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 />
1.1.1 <strong>Swirling</strong> Flow in a Pipe with different Lengths<br />
In this experiment the inlet to the measuring cylinder was kept fully opened<br />
<strong>and</strong> the measurements are conducted by changing the length <strong>of</strong> the cylinder<br />
to 8D, 6D <strong>and</strong> 4D.<br />
The results from LDA measurement show that in the inlet section, the wake<br />
effect behind the guide vanes reduces significantly before entering the<br />
contraction region. The velocity distribution in the inlet section at different<br />
circumferential position is not symmetric at a radial distance <strong>of</strong> 200 mm.<br />
However, after the flow passes through the contraction region the variation<br />
<strong>of</strong> the angle between radial <strong>and</strong> tangential component (along the<br />
circumferential positions) is reduced to 1.5°. At an axial position z/D <strong>of</strong><br />
0.368, the LDA measurements show a near symmetric distribution <strong>of</strong><br />
tangential velocity.<br />
The PIV results show that the resulting confined swirling flow has a<br />
tangential velocity pr<strong>of</strong>ile similar to Burgers vortex <strong>and</strong> the axial velocity has<br />
a wake-like pr<strong>of</strong>ile. The tangential velocity pr<strong>of</strong>ile shows that unlike the<br />
theoretical Burgers vortex pr<strong>of</strong>ile, the region surrounding the inner forced<br />
vortex core region is not irrotational. Instead, the region has a very weak<br />
vorticity that may possibly be as a result <strong>of</strong> a radially decaying vortex causing<br />
a vorticity transfer from vortex core to the surrounding regions. This result is<br />
in accordance with some other experimental results reported earlier in the<br />
scientific literature. The swirl decays downstream the flow <strong>and</strong> the vortex<br />
core size increases. This changes the tangential velocity pr<strong>of</strong>ile towards more<br />
forced vortex <strong>and</strong> the axial velocity to be more uniform by transferring more<br />
mass in to the central velocity deficit region. The effect <strong>of</strong> variation in<br />
Reynolds number is mostly observed in the vortex core region where for<br />
initial measuring positions the peak value <strong>of</strong> normalized tangential <strong>and</strong> axial<br />
velocity is found to be higher for low Reynolds number. Further, for axial<br />
velocity, the minimum velocity in the velocity deficit region is found to be<br />
lower in case <strong>of</strong> high Reynolds number. However, the axial velocity pr<strong>of</strong>ile at<br />
all measuring positions does not show any reverse flow. The average size <strong>of</strong><br />
the vortex core at low Reynolds number is observed to be relatively smaller<br />
than at high Reynolds number. For first five measuring positions close to<br />
cylinder inlet, which are common in cylinder lengths 8D, 6D <strong>and</strong> 4D, the<br />
variation in cylinder length seems to have no significant effect on the<br />
normalized tangential <strong>and</strong> axial velocity pr<strong>of</strong>iles for a given Reynolds<br />
number. Similar behavior is observed for the positions which are common in<br />
cylinder lengths 8D <strong>and</strong> 6D. For position z 6 (z/D=3.595) being very close to<br />
cylinder outlet for cylinder length 4D, a small increase in the tangential <strong>and</strong><br />
axial velocity is observed due to small diameter outlet pipe. This indicates<br />
that the downstream change in cylinder length is not detected by the flow at<br />
upstream positions <strong>and</strong> thus the flow mainly depends on the upstream<br />
conditions at the cylinder inlet.<br />
The magnitude <strong>of</strong> radial velocity at position z 1 (z/D=0.963), is almost a factor<br />
<strong>of</strong> 10 lower than tangential <strong>and</strong> axial velocity <strong>and</strong> decreases further<br />
<br />
165<br />
Summary & Conclusions