Mass Integration, Equilibrium - Process Design Practice - Lecture Slides, Slides of Process Engineering

Some topics for Process Design Practice course are Mass integration, Advanced column design, Physical property prediction, Process risk assessment and Integration of design and control. This lecture includes: Mass Integration, Equilibrium, Mass Exchanger, Dilute Systems, Special Cases, Interphase Mass Transfer, Rate of Mass Transfer, Multistage Contactors, Mass Exchangers, Multistage Contactors, Stagewise Columns

Typology: Slides

2012/2013

Uploaded on 08/21/2013

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Mass Integration

What is a Mass Exchanger?

Mass Exchanger

OutletComposition: y

outi Lean Stream (MSA)Flowrate:L

j Inlet Composition: x

in j

OutletComposition: x

outj Rich (Waste) StreamFlowrate:G

i Inlet Composition: y

ini

Mass Exchanger–^ A mass exchanger is any direct-contact mass-transferunit which employs a

Mass Separating Agent

(or a

lean phase) to selectively remove certain components(e.g.

pollutants)

from

a^

rich

phase

(e.g.

a^

waste

stream).

-^

Absorption, Adsorption, Extraction, Ion Exchange, ….

Special Cases–^ Raoult’s law for absorption–^ Henry’s law for stripping

Equilibrium 2:

0

(^ ) solute i^

j

p^ T Total y^

x P ^

i^

j^ j

y^

H^

x

^

-^ Mole fraction of solute in gas•^ Vapor pressure of solute at T•^ Mole fraction of solute in liquid•^ Total pressure of gas solubility 0

(^ )

Total(^ ) j^

i P solute H^

y^

T

p^

T

^

-^ Mole fraction of solute in gas•^ Mole fraction of solute in liquid•^ Henry’s coefficient -^ Liquid-phase solubilityof the pollutant attemperature T

-^

Special Cases–^ Distribution function used in solvent extraction

-^

Interphase Mass Transfer–^ For linear equilibrium the pollutant composition in thelean phase in equilibrium with y

can be calculated as:i

Equilibrium 3:4 *

i^

j^ j

y^

K^

x

^

-^ Solute composition in liquid•^ Solute composition in solvent•^ Distribution coefficient

*^

i^

j j

j y^

b x^

 m 

Multistage Contactors–^ Multistage countercurrent tray column

Mass Exchangers – I

Light Phase Out

Heavy Phase In Light Phase In

Heavy Phase Out

ShellPerforatedPlate (Tray)

WeirDowncomer

Multistage Contactors (Continued)–^ Multistage Mixer-Settler System

Mass Exchangers – I

MSAoutWastein^

MSAin Wasteout

Stagewise Columns (Continued)–^ Operating line (material balance)–^ The McCabe-Thiele diagram

Modeling – I

out y

inx in^ y

L outx^ G

^

^

^

in^

out^

out^

in

i^ i

i^

j^ j^

j

G^

y^

y^

L^

x^

x

^

^

in y i o u ty i

in^ x j

o u tx j x^ j

y^ i

O p e ra tin g

L in e E q u ilib riu mL in e

L^ /G^ j^ i

Stagewise Columns (Continued)–^ The Kremser equation•^

Isothermal• Dilute• Linear equilibrium

Modeling – I

ln^

in^ ln

in

j^ i^

i^

j^ j^

j^

j^ i

out^

in

j^

i^

j^ j^

j^

j

j j i

m G

y^

m x

b^

m G

L^

y^

m x

b^

L

NTP

L m G

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

Stagewise Columns (Continued)–^ Number of actual plates–^ Stage efficiency can be based on either the rich or thelean phase. If based on the rich phase, the Kremserequation can be rewritten as:

Modeling – I

NTP^ o NAP

^ ^ ln^1

ln 1

in^

in

j^ i^

i^

j^ j^

j^

j^ i

out^

in

j^

i^

j^ j^

j^

j

j^ i y

j

m G

y^

m x

b^

m G

L^

y^

m x

b^

L

NTP

m GL

^

^

 ^

^

^

^

^

 ^

^

 ^

^

^

^

 ^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

^

Differential (Continuous) Contactors–^ Countercurrent packed column

Mass Exchangers – II

LightPhase in

HeavyPhase In

Packing Restrainer

RandomPacking

Heavy-PhaseRe-Distributor HeavyPhase Out

Shell PackingSupport

LightPhase Out

RandomPacking

Differential (Continuous) Contactors (Continued)–^ Mechanically agitated mass exchanger

Mass Exchangers – II

Light PhaseOut

HeavyPhase In LightPhase In

Heavy PhaseOut

Shell

Mixer

Continuous Mass Exchangers–^ Height of a differential contactor

Modeling – II

y^

y

H^

HTU NTU

x^

x

H^

HTU NTU

  • log (^

in^

out i^

i

y

i^

i^

mean y^

y

NTU

y^

 y ^

^

^

^

^ 

  • log

ln in^

out^

out^

in

i^

j^ j^

j^

i^

j^ j^

j

i^

i^

in^

out

mean

i^

j^ j^

j

out^

in i^

j^ j^

j

y^

m x

b^

y^

m x

b

y^

y^

y^

m x

b

y^

m x

b

^

^

^

^

^

^

^

^

^

^

^

^

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Which Car is Cheaper? (Continued)–^ Annual Operating Cost (AOC):

How much to run

Crash Course in Economics 2:5 and maintain the car. $4,000/year

$700/year

$^ vs.

$/year ??? We need to

annualize the fixed cost of the car

Which Car is Cheaper? (Continued)–^ Annualized Fixed Cost (

AFC

)

-^

Total Annualized Cost (

TAC

)

Crash Course in Economics 3:

Initial Fixed Cost

Salvage or Resale Value

AFC

Useful Life Period

TAC

Annualized Fixed Cost

Annual Operating Cost

^