Fluidization characteristics of oil palm frond particles in agitated bed

被引:14
作者
Puspasari, Ifa [1 ]
Talib, Meor Zainal Meor [1 ]
Daud, Wan Ramli Wan [1 ]
Tasirin, Siti Masrinda [1 ]
机构
[1] Univ Kebangsaan Malaysia, Fac Engn & Built Environm, Dept Chem & Proc Engn, Ukm Bangi 43600, Selangor Darul, Malaysia
关键词
Agitated fluidized bed; Fibres; Hydrodynamics; Incipient fluidization; Minimum fluidization velocity; Stirred fluidized bed; HEAT-TRANSFER CHARACTERISTICS; COHESIVE POWDERS; PRESSURE-DROP; FINE POWDERS; MINIMUM; VELOCITY; BEHAVIOR; SYSTEMS; DRYER; HYDRODYNAMICS;
D O I
10.1016/j.cherd.2012.08.018
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluidization characteristics of crushed oil palm fronds were studied. The elongated shape of the particles and their fibrous nature created entanglement between the particles and caused the bed to form crack and plug flow when aerated in ordinary fluidized bed. Fluidization of the fibres became feasible with the aid of mechanical agitation. Agitation helped to loosen the entanglement of the fibres which prevents air to pass through the bed of particles, as a result, fluidization state could be attained. Experiments were carried out in a column with height of 72 cm and ID of 14.4 cm. Superficial air velocities used ranged from 0.1 to 1.1 m/s, bed heights ranged from 4 to 8.5 cm, agitation speeds ranged from 300 to 500 rpm and particle initial moisture contents from 0.5 to 2.4 gwater/g dry solids. Analysis of the fluidization characteristics showed that minimum fluidization velocity was independent with bed height and agitation speed. However, investigation on the effect of particle initial moisture content showed that minimum fluidization velocity increased with particle moisture content. A new empirical correlation to predict minimum fluidization velocity has been derived which gives good agreement with experimental data in this study and the data from other study in the literature. (C) 2012 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:497 / 507
页数:11
相关论文
共 45 条
[41]   Minimum fluidization velocity at elevated temperatures for Geldart's group-B powders [J].
Subramani, Hariprasad J. ;
Balaiyya, M. B. Mothivel ;
Miranda, Lima Rose .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 2007, 32 (01) :166-173
[42]   Fluidization behavior of vibrated and aerated beds of starch powders [J].
Tasirin, SM ;
Anuar, N .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2001, 34 (10) :1251-1258
[43]   HYDRODYNAMIC AND HEAT-TRANSFER CHARACTERISTICS OF LARGE AGRICULTURAL SEEDS AIR FLUIDIZED-BEDS [J].
VERMA, RS ;
SAXENA, SC .
POWDER TECHNOLOGY, 1984, 39 (02) :245-248
[44]   Drying of granules in agitation fluidized bed [J].
Watano, S ;
Yeh, N ;
Miyanami, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1998, 31 (06) :908-913
[45]   A GENERALIZED METHOD FOR PREDICTING MINIMUM FLUIDIZATION VELOCITY [J].
WEN, CY ;
YU, YH .
AICHE JOURNAL, 1966, 12 (03) :610-&