Axisymmetric gas-liquid displacement flow under a confined elastic slab

被引:1
|
作者
Peng, Gunnar G. [1 ,2 ,3 ]
Cuttle, Callum [4 ]
Macminn, Christopher W. [4 ]
Pihler-Puzovic, Draga [1 ]
机构
[1] Univ Manchester, Dept Phys & Astron, Oxford Rd, Manchester M13 9PL, England
[2] Univ Manchester, Manchester Ctr Nonlinear Dynam, Oxford Rd, Manchester M13 9PL, England
[3] Imperial Coll London, Dept Math, London SW7 2AZ, England
[4] Univ Oxford, Dept Engn Sci, Parks Rd, Oxford OX1 3PJ, England
来源
PHYSICAL REVIEW FLUIDS | 2023年 / 8卷 / 09期
基金
英国工程与自然科学研究理事会;
关键词
PRESSURE-DROP; SHAW;
D O I
10.1103/PhysRevFluids.8.094005
中图分类号
O35 [流体力学]; O53 [等离子体物理学];
学科分类号
070204 ; 080103 ; 080704 ;
摘要
A circular Hele-Shaw cell bounded by a volumetrically confined elastic solid can act as a fluidic fuse: during radially outward fluid flow, the solid deforms in response to the viscous pressure field such that the gap expands near the inlet (at the center) and contracts near the outlet (around the rim). If the flow rate exceeds a critical value, then the gap at the outlet can close completely, interrupting/choking the flow. Here, we consider the injection of gas into such a soft-walled Hele-Shaw cell filled with viscous liquid. Our theoretical model and numerical simulations for axisymmetric flow driven by the injection of an expanding gas bubble show that the bubble increases the critical flow rate of choking via two mechanisms. First, as the interface approaches the rim, it reduces the length over which the viscous pressure gradient deforms the solid, which increases the critical flow rate above which choking occurs. Second, compression of the gas reduces the outlet flow rate relative to the inlet flow rate. As a consequence, for large injection rates, a near-choking regime is established in which the outlet flow rate becomes independent of the injection rate and instead depends only on the instantaneous position of the interface. Our traveling-wave model for the advancement of the bubble front will enable future reduced-order modeling of nonaxisymmetric problems, such as viscous fingering.
引用
收藏
页数:22
相关论文
共 50 条
  • [41] Undulations on the surface of elongated bubbles in confined gas-liquid flows
    Magnini, M.
    Ferrari, A.
    Thome, J. R.
    Stone, H. A.
    PHYSICAL REVIEW FLUIDS, 2017, 2 (08):
  • [42] MODELING FLOW PATTERN TRANSITIONS FOR GAS-LIQUID FLOW
    DUKLER, AE
    TAITEL, Y
    TRANSACTIONS OF THE AMERICAN NUCLEAR SOCIETY, 1982, 41 : 666 - 667
  • [43] GAS-LIQUID FLOW AND GAS HOLDUP IN A HORIZONTAL LIQUID JET EJECTOR
    IMAMURA, Y
    KOBAYASHI, S
    INAZUMI, H
    KAGAKU KOGAKU RONBUNSHU, 1995, 21 (03) : 486 - 494
  • [44] SLUG FLOW TRANSITION IN HORIZONTAL GAS-LIQUID FLOW
    HIHARA, E
    SAITO, T
    BULLETIN OF THE JSME-JAPAN SOCIETY OF MECHANICAL ENGINEERS, 1984, 27 (234): : 2771 - 2778
  • [45] Flow regimes for adiabatic gas-liquid flow in microchannels
    Shao, N.
    Gavriilidis, A.
    Angeli, P.
    CHEMICAL ENGINEERING SCIENCE, 2009, 64 (11) : 2749 - 2761
  • [46] THE MIXING OF GAS-LIQUID FLOW WITH VAPOR AND GAS-SOLID FLOW
    林多敏
    蔡树棠
    AppliedMathematicsandMechanics(EnglishEdition), 1990, (06) : 513 - 518
  • [47] Performance of confined plunging liquid jet bubble column as a gas-liquid reactor
    Evans, GM
    Bin, AK
    Machniewskj, PM
    CHEMICAL ENGINEERING SCIENCE, 2001, 56 (03) : 1151 - 1157
  • [48] Instantaneous Mass Transfer under Gas-Liquid Taylor Flow in Circular Capillaries
    Pan, Zhiqun
    Zhang, Xubin
    Xie, Yunfeng
    Cai, Wangfeng
    CHEMICAL ENGINEERING & TECHNOLOGY, 2014, 37 (03) : 495 - 504
  • [49] Fluid dynamics of gas-liquid slug flow under the expansion effect in a microchannel
    Yin, Yaran
    Tian, Xinyu
    Zhu, Xingxing
    Liu, Huican
    Zhang, Xianming
    Zhu, Chunying
    Fu, Taotao
    Ma, Youguang
    CHEMICAL ENGINEERING SCIENCE, 2025, 302
  • [50] Flow and spray characteristics of a gas-liquid pintle injector under backpressure environment
    Li, Ziguang
    Zhou, Yaozhi
    Cheng, Peng
    Bai, Xiao
    Li, Qinglian
    PHYSICS OF FLUIDS, 2024, 36 (04)