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Code Manual for CONTAIN 2.0 - Federation of American Scientists

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10.0 HEAT AND MASS TRANSFER MODELS<br />

Heat and mass transfer processes are modeled at a number <strong>of</strong> interfaces in the CONTAJN code. The<br />

present chapter gives a general discussion <strong>of</strong> the heat and mass transfer modeling at such interfaces,<br />

in addition to a discussion <strong>of</strong> heat sink modeling and associated topics. Exceptions to this general<br />

treatment are noted in the discussion. Two types <strong>of</strong> heat sinks, heat transfer structures and lower cell<br />

layers, are discussed. The topics associated with heat sink modeling include heat sink characteristics<br />

and boundary conditions, heat conduction modeling, and the treatment <strong>of</strong> concrete outgassing. A<br />

discussion <strong>of</strong> the modeling available with respect to lower cell layers outside <strong>of</strong> these areas is given<br />

in Chapter 5.<br />

The present chapter is organized by process type. Natural convection and <strong>for</strong>ced convection heat<br />

transfer are discussed in Section 10.1, along with boundary layer properties and other quantities<br />

entering the expressions <strong>for</strong> convective heat transfer. Mass transfer processes are discussed in<br />

Section 10.2, along with quantities entering the expressions <strong>for</strong> mass transfer. Processes discussed<br />

in that section include condensate fdm flow on surfaces and condensation mass transfer. Radiative<br />

heat transfer is discussed in Section 10.3; boiling heat transfer is discussed in Section 10.4. The<br />

modeling <strong>of</strong> heat sinks and the associated topics mentioned above are discussed in Section 10.5. Key<br />

elements <strong>of</strong> the heat and mass transfer models are illustrated in Figure 10-1.<br />

Table 10-1 indicates the various code interfaces addressed by the present chapter, as well as the<br />

processes considered at each interface. The pool-structure interface listed in this table was<br />

implemented in <strong>CONTAIN</strong> 1.2, in conjunction with the pool tracking modifications, which allow<br />

the pool to be treated as a bulk fluid on the same footing as the gas. One consequence <strong>of</strong> these<br />

modifications is that heat transfer structures can now be submerged in the pool, as discussed in more<br />

detail in Section 10.1.1.4. Note that the distinction made in this table with regard to whether a<br />

process is simply modeled or modeled and coupled to the interface temperature calculation refers<br />

to the role <strong>of</strong> the process in determining the interface conditions. This distinction is explained in<br />

more detail in Section 10.6, in which the coupling between the heat and mass transfer processes is<br />

discussed.<br />

Table 10-1<br />

Heat and Mass Transfer Processes<br />

Considered at Various <strong>CONTAIN</strong> Interfaces*<br />

Interface<br />

Conv.<br />

HT<br />

Cond. Rad.<br />

HT<br />

Boiling<br />

HT<br />

Aerosol Film<br />

Inflow<br />

Gas-Structure c c c - c c<br />

Gas-Pool c c c - M M<br />

Gas-Lower Cell c c c - M -<br />

Pool-Structure c - - - - -<br />

Pool-Lower Cell c - - M -<br />

Gas-Engineered System c c - - M -<br />

●HT=heattransfe~MT=masstransfe~C=modeledandcoupledtointerfacetemperaturecalculation;M=modeled<br />

butnotcoupled<br />

Rev O 1o 1 6/30/97

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