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  1. 紀要VISIO
  2. 第31号

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/10.15005/00000142
0020de43-ffaf-43dd-b2e1-1dc5e2b3a627
名前 / ファイル ライセンス アクション
klcVISIO031033.pdf klcVISIO031033 (733.2 kB)
Item type 紀要論文 / Departmental Bulletin Paper(1)
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

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
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
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