Download presentation
Presentation is loading. Please wait.
1
DISTILLATION DESIGN RIGOROUS METHODS
2
COMPLEX METHODS METHODS FOR RIGOROUS MODELING STAGE TO STAGE
LEWIS-MATHESON THIELE-GEDDES TRIDIAGONAL MATRIX METHODS BUBBLE POINT (BP) SUM-RATES (SR) INSIDE-OUT
3
LEWIS-MATHESON METHOD
USED TO DETERMINE REQUIRED NUMBER OF TRAYS ABOVE FEED TOP SECTION STARTS AT THE TOP TRAY AND USES OPERATING LINES FOR EACH COMPONENT COMPLETE DEW POINT TEMPERATURE CALCULATIONS ON EACH TRAY CALCULATIONS STOP WHEN FEED TRAY CONCENTRATION IS ACHIEVED
4
LEWIS-MATHESON METHOD
USED TO DETERMINE REQUIRED NUMBER OF TRAYS BELOW FEED BOTTOM SECTION STARTS AT THE REBOILER USES OPERATING LINES FOR EACH COMPONENT COMPLETE BUBBLE POINT TEMPERATURE CALCULATIONS ON EACH TRAY CALCULATIONS STOP WHEN FEED TRAY CONCENTRATION IS ACHIEVED
5
LEWIS-MATHESON METHOD
REFINING VALUES ADJUST THE FEED TRAY VALUES TO AN INTERMEDIATE VALUE REVERSE THE CALCULATIONS BUBBLE POINT FROM FEED TO TOP DEW POINT FROM FEED TO BOTTOM REVISE PRODUCT STREAMS BASED ON RESULTS AND REPEAT CALCULATIONS SYSTEM WILL TYPICALLY CONVERGE THESE CALCULATIONS ARE FOR EQUILIBRIUM TRAYS DO NOT ALLOW FOR VARIATION IN L/V VALUES
6
THIELE-GEDDES METHOD FIXES THE NUMBER OF STAGES
ASSUMES LOCATION OF FEED STAGE ASSUMES A TEMPERATURE PROFILE ASSUMES A VAPOR FLOW PROFILE WORK WITH RATIOS ON EACH TRAY Vn/D, Ln/D, Vm/B AND Lm/B ITERATES FROM ENDS TO FEED
7
TRIDIAGONAL MATRICES BASED ON SIMULTANEOUS SOLUTION OF MESH EQUATIONS
MASS BALANCE MATRICES EQUILIBRIUM CONDITIONS ENTHALPY MATRICES
8
EQUATIONS USED IN TRI-DIAGONAL MATRICES
SCHEMATIC FOR n-STAGE COUNTERCURRENT CASCADE Monroy-Loperena, R., .Simulation of Multicomponent Multistage Vapor-Liquid Separations. An Improved Algorithm Using the Wang-Henke Tridiagonal Matrix Method Ind. Eng. Chem. Res.; (Article); 2003; 42(1);
9
TRI-DIAGONAL MATRIX BALANCES
MATERIAL BALANCE EQUILIBRIUM RELATIONSHIPS SUMMATION OF MOLE FRACTIONS HEAT BALANCE
10
BUBBLE POINT CALCULATIONS
INFORMATION FLOW BLOCK Monroy-Loperena, R., .Simulation of Multicomponent Multistage Vapor-Liquid Separations. An Improved Algorithm Using the Wang-Henke Tridiagonal Matrix Method Ind. Eng. Chem. Res.; (Article); 2003; 42(1);
11
OTHER VARIATIONS ON TRI-DIAGONAL MATRIX METHOD
SUM OF RATES METHOD APPLIES TO ABSORPTION & STRIPPING CONVERGES WHEN BP METHOD FAILS SIMULTANEOUS-CORRECTION PROCEDURES REDUCES NUMBER OF VARIABLES BY 2N USES A NEWTON-RAPHSON METHOD FOR CONVERGENCE
12
INSIDE-OUT METHOD MESH EQUATIONS ARE SOLVED BY ESTIMATING VALUES FOR K AND ENTHALPY INNER LOOPIS USED TO SOLVE MATERIAL AND HEAT BALANCES TO SOLVE DESIGN SPECIFICATIONS OUTER LOOP UPDATES ASSUMED THERMODYNAMIC VALUES CHECKS FOR CONVERGENCE
13
CHEMDIST METHOD - PROSIM
A NEWTON-RAPHSON BASED METHOD WHICH CAN BE USED FOR SYSTEMS WITH VLL EQUILIBRIUM FOR NON-IDEAL SYSTEMS FOR SYSTEMS WITH REACTION
Similar presentations
© 2024 SlidePlayer.com. Inc.
All rights reserved.