190 likes | 621 Views
Batch Distillation Model. By: Jason Hixson Jennifer Potter Wayne Johnson. dddddd. Objective: To develop a batch distillation model that can accurately adjust a batch process to provide constant distillate composition.
E N D
Batch Distillation Model By: Jason Hixson Jennifer Potter Wayne Johnson
dddddd • Objective: To develop a batch distillation model that can accurately adjust a batch process to provide constant distillate composition. • Problem: Batch distillation will have a variable bottoms concentration and minimum reflux ratio, therefore requiring a variable system operating line.
x, y Diagram • Shows Vapor Liquid Equilibrium (VLE) • Van Laar Fit • Determines Theoretical Stages Perry’s Data Van Laar Model
x, y Diagram • xB = Bottoms Composition • xD = Distillate Composition • 3 Theoretical Stages Required xB=0.24 xD=0.85
Effect of Bottoms Composition • Decreasing bottoms composition with time. xD=0.73 xB=0.05
Influence of Operating Lines xB=0.35 xB=0.25 xD=0.77 xB=0.13 xd=0.77
Method • Solve x, y Diagram for Binary Mixture • Determine minimum Reflux Ratio (RD) • Vary RD by: • Setting theoretical stages = Actual Stages • Setting Distillate composition = constant
Model Requirement Input: • Binary Mixture • Heat • Volume • Pressure • Trays • D & B Composition Output: • x, y Diagram • RD vs. BM • xB vs. BM • D vs. BM
User Interface (UI) • 12 previously solved mixtures. • Van Laar Fit available for any binary mixture data “other”.
“Other” Model UI Requirements: • x, y, T Data • Antoine Constants • Log Based • Physical Properties • Specific Volume • Heat of Vaporization
Precautions • Requires Accurate Fit • Azeotrope Complications
Model Verification • 12 tray distillation column. • Power=2.7 kW • Reflux varies to keep reflux temperature constant.
Model Results Controller Gain = 1 %/°C
Model Results Controller Gain = 9 %/°C
Conclusions • Model accurately predicts required reflux ratio. • Useful for column design and optimization. • Future work – To vary column reflux ratio based on model output.