Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate

The needs of energy sources are increasing, as the human population grows. Fossil fuel and coal reserves which were people’s main choice are running low. Therefore, renewable source of energy is required, one of which is by using hydrodeoxygenation (HDO) reaction to upgrade the bio oil quality in...

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Main Author: Kevin Suhendra (NIM : 13013069), Mannuel
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/22962
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Institution: Institut Teknologi Bandung
Language: Indonesia
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spelling id-itb.:229622017-09-29T09:32:00ZKinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate Kevin Suhendra (NIM : 13013069), Mannuel Indonesia Final Project INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/22962 The needs of energy sources are increasing, as the human population grows. Fossil fuel and coal reserves which were people’s main choice are running low. Therefore, renewable source of energy is required, one of which is by using hydrodeoxygenation (HDO) reaction to upgrade the bio oil quality into fuel that is feasible to use. <br /> <br /> This research takes up kinetics of HDO reaction of methyl laurate in n-hexadecane solvent using sufided NiMo/&#947;-Al2O3 catalyst. The data of kinetics are collected from the reaction which is held in a fixed-bed reactor with temperature 280-300oC and weight-hourly space velocity (WHSV) 2.2-4.5 hours-1, 60 bar pressure, alongside H2-to-feed ratio 1000 NmL/mL, and 45/60 mesh catalyst. 0.05%-w dimethyl disulfide (DMDS) is added to liquid reactant in order to retain the activities of the catalyst. Both feed and products are analyzed using gas chromatography – flame ionization detector (GC-FID). <br /> <br /> The kinetics models of HDO will be given in Power Law, according to the experimental data obtained. The kinetics models made are the overall kinetics of HDO methyl laurate and parallel reactions kinetics of HDO and HDCO2/HDCO. Integration method and optimization method are used to define the kinetics parameters. From integration method, the reaction is first-ordered with Arrhenius constant (A) 1,1509 s-1 and activation energy (Ea) 31.03 kJ/mol. Meanwhile, optimization method suggests the reaction order is 0.83 with A 1.64 M0.17.s-1 and Ea 33.483 kJ/mol. Kinetics parameters of parallel reaction HDO abd HDCO2/HDCO which are defined by optimization method are A 0.05 M0.55.s-1, Ea 21.29 kJ/mol, and order of 0.45 for n-dodecane formation; and for n-undecane reaction A 1.53 M-0.08.s-1 and Ea 38.39 kJ/mol, and order of 1.08. 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 The needs of energy sources are increasing, as the human population grows. Fossil fuel and coal reserves which were people’s main choice are running low. Therefore, renewable source of energy is required, one of which is by using hydrodeoxygenation (HDO) reaction to upgrade the bio oil quality into fuel that is feasible to use. <br /> <br /> This research takes up kinetics of HDO reaction of methyl laurate in n-hexadecane solvent using sufided NiMo/&#947;-Al2O3 catalyst. The data of kinetics are collected from the reaction which is held in a fixed-bed reactor with temperature 280-300oC and weight-hourly space velocity (WHSV) 2.2-4.5 hours-1, 60 bar pressure, alongside H2-to-feed ratio 1000 NmL/mL, and 45/60 mesh catalyst. 0.05%-w dimethyl disulfide (DMDS) is added to liquid reactant in order to retain the activities of the catalyst. Both feed and products are analyzed using gas chromatography – flame ionization detector (GC-FID). <br /> <br /> The kinetics models of HDO will be given in Power Law, according to the experimental data obtained. The kinetics models made are the overall kinetics of HDO methyl laurate and parallel reactions kinetics of HDO and HDCO2/HDCO. Integration method and optimization method are used to define the kinetics parameters. From integration method, the reaction is first-ordered with Arrhenius constant (A) 1,1509 s-1 and activation energy (Ea) 31.03 kJ/mol. Meanwhile, optimization method suggests the reaction order is 0.83 with A 1.64 M0.17.s-1 and Ea 33.483 kJ/mol. Kinetics parameters of parallel reaction HDO abd HDCO2/HDCO which are defined by optimization method are A 0.05 M0.55.s-1, Ea 21.29 kJ/mol, and order of 0.45 for n-dodecane formation; and for n-undecane reaction A 1.53 M-0.08.s-1 and Ea 38.39 kJ/mol, and order of 1.08.
format Final Project
author Kevin Suhendra (NIM : 13013069), Mannuel
spellingShingle Kevin Suhendra (NIM : 13013069), Mannuel
Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
author_facet Kevin Suhendra (NIM : 13013069), Mannuel
author_sort Kevin Suhendra (NIM : 13013069), Mannuel
title Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
title_short Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
title_full Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
title_fullStr Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
title_full_unstemmed Kinetics Study of Hydrodeoxygenation (HDO) Reaction of Methyl Laurate
title_sort kinetics study of hydrodeoxygenation (hdo) reaction of methyl laurate
url https://digilib.itb.ac.id/gdl/view/22962
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