Heat Transfer in a Fluidized Bed with Immersed Tubes Using Moist Coal Particles

被引:2
作者
Yang, Dongwei [1 ]
Yu, Hongling [1 ]
Li, Ruiyang [1 ]
机构
[1] Univ Shanghai Sci & Technol, Sch Energy & Power Engn, Dept Thermal Engn, Shanghai 200093, Peoples R China
关键词
Heat transfer; Moisture content; Fluidized beds; Angle of repose; CMC; Packet renewal model; HORIZONTAL TUBE; REPOSE; ANGLE; GELDART; BUNDLE;
D O I
10.1007/s13369-017-2680-2
中图分类号
O [数理科学和化学]; P [天文学、地球科学]; Q [生物科学]; N [自然科学总论];
学科分类号
07 ; 0710 ; 09 ;
摘要
The moisture content of coal (MCC) has an important effect on the thermophysical properties and the granular flowability. However, it brings both active and negative influence to the heat transfer between the fluidizing moist coal and the immersed tubes in the fluidized bed. Four groups of bituminous coal with same size distribution (0.25-2.8 mm) but different MCC (7.86-15.18%) have been examined to study the variation of the heat transfer in an experimental setup. The average heat transfer coefficients for the four groups of test samples have the same changing trend by increasing the superficial velocity . However, the maximum heat transfer coefficients display different peak values. With the increase in MCC, the rises at first and begins to fall when reaching a critical value. To predict the accurately with different MCC, the angle of repose has been imported to measure the variation of the granular flowability. A novel semiempirical correlation has been thereupon proposed by the dimensional analysis, and it accords well to the experimental data from this study and the previous research.
引用
收藏
页码:2263 / 2272
页数:10
相关论文
共 35 条
[1]  
[Anonymous], 2009, PRINCIPLES GAS SOLID, DOI DOI 10.1017/CBO9780511530142
[2]   HEAT-TRANSFER TO OBJECTS IMMERSED IN FLUIDIZED-BEDS [J].
BASKAKOV, AP ;
BERG, BV ;
VITT, OK ;
FILIPPOV.NF ;
KIRAKOSY.VA ;
GOLDOBIN, JM ;
MASKAEV, VK .
POWDER TECHNOLOGY, 1973, 8 (5-6) :273-282
[3]  
Cain J., 2002, Powder Handling Processing, V14, P218
[4]   Fluidization of moist sawdust in binary particle systems in a gas-solid fluidized bed [J].
Clarke, KL ;
Pugsley, T ;
Hill, GA .
CHEMICAL ENGINEERING SCIENCE, 2005, 60 (24) :6909-6918
[5]   Effects of coal moisture control and coal briquette technology on structure and reactivity of cokes [J].
Cui P. ;
Qu K.-L. ;
Ling Q. ;
Cheng L.-Y. ;
Cao Y.-P. .
Coke and Chemistry, 2015, 58 (05) :162-169
[6]   Coal Blend Moisture-A Boon or Bane in Cokemaking? [J].
Das, S. K. ;
Nandy, A. S. ;
Paul, A. ;
Sahoo, B. K. ;
Chakraborty, B. ;
Das, A. .
COKE AND CHEMISTRY, 2013, 56 (04) :126-136
[7]   A single particle model for surface-to-bed heat transfer in fluidized beds [J].
Di Natale, Francesco ;
Lancia, Amedeo ;
Nigro, Roberto .
POWDER TECHNOLOGY, 2008, 187 (01) :68-78
[8]   Heat transfer and void fraction profiles around a horizontal cylinder immersed in a bubbling fluidised bed [J].
Di Natale, Francesco ;
Bareschino, Piero ;
Nigro, Roberto .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2010, 53 (17-18) :3525-3532
[9]   Flowability of moist pharmaceutical powders [J].
Emery, Erica ;
Oliver, Jasmine ;
Pugsley, Todd ;
Sharma, Jitendra ;
Zhou, Joe .
POWDER TECHNOLOGY, 2009, 189 (03) :409-415
[10]   A MECHANISTIC THEORY FOR HEAT-TRANSFER BETWEEN FLUIDIZED-BEDS OF LARGE PARTICLES AND IMMERSED SURFACES [J].
GANZHA, VL ;
UPADHYAY, SN ;
SAXENA, SC .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1982, 25 (10) :1531-1540