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Pertinent information of the geometry of one module is given in Figure 4. Figure 4. Module of the Plate Heat Exchanger Coil The increase of heat transfer at the air side can be assumed to be of no influence to the convective heat transfer of the condensing refrigerant and to the conductive heat transfer through the wall. Therefore, the apparent air side convective heat transfer coefficient h* can be determined from u*. h*, the AA hydraulic diameter of the air passage, and the thermal conductivity of moist air together yield the Nusselt number Nu* and the augmentation of heat transfer can be expressed as Q is larger than the required Q and in a similar way as discussed above, the cw c Nu* A NuA A Nu A (1) heat exchanger area either could be decreased to A* or T could be lowered to cc T* in order to lower LMTD (Log Mean Temperature Difference). c schematically in the T vs. A plot of Figure 5. c This is shown B-5 Nu APDF Image | Development of the Zinc-Chlorine Battery for Utility
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