![]() Calculate and tabulate the external heat quantities to the base of Tray (B + 1). ![]() Set the temperature drop across the at 30 degrees F and calculate the heat content of the product leaving the system. Convert the of the unstripped hydrocarbon liquid on the draw tray to this partial pressure and check the assumed temperature. Presence in the vapor of the overhead distillate liquid and considering the overhead distillate vapor and steam as inerts. Heat and equations-top tray and condenser. Last Updated on Mon, (2) CIRCULATION RATE LC3 = QC3/(c)(t(n-2)-tC32) (3) CONDENSER DUTY-ENVELOPE ZT Qcoh= Qvn-(qnv+QNl + QH2o) Figure 4.7. From the Ballast Tray Design Manual Bulletin 4900. And perhaps the best overall tool for tray design. In the publication 'Ballast Tray Design Manual,' Bulletin No. ![]() 'Ballast Tray Design Manual,' Bulletin No.
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