• Title/Summary/Keyword: 개질 바이오 황

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Effect of Bio-Sulfur Modified by Slaked Lime on Cement Hydration Properties (소석회에 의해 개질된 바이오 황이 시멘트 수화 특성에 미치는 영향)

  • Woong-Geol Lee;Lae-Bong Han;Sung-Hyun Cho;Pyeong-Su Lee;Myong-Shin Song
    • Journal of the Korean Recycled Construction Resources Institute
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    • v.11 no.4
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    • pp.509-516
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    • 2023
  • The use of sulfur(S) in concrete has been variously studied as a way to improve salt resistance in concrete. However, sulfur is a solid material and is difficult to powder, which has disadvantages in its usability as an admixture or mixture for cement and concrete. For these problem, polymers such as dicyclopentadiene have been used to modify sulfur, but this also exists in a sticky state after modifying and does not improve the fundamental problem. So, reforming sulfur with slaked lime and the effect on cement hydration was examined by reforming sulfur with slaked lime, and the following conclusions were obtained. Depending on the reaction conditions, slaked lime modified bio-sulfur exists in a slurry state containing unreacted sulfur, unreacted slaked lime, calcium-sulfur(Ca-S) compounds and water. When slaked lime modified bio-sulfur is used as a cement mixture, salt resistance of concrete with slaked lime modified bio-sulfur is to be superior to that of plain concrete. This is believed to be because structure of cement hydrates with slaked lime modified bio-sulfur is to be more dense to that of plain cement hydrates by the continued presence of ettringite and can be used as a cement mixture in concrete.

Operation Characteristics of a Plasma Reformer for Biogas Direct Reforming (바이오가스 직접 개질을 위한 플라즈마 수소 추출기 운전 특성 연구)

  • Byungjin Lee;Subeen Wi;Dongkyu Lee;Sangyeon Hwang;Hyoungwoon Song
    • Applied Chemistry for Engineering
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    • v.34 no.4
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    • pp.404-411
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    • 2023
  • For the direct reforming of biogas, a three-phase gliding arc plasma reformer was designed to expand the plasma discharge region, and the operation conditions of the plasma reformer, such as the S/C ratio, the gas flow rate, and the plasma input power, were optimized. The H2 production efficiency is increased at a lower specific plasma input energy density, but byproducts such as CXHY and carbon soot are generated along with the increase in H2 production efficiency. The formation of byproducts is decreased at higher specific plasma input energy densities and S/C ratios. The optimized operation conditions are 5.5 ~ 6.0 kJ/L for the specific plasma input energy density and 3 for the S/C ratio, considering the conversion efficiency, H2 production, and byproduct formation. It is expected that the H2 production efficiency will improve with the decrease in fuel consumption in biogas burners because the heat generated from plasma discharge heats up the feed gas to over 500 ℃.