reaction rate of sub-bituminous coal are higher than those of bituminous coal.

Comparative Study of Char Burn-Out and NOx Emissions in O2/N2 and O2/CO2 environments (순산소 분위기에서 촤 연소 및 질소산화물 배기특성 비교)

  • Lee, Chun-Sung;Kim, Seong-Gon;Lee, Byoung-Hwa;Chang, Young-June;Jeon, Chung-Hwan;Song, Ju-Hun
    • Journal of Energy Engineering
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    • v.20 no.3
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    • pp.191-199
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    • 2011
  • The char burn-out and NOx emissions from sub-bituminous coal were investigated in drop tube furnace under $O_2/N_2$ and $O_2/CO_2$ environments with different $O_2$ concentrations of 12, 21 and 31%. Results show that the char burn-out rate is faster as $O_2$ concentration increases higher and char burn-out rate under $O_2/CO_2$ decreases due to the lower oxygen diffusion into coal surface through the $CO_2$ rich boundary layer. NO concentration increases with increasing $O_2$ concentration, but declines at $O_2$ concentration of 31%. Meanwhile, NO emission indexes decreases monotonically with increasing $O_2$ concentration, which indicates that more NO reduction occurs with higher $O_2$ concentration probably due to greater HCN formation. For all conditions of $O_2$ concentration, the NO concentration under $O_2/N_2$ maintains higher than those of $O_2/CO_2$ due to presence of thermal NO.