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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

Mathematical model<br />

The use <strong>of</strong> a specific multiphase model (the discrete phase, mixture, Eulerian model) to characterize<br />

momentum transfer depends on the volume fraction <strong>of</strong> solid particles and on the fulfillment <strong>of</strong> the requirements<br />

which enable the selection <strong>of</strong> a given model.<br />

Geometries for CFD simulation<br />

The computational grid for the horizontal pipe bend similar to that used in experiments having size <strong>of</strong><br />

5m before bend and 0.8m after bend in horizontal plane and it has 52mm internal diameter. It consists <strong>of</strong> 3001<strong>20</strong><br />

hexahedral cells and 322344 nodes has been generated using GAMBIT s<strong>of</strong>tware.<br />

Grid Generation<br />

The body-fitted coordinate technique was used with the help <strong>of</strong> the Gambit s<strong>of</strong>tware package to<br />

generate three-dimensional grids for bend and straight sections, according to the actual dimensions <strong>of</strong> the test<br />

sections.<br />

Volume statistics:<br />

Minimum volume: 5.5X 10 -9 m 3<br />

Maximum volume: 9.6X 10 -8 m 3<br />

Total volume: 4.17 X 10 -2 m 3<br />

Face area statistics:<br />

Minimum face area: 1.38X 10 -6 m 2<br />

Maximum face area: 2.47 X 10 -4 m 2<br />

Fig. 2 Meshing at interior <strong>of</strong> pipe bend (horizontal to horizontal)<br />

Numerical Simulation<br />

The grid files generated by Gambit were used for the simulation in Fluent. The experimental conditions<br />

were approximated using the following assumptions<br />

• The flow was assumed to be isothermal<br />

• The flow was assumed to be incompressible<br />

• The flow was assumed unsteady.<br />

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