# Pressure distributions of gaseous slip flow in straight and uniform rectangular microchannels

- First Online:

- Received:
- Accepted:

DOI: 10.1007/s10404-004-0005-8

- Cite this article as:
- Jang, J. & Wereley, S.T. Microfluid Nanofluid (2004) 1: 41. doi:10.1007/s10404-004-0005-8

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## Abstract

This paper presents analytical derivations of the pressure distribution in straight and uniform rectangular microchannels in the slip flow regime and new experimental data in those channels. The flow is to be steady state, two-dimensional, isothermal, and to have negligible transverse velocities with a first order slip boundary condition. The measured pressure distributions of airflows are compared with newly derived analytical results. There is close agreement between the measurements and calculation by the slip flow formula. The dimensionless location of the maximum deviation from the linear pressure distribution is found analytically and compared with the measurements. This dimensionless location of the maximum deviation increases with the increasing pressure ratios in the slip flow regime. The effect of several parameters such as the channel aspect ratio and the Knudsen number on the locations of maximum deviation from linearity are investigated. The nonlinearity of the pressure distribution is also discussed.

### Keywords

Gaseous slip flow Pressure distribution Rectangular microchannel DRIE Nonlinearity### Nomenclature

*a*channel aspect ratio (=height/width)

*D*_{h}hydraulic diameter of a noncircular channel (m)

*H*height of a channel (m)

*h*half of the height of a channel (m)

*Kn*Knudsen number,

*Kn*=*λ*/*H*- \( \overline{{Kn}} \)
modified Knudsen number \( \overline{{Kn}} = Kn{{\left( {2 - \sigma } \right)}} \mathord{\left/ {\vphantom {{{\left( {2 - \sigma } \right)}} \sigma }} \right. \kern-\nulldelimiterspace} \sigma \)

*L*channel or tube length between upstream and downstream (m)

*Ma*Mach number

*ṁ*mass flow rate (kg/s)

*p*pressure (Pa)

*p**(*ζ*)dimensionless pressure with respect to

*p*_{o}at*ζ**R*_{s}specific gas constant (J/(kg K))

*Re*Reynolds number

*T*temperature (K)

*u*velocity vector

- \( v \)
*z*direction velocity (m/s)- \( \bar{v} \)
dimensionless

*z*component velocity*W*width of a rectangular channel (m)

*w*_{c}half of the width of a channel (m)

*x*,*y*rectangular Cartesian coordinates at each cross-section (m)

*z*streamwise coordinate (m)

*γ*specific heat ratio

*ζ*dimensionless variable for

*z*direction (=*z*/*L*)*η*dimensionless variable for

*y*direction (=*y*/*h)**κ*eigenvalue

*λ*mean free path of a gas (m)

*μ*dynamic viscosity (kg/(m s))

*ξ*dimensionless variable for

*x*direction (=*x*/*w*_{c}*)*- Π
pressure ratio (Π=

*p*_{i}/*p*_{o}*)**ρ*density (kg/m

^{3})*σ*tangential momentum accommodation coefficient (TMAC)

### Subscript

- avg
cross-section average

- i
inlet or upstream

- o
outlet or downstream

### Superscript

- *
nondimensionalization