Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (9): 4734-4748.DOI: 10.16085/j.issn.1000-6613.2021-0393
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LIAO Peiyi1,2(), YANG Daijun1,2(), MING Pingwen1,2, XUE Mingzhe1,2, LI Bing1,2, ZHANG Cunman1,2
Received:
2021-03-01
Revised:
2021-05-17
Online:
2021-09-13
Published:
2021-09-05
Contact:
YANG Daijun
廖珮懿1,2(), 杨代军1,2(), 明平文1,2, 薛明喆1,2, 李冰1,2, 张存满1,2
通讯作者:
杨代军
作者简介:
廖珮懿(1991—)女,博士研究生,研究方向为燃料电池流体动力学。E-mail:基金资助:
CLC Number:
LIAO Peiyi, YANG Daijun, MING Pingwen, XUE Mingzhe, LI Bing, ZHANG Cunman. Research progress of gas-liquid two-phase flow in micro-channel and its application in PEMFC[J]. Chemical Industry and Engineering Progress, 2021, 40(9): 4734-4748.
廖珮懿, 杨代军, 明平文, 薛明喆, 李冰, 张存满. 微流道气-液两相流研究及其在PEMFC中的应用进展[J]. 化工进展, 2021, 40(9): 4734-4748.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2021-0393
流型 | 特征描述 |
---|---|
泡状流 | 以液相为连续相,气体以小气泡形式分散在液相中,气泡与气泡之间间距较大 |
段塞流 | 气泡的直径达到了流道的宽度,气泡具有椭圆形的“头部”和矩形的“身体” |
搅混流 | 大气泡破碎并以凌乱的状态、不规则的大小进入液相 |
环形流 | 具有被液膜包裹的气芯,形成带波浪形边缘环状的流态 |
帽状-气泡流 | 气泡呈“帽状”,有着近似半圆的“头部”和较“肥大”的尾部 |
段塞液滴流 | 长段气泡中含有液滴,但是液段中不含气泡 |
环形液滴流 | 具有被液膜包裹的气芯,且气芯中包含液滴并随着气泡移动 |
流型 | 特征描述 |
---|---|
泡状流 | 以液相为连续相,气体以小气泡形式分散在液相中,气泡与气泡之间间距较大 |
段塞流 | 气泡的直径达到了流道的宽度,气泡具有椭圆形的“头部”和矩形的“身体” |
搅混流 | 大气泡破碎并以凌乱的状态、不规则的大小进入液相 |
环形流 | 具有被液膜包裹的气芯,形成带波浪形边缘环状的流态 |
帽状-气泡流 | 气泡呈“帽状”,有着近似半圆的“头部”和较“肥大”的尾部 |
段塞液滴流 | 长段气泡中含有液滴,但是液段中不含气泡 |
环形液滴流 | 具有被液膜包裹的气芯,且气芯中包含液滴并随着气泡移动 |
研究者 | 发表年份 | 微流道参数 | 流体体系 | 操作条件 | 探究因素 | 主要结论 | |||
---|---|---|---|---|---|---|---|---|---|
流道水力直径 /mm | 流道表面特性 | 放置方式 | 气体和液体的表观速度 /m·s–1 | 气-液两相在入口处的夹角/(°) | |||||
Chung等[ | 2004 | 0.05,0.1,0.25,0.53 | — | 水平 | 氮气-水 | UG∶0.01~73 UL∶0.01~5.8 | 90 | 流道直径 | 随着流道直径减小,观测到的流型种类减少至只剩下段塞流 |
宋静[ | 2006 | 0.4 | 亲水 | 水平 | 氮气-液体(水,无水乙醇,不同浓度的CMC水溶液) | UG∶0.79~24 UL∶0.03~0.5 | 0 | 流体特性(密度,黏度) | 随着液体黏度的增加,越容易出现环形流 |
Venkatesan等[ | 2010 | 0.6, 1.2, 1.7, 2.6, 3.4 | 亲水 | 水平 | 空气-水 | UG∶0.01~50 UL∶0.01~3 | 0 | 流道直径 | 当流道直径小于2mm时观测不到分层流和环形流,小于1mm时只能观测到泡状流、段塞流、段塞-环形流和分散泡状流 |
Choi等[ | 2011 | 0.5 | 亲水,疏水 | 水平 | 氮气-水 | UG∶0.07~34.1 UL∶0.19~0.46 | 90 | 壁面接触角 | 亲水壁面可观测到泡状流、长泡状流、段塞-环形流,而疏水壁面则更倾向于形成分层流型 |
袁希钢等[ | 2012 | 0.53 | — | 水平 | 空气-液体(水,不同浓度的乙醇和丙三醇) | UG∶0.1~20 UL∶0.1~3 | 180 | 流体特性(密度,黏度) | 黏度增加对流型的过渡线的移动的影响并不明显 |
Saisorn等[ | 2015 | 0.53 | — | 水平,垂直向上 | 空气-水 | UG∶0.38~21.19 UL∶0.004~2.44 | 0,90 | 流道放置方向 | 垂直放置的流道内无法观测到弹状流;水平放置的流道内无法观测到环状流 |
Puccetti等[ | 2015 | 0.28 | — | 水平 | 空气-水 | UG, UL∶0.005~0.15 | 90 | 气体和液体的表观速度 | 表观气速和表观液速影响气泡长度 |
Zhou 等[ | 2017 | 0.18 | 亲水,疏水 | 水平 | 空气-水 | UG, UL∶0.001~10 | 0 | 壁面固有接触角和表面粗糙度 | 随着接触角增大,形成的流型减少至只剩段塞流,表面粗糙度增大时表面疏水程度增大 |
Lim等[ | 2019 | 0.2 | — | 水平 | He-乙醇 | UG∶0.06,0.1,0.15 UL∶0.04,0.07,0.1 | 20,45,90,135,160 | 两相入口夹角 | 入口夹角大于90°有利于增大气泡比表面积 |
王长亮等[ | 2019 | 0.1 | 亲水,疏水 | 水平 | 空气-水 | UG, UL∶0.12 | 90 | 壁面接触角 | 接触角的变化改变了气-液接触界面的形状 |
研究者 | 发表年份 | 微流道参数 | 流体体系 | 操作条件 | 探究因素 | 主要结论 | |||
---|---|---|---|---|---|---|---|---|---|
流道水力直径 /mm | 流道表面特性 | 放置方式 | 气体和液体的表观速度 /m·s–1 | 气-液两相在入口处的夹角/(°) | |||||
Chung等[ | 2004 | 0.05,0.1,0.25,0.53 | — | 水平 | 氮气-水 | UG∶0.01~73 UL∶0.01~5.8 | 90 | 流道直径 | 随着流道直径减小,观测到的流型种类减少至只剩下段塞流 |
宋静[ | 2006 | 0.4 | 亲水 | 水平 | 氮气-液体(水,无水乙醇,不同浓度的CMC水溶液) | UG∶0.79~24 UL∶0.03~0.5 | 0 | 流体特性(密度,黏度) | 随着液体黏度的增加,越容易出现环形流 |
Venkatesan等[ | 2010 | 0.6, 1.2, 1.7, 2.6, 3.4 | 亲水 | 水平 | 空气-水 | UG∶0.01~50 UL∶0.01~3 | 0 | 流道直径 | 当流道直径小于2mm时观测不到分层流和环形流,小于1mm时只能观测到泡状流、段塞流、段塞-环形流和分散泡状流 |
Choi等[ | 2011 | 0.5 | 亲水,疏水 | 水平 | 氮气-水 | UG∶0.07~34.1 UL∶0.19~0.46 | 90 | 壁面接触角 | 亲水壁面可观测到泡状流、长泡状流、段塞-环形流,而疏水壁面则更倾向于形成分层流型 |
袁希钢等[ | 2012 | 0.53 | — | 水平 | 空气-液体(水,不同浓度的乙醇和丙三醇) | UG∶0.1~20 UL∶0.1~3 | 180 | 流体特性(密度,黏度) | 黏度增加对流型的过渡线的移动的影响并不明显 |
Saisorn等[ | 2015 | 0.53 | — | 水平,垂直向上 | 空气-水 | UG∶0.38~21.19 UL∶0.004~2.44 | 0,90 | 流道放置方向 | 垂直放置的流道内无法观测到弹状流;水平放置的流道内无法观测到环状流 |
Puccetti等[ | 2015 | 0.28 | — | 水平 | 空气-水 | UG, UL∶0.005~0.15 | 90 | 气体和液体的表观速度 | 表观气速和表观液速影响气泡长度 |
Zhou 等[ | 2017 | 0.18 | 亲水,疏水 | 水平 | 空气-水 | UG, UL∶0.001~10 | 0 | 壁面固有接触角和表面粗糙度 | 随着接触角增大,形成的流型减少至只剩段塞流,表面粗糙度增大时表面疏水程度增大 |
Lim等[ | 2019 | 0.2 | — | 水平 | He-乙醇 | UG∶0.06,0.1,0.15 UL∶0.04,0.07,0.1 | 20,45,90,135,160 | 两相入口夹角 | 入口夹角大于90°有利于增大气泡比表面积 |
王长亮等[ | 2019 | 0.1 | 亲水,疏水 | 水平 | 空气-水 | UG, UL∶0.12 | 90 | 壁面接触角 | 接触角的变化改变了气-液接触界面的形状 |
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