English  |  正體中文  |  简体中文  |  全文筆數/總筆數 : 56816/90588 (63%)
造訪人次 : 12104763      線上人數 : 58
RC Version 7.0 © Powered By DSPACE, MIT. Enhanced by NTU Library & TKU Library IR team.
搜尋範圍 查詢小技巧:
  • 您可在西文檢索詞彙前後加上"雙引號",以獲取較精準的檢索結果
  • 若欲以作者姓名搜尋,建議至進階搜尋限定作者欄位,可獲得較完整資料
  • 進階搜尋
    請使用永久網址來引用或連結此文件: http://tkuir.lib.tku.edu.tw:8080/dspace/handle/987654321/71732


    題名: Mass Transfer for Dialysis with Ultrafiltration Flux Declined in Cross-Flow Membrane Modules
    作者: Yeh, Ho-ming;Cheng, Tung-wen;Chen, Y. J.
    貢獻者: 淡江大學化學工程與材料工程學系
    關鍵詞: Dialysis;Ultrafiltration;Cross Flow;Membrane Separation
    日期: 2000-06
    上傳時間: 2011-10-24 01:36:03 (UTC+8)
    出版者: The Society of Chemical Engineers, Japan
    摘要: This study deals with the effect of an exponential-decay flux of ultrafiltration on the mass transfer rate of solute for dialysis in cross-flow membrane modules. The numerical method of orthogonal collocation was used to solve this problem. The calculated results of solute concentrations and separation efficiencies were analyzed under various operating conditions and decay coefficients of flux in ultrafiltration. The mass transfer rate is usually enhanced by the addition of the effect of ultrafiltration, but this effect decreases as the decay coefficient increases. A significant influence of the decay coefficient on the mass transfer rate appears when the solute transport is dominated by the effect of ultrafiltration, i.e. the conditions of lower dialysate flow rate, lower solute sieving coefficient, or lower overall mass transfer coefficient.
    關聯: Journal of chemical engineering of Japan 33(3), pp.440-448
    DOI: 10.1252/jcej.33.440
    顯示於類別:[化學工程與材料工程學系暨研究所] 期刊論文

    文件中的檔案:

    沒有與此文件相關的檔案.

    在機構典藏中所有的資料項目都受到原著作權保護.

    TAIR相關文章

    DSpace Software Copyright © 2002-2004  MIT &  Hewlett-Packard  /   Enhanced by   NTU Library & TKU Library IR teams. Copyright ©   - 回饋