Distillation Program

I. Problem Statement: A rectification column is render 100kg gram molecule/h of a mixture of 40 mol % acetone and 60 mol % styrene at 101.32 kPa abs pressure. The work is liquid at the boiling point. The distillate is to cease 95 mol % acetone and the bottoms 10 mol % styrene. The ebb down ratio is 3.5:1. Calculate (a) the lower limit number of plates needed and (b) the minimum reflux ratio. Also calculate (c) the actual number of stages reach and (d) in which plate should the feed be introduced? II. Graph: propanone-Styrene ashes propanone-Styrene System III. Given: persist parsimoniousness:| XF = 0.40| Distillate Concentration:| XD = 0.95| Bottom Concentration:| XB = 0.10| campaign Condition:| q = 1| reflux Ratio:| R = 3.5| IV. solving: y = 0.409245x5 - 1.525415x4 + 2.516938x3 - 2.640275x2 + 2.239497x + 0.000060 y = 0.409245x5 - 0.520808x4 + 0.507726x3 + 0.149501x2 + 0.454327x - 0.000050 y intercept= XbR+1= 0.953.5+1 = 0.2 V. Program Listing: principal wedge # intromit<stdio.h> #include<conio.h> #include<math.h> rove acetonestyrene (float xyl, int xory) { float ans; if(xory==2) { ans=0.00006+(2.239497*xyl)-(2.640275*pow(xyl,2))+(2.516938*pow(xyl,3))-(1.525415*pow(xyl,4))+(0.

409245*pow(xyl,5)); } else { ans=-0.00005+(0.454327*xyl)+(0.149501*pow(xyl,2))+(00.507726*pow(xyl,3))-(0.520808*pow(xyl,4))+(0.409245*pow(xyl,5)); } retrieve (ans); } Source File #include <stdio.h> #include <stdlib.h> #include acet_styr.h int! main () { twin xd=0, xf=0, xb=0, xcoor [100], ycoor [100], q, ycoorf, xcoorr; branched ycoorr, mr, mb, rmin, bmin, bact, dcoorr, ref, delm, delb; int j, n=0, fplate; printf( This program will make for problems on Distillation of Acetone-Styrene); printf( Enter piece of Acetone in DISTILLATE: ); scanf(%lf,&xd); printf( Enter fraction of Acetone in...If you want to get a full essay, cabaret it on our website: BestEssayCheap.com

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