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- Mori Hideki
- Department of Applied Chemistry, Nagoya Institute of Technology
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- Ito Chikara
- Department of Applied Chemistry, Nagoya Institute of Technology
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- Oda Akiyoshi
- Department of Applied Chemistry, Nagoya Institute of Technology
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- Aragaki Tsutomu
- Department of Applied Chemistry, Nagoya Institute of Technology
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This paper presents a simulation algorithm with a rate-based model for a packed distillation column at total reflux.<BR>The proposed algorithm consists of 1) composition and temperature profile calculation, which is slightly modified from the one for steady-state continuous distillation at finite reflux, and 2) composition correction for accelerating convergence with the overall θ method based on the component material balance considering liquid hold-up within the distillation column.<BR>Simulation results are compared with the experimental results of a ternary system obtained from a 0.21 m diameter packed distillation column. Fairly good agreement is obtained, though proper evaluation of the effective interfacial area and liquid hold-up distribution is essential for better simulation.
収録刊行物
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- JOURNAL OF CHEMICAL ENGINEERING OF JAPAN
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JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 32 (1), 69-75, 1999
公益社団法人 化学工学会
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詳細情報 詳細情報について
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- CRID
- 1390282679543367296
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- NII論文ID
- 10002067116
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- NII書誌ID
- AA00709658
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- COI
- 1:CAS:528:DyaK1MXhsFyntrw%3D
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- ISSN
- 18811299
- 00219592
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- NDL書誌ID
- 4665084
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- 本文言語コード
- en
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- データソース種別
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- JaLC
- NDL
- Crossref
- CiNii Articles
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- 抄録ライセンスフラグ
- 使用不可