• Title/Summary/Keyword: 아세토젠

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Recent advances on bio-alcohol production from syngas using microorganisms (미생물을 이용한 합성가스로부터 바이오 알코올 생산 최신 동향)

  • Woo, Ji Eun;Jang, Yu-Sin
    • Journal of Applied Biological Chemistry
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    • v.60 no.4
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    • pp.333-338
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    • 2017
  • Cellulosic alcohol fermentation has recently gained more attention in the production of ethanol, butanol, and 2,3-butanediol. However, it was revealed that the process had several hurdles, such as, an expensive cost for biomass decomposition to yield fermentable sugars and a production of byproduct lignin. As an alternative for the process through biomass saccharification, the alcohol production through syngas from biomass has been studied. In this study, we reviewed acetogen and its central metabolic pathway, Wood-Ljungdahl route, capable of utilizing syngas. Furthermore, the metabolic engineering strategies of acetogen for bio-alcohol production from syngas was also reviewed with a brief perspective.

Municipal Solid Waste-derived Syngas Fermentation Process by Pressurization (가압을 통한 도시형 생활 폐기물 기반 합성가스발효 공정 개발)

  • Subin Shin;Jae Hee Go;Myounghoon Moon;Min-Sik Kim;Mungyu Lee;In Seop Chang;Seongsoo Son;Gwon Woo Park
    • New & Renewable Energy
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    • v.19 no.4
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    • pp.35-45
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    • 2023
  • Global efforts are focused on achieving carbon neutrality due to the increases in the levels of greenhouse gases. Moreover, the greenhouse gases generated from the disposal of municipal solid waste (MSW) are the primary sources of emissions in South Korea. In this study, we conducted the biological conversion of syngas (CO, H2, and CO2) generated from MSW gasification. The MSW-derived syngas was used as a feed source for cultivating Eubacterium limosum KIST612, and pressurization was employed to enhance gas solubility in culture broth. However, the pH of the medium decreased owing to the pressurization because of the CO2 in the syngas and the cultivation-associated organic acid production. The replacement of conventional HEPES buffer with a phosphate buffer led to an approximately 2.5-fold increase in acetic acid concentration. Furthermore, compared with the control group, the pressurized reactor exhibited a maximum 8.28-fold increase in the CO consumption rate and a 3.8-fold increase in the H2 consumption rate.