Separating Azeotropic Mixtures CHEN 4460 – Process Synthesis, Simulation and Optimization Dr. Mario Richard Eden Department of Chemical Engineering Auburn University Lecture No. 6 – Review of Non-ideal Thermodynamics September 23, 2008 Contains Material Developed by Dr. Daniel R. Lewin, Technion, Israel
Process Design/Retrofit Steps Assess Primitive Problem Development of Base-case Plant-wide Controllability Assessment Detailed Design, Equipment sizing, Cap. Cost Estimation, Profitability Analysis, Optimization Detailed Process Synthesis - Algorithmic Methods SECTION B
Algorithmic Methods
Lecture 6 – Introduction Separation sequences are complicated by the presence of azeotropes, often involving mixtures of oxygenated organic compounds: Alcohols Ketones Ethers Acids Water In these cases, distillation boundaries limit the product compositions of a column to lie within a bounded region. This prevents the removal of certain species in high concentrations.
Lecture 6 – Objectives Be able to sketch the residue curves on a ternary phase diagram Be able to define the range of possible product compositions using distillation, given the feed composition and the ternary phase diagram
Basics: The Lever Rule
Basics: Ternary Phase Diagrams 0.15 H 2 O 0.65 DTBP 0.2 TBA 0.2 DTBP
Basics: Ternary Phase Diagrams 0.6 H 2 O 0.2 DTBP 0.2 TBA
Homogeneous Azeotropes 1:4 At equilibrium: At fixed temperature
Homogeneous Azeotropes 2:4 Example – Phase diagrams for benzene- toluene mixture at 90 o C
Homogeneous Azeotropes 3:4 For non-ideal mixtures, the activity coefficients are different from unity: minimum If the mixture has a minimum-boiling azeotrope Example – Phase diagrams for Isopropyl ether-Isopropyl alcohol
Homogeneous Azeotropes 4:4 For non-ideal mixtures, the activity coefficients are different from unity: maximum If the mixture has a maximum-boiling azeotrope Example – Phase diagrams for Acetone-Chloroform
Heterogeneous Azeotropes For a minimum-boiling azeotrope with large deviation from Raoult’s law ( ), phase splitting may occur and a minimum-boiling heterogeneous azeotrope forms, having a vapor phase in equilibrium with two liquid phases. Homogeneous Azeotrope Heterogeneous Azeotrope
Residue Curves 1:3 Mass balance on species j: Simple Distillation Rearranging:
Residue Curves 2:3 Residue curves for Azeotropic system Residue curves for zeotropic system Residue Curves Liquid Compositions at Total Reflux
Residue Curves 3:3 Residue Curves Liquid Compositions at Total Reflux Species balance on top n-1 trays: Approximation for liquid phase: Substituting: At total reflux, D = 0 and V n = L n-1 Rectifying section of distillation column
Sketching Residue Curves Plot pure components on vertices along with T b Plot all azeotropes on diagram along with their T b Plot residue curves connecting all azeotropes, azeotropes & vertices, and finally vertices & vertices with arrow heads pointing towards increasing boiling point temperatures Plot additional residue curves that “arch” towards intermediate temperatures on the way to the end point
Product Compositions Regions For zeotropic systems –L: Lowest boiling component, I: Intermediate boiling component, H: Highest boiling component, F: Feed composition Pure L distillate Pure H bottoms
Product Compositions Regions For azeotropic systems –Shaded regions: Feasible distillate and bottoms product compositions Two binary azeotropes Three binary azeotropes and one ternary azeotrope
Summary – Non-ideal Thermo Be able to sketch the residue curves on a ternary phase diagram Be able to define the range of possible product compositions using distillation, given the feed composition and the ternary phase diagram On completion of this part, you should:
Other Business Homework –SSL: 7.14b-d, 7.15 –Due Tuesday October 7 No Lecture Next Week –I will be in Canada for a meeting – if you need help or have questions Next Lecture (October 7) –Part 1: Sequencing Azeotropic Distillation Columns (SSL ) –Part 2: Review for Midterm Exam Midterm Exam –October 14 during lecture –Open book or closed book?