) Heptane-Ethyl Benzene System. A feed of 200 mol/hr containing 36 mole % heptane and 64 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 92 mole...

$) Heptane-Ethyl Benzene System. A feed of 200 mol/hr containing 36 mole % heptane and 64 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 92 mole % heptane and a bottoms containing 8.0 mole % heptane. The reflux ratio used is 4.0:1. Equilibrium for system at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine ... a) Calculate the flowrates (mol/hr) of the distillate and bottoms. b) Determine the theoretical number of trays and the feed tray number for the specified operation. c) Determine the minimum reflux ratio, RMIN and the minimum number of theoretical trays at total reflux. Assuming that the feed mixture is saturated vapor determine ... d) Determine the theoretical number of trays and the feed tray number for the specified operation. e) Determine the minimum reflux ratio, RMIN and the minimum number of theoretical trays at total reflux. Isto 6 Is tne 5) Methyl Acetate-Ethyl Benzene System. A feed of 1000 mol/hr containing 40 mole % methyl acetate and 60 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 90 mole % methyl acetate and a bottoms containing 10.0 mole % methyl acetate. The reflux ratio used is 5.0:1. Equilibrium for the syster at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine .. a) Calculate the flowrates (mol/hr) of the distillate and bottoms. b) Determine the theoretical number of trays and the feed tray number for the specified operation. tho minimum reflux ratio, RMIN and the minimum number of theoretical trays at total refl determine ... L operation. $

Extracted text: ) Heptane-Ethyl Benzene System. A feed of 200 mol/hr containing 36 mole % heptane and 64 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 92 mole % heptane and a bottoms containing 8.0 mole % heptane. The reflux ratio used is 4.0:1. Equilibrium for system at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine ... a) Calculate the flowrates (mol/hr) of the distillate and bottoms. b) Determine the theoretical number of trays and the feed tray number for the specified operation. c) Determine the minimum reflux ratio, RMIN and the minimum number of theoretical trays at total reflux. Assuming that the feed mixture is saturated vapor determine ... d) Determine the theoretical number of trays and the feed tray number for the specified operation. e) Determine the minimum reflux ratio, RMIN and the minimum number of theoretical trays at total reflux. Isto 6 Is tne 5) Methyl Acetate-Ethyl Benzene System. A feed of 1000 mol/hr containing 40 mole % methyl acetate and 60 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 90 mole % methyl acetate and a bottoms containing 10.0 mole % methyl acetate. The reflux ratio used is 5.0:1. Equilibrium for the syster at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine .. a) Calculate the flowrates (mol/hr) of the distillate and bottoms. b) Determine the theoretical number of trays and the feed tray number for the specified operation. tho minimum reflux ratio, RMIN and the minimum number of theoretical trays at total refl determine ... L operation.

Heptane - Ethyl Benzene at 1atm<br>(101.325kPa)<br>Temperature<br>Heptane<br>T(F)<br>409.3<br>136.2<br>00 w00<br>to 0 0<br>406.3<br>133.2<br>0.050<br>0.125<br>403.5<br>130.3<br>0.234<br>400.8<br>127.6<br>0.150<br>0.329<br>398.3<br>125.1<br>0.200<br>0.412<br>395.9<br>122.8<br>0.250<br>0.485<br>393.7<br>120.5<br>0.300<br>0.550<br>391.5<br>118.4<br>0.350<br>0.607<br>389.5<br>116.4<br>0.659<br>387.6<br>114.5<br>0.450<br>0.705<br>385.8<br>112.7<br>0.500<br>0.746<br>111.0<br>0.550<br>0.783<br>382.5<br>109.3<br>0.817<br>380.9<br>107.7<br>0.650<br>0.848<br>379.4<br>106.2<br>0.700<br>0.876<br>378.0<br>104.8<br>0.750<br>0.901<br>376.6<br>103.4<br>0.800<br>0.924<br>375.3<br>102.1<br>0.850<br>0.946<br>374.0<br>100.8<br>0.965<br>372.8<br>99.6<br>0.950<br>0.983<br>371.6<br>98.4<br>to w0 0<br>to 0 0<br>

Extracted text: Heptane - Ethyl Benzene at 1atm (101.325kPa) Temperature Heptane T(F) 409.3 136.2 00 w00 to 0 0 406.3 133.2 0.050 0.125 403.5 130.3 0.234 400.8 127.6 0.150 0.329 398.3 125.1 0.200 0.412 395.9 122.8 0.250 0.485 393.7 120.5 0.300 0.550 391.5 118.4 0.350 0.607 389.5 116.4 0.659 387.6 114.5 0.450 0.705 385.8 112.7 0.500 0.746 111.0 0.550 0.783 382.5 109.3 0.817 380.9 107.7 0.650 0.848 379.4 106.2 0.700 0.876 378.0 104.8 0.750 0.901 376.6 103.4 0.800 0.924 375.3 102.1 0.850 0.946 374.0 100.8 0.965 372.8 99.6 0.950 0.983 371.6 98.4 to w0 0 to 0 0

Jun 09, 2022

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) Heptane-Ethyl Benzene System. A feed of 200 mol/hr containing 36 mole % heptane and 64 mole % ethyl benzene is to be fractionated at 101.325kPa (abs) in order to form a distillate containing 92 mole...

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