期刊文献+

温度对气-固-液三相搅拌反应器内气液分散特性的影响 被引量:1

Effect of temperature on gas-liquid dispersion in multi-impeller three-phase reactor
下载PDF
导出
摘要 在直径为0.476m的椭圆底搅拌槽中,采用以半椭圆管盘式涡轮(HEDT)为底桨、上提操作的宽叶翼形桨(WH_U)为中、上层桨的三层组合桨,研究24℃~95℃范围内不同温度下气-液-固体系中搅拌功率、气含率及固体颗粒完全离底悬浮特性。结果表明,体系相对功率需求(通气功率与不通气功率之比)RPD随温度的升高而增大,但随固含率的提高,温度对RPD的影响程度减弱。气含率随温度的升高而明显下降,其下降的幅度也随固含率增加而减小。本文结果及通气功率、气含率关联式对于工业热态通气三相搅拌反应器设计和操作具有一定的参考价值。 Power consumption, gas hold-up and critical impeller speed for just complete off-bottom solid suspension have been measured in a triple-impeller stirred tank of 0.476m diameter with dished base under six different temperatures from 24℃ to 95℃. The impeller combination consisted of a half elliptical disk turbine (HEDT) as the bottom and two up-pumping wide-blade hydrofoils (WHU) above HEDT. The results show that temperature has a great effect on the hydrodynamic characteristics. Relative power demand (RPD) increases for the higher temperature, but the effect of temperature on RPD becomes weaker when more solids added in the system. Gas holdup decreases apparently with the increasing of temperature, which becomes less at higher solid concentration. The results and the correlations are of particular relevance to the design and operation of hot sparged three-phase reactors.
出处 《中国科技论文在线》 CAS 2008年第3期184-188,共5页
基金 国家自然科学基金项目(20576009)
关键词 多相流反应工程(530.2440) 通气功率 气含率 热态通气 气-液-固三相体系 搅拌槽 multiphase reaction engineering (530.2440) RPD gas holdup hot sparged gas-liquid-solid three- phase system stirred tank
  • 相关文献

参考文献2

二级参考文献22

  • 1郝志刚,包雨云,高正明.多层组合桨搅拌槽内气-液分散特性的研究[J].高校化学工程学报,2004,18(5):547-552. 被引量:43
  • 2侯治中,冯连芳,李允明,许国军,王凯.不同类型搅拌器的气-液分散和混合特性[J].合成橡胶工业,1995,18(3):147-149. 被引量:5
  • 3侯治中,李允明,冯连芳,许国军,王凯.挡板进气多级搅拌槽内的气-液分散特性[J].合成橡胶工业,1995,18(4):218-220. 被引量:3
  • 4Kuzmanie N, Ljubieie B. Suspension of floating solids with up-pumping pitched blade impellers; mixing time and power characteristics [J]. Chemical Engineering Journal, 2001, 84(3): 325-333.
  • 5Mersmann A, Werner F, Maurer S, Bartosch K. Theoretical prediction of the minimum stirrer speed in mechanically agitated suspensions [J]. Chemical Engineering and Processing 1998, 37(6): 503-510.
  • 6Dutta N N, Pangarkar V G Critical impeller speed for solid suspension in multi-impeller three phase agitated contactors [J], The Canadian Journal of Chemical Engineering, 1995, 73(3): 273-283.
  • 7XU S A, Feng L F, Guo X P, et al. Gas-liquid floating particle mixing in an agitated vessel [J]. Chem Eng Technol, 2000, 23 (2):103-113.
  • 8BAO Y Y, HAO Z G, GAO Z M, et al. Suspension of buoyant particles in a three phase stirred tank [J]. Chemical Engineering Science, 2005, 60(8-9): 2283-2292.
  • 9Zwietering T N. Suspending of solid particles in liquids by agitators [J]. Chemical Engineering Science, 1958, 8 (3): 244-253.
  • 10Aubin J, Sauze N L, et al. Hydrodynamics in an aerated tank stirred by a down-and an up-pumping axial impeller [A]. 6th World Congress of Chemical Engineering [C]. Melbourne: Australia 23-27 September 2001.

共引文献51

同被引文献5

引证文献1

二级引证文献1

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