Applied Process Design for Chemical and Petrochemical Plants by E E Ludwig

By E E Ludwig

Quantity II is a part of a 3 quantity set. quantity 1 covers themes from 1-7. This quantity covers: eight. Distillation; nine. Packed Towers.

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And Seader, J. , EquilibriumStage Separation Operations in ChemicalEngineering, John Wiley, 0 (1981), p. 43, all rights reserved. Applied Process Design for Chemical and Petrochemical Plants 20 ParHal Condenser Qc Product Distillate Product Receiver A Column Conditions : yT = xD B Column Conditions: yD in Equilibrium with xo yT in Equilibrium with Tap Tray D is Liquid Total Condenser yD is Vapor D is Vapor Product Partial Condenser acts as One Plate with yo in Equilibriumwith Top Tray Condensate.

Now, read equilibrium curve at y(t - 1) and get x(, + 1) or xt- 1 which is liquid on plate below top. ). Then, read equilibrium curve to get corresponding liquid xt- 2. Continue until feed plate composition is reached, then switch to equation of stripping section and continue as before until desired bottoms composition is reached. 01455 Use this equation as described above following down from the feed plate cross-overfrom the rectifylng equation to the stripping equation. B. Fmq= 0 This represents feed as all vapor (not superheated).

763 No. of theoretical plates from graph = 11 No. 84 reflux/product Slope of operating line at minimum reflux: (L/V) . 0226 Use these equations as described for the (a) part of prob lem in solving for number of theoretical plates stepwise. 26) (50) = 363 mols liquid reflux = Lr + D = 363 + 50 = 413 = = 50 413 y n + l = 0 . 95) C. 5 This represents feed as a superheated vapor, and there is a decrease in liquid overflow from feed plate. 01535 Perchlor Use these equations as described for Part (a) in solving for theoretical plates.

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