Similar to Example 8.4-4 in F&R, 3rd Ed. energy balancing with phase changes A liquid process stream at 10°C contains 50.0 mol% benzene and 50.0 mol% toluene. This liquid mixture enters a process vessel where it is heated to 50°C and 164 mm Hg to form a vapor phase and liquid phase. The liquid product stream leaving the vessel contains 40 mol% benzene, while the vapor product stream leaving the vessel contains 66.3 mol% benzene. How much heat must be transferred to the mixture per mole of feed? 7. continuous process click here follow Blue Crib for the heat-of-reaction method Equation 7.5d-a with no heat-of-reaction terms v07.08.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 7-37 follow Blue Crib for the heat-of-reaction method Eq. 7.7 Eq. 7.8 Eq. 7.8 v07.08.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 7-38 follow Blue Crib for the heat-of-reaction method Eq. 7.7 Eq. 7.8 Eq. 7.8 v07.08.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 7-39 follow Blue Crib for the heat-of-reaction method Eq. 7.7 Eq. 7.8 Table B.2 in F&R, 3rd Ed. Table B.1 in F&R, 3rd Ed. Table B.2 in F&R, 3rd Ed. Eq. 7.8 v07.08.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 7-40 * v07.08.04 © 2007, Michael E. Hanyak, Jr., All Rights Reserved Page 7-41
© Copyright 2026 Paperzz