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  1. AU="Nguyen Nhut M."
  2. AU="Rusiecki, Jennifer"
  3. AU="Savarese, Beatrice"
  4. AU="Tian, Zhan-Ping"
  5. AU="Liying Xia"
  6. AU="Lipfert, Jan"
  7. AU="Sauchuk, Alina L"
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  13. AU="Hufert, F T" AU="Hufert, F T"
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  15. AU="Hinchliffe, Rod F" AU="Hinchliffe, Rod F"
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  17. AU="Kurskoy Аndrey Yu."
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  19. AU="Haustraete, Eglantine"
  20. AU="Li, Ziying"
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  22. AU="Gleeson, Sarah"
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  28. AU=Andrade D M
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  37. AU="Chang, Hanxuan" AU="Chang, Hanxuan"
  38. AU="Bellamy, Kyle" AU="Bellamy, Kyle"
  39. AU="Jensen, Kara L"
  40. AU=Wang Yun
  41. AU=Seimiya H
  42. AU="Victor Babos, Diego"
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  44. AU="Nackers, Elke"
  45. AU=Grobler Chistine
  46. AU="Norman H. L. Chiu"
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  48. AU="Scott Nugent"
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  50. AU="Wang, Zhaoqi"

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  1. Artikel: Chemical looping gasification of torrefied woodchips in a bubbling fluidized bed test rig using iron-based oxygen carriers

    Nguyen, Nhut M. / Alobaid, Falah / Epple, Bernd

    Renewable energy. 2021 July, v. 172

    2021  

    Abstract: Chemical looping gasification is an efficient technology to convert biomass into valuable syngas. The iron-based oxygen carriers are a promising option for large-scale commercial applications due to their low cost and environmentally-friendly properties. ...

    Abstract Chemical looping gasification is an efficient technology to convert biomass into valuable syngas. The iron-based oxygen carriers are a promising option for large-scale commercial applications due to their low cost and environmentally-friendly properties. The present study aims at evaluating the performance of the syngas production from the chemical looping gasification of torrefied woodchips in a pilot-scale bubbling fluidized bed reactor using iron ore and ilmenite as oxygen carriers. The effects of the operating parameters were investigated in this study. The results show that an increase in operating parameters could favor the process performance. Carbon conversion efficiency and the yields accelerate at high operating conditions. Carbon conversion efficiency showed a maximum value of 91.42% for iron ore at the ratio of oxygen carrier-to-biomass of 6, while the gas yield reaches the peak at SBR of 1.4 for ilmenite. The addition of steam in biomass chemical looping gasification improves hydrogen production and syngas quality in the product gas. Despite ilmenite provides better performance for hydrogen production, it characterizes by a lower reactivity compared to iron ore. It is also found that iron ore performs better at lower values of steam-to-biomass ratios and temperatures, while ilmenite shows good results at higher those parameters.
    Schlagwörter biomass ; carbon ; fluidized beds ; gasification ; hydrogen production ; oxygen ; renewable energy sources ; steam ; synthesis gas ; wood chips
    Sprache Englisch
    Erscheinungsverlauf 2021-07
    Umfang p. 34-45.
    Erscheinungsort Elsevier Ltd
    Dokumenttyp Artikel
    ZDB-ID 2001449-1
    ISSN 1879-0682 ; 0960-1481
    ISSN (online) 1879-0682
    ISSN 0960-1481
    DOI 10.1016/j.renene.2021.03.006
    Datenquelle NAL Katalog (AGRICOLA)

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  2. Artikel ; Online: Removal efficiency of dibenzofuran using CuZn-zeolitic imidazole frameworks as a catalyst and adsorbent

    Nguyen Thanh Q. C. / Tran Huy B. / Nguyen Nghia K. / Nguyen Nhut M. / Dang Giao H.

    Green Processing and Synthesis, Vol 12, Iss 1, Pp 251-

    2023  Band 61

    Schlagwörter adsorption ; bimetallic ; catalyst ; dibenzofuran ; zeolitic imidazolate framework ; Chemistry ; QD1-999
    Sprache Englisch
    Erscheinungsdatum 2023-01-01T00:00:00Z
    Verlag De Gruyter
    Dokumenttyp Artikel ; Online
    Datenquelle BASE - Bielefeld Academic Search Engine (Lebenswissenschaftliche Auswahl)

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