It is shown that the flow in planar and annular squish gaps of internal combustion engines at the near end of the compression stroke resembles an unsteady stagnation point flow. When the ratio of the diffusion time across the boundary layer to the characteristic time of the outer flow is constant, as is the case when the final squish gap height is zero, then the compressible unsteady stagnation boundary-layer flow is self-similar. For a nonvanishing final gap height, the flow is nonsimilar but is treated locally in time as a quasisimilar flow. This quasisimilar flow may be computed by expanding the solution in powers of the above-mentioned ratio. The first term in this expansion is the steady compressible stagnation point boundary-layer flow. The reported heat-transfer rates have been measured in a single-stroke compression device. These agree well with only the first term in the expansion. Even steady incompressible stagnation point heat-transfer rates are found to correlate the experimental data satisfactorily.
Nomenclaturea =time function in Eq. (6) A c = cross-sectional area of the cylinder C = constant in viscosity law (/-i/jn^ = CT/T^) c p = specific heat at constant pressure / = dimensionless stream function g = dimensionless temperature function h =gap height h 0 = final gap height at top dead center (TDC) £ =gap width (£=r 0 -r / ) Nu =Nusselt number p = pressure Pr =Prandtl number q = heat flux r = variable Re = Reynolds number r ; = inner radius (half-width of recess channel in piston) r 0 -outer radius (half-width of piston) s = stroke t = time T = temperature T + = dimensionless wall temperature (T + = T W /T QO ) u,v = velocity components in x and y directions v p = piston velocity (v p = h) V R = recess volume in piston x = Cartesian coordinate along cylinder head y = Cartesian coordinate normal to cylinder head Y -material coordinate 7 = specific heat ratio d = boundary-layer thickness e = compression ratio t]-independent variable of similarity solution X = coefficient of thermal conductivity fj, -dynamic viscosity v -kinematic viscosity p = density r = shear stress i/' = stream function a;= angular velocity