BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT

Benzene is one of air pollutants which is classified as toxic, carcinogenic, and generally produced from the petrochemical industry. Catalytic oxidation is considered as the best method to convert benzene into unharmful substance. This research performed development of nano-based copper oxide cata...

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Main Author: Adrian Rahardi, Ryan
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/33508
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:33508
spelling id-itb.:335082019-01-24T10:26:00ZBENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT Adrian Rahardi, Ryan Indonesia Theses benzene, catalytic oxidation, kinetics, copper metal catalyst, modeling and simulation, and reverse flow reactor INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/33508 Benzene is one of air pollutants which is classified as toxic, carcinogenic, and generally produced from the petrochemical industry. Catalytic oxidation is considered as the best method to convert benzene into unharmful substance. This research performed development of nano-based copper oxide catalysts and the operating methods of reverse flow reactor. This study aimed to investigate the performance of copper oxide catalysts that have been developed, to determine the kinetic parameters from the catalyst, and to do modeling and simulation of the reverse flow reactor. Activity test was performed nine nano-CuO/?-Al2O3 catalysts and one commercial catalyst from PTA industry. The experiment was performed with residence time of 0.24 s with 5,000 ppm benzene in air. The determination of benzene oxidation kinetic parameters was done by varying residence time and temperature. The kinetic equiation was based on power law model. The reverse flow operation simulation was conducted in one dimensional pseudohomogeneous model using FlexPDE V.06 software at switching time of 10, 30, and 60 minutes. The results of the activity test showed that nano-catalyst’s activity was lower than the commercial catalyst. Commercial catalysts could convert benzene 86% at temperature of 300oC, while nano-catalyst’s benzene conversion was in the range of 20-30%. The commercial catalyst had a reaction order to benzene of 1.5 and activation energy of 52 kJ/mol with Arrhenius constant of 2.1x106. Based on the simulation results, ST 60 minutes failed to trap the heat while ST 30 and 10 minutes could manage to trap the heat. Thirty minute switching time had longer time lag than 10 minutes. The simulations showed that the reverse flow reactor system was capable of maintaining the conversion and temperature despite disturbance of inlet concentration Keywords: benzene, catalytic oxidation, kinetics, copper metal catalyst, modeling and simulation, and reverse flow reactor text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Benzene is one of air pollutants which is classified as toxic, carcinogenic, and generally produced from the petrochemical industry. Catalytic oxidation is considered as the best method to convert benzene into unharmful substance. This research performed development of nano-based copper oxide catalysts and the operating methods of reverse flow reactor. This study aimed to investigate the performance of copper oxide catalysts that have been developed, to determine the kinetic parameters from the catalyst, and to do modeling and simulation of the reverse flow reactor. Activity test was performed nine nano-CuO/?-Al2O3 catalysts and one commercial catalyst from PTA industry. The experiment was performed with residence time of 0.24 s with 5,000 ppm benzene in air. The determination of benzene oxidation kinetic parameters was done by varying residence time and temperature. The kinetic equiation was based on power law model. The reverse flow operation simulation was conducted in one dimensional pseudohomogeneous model using FlexPDE V.06 software at switching time of 10, 30, and 60 minutes. The results of the activity test showed that nano-catalyst’s activity was lower than the commercial catalyst. Commercial catalysts could convert benzene 86% at temperature of 300oC, while nano-catalyst’s benzene conversion was in the range of 20-30%. The commercial catalyst had a reaction order to benzene of 1.5 and activation energy of 52 kJ/mol with Arrhenius constant of 2.1x106. Based on the simulation results, ST 60 minutes failed to trap the heat while ST 30 and 10 minutes could manage to trap the heat. Thirty minute switching time had longer time lag than 10 minutes. The simulations showed that the reverse flow reactor system was capable of maintaining the conversion and temperature despite disturbance of inlet concentration Keywords: benzene, catalytic oxidation, kinetics, copper metal catalyst, modeling and simulation, and reverse flow reactor
format Theses
author Adrian Rahardi, Ryan
spellingShingle Adrian Rahardi, Ryan
BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
author_facet Adrian Rahardi, Ryan
author_sort Adrian Rahardi, Ryan
title BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
title_short BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
title_full BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
title_fullStr BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
title_full_unstemmed BENZENE CATALYTIC OXIDATION USING NANO-CUO/?-AL2O3 CATALYST IN FIXED BED REACTOR: MODELING, SIMULATION, AND EXPERIMENT
title_sort benzene catalytic oxidation using nano-cuo/?-al2o3 catalyst in fixed bed reactor: modeling, simulation, and experiment
url https://digilib.itb.ac.id/gdl/view/33508
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