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[1]郑小涛,龚程,徐红波,等.相间作用下脱油水力旋流器油相分布[J].武汉工程大学学报,2014,(08):51-55.[doi:103969/jissn16742869201408009]
 ZHENG Xiao tao,GONG Cheng,XU Hong bo,et al.Oil distribution in deoiling hydrocyclone under interphase interaction[J].Journal of Wuhan Institute of Technology,2014,(08):51-55.[doi:103969/jissn16742869201408009]
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相间作用下脱油水力旋流器油相分布(/HTML)
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《武汉工程大学学报》[ISSN:1674-2869/CN:42-1779/TQ]

卷:
期数:
2014年08期
页码:
51-55
栏目:
机电与信息工程
出版日期:
2014-08-31

文章信息/Info

Title:
Oil distribution in deoiling hydrocyclone under interphase interaction
文章编号:
16742869(2014)08005105
作者:
郑小涛1龚程1徐红波2喻九阳1刘昊1
1.化工装备强化与本质安全湖北省重点实验室(武汉工程大学),湖北 武汉 430205;2.广州民航职业技术学院飞机维修工程学院,广东 广州 510470
Author(s):
ZHENG Xiaotao GONG Cheng XU Hongbo YU Jiuyang LIU Hao
Hubei Key Laboratory of Chemical Equipment Intensification and Intrinsic Safety(Wuhan Institute of technology), Wuhan 430205,China;Department of Aircraft Maintenance and Engineering, Guangzhou Civil Aviation College, Guangzhou 510470,China
关键词:
聚合破裂分散相水力旋流器
Keywords:
coalescence breakage dispersed phase hydrocyclone
分类号:
TE991.2
DOI:
103969/jissn16742869201408009
文献标志码:
A
摘要:
在旋流分离过程中,油滴尺寸分布会因聚合与破裂现象而产生改变,从而对分离效率产生影响.利用Fluent软件结合群体平衡模型及多尺寸分组方法在考虑相间相互作用的情况下,对脱油Matthias Meyer水力旋流器中油滴浓度及直径分布进行了模拟.结果表明:含群体平衡模型的方法较不含群体平衡模型的方法所得到的分离效率精确度更高,与实验数据相比较误差分别为2%与6%.模型中聚合现象较破裂现象明显,使得大直径油滴含量增大且聚集在内旋流及圆柱段,而小直径油滴含量减小且聚集在圆锥段.分散相破裂效率与湍流耗散率成正比,聚合效率与油相浓度成正比的关系得到了验证.
Abstract:
In the separation process of hydrocyclone, the distribution of the size of oil droplets changes with the coalescence and breakage, and it affects the separation efficiency. Considering the interphase interaction,the Fluent software combined with population balance model and multisizemodel was adopted to simulate the concentration and size distribution of oil droplets in the deoiling Matthias Meyer’s hydrocyclone. The results show that the separation efficiency obtained by the population balance model is more accurate than that without the population balance model and the errors between the simulated data and the experimental data are 2% and 6% respectively. As coalescence is more obvious than breakage in this model, the concentration of the large oil droplets increases and the large oil droplets gather in the inner swirling flow and the cylindrical section, while the concentration of the small oil droplets decreases and the small oil droplets gather in the conic section. The relationships are verified that the efficiency of breakage is proportional to the turbulent dissipation rate and the efficiency of coalescence is proportional to the concentration of the oil phase.

参考文献/References:

[1]郑小涛,徐成,喻九阳,等.液液旋流分离器分离特性数值模拟[J].武汉工程大学学报,2014,36(3):4852.ZHENG Xiaotao, XU Cheng, YU Jiuyang, et al. Numerical simulation of separation character in liquidliquid hydrocyclone [J]. Journal of Wuhan Institute of Technology, 2014, 36(3): 4852.(in Chinese)[2]SCHUTZ S, GORBACH G, Piesche. Modeling fluid behavior and droplet interactions during liquidliquid separation in hydrocyclones [J]. Chem Eng Sci, 2009(64): 3539.[3]NOROOZI S S, HASHEMABADI H, CHAMKHA A J. Numerical analysis of drops coalescence and breakage effects on Deoiling hydrocyclone performance [J]. Separation Science and Technology, 2013(48): 9911002.[4]舒朝辉. 油水分离水力旋流器分离特性及其软件设计的研究[D]. 成都:四川大学,2001.SHU Zhaohui. Study on separation characteristics and software design of hydrocyclones for Oilwater separation [D]. Chendu:Sichuan University, 2001.(in Chinese)[5]PATRUNO L E, DORAO C A, SVENDSEN H F, et al. Analysis of breakage kernels for population balance modeling [J]. Chemical Engineering Science, 2009, 64(3): 501508.[6]曹杨. Rushton搅拌釜式生物反应器的射线CT测量及流体力学模拟计算[D].湘潭:湘潭大学,2010.CAO Yang. The CT measurement and CFD simulation of rushton stirred tank bioreactor [D]. Xiangtan:Xiangtan University, 2010.(in Chinese)[7]MICHAEL J Prince, HARVEY W Blanch. Bubble coalescence and breakup in Airsparged bubble columns [J]. AIChE Journal, 1990, 36(10): 14851499.[8]MATTHIAS Meyer, MATTHIAS Bohnet. Influence of Entrance Droplet Size Distribution and Feed Concentration on Separation of Immiscible Liquids Using Hydrocyclones [J]. Chem Eng Technol, 2003, 26(6): 660665

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备注/Memo

备注/Memo:
收稿日期:20140611基金项目:湖北省自然科学基金项目(2012FFB04707),武汉工程大学科学研究基金项目,武汉工程大学研究生教育创新基金项目(CX2013080);作者简介:郑小涛(1982),男,湖北武汉人,讲师,博士.研究方向:结构完整性、流体设备以及传热与传质.
更新日期/Last Update: 2014-09-16