Experimental and Numerical Study of Swirling ... - Solid Mechanics
Experimental and Numerical Study of Swirling ... - Solid Mechanics
Experimental and Numerical Study of Swirling ... - Solid Mechanics
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<strong>Experimental</strong> <strong>and</strong> <strong>Numerical</strong> <strong>Study</strong> <strong>of</strong> <strong>Swirling</strong> Flow in Scavenging Process for 2-Stroke<br />
Marine Diesel Engines<br />
In general the magnitudes <strong>of</strong> shear stress components, at different measuring<br />
positions are observed to be smaller than normal stress components.<br />
Considering the maximum values, for shear stresses (Cartesian coordinates)<br />
uw vw uv indicating anisotropy <strong>of</strong> the flow. However, with swirl<br />
decay downstream at z (z/D=3.068), the maximum values become almost<br />
5<br />
equal for individual components <strong>of</strong> both normal <strong>and</strong> shear stress<br />
components i.e. ww uu vv <strong>and</strong> uw vw uv .<br />
The Reynolds<br />
stresses decay with the swirl <strong>and</strong> distribution <strong>of</strong> normal <strong>and</strong> shear<br />
components tends to become comparatively <strong>and</strong> gradually more uniform in<br />
the flow domain. With swirl decay downstream, the flow at high Reynolds<br />
number has higher tendency towards a more uniform spatial distribution <strong>of</strong><br />
individual Reynolds stress components in the flow domain.<br />
At z 1 (z/D=0.963) the turbulent kinetic energy is strong in the vortex core <strong>and</strong><br />
near wall region. The maximum value is observed in the vortex core region<br />
<strong>and</strong> the contours show an asymmetric distribution. The turbulent kinetic<br />
energy decreases downstream.<br />
The flow at low Reynolds number is less responsive or in other words more<br />
resistive to the variations in vorticity, Reynolds stresses <strong>and</strong> turbulent kinetic<br />
energy as the swirl decays along the pipe.<br />
1.1.2 Effect <strong>of</strong> Piston Position on the Confined <strong>Swirling</strong><br />
Flow<br />
In this experiment the length <strong>of</strong> cylinder was kept 4D but the piston is<br />
translated <strong>and</strong> adjusted to fixed positions where it closes the intake to the<br />
cylinder by 0% (Fully Open intake port), 25%, 50% <strong>and</strong> 75%. For each piston<br />
position, stereoscopic PIV measurements were conducted at the<br />
aforementioned Reynolds numbers.<br />
When the piston is partially closing the cylinder intake port, the piston serves<br />
as a forward-step facing the incoming flow into the cylinder <strong>and</strong> affects the<br />
magnitude <strong>of</strong> radial velocity in particular <strong>and</strong> also tangential velocity to some<br />
extent. This consequently increases the axial velocity magnitude. Since the<br />
flow rate is kept constant but the inlet area is reduced, therefore, the average<br />
velocity at the inlet increases. The piston also behaves as a bluff-body in the<br />
flow path generating unsteady fluctuations/ disturbances at the sharp-edge<br />
interface <strong>of</strong> the piston top <strong>and</strong> outer wall. These fluctuations result in growth<br />
<strong>of</strong> instabilities <strong>and</strong> waves <strong>and</strong> are superimposed on already precessing helical<br />
vortical flow that is observed when the port is fully open. This indicates that<br />
the resulting in-cylinder swirling flow becomes more transient. This also puts<br />
some challenge for making non-time resolved PIV measurements.<br />
At 25% intake port closure <strong>and</strong> a given Reynolds number, the peak values <strong>of</strong><br />
tangential velocity decreases <strong>and</strong> axial velocity increases. At z 1 (z/D=0.963),<br />
<br />
167<br />
Summary & Conclusions