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Code Manual for CONTAIN 2.0 - Federation of American Scientists

Code Manual for CONTAIN 2.0 - Federation of American Scientists

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Flow Time Co nstants. The flow calculations are done with either a Runge-Kutta timestep, in the<br />

explicit flow option, or a convective timestep, in the implicit flow option. In the latter case, the flow<br />

timestep is set to the minimum <strong>of</strong> convection timestep or the system timestep. With the<br />

recommended implicit flow option, there is relatively little advantage to using a system timestep that<br />

is much larger than the flow timestep, and the system timestep should be set to a comparable value.<br />

Since the system timestep determines the frequency at which global conditions are provided to other<br />

modules, use <strong>of</strong> a system timestep much larger than the flow timestep may mean that the conditions<br />

are not updated frequently enough. In general, one should check on the sensitivity to the system<br />

timestep by reducing it by a factor <strong>of</strong> two or more in the time domain <strong>of</strong> interest.<br />

The convection time will depend on the relative pressure differences between cells. In the blowdown<br />

<strong>of</strong> cell at high pressure, the cell contents will convect out with a time constant equal to the pressure<br />

relaxation time. A simple rule <strong>of</strong> thumb <strong>for</strong> such transient conditions is that if the system timestep<br />

is short enough to resolve a 20% change in the pressures, it should be adequate with respect to the<br />

cell convection time <strong>of</strong> the blowdown cell.<br />

If the initial pressure difference is not large, the cell contents will not convect out significantly during<br />

the pressure relaxation to the steady state. In this case, most <strong>of</strong> the convection, if any, will occur<br />

under low, steady-state pressure differences. The timestep to use in this case is less obvious than the<br />

one to use <strong>for</strong> transients. For cases in which the gas convection time controls the flow timestep, the<br />

steady-state convection time, t,, <strong>for</strong> cell i with total volume Vi should be obtained from<br />

where the k sum is carried out over all flows into cell i and the j sum is carried out <strong>for</strong> all flows out<br />

<strong>of</strong> cell i, Wij is the mass flow rate, and pij is the flow density in the flow path. The steady-state<br />

convection time is typically much longer than the pressure relaxation time in such cases.<br />

Fluid-Structure Time Constant. Another important potential source <strong>of</strong> inaccuracy or instability due<br />

to explicit coupling occurs at the cell level, where a bulk fluid may transfer an excessive amount <strong>of</strong><br />

heat into a structure, because the effect on the surface temperature is not properly taken into account.<br />

A criterion <strong>for</strong> the maximum cell timestep can be obtained if the fluid-to-structure heat transfer<br />

coefficient his known. By requiring the temperature rise in the first node during a single timestep<br />

Atl to be less than the fluid-structure temperature difference, one obtains <strong>for</strong> an insulated first node,<br />

Atl

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