期刊文献+

气-液-固三相流化床气体分布器区局部相含率和床层膨胀比的实验研究

Study on Three Phase Local Holdups and Expansion Ratio in Gas Distributor Region of G-L-S Three Phase Fluidized Bed
下载PDF
导出
摘要 在内径150 mm,高4 350 mm的三相流化床中,分别以空气、水和0.48 mm、1.25mm的玻璃珠及1.45 mm的苯乙烯树脂为气相、液相和固相,应用开发的微电导探针测试技术同时测得三相局部含率,并对气体分布器区的局部相含率和床层膨胀比(H/H0)进行了实验研究,考察了固体颗粒的粒径、密度及表观液速和气速对床层膨胀比的影响。研究发现,在距气体分布器轴向一定距离范围内,三相局部含率的径向分布存在明显的不对称分布;随着轴向距离的增加,局部气含率的径向不对称分布逐渐消失,局部固含率的径向不对称分布变化不明显;床层膨胀比随表观气速和液速的增大而增大;较低密度颗粒系统的H/H0开始增加缓慢,后来增加很快;较高密度颗粒系统的H/H0开始迅速增加,后来增加缓慢。 The experiments were carried out with air, water, and 0.48 mm, 1.25 mm glass beads, 1.45 mm styrene resin as gas, liquid and solid phases, respectively. Threephase local holdups were measured simultaneously with micro-conductivity probe technique at on four levels with at 200 mm intervals along the three-phase fluidized bed with 150 mm in diameter and 4 350 mm in height. Local phase holdups and bed expansion ratio (H/Ho) near gas distributor region were investigated. H/H0 was also studied with various kinds of particle, superficial gas velocity and liquid velocity, It was shown that radial profiles of the three phase local holdups were severe radial mal-distribution near the gas distributor. Also, the experimental results indicated that such radial mal-distri- bution of local gas holdup was disappeared with increasing axial height, corresponding transition to symmetry distribution. H/H0 increases with increasing superficial gas velocity and liquid velocity. H/Ho increases incipiently slowly and then quickly for lower density system. However, the variation of H/H0 is opposition for higher density system.
出处 《青岛科技大学学报(自然科学版)》 CAS 2007年第6期516-520,共5页 Journal of Qingdao University of Science and Technology:Natural Science Edition
基金 国家自然科学基金项目(20676064) 山东省"泰山学者"建设工程基金项目(200510036)
关键词 三相流化床 气体分布器区 微电导探针 三相局部含率 不对称分布 床层膨胀比 three-phase fluidized bed gas distributor region micro-conductivity probe three phase local hold-up mal-distribution bed expansion ratio
  • 相关文献

参考文献10

  • 1Yuan X W, Boon C O, AI-Dahhan M H . Predictions of radial gas holdup profiles in bubble column reactors [J]. Chem Eng Sci , 2001, 56:1207.
  • 2Epstein N . Three-phase fluidization: some knowledge gaps[J]. Can J Chem Eng , 1981, 59:659.
  • 3Wild G, Saberrian M, Schwartz J L, et al. Gas-liquid-solid fluidized bed reactors, state of the art and industrial possibilities[J]. Int Chem Eng, 1984, 24: 639.
  • 4Nacef S, Wild G , Laurent A, et al. Scale effects in as-liquidsolid fluidization[J]. Int Chem Eng, 1992, 32: 51.
  • 5Kim S D, Kang Y. Heat and mass transfer in three-phase fluidized bed reactors-an overview[J]. Chem Eng Sci, 1997, 52:3639.
  • 6Safoniuk M, Grace R, Hackman L, et al. Gas holdup in a three-phase fluidized bed[J]. AIChE Journal, 2002, 48(6): 1581.
  • 7Bloxom V R, Costa J M, Herranz J, et al. Determination and correlation of hydrodynamic variables in a three-phase fluidized bed[J]. Chem Eng Sci, 1985, 46:219.
  • 8曹长青,刘明言,王一平,秦秀云,胡宗定.气液固三相流化床局部相含率轴径向分布[J].化工学报,2005,56(2):249-256. 被引量:11
  • 9胡宗定 王一平.电导探针应于测定三相流化床局部含率.天津大学学报,1984,(1):17-22.
  • 10Lee D, Mscchi A, Grace J R, et al. Fluid mal-distribution effects on phase holdups in three-phase fluidized beds[J]. Chem Eng Sci, 2001, 56: 6031.

二级参考文献14

  • 1Sang Done Kim, Yong Kang.Heat and mass transfer in three-phase fluidized-bed reactors-an overview.Chem. Eng. Sci.,1997,52(21/22):3639-3660.
  • 2胡宗定 于宝田.Gas-liquid-solid three-phase fluidization engineering[J].化学工程,1986,2:20-27.
  • 3Schweitzer J M, Bayle J, Gauthier T. Local gas holdup measurements in fluidized bed and slurry bubble column. Chem. Eng. Sci.,2001,56:1103-1110.
  • 4胡宗定 于宝田.A study of local holdups and liquid velocity in a large-diameter three-phase fluidized bed[J].化工学报,1988,39(2):153-161.
  • 5Lang W, Wu Q, Yu Z, Jin Y, Wang Z.Hydrodynamics of a gas-liquid-solid three phase circulating fluidized bed.The Journal of Chemical Engineering, 1995,73:656-661.
  • 6Ryuji Kikuchi, Atsushi Tsutsumi, Kunio Yoshida.Fractal aspect of hydrodynamics in a three-phase fluidized bed,Chem. Eng. Sci.,1996, 50(11):2865-2870.
  • 7胡宗定 王一平.Application of electric conductivity probe to measurement of local phase holdups in three-phase fluidized beds[J].天津大学学报,1984,1:17-22.
  • 8张俊平,金涌.Investigation parameters of wake model using separate-fall technique in three-phase fluidized beds.In: 5th National Conference on Fluidization.Beijing:1990.327-331.
  • 9胡宗定 于宝田 王一平.Study on the local holdup and liquid velocity distribution in G-L-S three-phase fluidized beds[J].化学反应工程与工艺,1985,3:66-74.
  • 10Miura H, Takahashi T, Kawase Y. Effect of pseudo-plastic behavior of liquid in co-current three-phase fluidized beds on bed expansion.Chem. Eng. Sci., 2001,56:6047-6053.

共引文献10

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部