Distillation Theory and its Application to Optimal Design of Separation Units

Nomenclature

Overview

A

separation work

A

stationary point of bond chain

A

vertex of product simplex

B

bottom stream (flow rate), kmol/sec

C ( k)

k-component boundary element of concentration simplex

C n

concentration simplex for n-component mixture

d

dimension of trajectory bundle

D

overhead stream (flow rate), kmol/sec

E

entrainer stream (flow rate), kmol/sec

F

feed stream (flow rate), kmol/sec

h

enthalpy of liquid, kJ/kg or kcal/kg

H

enthalpy of vapor, kJ/kg or kcal/kg

h

heave key component

i D : i B

split in column ( i D and i B components of overhead and bottom products respectively)

i : j

split in section ( i and j present and absent component of section product or pseudoproduct respectively)

K

equilibrium ratio

k

number of product components at sharp distillation

k

key component

k

key stationary point (pseudocomponent)

equilibrium ratio of component j at infinite dilution

K t

equilibrium ratio in tear-off point

l

light key component

L

liquid stream (flow rate), kmol/sec

m

number of product components at sharp distillation

m

number of stationary points of bond chain

n

number of components in a mixture

N

number of equilibrium stages

N + or N ?

stable or unstable node respectively

or

stable or unstable node of overhead boundary element...

UNLIMITED FREE
ACCESS
TO THE WORLD'S BEST IDEAS

SUBMIT
Already a GlobalSpec user? Log in.

This is embarrasing...

An error occurred while processing the form. Please try again in a few minutes.

Customize Your GlobalSpec Experience

Category: Scrubbers
Finish!
Privacy Policy

This is embarrasing...

An error occurred while processing the form. Please try again in a few minutes.