Experimental and Numerical Study of Swirling ... - Solid Mechanics
Experimental and Numerical Study of Swirling ... - Solid Mechanics Experimental and Numerical Study of Swirling ... - Solid Mechanics
Experi imental and Numerical N Stud dy of Swirling g Flow in Scaveenging Processs for 2-Stroke Marin ne Diesel Engin nes Figure 4.40 0: Normalized Rad dial Velocity Profiles s for L=8D. profile towards a mo ore uniform diistribution by an increase inn the V in thhe z vortex core c and decre ease in its maxximum value ( Figure 4.39). At positions zz11 z13 for L3, L the axial ve elocity becomees nearly consttant in most oof the regions of cylinder cross-section n except near wwall regions. 4.3.3 Radial Velocity Ve Prof ofile Chapter 4 The ma agnitude of radial velocity Vr is small compared too almost a factor of 10 0 lower (Figurre 4.40). The ffigure shows V V and Vz i. .e. Vr profile for z1 92 Swirling Flow in a Pipe
Experi imental and Numerical N Stud dy of Swirling g Flow in Scaveenging Processs for 2-Stroke Marin ne Diesel Engin nes Figu ure 4.41: Swirl l Parameter S Profil les (absolute valu ues) for L= =8D. and the en from z7-z13. . The decay inn the radial veelocity downsstream the floow can be understood fr rom Vr profilles at z1 and zz7. At z7 the radial velocity is very clo ose to zero and a then at further downnstream position z8 it starrts increasi ing again but with its direction reversedd along Xv i.ee. from z1-z6 thhe positive e values (vecto or direction nootation) of Vr are along poositive Xv and zz8 z11 along g negative Xv. At z12 and z13 Vr is in the same direction on both siddes of Xv. Flow F exhibits same behavioor for Vr at bboth Reynoldds numbers ReA and ReB B. 4.3.4 Swirl Par rameter Chapter 4 The sw wirl parameter S as definedd in Chapter 2 is the ratioo of V to V . z Since th he variation in n cylinder lenggth, in generaal, has no signiificant effect oon the tang gential and ra adial velocity pprofile at a givven measuringg position, onnly the resu ults for L1 ar re presented here (Figure 4.41). This wwill provide aan overview w of local swirl distributionn as well as thee decay in thee swirl along thhe flow dir rection for ReA A and ReB. To get a better overv view of swirl parameter aloong the cylindder, figure 4.442 gives th he profile of f S whichh is the maxximum value of local swiirl max parame eter for a given measuring position. Proffile generally demonstratess a sharp li inear like deca ay in swirl fromm z1-z4 and then a very small. The linear ffit has a slo ope of 1.7732 and a Y-axis intercept of -0. .52964. For L33 at z6 a increaase in S is observed which, w as descrribed before, iss due to the efffect of cylindder max 93 Swirling Flow in a Pipe
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Experi imental <strong>and</strong> <strong>Numerical</strong> N Stud dy <strong>of</strong> <strong>Swirling</strong> g Flow in Scaveenging<br />
Processs<br />
for 2-Stroke<br />
Marin ne Diesel Engin nes<br />
Figu ure 4.41:<br />
Swirl l Parameter S<br />
Pr<strong>of</strong>il les (absolute valu ues)<br />
for L= =8D.<br />
<strong>and</strong> the en from z7-z13. . The decay inn<br />
the radial veelocity<br />
downsstream<br />
the floow<br />
can be understood fr rom Vr pr<strong>of</strong>illes<br />
at z1 <strong>and</strong> zz7.<br />
At z7 the radial<br />
velocity is<br />
very clo ose to zero <strong>and</strong> a then at further downnstream<br />
position<br />
z8 it starrts<br />
increasi ing again but with its direction<br />
reversedd<br />
along Xv i.ee.<br />
from z1-z6 thhe<br />
positive e values (vecto or direction nootation)<br />
<strong>of</strong> Vr are along poositive<br />
Xv <strong>and</strong> zz8<br />
z11 along g negative Xv. At z12 <strong>and</strong> z13 Vr is in the same direction<br />
on both siddes<br />
<strong>of</strong> Xv. Flow F exhibits same behavioor<br />
for Vr at bboth<br />
Reynoldds<br />
numbers ReA<br />
<strong>and</strong> ReB B.<br />
4.3.4<br />
Swirl Par rameter<br />
Chapter 4<br />
The sw wirl parameter S as definedd<br />
in Chapter 2 is the ratioo<br />
<strong>of</strong> V to V .<br />
z<br />
Since th he variation in n cylinder lenggth,<br />
in generaal,<br />
has no signiificant<br />
effect oon<br />
the tang gential <strong>and</strong> ra adial velocity ppr<strong>of</strong>ile<br />
at a givven<br />
measuringg<br />
position, onnly<br />
the resu ults for L1 ar re presented here (Figure 4.41). This wwill<br />
provide aan<br />
overview w <strong>of</strong> local swirl<br />
distributionn<br />
as well as thee<br />
decay in thee<br />
swirl along thhe<br />
flow dir rection for ReA A <strong>and</strong> ReB.<br />
To get a better overv view <strong>of</strong> swirl parameter aloong<br />
the cylindder,<br />
figure 4.442<br />
gives th he pr<strong>of</strong>ile <strong>of</strong> f S whichh<br />
is the maxximum<br />
value <strong>of</strong> local swiirl<br />
max<br />
parame eter for a given<br />
measuring position. Pr<strong>of</strong>file<br />
generally demonstratess<br />
a<br />
sharp li inear like deca ay in swirl fromm<br />
z1-z4 <strong>and</strong> then<br />
a very small.<br />
The linear ffit<br />
has a slo ope <strong>of</strong> 1.7732 <strong>and</strong> a Y-axis intercept<br />
<strong>of</strong> -0. .52964. For L33<br />
at z6 a increaase<br />
in S is observed which, w as descrribed<br />
before, iss<br />
due to the efffect<br />
<strong>of</strong> cylindder<br />
max<br />
93<br />
<strong>Swirling</strong> Flow in a Pipe