Example 3.7: For the rectification in previous example, where a benzene-toluene feed is being distilled to give a distillate composition of xd =0.95 and a bottoms composition of xw = 0.10, %3D...


Example 3.7: For the rectification in previous example, where a benzene-toluene feed is being<br>distilled to give a distillate composition of xd =0.95 and a bottoms composition of xw = 0.10,<br>%3D<br>calculate the following graphically and analytically.<br>(a) Minimum reflux ratio Rm ,<br>(b) Minimum number of theoretical plates at total reflux.<br>1.0<br>YA<br>q line<br>0.8-<br>enriching operating<br>line for Rm<br>!!<br>steps for<br>total reflux<br>1.000<br>1.000<br>0.6-<br>0.780<br>0.900<br>4.<br>0.4-<br>5.<br>0.581<br>0.777<br>0.411<br>0.632<br>0.2-<br>0.258<br>0.456<br>0.130<br>0.261<br>0.2<br>0.4<br>0.6<br>0.8<br>1.0<br>Mole fraction in liquid, x<br>Moie fraction in vapor, y<br>

Extracted text: Example 3.7: For the rectification in previous example, where a benzene-toluene feed is being distilled to give a distillate composition of xd =0.95 and a bottoms composition of xw = 0.10, %3D calculate the following graphically and analytically. (a) Minimum reflux ratio Rm , (b) Minimum number of theoretical plates at total reflux. 1.0 YA q line 0.8- enriching operating line for Rm !! steps for total reflux 1.000 1.000 0.6- 0.780 0.900 4. 0.4- 5. 0.581 0.777 0.411 0.632 0.2- 0.258 0.456 0.130 0.261 0.2 0.4 0.6 0.8 1.0 Mole fraction in liquid, x Moie fraction in vapor, y

Jun 09, 2022
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