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Kamis, 10 Mei 2018

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Forced convection is type of heat transport in which fluid motion is generated by an external source like a (pump, fan, suction device, etc.). Heat transfer through porus media is very effective and efficiently. Porous medium is defined as a material volume consisting of solid matrix with an interconnected void. Flow in porous media have revealed the Darcy law< which relates linearly the flow velocity to the pressure gradient across the porous medium. Forced convection heat transfer in a confined porous medium has been a subject of intensive studies during the last decades because of its wide applications, including: Chemical, Environmental, Mechanical, Geological and Petroleum.

The basic problem in heat convection through porous media consists of predicting the heat transfer rate between a deferentially heated, solid impermeable surface and a fluid-saturated porous medium.We begin with constant wall temperature.

In 2D steady state system

? u / ? x + ? v / ? y = 0 {\displaystyle \partial u/\partial x+\partial v/\partial y=0}

According to Darcy's law

u = - ( K / ? ) ? P / ? x {\displaystyle u=-(K/\mu )\partial P/\partial x}

v = - ( K / ? ) ? P / ? y {\displaystyle v=-(K/\mu )\partial P/\partial y}

u ? T / ? x + v ? T / ? y = ? ? 2 ? x 2 T {\displaystyle u\partial T/\partial x+v\partial T/\partial y={\boldsymbol {\alpha }}{\partial ^{2} \over \partial x^{2}}T}

u = {\displaystyle u=} U ? {\displaystyle U_{\infty }} v = 0 {\displaystyle v=0}

P ( x ) = - ( ? / K ) U ? x + c o n s t a n t {\displaystyle P(x)=-(\mu /K)U\infty x+constant}

Let ? t {\displaystyle \delta _{t}} be the thickness of the slender layer of length x that affects the temperature transition from T 0 {\displaystyle T_{0}} to T ? {\displaystyle T_{\infty }} .

Balancing the energy equation between enthalpy flow in the x direction and thermal diffusion in the y direction

U ? ? T / ? x ~ ? ? T / ? t 2 {\displaystyle U_{\infty }\partial T/\partial x\sim \alpha \Delta T/\delta _{t}^{2}}

boundary is slender so ? t << x {\displaystyle \delta _{t}<<x}

? t / x ~ P e x - .5 {\displaystyle \delta _{t}/x\sim Pe_{x}^{-}.5}

N u = h x / K ~ x / ? t ~ P e x 0 .5 {\displaystyle Nu=hx/K\sim x/\delta _{t}\sim Pe_{x}^{0}.5}

The Peclet number is a dimensionless number used in calculations involving convective heat transfer. It is the ratio of the thermal energy convected to the fluid to the thermal energy conducted within the fluid.

P e x {\displaystyle Pe_{x}} = {\displaystyle =} Advective transport rate / {\displaystyle /} Diffusive transport rate

P e x = U ? x / ? {\displaystyle Pe_{x}=U_{\infty }x/\alpha }


Video Forced convection in porous media



See also

  • Darcy's law
  • Nusselt Number
  • Porous media
  • Convective heat transfer
  • Heat transfer coefficient
  • Porous media

Maps Forced convection in porous media



References


Analyze Thermal Effects with the Heat Transfer Module
src: cdn.comsol.com


External links

  • http://www.me.ust.hk/~mezhao/pdf/20.PDF

Source of the article : Wikipedia

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