留言板

尊敬的读者、作者、审稿人, 关于本刊的投稿、审稿、编辑和出版的任何问题, 您可以本页添加留言。我们将尽快给您答复。谢谢您的支持!

姓名
邮箱
手机号码
标题
留言内容
验证码

气液鼓泡床反应器中气泡行为光纤探针测量方法

何广湘 郭晓燕 杨索和 靳海波

何广湘, 郭晓燕, 杨索和, 等 . 气液鼓泡床反应器中气泡行为光纤探针测量方法[J]. 北京航空航天大学学报, 2017, 43(2): 253-259. doi: 10.13700/j.bh.1001-5965.2016.0149
引用本文: 何广湘, 郭晓燕, 杨索和, 等 . 气液鼓泡床反应器中气泡行为光纤探针测量方法[J]. 北京航空航天大学学报, 2017, 43(2): 253-259. doi: 10.13700/j.bh.1001-5965.2016.0149
HE Guangxiang, GUO Xiaoyan, YANG Suohe, et al. Measurement method of bubble behavior by optical probe in gas-liquid bubble column reactor[J]. Journal of Beijing University of Aeronautics and Astronautics, 2017, 43(2): 253-259. doi: 10.13700/j.bh.1001-5965.2016.0149(in Chinese)
Citation: HE Guangxiang, GUO Xiaoyan, YANG Suohe, et al. Measurement method of bubble behavior by optical probe in gas-liquid bubble column reactor[J]. Journal of Beijing University of Aeronautics and Astronautics, 2017, 43(2): 253-259. doi: 10.13700/j.bh.1001-5965.2016.0149(in Chinese)

气液鼓泡床反应器中气泡行为光纤探针测量方法

doi: 10.13700/j.bh.1001-5965.2016.0149
基金项目: 

国家自然科学基金 21073020

北京市属高等学校高层次人才引进与培养计划 CIT & TCD20130325

详细信息
    作者简介:

    何广湘, 男, 博士, 副教授。主要研究方向:多相流反应工程与分离技术等

    郭晓燕, 女, 博士研究生, 讲师。主要研究方向:生化反应工程与分离技术等

    杨索和, 男, 硕士, 讲师。主要研究方向:多相流反应工程与分离技术等

    通讯作者:

    靳海波, 男, 博士, 教授, 博士生导师。主要研究方向:多相流反应工程与分离技术等, E-mail:jinhaibo@bipt.edu.cn

  • 中图分类号: TQ021.1

Measurement method of bubble behavior by optical probe in gas-liquid bubble column reactor

Funds: 

National Natural Science Foundation of China 21073020

The Importation and Development of High-Caliber Talents Project of Beijing Municipal Institutions CIT & TCD20130325

More Information
  • 摘要:

    本文分别采用电导探针和光纤探针测量气液鼓泡床反应器中的气含率、气泡速率和气泡弦长等气泡行为,结果表明光纤探针对气泡具有响应迅速、阶跃显著的特点。将光纤探针信号进行方波化处理,探针在气相中的采样点数与总采样点数之比即为局部气含率,再沿径向积分可得平均气含率,以压差法测得的平均气含率为基准,光纤探针比电导探针准确性更高。将改造后的光纤探针应用于高温、高压、液相为有机体系的气液鼓泡床反应器,测得该反应器的气含率呈中心及边壁低、0.4倍半径处最大的抛物形分布。因此,开发的光纤探针可用于高温、高压、液相有机体系中气泡行为的测量。

     

  • 图 1  费托合成反应器流程图

    Figure 1.  Flowchart of Fischer-Tropsch synthesis reactor

    图 2  电导探针信号时间序列

    Figure 2.  Time series of conductivity probe signals

    图 3  光纤探针示意图

    Figure 3.  Schematic diagram of optical probe

    图 4  光纤探针信号时间序列

    Figure 4.  Time series of optical probe signals

    图 5  局部放大后的光纤探针信号

    Figure 5.  Partially enlarged optical probe signals

    图 6  不同方法所得平均气含率的比较

    Figure 6.  Comparsion of average gas holdup measured by different methods

    图 7  双光纤探针信号时间序列

    Figure 7.  Time series of optical twin probe signals

    图 8  探针法计算得到的表观气速与实际表观气速对比

    Figure 8.  Comparison between superficial gas velocity calculated by probe method and practical superficial gas velocity

    图 9  费托合成反应器中气含率径向分布

    Figure 9.  Radial profile of gas holdup in Fischer-Tropsch synthesis reactor

  • [1] 张同旺, 何广湘, 靳海波, 等.浆态床鼓泡反应器液体力学的研究进展[J].北京石油化工学院学报, 2001, 9(2):47-53. http://www.cnki.com.cn/Article/CJFDTOTAL-BJSY200102015.htm

    ZHANG T W, HE G X, JIN H B, et al.Process of hydrodynamics in slurry bubble column reactor[J].Journal of Beijing Institure of Petrochemical Technolgy, 2001, 9(2):47-53(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-BJSY200102015.htm
    [2] ZHANG T W, ZHAO B, WANG J F.Mathematical models for macro-scale mass transfer in airlift loop reactors[J].Chemical Engineering Journal, 2006, 119(1):19-26. doi: 10.1016/j.cej.2006.03.005
    [3] ZHANG T W, WANG J F, WANG T F, et al.Effect of internal on the hydrodynamics in external-loop airlift reactors[J].Chemical Engineering and Processing:Process Intensification, 2005, 44(1):81-87. doi: 10.1016/j.cep.2004.05.003
    [4] SAMARAS K, KOSTOGLOU M, KARAPANTSIOS T D, et al.Effect of adding glycerol and tween 80 on gas holdup and bubble size distribution in an aerated stirred tank[J].Colloids and Surfaces A:Physicochemical and Engineering Aspects, 2014, 441(3):815-824.
    [5] 张同旺, 靳海波, 何广湘, 等.采用压力传感技术测量鼓泡床中流体力学参数[J].化工学报, 2004, 55(3):476-480. http://www.cnki.com.cn/Article/CJFDTOTAL-HGSZ200403030.htm

    ZHANG T W, JIN H B, HE G X, et al.Application of pressure transducing technology to measurement of hydrodynamics in bubble column[J].CIESC Journal, 2004, 55(3):476-480(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-HGSZ200403030.htm
    [6] SUPARDAN M D, MASUDA Y, MAEZAWA A, et al.The investigation of gas holdup distribution in a two-phase bubble column using ultrasonic computed tomography[J].Chemical Engineering Journal, 2007, 130(2-3):125-133. doi: 10.1016/j.cej.2006.08.035
    [7] FRANSOLET E, CRINE M, MARCHOT P, et al.Analysis of gas holdup in bubble columns with non-Newtonian fluid using electrical resistance tomography and dynamic gas disengagement technique[J].Chemical Engineering Science, 2005, 60(22):6118-6123. doi: 10.1016/j.ces.2005.03.046
    [8] PJONTEK D, PARISIEN V, MACCHI A.Bubble characteristics measured using a monofibre optical probe in a bubble column and freeboard region under high gas holdup conditions[J].Chemical Engineering Science, 2014, 111(1):153-169.
    [9] 朱姝, 包雨云, 陈雷, 等.用电导探针测定气-液多层桨搅拌槽内气泡尺寸分布[J].高校化学工程学报, 2011, 25(6):977-984. http://www.cnki.com.cn/Article/CJFDTOTAL-GXHX201106013.htm

    ZHU S, BAO Y Y, CHEN L, et al.Bubble size distributions measurement in a gas-liquid multi-impeller stirred tank by using dual-conductivity probe[J].Journal of Chemical Engineering of Chinese Universities, 2011, 25(6):977-984(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-GXHX201106013.htm
    [10] 张同旺.气升式环流浆态床流动与传质行为的研究[D].北京:清华大学, 2005:35-36.

    ZHANG T W.Hydrodynamics and mass transfer in airlift loop slurry reactors[D].Beijing:Tsinghua University, 2005:35-36(in Chinese).
    [11] CHEN C M, LEU L P.Flow regimes and radial gas holdup distribution in three-phase magnetic fluidized beds[J].Industrial & Engineering Chemistry Research, 2002, 41(7):1877-1884.
    [12] 唐人虎, 陈听宽, 罗毓珊, 等.高温高压上用光纤探针测量截面含气率的实验研究[J].化工学报, 2001, 52(6):560-563. http://www.cnki.com.cn/Article/CJFDTOTAL-HGSZ200106022.htm

    TANG R H, CHEN T K, LUO Y S, et al.Void fraction measurement by using optical probes at high temperature and high pressure[J].CIESC Journal, 2001, 52(6):560-563(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-HGSZ200106022.htm
    [13] 周立进, 王磊, 黄慧慧, 等.费托合成工艺研究进展[J].石油化工, 2012, 41(12):1429-1436. http://www.cnki.com.cn/Article/CJFDTOTAL-SYHG201212022.htm

    ZHOU L J, WANG L, HUANG H H, et al.Research progresses in Fischer-Tropsch synthesis process[J].Petrochemical Technology, 2012, 41(12):1429-1436(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-SYHG201212022.htm
    [14] LEE B W, DUDUKOVIC M P.Determination of flow regime and gas holdup in gas-liquid stirred tanks[J].Chemical Engineering Science, 2014, 109(14):264-275.
    [15] 邹华生, 程小平, 周超.超声场中鼓泡塔内气泡直径分布特征研究[J].现代化工, 2011, 31(11):64-67. http://www.cnki.com.cn/Article/CJFDTOTAL-XDHG201111019.htm

    ZOU H S, CHENG X P, ZHOU C.Study on bubble diameter distribution in bubble column unde ultrasonic field[J].Modern Chemical Industry, 2011, 31(11):64-67(in Chinese). http://www.cnki.com.cn/Article/CJFDTOTAL-XDHG201111019.htm
  • 加载中
图(9)
计量
  • 文章访问数:  1166
  • HTML全文浏览量:  162
  • PDF下载量:  412
  • 被引次数: 0
出版历程
  • 收稿日期:  2016-02-29
  • 录用日期:  2016-07-14
  • 网络出版日期:  2017-02-20

目录

    /

    返回文章
    返回
    常见问答