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Hydrocarbon Fuel Production from Lignocellulosic Biomass by Solvolysis and Catalytic Cracking
http://hdl.handle.net/10091/00021874
http://hdl.handle.net/10091/00021874178f61a7-5de0-4a9b-ac23-39cba982a5e0
名前 / ファイル | ライセンス | アクション |
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15K21038_01.pdf (874.6 kB)
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Item type | 学術雑誌論文 / Journal Article(1) | |||||
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公開日 | 2020-02-28 | |||||
タイトル | ||||||
言語 | en | |||||
タイトル | Hydrocarbon Fuel Production from Lignocellulosic Biomass by Solvolysis and Catalytic Cracking | |||||
言語 | ||||||
言語 | eng | |||||
DOI | ||||||
識別子タイプ | DOI | |||||
関連識別子 | https://doi.org/10.1627/jpi.61.302 | |||||
関連名称 | 10.1627/jpi.61.302 | |||||
キーワード | ||||||
主題 | Lignocellulosic biomass, Solvolysis, Catalytic cracking, Hydrogen transfer, Deoxygenation, Renewable fuel | |||||
資源タイプ | ||||||
資源 | http://purl.org/coar/resource_type/c_6501 | |||||
タイプ | journal article | |||||
著者 |
Shimada, Iori
× Shimada, Iori× Kobayashi, Yutaka× Ohta, Haruhisa× Suzuki, Kengo× Takatsuka, Toru |
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信州大学研究者総覧へのリンク | ||||||
氏名 | Shimada, Iori | |||||
URL | http://soar-rd.shinshu-u.ac.jp/profile/ja.gFcVjFkV.html | |||||
出版者 | ||||||
出版者 | JAPAN PETROLEUM INST | |||||
引用 | ||||||
内容記述タイプ | Other | |||||
内容記述 | JOURNAL OF THE JAPAN PETROLEUM INSTITUTE.61(5):302-310(2018) | |||||
書誌情報 |
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE 巻 61, 号 5, p. 302-310, 発行日 2018-09-01 |
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抄録 | ||||||
内容記述タイプ | Abstract | |||||
内容記述 | Utilization of lignocellulosic biomass for alternative fuels requires efficient and low-cost processes for deoxygenation and conversion to hydrocarbons. We propose a 2-step biomass conversion process consisting of solvolysis pretreatment and co-processing with heavy petroleum oil in catalytic cracking. High liquefied yield (> 90 C%) was achieved by solvolysis in guaiacol and water with acetic acid catalysts. Bio-oil was mainly converted to gaseous hydrocarbons and coke by co-processing with model heavy oil (n-eicosane). Deoxygenation pathway to H2O formation was accelerated by enhancing hydrogen-transfer activity even without supplying hydrogen. Hydrogen-transfer deoxygenation proceeded preferentially to olefin hydrogenation. Consequently, enhancing hydrogen-transfer activity in the co-processing of bio-oil and heavy petroleum oil was effective for efficient deoxygenation without lowering octane rating. | |||||
資源タイプ(コンテンツの種類) | ||||||
内容記述タイプ | Other | |||||
内容記述 | Article | |||||
ISSN | ||||||
収録物識別子タイプ | ISSN | |||||
収録物識別子 | 1346-8804 | |||||
書誌レコードID | ||||||
収録物識別子タイプ | NCID | |||||
収録物識別子 | AA11590615 | |||||
権利 | ||||||
権利情報 | © 2018 by The Japan Petroleum Institute | |||||
出版タイプ | ||||||
出版タイプ | VoR | |||||
出版タイプResource | http://purl.org/coar/version/c_970fb48d4fbd8a85 | |||||
WoS | ||||||
表示名 | Web of Science | |||||
URL | http://gateway.isiknowledge.com/gateway/Gateway.cgi?&GWVersion=2&SrcAuth=ShinshuUniv&SrcApp=ShinshuUniv&DestLinkType=FullRecord&DestApp=WOS&KeyUT=000448635000010 |