The Matlab CAPE-OPEN Unit Operation is a unit operation implementation for which the
calculations can be entered in Matlab.
To get started with the Matlab CAPE-OPEN unit operation, start your CAPE-OPEN capable simulation environment. Insert
a Matlab CAPE-OPEN unit operation. Edit a unit operation. Define feed and product ports. Go back to the simulation
environment and connect streams to the ports.
Now edit the unit operation again. On the Matlab tab, you can enter the Matlab calculation script. This script
can obtain feed properties using the getFeedProp function. It can then do calculations, using thermo-dynamic
calculations that are based on the underlying thermodynamic system of the simulation environment the unit operation
is running in. It must specify all the product streams using setProduct, that takes composition and
flow as well as two other properties required to specify the thermodynamic phase equilibrium.
The Matlab unit operation will function in CAPE-OPEN compliant simulation environments
that support version 1.1 thermodynamics or version 1.0 thermodynamics. It has been tested in COCO simulator, AVEVA Pro/II, AspenPlus, Honeywell Unisim Design and other simulators.
Matlab version 7.7 or higher must be installed and running at your system. The
Matlab CAPE-OPEN unit operation has been tested with Matlab versions 7.7, 7.8, 7.9, 7.10, 7.11, 7.12, 7.13, 7.14, 8.0, 8.1, 8.2, 8.3, 8.4, 8.5, 8.6, 9.0, 9.1, 9.2, 9.3, 9.4, 9.5, 9.6, 9.7, 9.8, 9.9, 9.10, 9.11, 9.12 and 9.13.
De María, R., Díaz, I., Rodríguez, M., and Adrián Sáiz, Industrial Methanol from Syngas: Kinetic Study and Process Simulation, International Journal of Chemical Reactor Engineering 11/1 (2013) 1-9
Peshev, D., Livingston, A.G., OSN Designer, a tool for predicting organic solvent nanofiltration technology performance using Aspen One, MATLAB and CAPE OPEN. Chemical Engineering Science 104 (2013), 975-987
Gozálvez-Zafrilla, J.M., Santafé-Moros, A., Sanchis-Sebastiá, M and Gomis-Fons, J., Implementation of membrane models on a CAPE-OPEN tool to simulate a process including RO membranes, Desalination and Water Treatment (2014), DOI: 10.1080/19443994.2014.995718
Jullok, N., Patricia, L., Degrève, J. , Van der Bruggen, B., A cascaded pervaporation process for dehydration of acetic acid. Chemical Engineering Science 105 (2014) 208 - 212
Tolksdorf, G.,Esche, E., van Baten, J.M., Wozny, G., Taylor-Made Modeling and Solution of Novel Process Units by Modular CAPE-OPEN-based Flowsheeting, Proceedings of the 26th European Symposium on Computer Aided Process Engineering (2016)
Shi, B., Peshev, D., Marchetti, P., Zhang, S., Livingston, A.G., Multi-scale modelling of OSN batch concentration with spiral-wound membrane modules using OSN Designer, Chemical Engineering Research And Design, 109 (2016) 385-396
Wang, Q., Chen, J.Y., Pan, M., He, C., He, C.C., Zhang, B.J., Chen, Q.L., A new sulfolane aromatic extractive distillation process and optimization for better energy utilization, Chemical Engineering & Processing: Process Intensification 128 (2018), 80-95
Dalane, K., Svendsen, H.F., Hillestad, M., Deng, L., Membrane contactor for subsea natural gas dehydration: Model development and sensitivity study, Journal of Membrane Science 556 (2018) 263-276
Hillestad, M., Ostadi, M., Alamo Serrano, G.d., Rytter, E., Austbø, B., Pharoah, J.G., Burheim, O.S., Improving carbon efficiency and profitability of the biomass to liquid process with hydrogen from renewable power, Fuel 234 (2018) 1431-1451
Usman, M., Hillestad, M., Deng, L., Assessment of a membrane contactor process for pre-combustion CO2 capture by modelling and integrated process simulation, International Journal of Greenhouse Gas Control 71 (2018) 95-103
Uebbing, J., Rihko-Struckmann, L.K.,Sundmacher, K., Exergetic assessment of CO2 methanation processes for the chemical storage of renewable energies, Applied Energy 233-234 (2019) 271-282
Dalane, K., Hillestad, M., Deng, L. Subsea natural gas dehydration with membraneprocesses: Simulation and process optimization, Chemical Engineering Research and Design 142 (2019) 257-267
Ostadi, M., Austbø, B., Hillestad, M., Parametric Optimization of a Power and Biomass to Liquid Process, Computer Aided Chemical Engineering 47 (2019) 287-292
Ostadi, M., Rytter, E., Hillestad, M., Boosting carbon efficiency of the biomass to liquid process with hydrogen from power: The effect of H2/CO ratio to the Fischer-Tropsch reactors on the production and power consumption, Biomass and Bioenergy 127 (2019)
Chu, Y., Lindbråthen, A., Lei, L., He, X., Hillestad, M., Mathematical modeling and process parametric study of CO2 removal from natural gas by hollow fiber membranes, Chemical Engineering Research and Design 148 (2019) 45-55
The Matlab CAPE-OPEN Unit Operation installer is available from the Downloads Page.
The Matlab CAPE-OPEN Unit Operation is free of charge for personal and academic use.
For commercial use, a license fee must be paid. Licensing is on a per-person basis (and can be
used on multiple computers). Commercial license fee for a perpetual license is € 400,- (if you are outside
the European union or inside Spain, VAT of 21% is applicable).