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清华大学学报(自然科学版)  2014, Vol. 54 Issue (6): 775-780    
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重质大颗粒在非均匀布风流化床内停留时间
蔡容容,张衍国(),蒙晨玮,李清海,蒙爱红
Residence time of a large heavy object in a fluidized bed with an uneven air distribution
Rongrong CAI,Yanguo ZHANG(),Chenwei MENG,Qinghai LI,Aihong MENG
Department of Thermal Engineering, Tsinghua University, Beijing 100084, China
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摘要 

用电容层析成像(ECT)示踪法研究了单个球形重质大颗粒在流化床密相区的停留时间分布特性及随流化风速变化时运动状态的演化过程。 通过对实验结果的概率统计分析和对大颗粒受力特征的分析,揭示了大颗粒在床内运动行为的统计规律性和随机性。研究发现: 大颗粒在床内的平均停留时间随流化风速的降低先缓慢增大,当流化风速低于某一临界值后,停留时间急剧增大,并过渡到以一定的概率到达布风板低侧,直至最终滞留在床中间; 大颗粒密度越大,演变过程对应的流化风速越大。由于周围两相流压力场、速度场随时间的随机脉动性,大颗粒在床内的停留时间分布很宽。

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关键词 流化床重质大颗粒停留时间非均匀布风概率分布    
Abstract

The influence of the superficial gas velocity on the residence time distributions (RTDs) of large spherical objects of different densities in the dense phase of a fluidized bed was studied using electrical capacitance tomography (ECT) tracing technique. The regularity and randomness of the motion of a large object were decided by a probabilistic statistical analysis to investigate the mechanical characteristics of an object in a bed. The results show that decreasing the fluidization velocity first slowly reduces the residence time. When the gas velocity is lower than a critical value, the residence time sharply increases until the object does not reach the low side of the air distributor. Heavier objects have higher critical gas velocities. The RTD curves are very broad due to the stochastic pressure and velocity pulsations in the fluidization bed.

Key wordsfluidized bed    large heavy object    residence time    uneven air distribution    probability distribution
收稿日期: 2013-04-28      出版日期: 2014-06-15
基金资助:国家“九七三”重点基础研究项目(2011CB201502)
引用本文:   
蔡容容,张衍国,蒙晨玮,李清海,蒙爱红. 重质大颗粒在非均匀布风流化床内停留时间[J]. 清华大学学报(自然科学版), 2014, 54(6): 775-780.
Rongrong CAI,Yanguo ZHANG,Chenwei MENG,Qinghai LI,Aihong MENG. Residence time of a large heavy object in a fluidized bed with an uneven air distribution. Journal of Tsinghua University(Science and Technology), 2014, 54(6): 775-780.
链接本文:  
http://jst.tsinghuajournals.com/CN/  或          http://jst.tsinghuajournals.com/CN/Y2014/V54/I6/775
  实验系统
  倾斜布风板和定向风帽
ρo/(g·cm-3) D/cm 外壳 内填充物
0.90 3/4/5 硝化纤维
塑料,PE
纯净水、无水乙醇
1.63 3/4/5 001×7聚甲基丙烯酸甲
酯颗粒、一氧化铅粉末
3.00 3/4/5 一氧化铅粉末
  球体大颗粒的性质
  大颗粒运动图谱
  流化风速对平均停留时间的影响 (ρo/ρb =1.9, D/L=0.143)
  流化风速对平均停留时间的影响 (ρo/ρb =3.5, D/L=0.143)
  流化风速对平均停留时间的影响 (ρo/ρb =6.4, D/L=0.143)
  停留时间分布(D/L=0.143)
[1] 李佑楚. 流态化过程工程导论[M]. 北京: 科学出版社, 2008. LI Youchu. An Introduction to Fluidization Process Engineering [M]. Beijing: Science Press, 2008. (in Chinese)
[2] Daizo K, Octave L. Fluidization Engineering[M]. Boston, MA: Butterworth-Heinemann, 1991.
[3] Dora D, Mohanty Y, Roy G. Hydrodynamics of three-phase fluidization of a homogeneous ternary mixture of irregular particles[J]. Chemical Engineering Science, 2012, 79: 210-218.
[4] Feng Y, Yu A. Microdynamic modeling and analysis of the mixing and segregation of binary mixtures of particles in gas fluidization[J].Chemical Engineering Science, 2007, 62(1/2): 256-268.
[5] Formisani B, Girimonte R, Longo T. The fluidization process of binary mixtures of solids: Development of the approach based on the fluidization velocity interval[J]. Powder Technology, 2008, 185: 97-108.
[6] ZHANG Yong, JIN Baosheng, ZHONG Wenqi. Experimental investigation on mixing and segregation behavior of biomass particle in fluidized bed[J].Chemical Engineering and Processing: Process Intensification, 2009, 48: 745-754.
[7] Rees A, Davidson J, Hayhurst A. The rise of a buoyant sphere in a gas fluidized bed[J]. Chemical Engineering Science, 2005, 60: 1143-1153.
[8] 吴玖桓,张衍国,李清海. 大颗粒在循环床密相区运动规律的可视化研究 [J]. 中国电机工程学报, 2006, 26(4): 41-45. WU Jiuhuan, ZHANG Yanguo, LI Qinghai. Visual research on big particle behavior in dense-phase zone of circulating fluidized bed[J].Proceedings of the CSEE, 2006, 26(4): 41-45. (in Chinese)
[9] CUI Heping, Grace J. Fluidization of biomass particles: A review of experimental multiphase flow aspects[J].Chemical Engineering Science, 2007, 62: 45-55.
[10] Soria-Verdugo A, Garcia-Hernando N, Almendros-Lbanez J, et al.Motion of a large object in a bubbling fluidized bed with a rotating distributor[J]. Chemical Engineering and Processing, 2011, 50: 859-868.
[11] WEI Lubin, WANG Gengyu, HAO Liang, et al.Moving behavior of an object in gas-solid fluidized beds[J]. Journal of China University of Mining and Technology, 2005, 15(1): 7-11.
[12] Tran-Cong S, Gay M, Michaelides E. Drag coefficients of irregularly shaped particles[J]. Powder Technology, 2004, 139: 21-32.
[13] 张立斌, 姜凡, 潘忠刚, 等.非均匀布风条件下布风板上大块物料运动规律的实验研究[J]. 锅炉技术, 2000, 31(6):7-11. ZHANG Libin, JIANG Fan, PAN Zhonggang, et al.Motion of large particles on the distributor of a circulating fluidized bed[J]. Boiler Technology, 2000, 31(6): 7-11. (in Chinese)
[14] 田凤国, 章明川, 范浩杰, 等. 内循环流化床大块物分布特性的实验研究[J]. 动力工程, 2005, 25(6): 820-824. TIAN Fengguo, ZHANG Mingchuan, FAN Haojie, et al.Distribution of lumped matter in internally circulating fluidized bed boilers[J]. Powder Technology, 2005, 25(6): 820-824. (in Chinese)
[15] 李静海, 文利雄, 钱贵华, 等. 颗粒流体系统的不均匀性、多态性及非线性行为[J]. 中国科学B, 1996, 26(5): 445-451. LI Jinghai, WEN Lixiong, QIAN Guihua, et al.Inhomogeneity polymorphism and nonlinearity in particle-fluid systems[J]. Science in China B, 1996, 26(5): 445-451. (in Chinese)
[16] Landweber L. An iteration formula for Fredholm integral equations of the first kind[J]. American Journal of Mathematics, 1951, 73: 615-624.
[17] YIN Bin, ZHANG Mingchuan, WU Jiang, et al.Discrete particle simulation and visualized research of the gas-solid flow in fluidized beds with L-type wind caps[J]. Proceedings of the CSEE, 2003, 23(7): 183-190.
[18] CUI Heping, LI Jinghai, Kwauk M, et al.Dynamic behaviors of heterogeneous flow structure in gas-solid fluidization[J]. Powder Technology, 2007, 112: 7-23.
[19] Briensa L, Ellisb N. Hydrodynamics of three-phase fluidized bed systems examined by statistical, fractal, chaos and wavelet analysis methods[J]. Chemical Engineering Science, 2005, 60: 6094-6106.
[20] Hao B, Bi H. Forced bed mass oscillations in gas-solid fluidized beds[J]. Powder Technology, 2005, 149: 51-61.
[21] Sasic S, Leckner B, Johnsson F. Fluctuations and waves in fluidized bed systems: The influence of the air-supply system[J]. Powder Technology, 2005, 153: 176-195.
[22] Bi H. A critical review of the complex pressure fluctuation phenomenon in gas-solids fluidized beds[J]. Chemical Engineering Science, 2007, 62: 3473-3493.
[23] Llop M, Jand N, Gallucci K, et al.Characterizing gas-solid fluidization by nonlinear tools: Chaotic invariants and dynamic moments[J]. Chemical Engineering Science, 2012, 71: 252-263.
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