00:01
Hi friends the mole numbers of components, mole numbers of ch4, mass upon bowler mass, 75 upon 16.
00:23
So it is to be 4 .6875 pound mold.
00:35
Just a minute.
00:41
For ethane, 25 upon 30 .833 pound mole.
00:59
Apparent specific heat at constant pressure summation mass fraction into cp that is 0 .75 into 0 .532 plus 1 .25 into 0 .427 so you will get 0 .506 b at u per pound mass per rumour pseudo critical temperature and pressure pseudo critical temperature and pressure t -des critical of mixture submission yt critical that is 4 .6875 upon 4 .6875 plus 0 .833 into 343 .9 point nine plus 0 .8 triple three four point six eight seven five plus point eight triple three into five forty nine so it is to be three seventy five volume pressure critical of mixture summation by into p critical so four point six eight seven upon 4 .687 plus 0 .8 triple into 673 plus 0 .8 triple 3 upon 4 .6875 plus 0 .8 triple 3 into 708.
03:34
So you will get critical pressure of mixture 675 28 .3 psia relative pressure and temperature tr1 tm1 upon t critical substitute the value 760 upon 375 so it is to be 2 .03 relative pressure first 1300 upon 678 .3 that is 1 .92 that is 1 .92 relative temperature second 660 670 .75, 1 .76 and relative pressure 20 178 .3, that is 0 .095.
04:53
The compressibility factor using the table.
05:02
Compressibility factor using table, you have to write zm1, 0 .96, zh1, 04857, zh2, 01152...