Sunday, December 8, 2013

Distillation Program

I. Problem Statement: A rectification column is cater 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 dispel 95 mol % acetone and the bottoms 10 mol % styrene. The decrease ratio is 3.5:1. Calculate (a) the stripped-down number of plates needed and (b) the minimum reflux ratio. Also calculate (c) the actual number of stages return and (d) in which plate should the feed be introduced? II. Graph: propanone-Styrene brass dimethyl ketone-Styrene System III. Given: persist meanness:| 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: chief register # intromit<stdio.h> #include<conio.h> #include<math.h> cast 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. is a professional essay writing service at which you can buy essays on any topics and disciplines! All custom essays are written by professional writers!
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; divalent 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:

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