Batch and continuous fluidised bed drying of granular cellular materials has been experimentally investigated at different temperatures and flow rates of the heating medium, particle size and mass of solids. A receding core model is proposed for the drying kinetics and compared with the experimental data. Assuming ideal mixing for the solids, the performance of the continuous fluidised bed dryer is predicted using the drying kinetics evaluated from the batch fluidised bed.
机构:
Dept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, ChinaDept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, China
Ma, J.H.
Liu, H.
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Dept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, ChinaDept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, China
Liu, H.
Feng, D.Z.
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Dept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, ChinaDept. of Air-Condition Eng., Shandong Inst. of Civil Eng., Jinan 250014, China
机构:
Moscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSRMoscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSR
Sazhin, V.B.
Oygenblik, A.A.
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Moscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSRMoscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSR
Oygenblik, A.A.
Dorokhov, I.N.
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Moscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSRMoscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSR
Dorokhov, I.N.
Kafarov, V.V.
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Moscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSRMoscow Inst of Chemical Engineering, USSR, Moscow Inst of Chemical Engineering, USSR