# 51 results

This program is for the learning process of Fenske - Underwood - Gilliland's model.

Multi-Objective Optimization of Aspen Plus Distillation Column using Stochastic Algorithm (NSGA II).

integer variables, for example, BARON algorithm (deterministic) or NSGA II (Stochastic).This matlab code is an example of Multi-Objective optimization of Aspen Plus distillation column using NSGA II

The file prsrk.m calculates major thermodynamic properties using any of PR, RK or SRK EoS.

energy of vapor and liquid mixtures. The other Matlab functions/scripts are part of a steady-state distillation example as depicted in Fig. 15.6 (pp. 568) of Henley, E. J. and Seader, J. D

A GUI which makes a McCabe-Thiele plot for a binary column distillation.

Dynamic Distillation Column using ode45

Solve for the transient stage compositons in an ideal binary distillation column using ode45.Source: (c) 1997 B. Wayne Bequette - 24 Jan 1997 revised 31 Dec

GUI tool for estimating the theoretical number of plates of a distillation column

Companion Software

### Dynamics of a continuous distillation column for the separation of a mixture of Benzene, Toluene ...

Version 1.0.0.0

Housam BinousUses ode45 to compute the composition profile in a continuous multicomponent column.

A standard 2 component distillation column model with constant relative volitility.

Distillation column model found in a few chemical engineering papers on the topics of nonlinear model reduction, nonlinear model predictive control, and nonlinear differential equation

Computes number of theoretical plates.

### Separation of a water-methanol mixture using a four stage batch distillation column

Version 1.0.0.0

Housam BinousComputes mole fractions and temperatures in the still, condenser and plates

visit:http://library.wolfram.com/infocenter/MathSource/5929/A Mathematica demonstration using version 6.0 is available at:http://demonstrations.wolfram.com/StudyOfAFourStageBatchDistillationColumn/

Solving simple flash distillation column by 4 components

Solving simple flash distillation column by 4 components

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Calculating and ploting the stages of a distillation process for McCace method

This GUI calculates and represents the stages of a distillation column using the McCabe method.

Calculates binary system liquid and vapour composition & temperature in a flash distillation process

Flash distillation,Temperature,Liquid and vapour composition,Binary system

Several applications of fuzzy modeling

### Constrained Fuzzy Model Identification - Files for Fuzzy Modeling and Identification Toolbox

Version 1.0.0.0

Janos AbonyiCan be used for estimation of the consequent model parameters

This application is designed to facilitate the estimation of critical parameters in the batch distillation process.

This application was developed for the Separation Laboratory course at UNIMET to simulate the distillation of an isopropanol-water mixture through a batch distillation process. Starting with the

GUI model has been prepared for Distillation Column using FUG method.

GUI model has been prepared for Distillation Column using FUG method. This is a part of post graduate work and I need support from all the users. Users can run the Distillation.fig file but make sure

APM MATLAB toolbox for nonlinear control and estimation of DAE models with IPOPT

A project that performs useful Process Integration calculations given the streams of the process (Pinch Analysis, Heat Exchanger Network).

network. It calls the thermocascade.m file to get the pinch.distillation.mThis function must be called independently, after the Grand Composite Curve has been generated by the thermocascade.m function. As

How to put and what will be gain value for this

This tells how to verify linear and nonlinear model of distillation

Matlab Dynamics and Control course with Live Scripts and the Temperature Control Lab

RegressionL29Simulation of FOPDT, SOPDT, and Higher Order SystemsDistillation ControlHigher Order RegressionL30Stability AnalysisController Stability LimitsP-Only Stability AnalysisL31Cascade Control and Feedforward

### Application of the Riccati Equation to Solve Binary Distillation Problems

Version 1.0.0.0

Housam BinousComputes number of stages of a column

We solve a binary distillation problem using the solution of a Riccati equation. We find that four plates are needed to achieve the desired product purity. We also compute the number of stages with

A code that automatically computes the required number of plates, optimal feed plate, and minimum number of plates at Const. Rel. Volatility

System: Binary Design method: McCabe-ThieleCondition: Distillation with Constant Relative VolatilityRequired User inputs:-Feed amount (in mol)-Mole fraction of More Volatile Component (MVC) in Feed

Code for Smoker's Equation. Calculate Number of Theoretical Trays for Binary Distillation System.

Computes number of plates, minimum reflux ratio, optimum feedplate, product recovery and flow rates.

Code for Distillation study

This is a simple code I came up with to analyze Distillation. It gives you the Theoretical number of trays, E_overall, R_min and the optimum feed tray location using the McCabe-Thiele method. Hope it

Finding number of stages for a binary mixture in flash distillation column using the minimum reflux ratio concept

The McCabe-Thiele method provides a simplified graphical approach to estimate the number of stages required for distillation, assuming idealized conditions. It serves as a starting point for

MATLAB versions of the MathCad example programs included in the textbook.

Control of a distillation column using Simulink

distillation column, Chemical Engineering Science, 1973, Vol. 28, pp. 1707-1717.

Using this people will be able to calculate the number of theoretical stages required for desired distillate composition.

computes residue curve map

play an important role in the conceptual design of distillation columns. The pointer's position gives an initial point from which the simulation runs forward and backward in warped time. The lightest

This function creates McCabe-Thiele Diagrams from various user inputs

This function creates McCabe-Thiele Diagrams from various user inputs. It also displays some key distillation parameters such as the reflux and boilup ratios and the feed conditions. Additionally, it

Incremental implementation of the principal component analysis (PCA).

Uses ode15s to solve a system of differential algebraic equations.

given in the book by Doherty, M. F., and M. F. Malone, Conceptual Design of Distillation Systems, McGraw-Hill, New York, 2001.Please visit these links for the paper by Housam Binous concerning this

GUI tutorial for understanding the PCA-based Multivatiate Statistical Process Control (MSPC) strategy

A Graphical User Interface (GUI) is developed in MATLAB as a tutorial for understanding the PCA-based MSPC strategy. It uses a nonlinear model of a binary distillation column implemented in Simulink

Linking Matlab and Aspen Hysys through COM technology ("actxserver")

useful.I present an example of connection between Aspen HYSYS V.10.0 and Matlab. The simulation corresponds to a distillation column. As an application of the connection, a sensitivity analysis is done using

This file outline the Aspen Plus and Matlab connection through COM Technology.

: https://www.researchgate.net/post/How_can_I_integrate_Aspen_Plus_and_Matlab_for_optimization_proposeI present an example of connection between Aspen Plus V.10.0 and Matlab. The simulation corresponds to a reactive distillation column. As an application of the connection, a sensitivity analysis is

Finds pairings for decentralized control which satisfy necessary conditions for integrity.

Relative Interaction Array accumulated for all the possible partially controlled systems. Example: Consider the following DC-gain system fot a Petlyuk distillation column used in by K.E. Haeggblom (1997)with

Creates multiple McCabe Thiele Diagrams from user inputs to show the effects of changing parameters

This function creates multiple McCabe Thiele Diagrams from user inputs to show the effects of changing parameters on the possible separation for a given binary distillation column.

Perform flash calculations using SRK EOS

M-files for design of the Mass/Damper/Spring control system using Robust Control Toolbox, ver. 3

, 2005(http://www.springer.com/sgw/cda/frontpage/0,11855,4-192-22-46383093-0,00.html?changeHeader=true).The book also presents other 5 case studies including robust control systems design of a triple inverted pendulum, a hard disk drive, a distillation column, a rocket system and a flexible-link

Residue curve map.

### Residue Curve Map for the mixture MTBE/Methanol/isobutene/n-butane at P=1 atm

Version 1.0.0.0

Housam BinousComputes RCM for MTBE Chemistry

Uses Moving Averages to Trade the VIX

Uses the produce from a distillation plant and sells/buys ethanol based on the moving averages.

Calculation of the Partial Relative Gain defined by K.E. Haeggblom (1997)

distillation column are included. The examples reproduce the ones used by K.E. Haeggblom (1997).

McCabe-Thiele Graphing for an Ideal Mixture

This script computes and plots required number of stages in distillation column. The values of reflux ratio, boilup ratio as well as percentage of LK in distillate in bottoms are needed to run this

T-x-y Diagram for Methanol/Methyl Acetate system

This program generates T-x-y Diagram for Methanol/Methyl Acetate system. It also generates a video file to record the iterations as an animation.It is a very important data required in distillation

Zero inflated poison regression Zero inflated poison factor analysis