13 14 Solution: ni X18 XIT 05 XIX 0.35 COLUMN 1 112 X2-0.673 XIT-0.306 X2X FUJ XxIB XIT XIX COLUMN 2 ******* 114 x4-0.05

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answerhappygod
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13 14 Solution: ni X18 XIT 05 XIX 0.35 COLUMN 1 112 X2-0.673 XIT-0.306 X2X FUJ XxIB XIT XIX COLUMN 2 ******* 114 x4-0.05

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13 14 Solution Ni X18 Xit 05 Xix 0 35 Column 1 112 X2 0 673 Xit 0 306 X2x Fuj Xxib Xit Xix Column 2 114 X4 0 05 1
13 14 Solution Ni X18 Xit 05 Xix 0 35 Column 1 112 X2 0 673 Xit 0 306 X2x Fuj Xxib Xit Xix Column 2 114 X4 0 05 1 (21.36 KiB) Viewed 14 times
13 14 Solution Ni X18 Xit 05 Xix 0 35 Column 1 112 X2 0 673 Xit 0 306 X2x Fuj Xxib Xit Xix Column 2 114 X4 0 05 2
13 14 Solution Ni X18 Xit 05 Xix 0 35 Column 1 112 X2 0 673 Xit 0 306 X2x Fuj Xxib Xit Xix Column 2 114 X4 0 05 2 (38.7 KiB) Viewed 14 times
13 14 Solution: ni X18 XIT 05 XIX 0.35 COLUMN 1 112 X2-0.673 XIT-0.306 X2X FUJ XxIB XIT XIX COLUMN 2 ******* 114 x4-0.059 XAT 0.926 xxx 4? X*X X3
Balances on Chemical Processes 9 2 3 4 Example 10.3-1 A stream containing 35wt% benzene (B), 50% toluene (T), and the balance xylene (X) is fed to a distillation column. The overhead product from the column contains 67.3 wt% benzene and 30.6 % toluene. The bottoms product is fed to a second column. The overhead product from the second column contains 5.9 wt% benzene and 92.6% toluene Of the toluene fed to the process, 10% is recovered in the bottom product from the second column, and 85% of the xylene fed to the process is recovered in the top product from the second column. Assume Isothermal process operations. 5 6 7 8 a) Set up the equations for all unknown stream variables, 9 b) Perform a df analysis on this process, 10 c) Outline a manual calculation procedure to determine the compositions of all streams d) Determine the values of all stream compositions 11 [[ 12 COLUMN 1 COLUMN 2 13 Solution: 122 X280.673 X27-0.306 XXX 11) Xin 035 X17-05 Xxx 42 113 XAR NI.. XIX 14 COLUMN 1 COLUMN 2 14 X-0.059 Xer-0926 X-47 XX
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