期刊文献+

加压气升式内环流反应器流动特性 被引量:4

Local flow characteristics in pressurized internal air loop reactor
下载PDF
导出
摘要 The flow characteristics of a 600 mm×6000 mm pressurized internal airloopreactor was studied.During the experiment the liquid superficial velocity in the draught tube was fixed at 0.008 m·s-1,gas superficial velocity ranged from 0.02 m·s-1 to 0.12 m·s-1,pressure of the reactor varied from 0 to 2.0 MPa.Local gas holdup in the draught tube and annual space was measured and correlations for these parameters were obtained.Meanwhile,the model of liquid circulation velocity on the basis of the energy balance analysis in the reactor was derived.Reasonable agreement was found between the calculated and measured data.From the model and experiment data,it was easily found that liquid circulation velocity increased with increasing gas superficial velocity and system pressure,however when gas superficial velocity and system pressure exceeded respective critical values,liquid circulation velocity increased only gently. The flow characteristics of a 600 mm×6000 mm pressurized internal airloopreactor was studied.During the experiment the liquid superficial velocity in the draught tube was fixed at 0.008 m·s-1,gas superficial velocity ranged from 0.02 m·s-1 to 0.12 m·s-1,pressure of the reactor varied from 0 to 2.0 MPa.Local gas holdup in the draught tube and annual space was measured and correlations for these parameters were obtained.Meanwhile,the model of liquid circulation velocity on the basis of the energy balance analysis in the reactor was derived.Reasonable agreement was found between the calculated and measured data.From the model and experiment data,it was easily found that liquid circulation velocity increased with increasing gas superficial velocity and system pressure,however when gas superficial velocity and system pressure exceeded respective critical values,liquid circulation velocity increased only gently.
出处 《化工学报》 EI CAS CSCD 北大核心 2010年第6期1437-1442,共6页 CIESC Journal
基金 国家重点基础研究发展计划项目(2004CB217604)~~
关键词 加压环流反应器 气含率 液相循环速度 pressurized internal airloopreactor gas holdup liquid circulation velocity
  • 相关文献

参考文献15

  • 1ShuGeping(舒歌平),ShiShidong(史士东),LiKejian(李克健).Coal Direct Liquefaction Technology(煤炭液化技术).Beijing:Coal Industry Press,2003:85-105.
  • 2Ryoichi Yoshida. Clean coal technologies in Japan. Energy Sources, 1997, 19 (9): 931-943.
  • 3International Energy Agency. Coal industry advisory board workshop report [-R]. Paris: IEA, 2006:34-59.
  • 4ShiShidong(史士东),ShuGeping(舒歌平),HuoWeidong(霍卫东).To explore the application of loop reactor in coal direct liquefaction area//International Rap Session of Coal Direct Liquefaction Technology. Beijing, 2008:166-177.
  • 5李红星,黄海,谷奎庆,刘辉,李建伟,李成岳.连续内环流三相反应器局部流动特性[J].化工学报,2007,58(10):2493-2499. 被引量:8
  • 6Young M A, Carbonell R G. Airlift bioreactors., analysis of local two-phase hydrodynamics. Journal of American Institute of Chemical Engineers, 1991, 37 (3) : 403-428.
  • 7Koide K, Iwamoto S, Takasaka Y, Matsuura S. Liquid circulation, gas holdup and pressure drop in bubble column with draught tube. Journal of Chemical Engineering in Japan, 1984, 17 (6): 611-618.
  • 8汪洋,徐春明,高金森,林世雄.液固环流反应器中固体流速及固含率分布[J].化学反应工程与工艺,2003,19(3):284-288. 被引量:17
  • 9Shamlou P A, Pollard D J, Ison A P, Lilly M D. Gas holdup and liquid circulation rate in concentric~tube airlift bioreactors. Chemical Engineering Science, 1994, 49 (3): 303-312.
  • 10Sevik M, Park S H. The splitting of drops and bubbles by turbulent fluid flow. Journal of Fluids Engineering, 1973, 95 (7): 53-60.

二级参考文献55

  • 1邓光君,张于喆,李昱岩,余京洋,李山梅,郭建伟.“煤变油”技术产业化的可行性与对策分析[J].资源.产业,2004,6(3):34-37. 被引量:4
  • 2刘梦溪,卢春喜,储凌,时铭显.中心气升式三相强化环流反应器内局部气含率分布的实验研究[J].高校化学工程学报,2005,19(1):36-41. 被引量:15
  • 3张玉卓.中国神华煤直接液化技术新进展[J].中国科技产业,2006(2):32-35. 被引量:39
  • 4[1]Livingston, Zhang. Hydrodynamic behaviour of airlift reactors[J]. Chemical Engineering Science, 1993, 48: 1641-1654.
  • 5[2]Carla Freitas, Maria Fialova, Jindrich Zahradnik et al. Hydrodynamic model for three-phase internal- and external-loop airlift reactors[J]. Chemical Engineering Science, 1999, 54: 5253-5258.
  • 6[3]Kawase Y. Liquid-phase mixing in internal-loop airlift bioreactors[J]. Chemical technology and biotechnology, 1994, 61: 49-55.
  • 7[4]Chia-Min Chen, Lii-Ping Leu. Hydrodynamics and mass transfer in three-phase magnetic fluidized beds[J]. Power Technology, 2001, 117: 198-206.
  • 8[5]Garcia-Calvo E, Leton P. Prediction of gas hold-up and liquid velocity in airlift reactors using two-phase flow friction coefficients[J]. Journal of Chemical Technology and Biotechnology, 1996, 67: 388-396.
  • 9[6]Lu W J, Hwang S J, Chang C M. Liquid velocity and gas holdup in three-phase internal loop airlift reactors with low-density particles[J]. Chemical Engineering Science, 1995, 50: 1301-1310.
  • 10[7]Shamlou P A, Pollard D J, Ison A P, Lilly M D. Gas holdup and liquid circulation rate in concentric-tube airlift bioreactors[J]. Chemical Engineering Science, 1994, 49: 303-312.

共引文献53

同被引文献64

引证文献4

二级引证文献12

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