Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated llyu ) Calculate the flowrates (mol/hr) of the distillate and bottoms. ) Determine the theoretical number of trays and...

$Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated llyu ) Calculate the flowrates (mol/hr) of the distillate and bottoms. ) Determine the theoretical number of trays and the feed tray number for the specified operation. :) 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. 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 system at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine ...o 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. ul 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. unOouraged as a tool useful to solve the problems. $

Extracted text: Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated llyu ) Calculate the flowrates (mol/hr) of the distillate and bottoms. ) Determine the theoretical number of trays and the feed tray number for the specified operation. :) 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. 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 system at 101.325kPa are available. Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated liquid) determine ...o 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. ul 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. unOouraged as a tool useful to solve the problems.

Methyl Acetate Ethyl Benzene<br>at 1atm (101.325kPa)<br>Temperature<br>Methyl Acetate<br>T (K)<br>136.2<br>409.3<br>00 0 0<br>00 0 0<br>124.0<br>397.2<br>0.050<br>0.323<br>114.4<br>387.5<br>0.100<br>0.518<br>106.6<br>379.8<br>0.150<br>0.643<br>100.2<br>373.3<br>0.200<br>0.728<br>94.7<br>367.8<br>0.250<br>0.788<br>363.1<br>0.300<br>0.833<br>85.9<br>359.0<br>0.350<br>9986<br>82.3<br>355.4<br>0.400<br>0.892<br>352.2<br>0.450<br>0.912<br>76.1<br>349.3<br>0.500<br>0.929<br>73.5<br>346.6<br>0.550<br>0.942<br>71.0<br>344.2<br>0.953<br>68.8<br>342.0<br>0.650<br>0.963<br>66.8<br>339.9<br>0.700<br>0.971<br>64.9<br>338.0<br>0.750<br>0.977<br>63.1<br>336.2<br>0.800<br>0.983<br>61.4<br>334.6<br>0.850<br>0.988<br>59.9<br>333.0<br>0.993<br>58.4<br>331.5<br>0.950<br>0.997<br>57.0<br>330.1<br>to w0 0<br>to w0 0<br>

Extracted text: Methyl Acetate Ethyl Benzene at 1atm (101.325kPa) Temperature Methyl Acetate T (K) 136.2 409.3 00 0 0 00 0 0 124.0 397.2 0.050 0.323 114.4 387.5 0.100 0.518 106.6 379.8 0.150 0.643 100.2 373.3 0.200 0.728 94.7 367.8 0.250 0.788 363.1 0.300 0.833 85.9 359.0 0.350 9986 82.3 355.4 0.400 0.892 352.2 0.450 0.912 76.1 349.3 0.500 0.929 73.5 346.6 0.550 0.942 71.0 344.2 0.953 68.8 342.0 0.650 0.963 66.8 339.9 0.700 0.971 64.9 338.0 0.750 0.977 63.1 336.2 0.800 0.983 61.4 334.6 0.850 0.988 59.9 333.0 0.993 58.4 331.5 0.950 0.997 57.0 330.1 to w0 0 to w0 0

Jun 09, 2022

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Assuming that the feed mixture is liquid at its boiling point (e.g. a saturated llyu ) Calculate the flowrates (mol/hr) of the distillate and bottoms. ) Determine the theoretical number of trays and...

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