首页 | 本学科首页   官方微博 | 高级检索  
     

加温加压下CFD-PBM耦合模型空气-水两相流数值模拟研究
引用本文:张文龙,侯燕,靳海波,马磊,何广湘,杨索和,郭晓燕,张荣月.加温加压下CFD-PBM耦合模型空气-水两相流数值模拟研究[J].化工学报,2021,72(9):4594-4606.
作者姓名:张文龙  侯燕  靳海波  马磊  何广湘  杨索和  郭晓燕  张荣月
作者单位:1.北京石油化工学院化学工程学院,北京 102617;2.燃料清洁化及高效催化减排技术 北京市重点实验室,北京 102617
摘    要:计算流体力学与群体平衡模型(CFD-PBM)结合可有效地模拟鼓泡塔内流体行为,较准确地预测流场、相含率以及局部气泡尺寸分布。以直径100 mm、高1.3 m的加温加压鼓泡塔为模拟对象,在系统压力为1 MPa、表观气速为0.08~0.24 m/s、温度为30~160℃条件下系统地考察了空气-水体系的表观气速、温度以及固含率对平均气含率、大小气泡气含率、气泡直径和气泡尺寸分布等参数的影响。结果表明,平均气含率的模拟结果和实验值在10%的误差范围内吻合较好;温度的变化主要影响了塔内气泡的聚并和破碎,并用聚并破碎的机理解释了温度对其流体行为的影响。

关 键 词:鼓泡塔  计算流体力学  两相流  气含率  大小气泡  加温加压  固含率  
收稿时间:2021-01-29

Numerical simulation of air-water two-phase flow under elevated pressures and temperatures using CFD-PBM coupled model
Wenlong ZHANG,Yan HOU,Haibo JIN,Lei MA,Guangxiang HE,Suohe YANG,Xiaoyan GUO,Rongyue ZHANG.Numerical simulation of air-water two-phase flow under elevated pressures and temperatures using CFD-PBM coupled model[J].Journal of Chemical Industry and Engineering(China),2021,72(9):4594-4606.
Authors:Wenlong ZHANG  Yan HOU  Haibo JIN  Lei MA  Guangxiang HE  Suohe YANG  Xiaoyan GUO  Rongyue ZHANG
Affiliation:1.College of Chemical Engineering, Beijing Institute of Petrochemical Technology, Beijing 102617, China;2.Beijing Key Laboratory of Fuels Cleaning and Advanced Catalytic Emission Reduction Technology, Beijing 102617, China
Abstract:The combination of computational fluid dynamics and the population balance model (CFD-PBM) can effectively simulate the fluid behavior in the bubble column, and more accurately predict the flow characteristic, phase holdup and local bubble size distribution. In this paper, numerical simulations of air-water two-phase flow are studied under thermal conditions by using CFD-PBM coupled model in a pressurized bubble column with a 100 mm diameter and 1.3 m height. The system has been investigated in the range of 1MPa, the superficial gas velocity of 0.08—0.24 m/s, and the temperature of 30—160℃. The effect of the superficial gas velocity, temperature and solid content of air-water system on the average gas holdup, large and small bubbles gas holdup, bubble diameter, and bubble size distribution are discussed. The results show that the simulation results of the average gas holdup are in good agreement with the experimental values within the error range of 10%. The temperature change mainly affects the coalescence and breakage of bubbles in the tower, and the coalescence and breakage mechanism is used to explain the influence of temperature on the fluid behavior.
Keywords:bubble column  computational fluid dynamics  two-phase flow  gas holdup  large and small bubbles  high temperature and pressure  solid holdup  
点击此处可从《化工学报》浏览原始摘要信息
点击此处可从《化工学报》下载全文
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号