📄 cola_simulink_readme
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%% The files to simulate the distillation column are:% colamod.m - model of the distillation column which % returns the derivative of the states% dx/dt = f(t,x,u).% colas.m - SIMULINK interface to colamod.m.% cola_init.mat - Binary file containig the default% initial values of the states and the % controls.% cola_nonlin.m - Type:% cola_nonlin% in the MATLAB window and the non-linear% SIMULINK model of the distillation column % appears.% cola_lv_nonlin.m - Type:% cola_lv_nonlin% in the MATLAB window and the non-linear% SIMULINK model of the distillation column % with LV-configuration appears.% cola_lin.m - A linearized Simulink model of the % distillation column. Use the following% MATLAB commands:% clear all% load cola_init% [A,B,C,D] = linmod('colas',Xinit,Uinit); % and the linearized model of the open-loop % model appears.% cola_test_simulink.m - contains further description on % use of the distillation column model with % SIMULINK. % %% States: X - State, the first 41 states are compositions of light% component A with reboiler/bottom stage as X(1) and % condenser as X(41). State X(42)is holdup in reboiler/% bottom stage and X(82) is hold-up in condenser. % Inputs: U(1) - reflux L,% U(2) - boilup V,% U(3) - top or distillate product flow D,% U(4) - bottom product flow B,% U(5) - feed rate F,% U(6) - feed composition, zF.% U(7) - liquid feed fraction, qF.%% Outputs: sys and x0 as described in the SIMULINK manual.% when flag is 0 sys contains sizes and x0 contains % initial condition. % when flag is 1, sys contains the derivatives,% and when flag is 3 sys contains outputs; % y(1) - top composition,% y(2) - bottom composition,% y(3) - condenser holdup,% y(4) - reboiler holdup,% y(5:45) - tray composition, y(5) is reboiler y(45) is top.
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