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Operational planning of an engine generator using a high pressure working fluid composed of CO2 hydrate
https://kitami-it.repo.nii.ac.jp/records/7680
https://kitami-it.repo.nii.ac.jp/records/7680a1bd918c-9e24-4e9d-a826-473706826e94
| 名前 / ファイル | ライセンス | アクション |
|---|---|---|
No187.pdf (310.1 kB)
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| Item type | 学術雑誌論文 / Journal Article(1) | |||||
|---|---|---|---|---|---|---|
| 公開日 | 2014-09-04 | |||||
| タイトル | ||||||
| タイトル | Operational planning of an engine generator using a high pressure working fluid composed of CO2 hydrate | |||||
| 言語 | en | |||||
| 言語 | ||||||
| 言語 | eng | |||||
| キーワード | ||||||
| 主題Scheme | Other | |||||
| 主題 | CO2 hydrate | |||||
| キーワード | ||||||
| 主題Scheme | Other | |||||
| 主題 | Hydrate actuator | |||||
| キーワード | ||||||
| 主題Scheme | Other | |||||
| 主題 | Hybrid power system | |||||
| キーワード | ||||||
| 主題Scheme | Other | |||||
| 主題 | Operation planning | |||||
| キーワード | ||||||
| 主題Scheme | Other | |||||
| 主題 | Working fluid | |||||
| 資源タイプ | ||||||
| 資源タイプ識別子 | http://purl.org/coar/resource_type/c_6501 | |||||
| 資源タイプ | journal article | |||||
| アクセス権 | ||||||
| アクセス権 | open access | |||||
| アクセス権URI | http://purl.org/coar/access_right/c_abf2 | |||||
| 著者 |
Obara, Shin’ya
× Obara, Shin’ya× Yamada, Takanobu× Matsumura, Kazuhiro× Takahashi, Shiro× Kawai, Masahito× Rengarajan, Balaji |
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| 著者別名 | ||||||
| 識別子Scheme | WEKO | |||||
| 識別子 | 44843 | |||||
| 識別子Scheme | KAKEN | |||||
| 識別子URI | https://nrid.nii.ac.jp/ja/nrid/1000010342437 | |||||
| 識別子 | 10342437 | |||||
| 姓名 | 小原, 伸哉 | |||||
| 言語 | ja | |||||
| 抄録 | ||||||
| 内容記述タイプ | Abstract | |||||
| 内容記述 | An actuator system (gas-hydrate engine) using the dissociation and recombined continuous cycle of CO2 gas hydrate was developed. The heat source temperatures required for the operation of the proposed system are in the temperature range of green energy and low-quality exhaust heat. The energy flow of this proposed system was investigated by numerical analysis. From these results, for example, the entrance operating conditions of the recombination equipment are 9 °C and 1.2 MPa, and the exit conditions are 0 °C and 5 MPa. In the case of a heat source temperature of 20 °C of the recombination equipment, a heat source temperature of −5 °C of the dissociation equipment and the passing of a working fluid comprised of 1150 g/s of CO2 and H2O about 5 kW of electric power can be obtained. Moreover, although the recombined speed was remarkably slow compared with dissociation, this study considered the relation of recombined speed between the physical conditions of the working fluid and the volume of the recombination equipment. Based on the results obtained in this study, a prototype will be developed next. | |||||
| 書誌情報 |
Applied Energy 巻 88, 号 12, p. 4733-4741, 発行日 2011-12 |
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| 出版者 | ||||||
| 出版者 | Elsevier | |||||
| 著者版フラグ | ||||||
| 値 | author | |||||
| 出版タイプ | ||||||
| 出版タイプ | AM | |||||
| 出版タイプResource | http://purl.org/coar/version/c_ab4af688f83e57aa | |||||
