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5% - eTheses Repository - University of Birmingham

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Chapter 5<br />

DENSITY PARTICLE=2850.000 Kg/m3<br />

TERMINAL SPEED = O.280 n/s<br />

DENSITY LIQUID =1000.000 Kg/m3<br />

ANGULAR UELOCITY= 3.571 Non-d<br />

CORE RADIUS = 0.005 m<br />

SCALE FACTOR = 10.000<br />

CUM, CL, DT= 0.5000 0.5000 0.0112<br />

Nondimensional<br />

Fall Time<br />

Fall Time vs Starting Position<br />

2 4 6 8 10 12<br />

Figure 9a<br />

Starting Location (Non-dimensional Radii)<br />

DENSITY PARTICLE=2850, 000 Kg/m3<br />

TERMINAL SPEED = 0 280 nxs<br />

DENSITY LIQUID =1000, 000 Kg/n3<br />

ANGULAR UELOCITY= 3. 571 Non-d<br />

CURE RADIUS = 0. 010 n<br />

SCALE FACTOR = 10. 000<br />

CUM, CL, DT= 0.5000 0. 5000 0.0056<br />

Nondimensional<br />

Fall Ike<br />

Fall Time vs Starting Position<br />

2 4 6 8 10 12<br />

Figure 9b<br />

Starting Location (Non-dimensional Radii)<br />

DENSITY PftRTICLE=2850.000 Kg/ro3<br />

TERMINAL SPEED = 0.280 n/s<br />

DENSITY LIQUID =1000.000 Kg/ji>3<br />

ANGULAR VELOCITY= 3.571 Non d<br />

CORE RADIUS = 0.020 n<br />

SCftLE FACTOR = 10.000<br />

CVM t CL, DT=0.500, 0.500, 0.0028<br />

Nondimensional<br />

Fall Time<br />

Fall Time vs Starting Position<br />

10 12<br />

Starting Location (Non-dimensional Radii)<br />

Figure 9c<br />

Figure 9a-c. The above plates show the effect <strong>of</strong> keeping the velocity at<br />

the core radius constant whilst increasing the core size. The graph on<br />

the right shows the fall time for each <strong>of</strong> the trajectories in the picture<br />

on the left.

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