Auburn UniversityRobert Kline
1/19/12
Chemistry
Thermodynamics
Flowsheet Development
What are esters?
ReactionsCarboxylic Acid + Alcohol Ester + Water
R O C R’O
CH3COOH + CH3(CH2)3OH CH3COO(CH2)3CH3 + H2O
Equilibrium Limited
Catalysts• Typically acid catalyzed• Homogeneous (sulfuric acid)• Heterogenous (amberlyst resins)
Ester Keq (@ 363 K)
Equimolar Equilibrium Conversion
Methyl Acetate 16.8 80%
Ethyl Acetate 3.5 65%
Isopropyl Acetate 8.7 75%
Butyl Acetate 10.9 77%
Pentyl Acetate 1.6 56%
Nonideal liquids• This is a chemical system rather than a
hydrocarbon or petrochemical one Significant liquid phase noidealities
can exist• Azeotropes• Liquid-Liquid Behavior
Satiiiii PxPy
Binary data from Horsely’s Azeotropic data, reprinted in Reactive Distillation Design and Control by Luyben and Yu
Azeotrope Temperature (C ) Mole Fraction TypeBuOH/BuOAc/H2O 89.4 0.11/0.13/0.754 Heterogenous
BuOAc/H2O 90.2 0.278/0.722 HeterogenousBuOH/H2O 92.7 0.248/0.752 Heterogenous
BuOH/BuOAc 116.2 0.73/0.27 Homogenous
Vapor Phase Association
HR C OO
H O C RO
H O C RO
HR C OO
H O C RO
Vapor Phase Association• In the vapor phase carboxylic acids can
form weakly bound dimers & trimers• This has an impact on vapor phase density,
fugacity, and enthalpy
Satiiiii PxPy
What are your thermodynamic model choices?• Liquid phase nonideality capable of
modeling 2 liquid phases NTRL UNIQUAC UNIFAQ
• Vapor phase dimerization Hayden O’Connell Nothnagel
Chemistry Issues• Equlibrium limited• Solid or homogenous catalyst
Thermodynamic Issues• Azeotropes• Liquid-Liquid Equilibria
Reaction SeparationRaw
Materials
Recycles
Products
Wastes
Reaction Section CSTR(s) PFR Feed ratios (which RM is easier
to recover?) Catalyst introduction & recovery
Separation Section How can raw materials be
recovered? Can LLE be exploited?
(extractors/decanters/reflux decanters)
What sequence should the separation be done?
Reaction&
SeparationSeparation
RawMaterials
Recycles
Products
Wastes
Rxn & Separation Section Multistage reactor + separator Reactor in a reboiler Reactive distillation Catalyst introduction & recovery
Separation Section How can raw materials be
recovered? Can LLE be exploited?
(extractors/decanters/reflux decanters)
What sequence should the separation be done?