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Linear stability of a fluid channel with a porous layer in the center 被引量:2

Linear stability of a fluid channel with a porous layer in the center
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摘要 We perform a Poiseuille flow in a channel linear stability analysis of a inserted with one porous layer in the centre, and focus mainly on the effect of porous filling ratio. The spectral collocation technique is adopted to solve the coupled linear stability problem. We investigate the effect of permeability, σ, with fixed porous filling ratio ψ = 1/3 and then the effect of change in porous filling ratio. As shown in the paper, with increasing σ, almost each eigenvalue on the upper left branch has two subbranches at ψ = 1/3. The channel flow with one porous layer inserted at its middle (ψ = 1/3) is more stable than the structure of two porous layers at upper and bottom walls with the same parameters. By decreasing the filling ratio ψ, the modes on the upper left branch are almost in pairs and move in opposite directions, especially one of the two unstable modes moves back to a stable mode, while the other becomes more instable. It is concluded that there are at most two unstable modes with decreasing filling ratio ψ. By analyzing the relation between ψ and the maximum imaginary part of the streamwise phase speed, Cimax, we find that increasing Re has a destabilizing effect and the effect is more obvious for small Re, where ψ a remarkable drop in Cimax can be observed. The most unstable mode is more sensitive at small filling ratio ψ, and decreasing ψ can not always increase the linear stability. There is a maximum value of Cimax which appears at a small porous filling ratio when Re is larger than 2 000. And the value of filling ratio 0 corresponding to the maximum value of Cimax in the most unstable state is increased with in- creasing Re. There is a critical value of porous filling ratio (= 0.24) for Re = 500; the structure will become stable as ψ grows to surpass the threshold of 0.24; When porous filling ratio ψ increases from 0.4 to 0.6, there is hardly any changes in the values of Cimax. We have also observed that the critical Reynolds number is especially sensitive for small ψ where the fastest drop is observed, and there may be a wide range in which the porous filling ratio has less effect on the stability (ψ ranges from 0.2 to 0.6 at σ = 0.002). At larger permeability, σ, the critical Reynolds number tends to converge no matter what the value of porous filling ratio is. We perform a Poiseuille flow in a channel linear stability analysis of a inserted with one porous layer in the centre, and focus mainly on the effect of porous filling ratio. The spectral collocation technique is adopted to solve the coupled linear stability problem. We investigate the effect of permeability, σ, with fixed porous filling ratio ψ = 1/3 and then the effect of change in porous filling ratio. As shown in the paper, with increasing σ, almost each eigenvalue on the upper left branch has two subbranches at ψ = 1/3. The channel flow with one porous layer inserted at its middle (ψ = 1/3) is more stable than the structure of two porous layers at upper and bottom walls with the same parameters. By decreasing the filling ratio ψ, the modes on the upper left branch are almost in pairs and move in opposite directions, especially one of the two unstable modes moves back to a stable mode, while the other becomes more instable. It is concluded that there are at most two unstable modes with decreasing filling ratio ψ. By analyzing the relation between ψ and the maximum imaginary part of the streamwise phase speed, Cimax, we find that increasing Re has a destabilizing effect and the effect is more obvious for small Re, where ψ a remarkable drop in Cimax can be observed. The most unstable mode is more sensitive at small filling ratio ψ, and decreasing ψ can not always increase the linear stability. There is a maximum value of Cimax which appears at a small porous filling ratio when Re is larger than 2 000. And the value of filling ratio 0 corresponding to the maximum value of Cimax in the most unstable state is increased with in- creasing Re. There is a critical value of porous filling ratio (= 0.24) for Re = 500; the structure will become stable as ψ grows to surpass the threshold of 0.24; When porous filling ratio ψ increases from 0.4 to 0.6, there is hardly any changes in the values of Cimax. We have also observed that the critical Reynolds number is especially sensitive for small ψ where the fastest drop is observed, and there may be a wide range in which the porous filling ratio has less effect on the stability (ψ ranges from 0.2 to 0.6 at σ = 0.002). At larger permeability, σ, the critical Reynolds number tends to converge no matter what the value of porous filling ratio is.
出处 《Acta Mechanica Sinica》 SCIE EI CAS CSCD 2014年第1期28-36,共9页 力学学报(英文版)
基金 supported by the National Natural Science Foundation of China(40972160 and 51306130)
关键词 Porous layer Linear stability Porous filling ratio Poiseuille flow Interface Porous layer Linear stability Porous filling ratio Poiseuille flow Interface
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参考文献7

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同被引文献14

  • 1Vafai K, Kim S J. Forced Convection in a Channel Filled with a Porous Medium:an Exact Solution [ J ]. Journal of Heat Transfer, 1989,32 (4) : 1103 - 1106.
  • 2Nield D A. The Stability of Flow in a Channel or Duct Occupied by a Porous Medium [ J]. Journal of Heat Transfer, 2003,46 ( 22 ) :4351 - 4354.
  • 3Chandesris M,Jamet D. Boundary Conditions at a Pla- nar Fluid-Porous Interface for a Poiseuille Flow [ J ]. International Journal of Heat and Mass Transfer,2006, 49(13) :2137 -2150.
  • 4Beavers G S, Joseph D D. Boundary Conditions at a Naturally Permeable Wall [ J]. Journal of Fluid Me- chanics, 1967,30 ( 1 ) :197 -207.
  • 5Tilton N, Cortelezzi L. The Destabilizing Effects ofWall Permeability in Channel Flows:a Linear Stabili- ty Analysis [ J ]. Physics of Fluids, 2006, 18 ( 5 ) : 051702.
  • 6Ochoa-Tapia J A,Whitaker S. Momentum Transfer at the Boundary between a Porous Medium and a Homo- geneous Fluid I : Theoretical Development[ J]. Inter- national Journal of Heat and Mass Transfer, 1995,38 (14) :2635- 2646.
  • 7Whitaker S. The Forchheimer Equation:a Theoretical Development[ J]. Transport in Porous Media, 1996, 25(1) :27 -61.
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  • 9伊松林,张璧光,何正斌,苑青微.木材真空干燥设备加热系统理论计算的探讨[J].化工机械,2010(3):312-315. 被引量:3
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