Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation

This work aims to present an industrial perspective on Catalytic Wet Peroxide Oxidation (CWPO) technology. Herein, process simulation and experimental design have been coupled to study the optimal process conditions to ensure high-performance oxidation, minimum H<sub>2</sub>O<sub>2...

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Main Authors: Jose L. Diaz de Tuesta, Asunción Quintanilla, Daniel Moreno, Víctor R. Ferro, Jose A. Casas
Format: Article
Language:English
Published: MDPI AG 2020-05-01
Series:Catalysts
Subjects:
Online Access:https://www.mdpi.com/2073-4344/10/5/548
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spelling doaj-c916a2f8823c4910af5934917213f8052020-11-25T03:12:47ZengMDPI AGCatalysts2073-43442020-05-011054854810.3390/catal10050548Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal OperationJose L. Diaz de Tuesta0Asunción Quintanilla1Daniel Moreno2Víctor R. Ferro3Jose A. Casas4Mountain Research Center (CIMO), Polytechnic Institute of Bragança, Campus de Santa Apolónia, 5300 253 Bragança, PortugalChemical Engineering Department, Faculty of Science, Autonomous University of Madrid, Cantoblanco, Ctra. de Colmenar km 15, 28049 Madrid, SpainChemical Engineering Department, Faculty of Science, Autonomous University of Madrid, Cantoblanco, Ctra. de Colmenar km 15, 28049 Madrid, SpainChemical Engineering Department, Faculty of Science, Autonomous University of Madrid, Cantoblanco, Ctra. de Colmenar km 15, 28049 Madrid, SpainChemical Engineering Department, Faculty of Science, Autonomous University of Madrid, Cantoblanco, Ctra. de Colmenar km 15, 28049 Madrid, SpainThis work aims to present an industrial perspective on Catalytic Wet Peroxide Oxidation (CWPO) technology. Herein, process simulation and experimental design have been coupled to study the optimal process conditions to ensure high-performance oxidation, minimum H<sub>2</sub>O<sub>2</sub> consumption and maximum energetic efficiency in an industrial scale CWPO unit. The CWPO of phenol in the presence of carbon black catalysts was studied as a model process in the Aspen Plus<sup>®</sup> v11 simulator. The kinetic model implemented, based on 30 kinetic equations with 11 organic compounds and H<sub>2</sub>O<sub>2</sub> involvement, was valid to describe the complex reaction network and to reproduce the experimental results. The computer experiments were designed on a six-factor Doehlert Matrix in order to describe the influence of the operating conditions (i.e., the different process temperatures, inlet chemical oxygen demands, doses of H<sub>2</sub>O<sub>2</sub> and space time) on each selected output response (conversion, efficiency of H<sub>2</sub>O<sub>2</sub> consumption and energetic efficiency) by a quadratic model. The optimization of the WPO performance by a multi-criteria function highlighted the inlet chemical oxygen demand as the most influential operating condition. It needed to have values between 9.5 and 24 g L<sup>−1</sup> for autothermal operation to be sustained under mild operating conditions (reaction temperature: 93–130 °C and pressure: 1–4 atm) and with a stoichiometric dose of H<sub>2</sub>O<sub>2</sub>.https://www.mdpi.com/2073-4344/10/5/548catalytic wet peroxide oxidationcarbon catalystASPEN plussimulation and optimizationdesign of experimentsenergetic efficiency
collection DOAJ
language English
format Article
sources DOAJ
author Jose L. Diaz de Tuesta
Asunción Quintanilla
Daniel Moreno
Víctor R. Ferro
Jose A. Casas
spellingShingle Jose L. Diaz de Tuesta
Asunción Quintanilla
Daniel Moreno
Víctor R. Ferro
Jose A. Casas
Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
Catalysts
catalytic wet peroxide oxidation
carbon catalyst
ASPEN plus
simulation and optimization
design of experiments
energetic efficiency
author_facet Jose L. Diaz de Tuesta
Asunción Quintanilla
Daniel Moreno
Víctor R. Ferro
Jose A. Casas
author_sort Jose L. Diaz de Tuesta
title Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
title_short Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
title_full Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
title_fullStr Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
title_full_unstemmed Simulation and Optimization of the CWPO Process by Combination of Aspen Plus and 6-Factor Doehlert Matrix: Towards Autothermal Operation
title_sort simulation and optimization of the cwpo process by combination of aspen plus and 6-factor doehlert matrix: towards autothermal operation
publisher MDPI AG
series Catalysts
issn 2073-4344
publishDate 2020-05-01
description This work aims to present an industrial perspective on Catalytic Wet Peroxide Oxidation (CWPO) technology. Herein, process simulation and experimental design have been coupled to study the optimal process conditions to ensure high-performance oxidation, minimum H<sub>2</sub>O<sub>2</sub> consumption and maximum energetic efficiency in an industrial scale CWPO unit. The CWPO of phenol in the presence of carbon black catalysts was studied as a model process in the Aspen Plus<sup>®</sup> v11 simulator. The kinetic model implemented, based on 30 kinetic equations with 11 organic compounds and H<sub>2</sub>O<sub>2</sub> involvement, was valid to describe the complex reaction network and to reproduce the experimental results. The computer experiments were designed on a six-factor Doehlert Matrix in order to describe the influence of the operating conditions (i.e., the different process temperatures, inlet chemical oxygen demands, doses of H<sub>2</sub>O<sub>2</sub> and space time) on each selected output response (conversion, efficiency of H<sub>2</sub>O<sub>2</sub> consumption and energetic efficiency) by a quadratic model. The optimization of the WPO performance by a multi-criteria function highlighted the inlet chemical oxygen demand as the most influential operating condition. It needed to have values between 9.5 and 24 g L<sup>−1</sup> for autothermal operation to be sustained under mild operating conditions (reaction temperature: 93–130 °C and pressure: 1–4 atm) and with a stoichiometric dose of H<sub>2</sub>O<sub>2</sub>.
topic catalytic wet peroxide oxidation
carbon catalyst
ASPEN plus
simulation and optimization
design of experiments
energetic efficiency
url https://www.mdpi.com/2073-4344/10/5/548
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