publication . Article . 2017

Simulation of the styrene production process via catalytic dehydrogenation of ethylbenzene using CHEMCAD® process simulator

Amaury Pérez Sánchez; Eddy Javier Pérez Sánchez; Rutdali María Segura Silva;
Open Access English
  • Published: 01 Jul 2017
  • Publisher: Universidad Distrital Francisco José de Caldas
Abstract
Abstract Background: Process simulation has been extensively used in recent years to design, evaluate or optimize processes, systems and specific operations of the chemical industry and its related disciplines. Currently, CHEMCAD® constitute one of the most used process simulators because of the great number of chemical and petrochemical processes that can be simulated. Method: The simulation of the production process of styrene via catalytic dehydrogenation of ethyl-benzene is carried out by using the process simulator CHEMCAD® version 5.2.0, in order to determine the composition and mass flow-rate of each process involved in the production, as well as the main...
Subjects
free text keywords: CHEMCAD®, sensitivity analysis, simulation, styrene, yield, análisis de sensibilidad, estireno, rendimiento, simulación, Technology, T, Engineering (General). Civil engineering (General), TA1-2040
18 references, page 1 of 2

Auli, N., Sakinah, M., Bakri, A., Kamarudin, H. & Norazian, M. (2013). Simulation of Xylitol Production: A Review. Australian Journal of Basic and Applied Sciences, 7(5), 366-372.

Benanti, E., Freda, C., Lorefice, V., Braccio, G., & Sharma, V. (2011). Simulation of Olive Pits Pyrolysis in a Rotary Kiln Plant. Thermal Science, 15(1), 145-158. [OpenAIRE]

Boyadjiev, C. (2010). Theoretical Chemical Engineering: Modeling and Simulation. New York: Springer-Verlag. [OpenAIRE]

Cao, E. (2010). Heat Transfer in Process Engineering. New York: McGraw-Hill.

Chemstations. (2002). ChemCAD Professional® (Version 5.2.0). Houston, Texas: Chemstations Inc. Recovered from www.chemstations.com

Chilev, C. & Simeonov, E. (2014). Simulation of Biodiesel Production by Transesterification of Vegetable Oils. Journal of Chemical Technology and Metallurgy, 49(5), 479-486.

Dimian, A. & Bildea, C. (2008). Chemical Process Design: Computer-Aided Case Studies. Weinheim: WILEY-VCH Verlag GmbH & Co. KGaA.

Diwekar, U. (2005). Green Process Design, Industrial Ecology, and Sustainability: a Systems Analysis Perspective. Resources, Conservation and Recycling, 44, 215-235, doi:10.1016/j.resconrec.2005.01.007.

Eliasson, J. (2010). Design of an Plant for Manufacturing of Acetaldehyde. Sweden: Department of Chemical Engineering, Lund University.

Forero, F. Pulido, A. y Cabrera, S. (2016). Modelación y simulación computacional del proceso de evaporación osmótica. Revista Tecnura, 20(49), 29-44, doi: 10.14483/udistrital.jour.tecnura.2016.3.a02.

Johansen, T., Johnsen, A. & Christiansen, I. (2013). A Comparison of Training Simulators for the Formox Process. Norway: Norwegian University of Science, Faculty of Natural Sciences and Technology. Department of Chemical Engineering and Technology.

Moneti, M., Delfanti, L., Marucci, A. & Bedini, R. (2015). Simulations of a Plant with a Fluidized Bed Gasifier WGS and PSA. Contemporary Engineering Sciences, 8(31), 1461-1473, doi: http://dx.doi. org/10.12988/ces.2015.56191. [OpenAIRE]

Otte, D., Lorenz, H.-M., & Repke, J.-U. (2016). A Toolbox Using the Stochastic Optimization Algorithm MIPT and Chemcad for the Systematic Process Retrofit of Complex Chemical Processes. Computers and Chemical Engineering, 84, 371-381, doi: http:// dx.doi.org/10.1016/j.compchemeng.2015.08.023

Sarwar, A. (2012). Plant Design for the Separation of Various Components from Turpentine Oil. (Master of Science Thesis). Göteborg, Sweden: Chalmers University of Technology.

Snyder, J. & Subramaniam, B. (1994). A Novel Reverse Flow Strategy for Ethylbenzene Dehydrogenation in a Packed-Bed Reactor. Chem. Eng. Sci., 49, 5585-5601.

18 references, page 1 of 2
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