How did you do the drawing the Mc cabe step by step?

i want an solution in stpe by step

- Distillation & Benzen - Toluene & Bil Good 95% Benzen 5% Toluene Benzon 45% Toluene 55% 327.6 12 10% Bauzen 107. Toluene * Determine Equilibrum (x, y) for a miture (B-T) % w * Refractiontar * Mc Cabe thiele to know #of plate. How did you do the drawing the Mc cabe step by step? Panilates | Benzen - Toluene & s 95% Banten 5% Toluene Benzon 45% Toluene 55% 327.6k 20% Barn 17. Tiene (B-T) a mizure * Determine Equilibrum (x,y) for %w * Refractionlar * Mc Cabe thicle to know of plate. TABLET... Vapor-Presure and Equilibrium-Mole Fraction Data for Bentene-Tolure System Yap Pretre Mole Frantie en at 10 Jara Temperatur B. Telur 'C ara lo Pa . 33.3 3552 363.2 3682 3732 3792 3338 801 85 90 95 100) IOS 1106 10132 116.9 1355 1557 1792 2012 2400 760 377 1016 1168 1341 1532 450 $40 69) 743 550 101.32 345 405 475 557 605 760 1000 0.780 0531 0411 0255 0130 0 1.000 0.900 0777 0632 0456 0261 0 is plotted versus, for the benzene-Toluene system The 45 line is piven to show that is sicher in component Athaniss. The boling point diagram in For 111-1 is typical of an teal system following Raoult's ta. Non deal systems differ contiderably. In Fig 11.1.3a the boiling point diagram is shown for a maximun being areotrope The marmum temperature T... corresponds to a concentration, and x..-Y., at this pointThe plot oly, versus would show the curve crossing the 45 live at this point. Acetone-chloroform is an tuample of such a system. In F 11.1-3b a minimum boiling azeotrope is shown with Y.. - *., T... Ethanol-water is such asysten. 11.2 SINGLE-STAGE EQUILIBRIUM CONTACT FOR VAPOR-LIQUID SYSTEM Ha vapor-liquid synem is being considered, where the strain is a vapor andl, isa Iquid, and the two streams are contacted in a single equilibrium stage which is quite similar to hg 103-1, the boiling point or they equilibrium diagram must be used because an equilibrium relation similar to lienry's law is not available Since we are considering only two components A and only Ecs (10.3.!) and (10.5-2) are used for the material balance of sensible heat effects are small and the latent heats of both con pounds are the same, then when I mol of Acondentes, 1 mol of Butt vaporise Hence, the total moles of vapor tiene qui leaving Alo, moles L. - This case is called one of comman molal overflow. Ancrample is the benene-toluene ayatem EXAMPLE 11.2.1. Equilibrium Context of t'apor-Liquid Misture A vapor at the dew point and 1013: A Pa containing a mole fraction of 0.40 benzere (1) and 0 60 toluene (S) and 100 mo total is contacted with 110 kg mol of a liquid at the boiling point containing a mole fraction of 0.0 benzene and 0 70 toluene The two streams are contacted in a single stage. and the outlet stream leave in librium with each other Aviome con stant moll overtow Calculate the amounts and compositions of the ent streams Solution: The process frow diagram is the same as in Fix 10.3-L. The given 612 Chy11 Vuporabil Srpuration Process TALE 11:11. Vapor Pra Mile Fraction Des for Beesten PP Te Mole HP are NO.1 35 3533 1582 361 3652 3732 3752 101.32 1166 1355 155.7 1742 2042 2000 760 171 1016 HI 1344 1532 TRO 45.0 540 633 943 M50 10032 1000 551 0:411 6258 10 0 345 405 415 557 45 760 100 IOS 1106 1000 0900 0.711 63 0.4 0241 plotted vers, for the best toute em The 45 incisive to show is richet in compte The boli podal trial of Weal fotlowing Racal's is Noidalis differ considerably in the boiling point diamo ora maximoine More Theeperstar corresponds to conth point. The platy, v would show the curve crossing the 45'e this post trechformis cuample of such a system in F 11.1.3b mambo show with yox, 1. this with a ten 11.2 SINGLE STAGE EQUILIBRIUM CONTACT FOR VAPOR-LIQUID SYSTEM If a vaporudes being condered where the vaporind, quid, and the two streams we contacted to a single equilibrium at which it similar to F10 3:1, the boiling point they darama because an equilibrium relation to Honey who wille Since we are considering only two components and any E1103-1)(103-7) are used for the al balance of the ele we all and the of both con pouldi are the same, then when 1 mol of Acondes et malorie Hoce. the totalmols of vapor, Aqualine Aloe This case is called ones.com fow Asample is the best em EXAMPLE 1. Egia Costarfaper-Liquid Mitter Avapor at the dew point and 101:32Pacotina mole fraction oro) benese (A) 060 (8) 100 kmol total in contacted with 110 kemel of liquid at the boiling point com mole fractors beese and one. The two are con inglese and the outlet strani obum with the other com sunt mollitow. Calculate the amounts and compositions of the Swati The process fow darm is the same as FL 107-1. The given Che Shoc The point of the oricing and he wipingering exy porn bedrieg 1411-10) without the who Vy - Lets (11.4-16) Y-W (114-11) where they und was the point of the two persing Subtractie 1114-16 om 114-17) 1.-3-1-1-(O+W. (14-18 Subutituting Eq. (11.440134-14).and (114-15 (1.1) and rearrangin, (11.4-19 This is the requisits the focus of the Interviene Operating in Suity in 0114-17). the then with the 45'linisy - when the wil.composition of the feed In Fig 114 the line isted for various foed content The top of the 14-1) For for the guide the bodi po > 1, and the ope > 10, shown The King operating lines are planned for the case of a fred of part liquid and on the conveniest way to locate the wyping Operating in te spot the cariching operating and the line. Then draw the stripping line between the intersectice of the line and enriching operating in and the policy Location of the feed tray in a wobertrays To determine the of theoretical trays werd in the wind operating lines are drawn to interact on the ideas shoes in F 114 Sting the top at they are stepped off Fortrays 2 and the steps can go to the riching operating lines TTE if the food is belingi OCCI within operating Molt fraction is vapor. striping operating 10 Mole fraction is uit, To the forme > 1, and the ope > 10, shown The King operating lines are planned for the case of a fred of part liquid and on the conveniest way to locate the wyping Operating in te spot the cariching operating and the line. Then draw the stripping line between the intersectice of the line and enriching operating in and the policy Location of the feed tray in a wobertrays To determine the of theoretical trays werd in the wind operating lines are drawn to interact on the ideas shoes in F 114 Sting the top at they are stepped off Fortrays 2 and the steps can go to the riching operating lines TTE if the food is belingi OCCI within operating Molt fraction is vapor. striping operating 10 Mole fraction is uit, To the forme >