کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
238410 465756 2008 6 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas–solid tapered fluidized beds
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas–solid tapered fluidized beds
چکیده انگلیسی

Recently, tapered fluidized bed has become more attractive because of the problems associated with conventional (cylindrical) beds like fluidization of widely distributed particles, entrainment of particles and limitation of fluidization velocity. There have been some investigations on hydrodynamics of uniform single size particles but there have been no detailed studies of homogeneous binary mixture of particles of different sizes and different particles in tapered beds. In the present work, an attempt has been made to study the hydrodynamic characteristics of homogeneous binary mixture of irregular particles in tapered beds having different tapered angles. Correlations have been developed for important characteristics, especially critical fluidization velocities and maximum bed pressure drops of homogeneous binary mixture of irregular particles in gas–solid tapered fluidized beds. Experimental values of critical fluidization velocities and maximum bed pressure drops have been compared with the developed correlations.

In the present work, an attempt has been made to study the hydrodynamic characteristics of homogeneous binary mixture of irregular particles in tapered beds having different tapered angles. Correlations have been developed for some characteristics, especially critical fluidization velocities and maximum bed pressure drops of gas–solid tapered fluidized beds of homogeneous binary mixture of irregular particles (coal, iron ore and dolomite). Experimental values of critical fluidization velocities and maximum bed pressure drops have been compared with the developed correlations. Fairly good agreement was found to exist between the calculated and the experimental values.Experimental set-up1. Compressor. 2. Receiver. 3. Silica gel tower. 4. Bypass valve. 5. Line valve. 6. Rota meter. 7. Bed materials. 8. Fluidizer. 9. Pressure tapping to manometer.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Powder Technology - Volume 186, Issue 3, 10 September 2008, Pages 241–246
نویسندگان
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