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This lecture provides an overview of mass exchange operations, including the concept of a mass exchanger, equilibrium relationships, interphase mass transfer, modeling techniques, and various types of mass exchangers.
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Mass Integration CHEN 4470 – Process Design Practice Dr. Mario Richard EdenDepartment of Chemical EngineeringAuburn University Lecture No. 7 – Overview of Mass Exchange Operations January 31, 2013
What is a Mass Exchanger? • Mass Exchanger • A mass exchanger is any direct-contact mass-transfer unit 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, ….
Equilibrium 1:4 • Generalized Description • The composition of the rich stream (yi) is a function of the composition of the lean phase (xj) • Dilute Systems • For some applications the equilibrium functions may be linearized over the operating range
Mole fraction of solute in gas • Vapor pressure of solute at T • Mole fraction of solute in liquid • Total pressure of gas • Mole fraction of solute in gas • Mole fraction of solute in liquid • Henry’s coefficient • Liquid-phase solubility of the pollutant at temperature T Equilibrium 2:4 • Special Cases • Raoult’s law for absorption • Henry’s law for stripping
Solute composition in liquid • Solute composition in solvent • Distribution coefficient Equilibrium 3:4 • Special Cases • Distribution function used in solvent extraction • Interphase Mass Transfer • For linear equilibrium the pollutant composition in the lean phase in equilibrium with yi can be calculated as:
Overall mass transfer coefficient for rich phase • Overall mass transfer coefficient for lean phase Equilibrium 4:4 • Interphase Mass Transfer (Continued) • For linear equilibrium the pollutant composition in the rich phase in equilibrium with xj can be calculated as: • Rate of Mass Transfer Correlations for estimating overall mass transfer coefficients can be found in McCabe et al. (1993), Perry and Green (1984), King (1980) and Treybal (1980).
Mass Exchangers – I 1:2 • Multistage Contactors • Multistage countercurrent tray column
Mass Exchangers – I 2:2 • Multistage Contactors (Continued) • Multistage Mixer-Settler System
Modeling – I 1:5 • Stagewise Columns • A generic mass exchanger • Schematic of a multistage mass exchanger
Modeling – I 2:5 • Stagewise Columns (Continued) • Operating line (material balance) • The McCabe-Thiele diagram
Modeling – I 3:5 • Stagewise Columns (Continued) • The Kremser equation • Isothermal • Dilute • Linear equilibrium
Modeling – I 4:5 • Stagewise Columns (Continued) • Other forms of the Kremser equation
Modeling – I 5:5 • Stagewise Columns (Continued) • Number of actual plates • Stage efficiency can be based on either the rich or the lean phase. If based on the rich phase, the Kremser equation can be rewritten as:
Mass Exchangers – II 1:3 • Differential (Continuous) Contactors • Countercurrent packed column
Mass Exchangers – II 2:3 • Differential (Continuous) Contactors (Continued) • Spray column
Mass Exchangers – II 3:3 • Differential (Continuous) Contactors (Continued) • Mechanically agitated mass exchanger
Modeling – II • Continuous Mass Exchangers • Height of a differential contactor
Crash Course in Economics 1:5 • Which Car is Cheaper? • Fixed cost: The car itself, i.e. body, engine, tires, etc. $500 $21,000
Crash Course in Economics 2:5 • Which Car is Cheaper? (Continued) • Annual Operating Cost (AOC): How much to run and maintain the car. $ vs. $/year ??? We need to annualize the fixed cost of the car $4,000/year $700/year
Crash Course in Economics 3:5 • Which Car is Cheaper? (Continued) • Annualized Fixed Cost (AFC) • Total Annualized Cost (TAC)
Crash Course in Economics 4:5 • Which Car is Cheaper? (Continued) Useful Life: 2 Years Salvage Value: $200 AFC = ($500-$200)/2 yr = $150/yr Useful Life: 20 Years Salvage Value: $1000 AFC = ($21,000-$1,000)/20 yr = $1000/yr
Crash Course in Economics 5:5 • Which Car is Cheaper? (Continued) TAC = $4,000 + $250 = $4,250/yr TAC = $1,000 +$700 = $1,700/yr
Minimizing Cost of MENs 1:3 • Total Annualized Cost of Mass Exchange System • Fixed cost: Trays, shell, packing, etc. • Operating cost: solvent makeup, pumping, heating/cooling, etc. • Driving Force • Minimum allowable composition • difference • Must stay to the left of • equilibrium line
Minimizing Cost of MENs 2:3 • Driving Force (Continued) • Minimum allowable composition difference at rich end of mass exchanger When the minimum allowable composition difference εj increases, then the ratio of L/G increases. AOC increases, due to higher MSA flow AFC decreases, due to smaller equipment, e.g. fewer stages
Minimizing Cost of MENs 3:3 • Driving Force (Continued) Trade-off between reducing fixed cost and increasing operating cost Composition driving force, becomes a optimization variable OPTIMUM
Other Business • Next Lecture – February 5 • Synthesis of mass exchange networks part I • SSLW pp. 297-308