کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
620370 1455168 2015 9 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Optimum solids concentration for solids suspension and solid–liquid mass transfer in agitated vessels
ترجمه فارسی عنوان
غلظت جامدات مطلوب برای جابجایی جامدات و انتقال جرم مایع به حلال در مخازن مخلوط
کلمات کلیدی
انتقال جامد مایع، تعلیق جامد، انجماد بهره وری انرژی پروانه
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی تصفیه و جداسازی
چکیده انگلیسی


• Solid–liquid mass transfer was studied at high solids concentrations.
• Specific impeller power consumption is the lowest for solids concentration of 0.2 (v/v).
• Solid–liquid mass transfer coefficient (kSL) is the highest between solids concentration of 0.15 and 0.20 (v/v).
• A mathematical correlation is proposed to estimate kSL with increasing solids concentration.

SummaryThe effect of solids concentration on specific impeller power consumption and solid–liquid mass transfer coefficient was investigated in a 0.2 m diameter baffled agitated vessel with standard six-bladed Rushton turbine for solids concentration up to 0.40 (v/v). It was found that the increase of solids concentration significantly increases the mass transfer coefficient up to an optimum solids concentration and decreases thereafter when the system is operated at a just-suspended condition. The increase in mass transfer coefficient with an increase of solid concentrations is mainly due to the increase in Njs (critical impeller speed) with increasing solids concentration, thereby leading to an upsurge of turbulence around the particles. The solids concentration at which the highest mass transfer coefficient is obtained is designated as the effective solids concentration. In a geometrically similar 0.3 m diameter tank, the trends in impeller energy efficiency and solid–liquid mass transfer coefficient values with increasing solids concentration are similar. The experimental data are satisfactorily correlated using the concept of the Kolmogoroff's theory of isotropic turbulence to develop an equation to estimate the solid–liquid mass transfer coefficient in agitated vessels.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Chemical Engineering Research and Design - Volume 100, August 2015, Pages 148–156
نویسندگان
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