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Patel-Teja 式による新規冷媒物質の気液平衡
https://doi.org/10.15005/00000142
https://doi.org/10.15005/000001420020de43-ffaf-43dd-b2e1-1dc5e2b3a627
名前 / ファイル | ライセンス | アクション |
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Item type | 紀要論文 / Departmental Bulletin Paper(1) | |||||||
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公開日 | 2013-01-31 | |||||||
タイトル | ||||||||
タイトル | Patel-Teja 式による新規冷媒物質の気液平衡 | |||||||
タイトル | ||||||||
タイトル | Vapor-liquid Equilibrium Computed Using the Patel-Peja Equation of State for Alternative Refrigerants | |||||||
言語 | en | |||||||
言語 | ||||||||
言語 | jpn | |||||||
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 | departmental bulletin paper | |||||||
著者 |
赤坂, 亮
× 赤坂, 亮
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著者別名 | ||||||||
姓名 | Akasaka, Ryo | |||||||
抄録 | ||||||||
内容記述タイプ | Abstract | |||||||
内容記述 | The vapor-liquid equilibrium (VLE) of alternative refrigerants was computed using the Patel-Teja (PT) equation of state, and its validity was examined. The equation of state has three parameters, and the third parameter is introduced to lessen a failure of two-parameter equations of state in a prediction of liquid density. Expressions of fugacity, residual enthalpy, and residual entropy were derived first. It was confirmed that the PT equation of state yielded reasonably accurate predictions of saturation properties for the pure substance of alternative refrigerants. Relative errors of the predictions from the formula or the correlation developed exclusivelry for the pure substances were less than 4 percent. In a prediction of the VLE for the mixtures, values obtained from the PT equation of state showed a good agreement with actual measurements. The maximum relative error of equilibrium composition or bubble-point pressure was about 2 percent. It was concluded that the PT equation of state can represent the VLE of alternative refrigerants and their mixtures with sufficient accuracy. | |||||||
内容記述 | ||||||||
内容記述タイプ | Other | |||||||
内容記述 | The vapor-liquid equilibrium (VLE) of alternative refrigerants was computed using the Patel-Teja (PT) equation of state, and its validity was examined. The equation of state has three parameters, and the third parameter is introduced to lessen a failure of two-parameter equations of state in a prediction of liquid density. Expressions of fugacity, residual enthalpy, and residual entropy were derived first. It was confirmed that the PT equation of state yielded reasonably accurate predictions of saturation properties for the pure substance of alternative refrigerants. Relative errors of the predictions from the formula or the correlation developed exclusivelry for the pure substances were less than 4 percent. In a prediction of the VLE for the mixtures, values obtained from the PT equation of state showed a good agreement with actual measurements. The maximum relative error of equilibrium composition or bubble-point pressure was about 2 percent. It was concluded that the PT equation of state can represent the VLE of alternative refrigerants and their mixtures with sufficient accuracy. | |||||||
書誌情報 |
紀要visio : research reports Visio 巻 31, p. 33-48, 発行日 2004-07-31 |
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出版者 | ||||||||
出版者 | 九州ルーテル学院大学 | |||||||
ISSN | ||||||||
収録物識別子タイプ | ISSN | |||||||
収録物識別子 | 13432133 |