首页> 外文期刊>Chemical Engineering & Technology: Industrial Chemistry -Plant Equipment -Process Engineering -Biotechnology >Experimental Study on Bubble Rising and Descending Velocity Distribution in a Slurry Bubble Column Reactor
【24h】

Experimental Study on Bubble Rising and Descending Velocity Distribution in a Slurry Bubble Column Reactor

机译:浆态鼓泡塔反应器中气泡上升和下降速度分布的实验研究

获取原文
获取原文并翻译 | 示例
           

摘要

To determine bubble rising and descending velocity simultaneously,a BVW-2 four-channel conductivity probe bubble parameters apparatus and its analysis are used in gas-liquid and gas-liquid-solid bubble columns.The column is 100 mm in internal diameter and 1500 mm in height.The solid particles used are glass beads with an average diameter of 17.82 mu m,representing typical particle size for catalytic slurry reactors.The effects of superficial gas velocity(1.0 cm/s<=U_g<=6.4 cm/s),solid holdup(0%<=epsilon_s<=30%),and radial location(r/R=0,0.4,and 0.7)on bubble velocity distributions are determined.It is found that increasing U_g can increase the velocity of bubbles but do not exert much influence on bubble velocity distribution.Solid holdup mainly affects the distribution of bubble velocity while the radial direction affects bubble velocity distribution only slightiy.The ratio of descending bubbles to rising bubbles increases from the bubble column center to the wall.It can be proved experimentally that large bubbles do not always rise faster than small bubbles at higher U_g(for example 6.4 cm/s).
机译:为了同时测定气泡的上升和下降速度,将BVW-2四通道电导率探针气泡参数仪及其分析用于气液和气液固泡塔中。该塔的内径为100 mm,柱径为1500 mm所使用的固体颗粒是平均直径为17.82微米的玻璃珠,代表了催化淤浆反应器的典型粒径。表观气体速度(1.0 cm / s <= U_g <= 6.4 cm / s)的影响,确定了固体滞留率(0%<=ε_s<= 30%),并确定了气泡速度分布的径向位置(r / R = 0,0.4和0.7)。发现增加U_g可以增加气泡速度,但固持率主要影响气泡速度的分布,而径向仅影响气泡速度的分布,下降气泡与上升气泡的比例从气泡柱中心到壁的比例增加。证明的经验有趣的是,在较高的U_g(例如6.4 cm / s)下,大气泡的上升速度并不总是比小气泡快。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号