DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION

Diesel produced from petroleum processing contains sulfur compounds that can harm the environment and human health. The Government of Indonesia has issued a Ministerial Regulation which requires sulfur in diesel used in Indonesia not to exceed 50 ppm (Euro IV standard), no later than 2021. The sulfu...

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Main Author: Hendra, Theodorus
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/38801
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:38801
spelling id-itb.:388012019-06-18T08:40:35ZDEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION Hendra, Theodorus Indonesia Final Project 4,6-DMDBT, citric acid, DBT, hydrodesulfurization, redispersion INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/38801 Diesel produced from petroleum processing contains sulfur compounds that can harm the environment and human health. The Government of Indonesia has issued a Ministerial Regulation which requires sulfur in diesel used in Indonesia not to exceed 50 ppm (Euro IV standard), no later than 2021. The sulfur compound in diesel which is the most difficult to react are 4,6-DMDBT. One important factor in the reaction is the type of catalyst used. The most commonly used catalyst in diesel hydrotreating is NiMo/?-Al2O3. The method that can be used to increase the activity of the catalyst is the addition of chelating agent. Citric acid is commonly used as chelating agent in the synthesis of diesel hydrotreating catalysts. The purpose of this study was to determine the best method of adding citric acid in the synthesis of diesel hydrotreating catalysts. Citric acid was impregnated into a calcined NiMo/?-Al2O3 catalyst, then the effect of post-impregnation treatment was investigated (calcination and drying). The results of the XRD pattern analysis showed that the two types of treatment were able to provide the effects of phase redispersion of NiMoO4 and MoO3 which were the inactive phase of the catalyst. The catalyst activity test in the batch reactor using DBT (dissolved in hexadecane) as feed at 300oC and 30 bar indicates that the best post-impregnation method is calcination which is able to increase the catalyst activity up to 1.80 times the activity of NiMo/?-Al2O3 catalyst. Comparison with commercial catalysts using batch reactor at 330oC and 60 bar shows that citric acid modified NiMo/?-Al2O3 catalyst has 1.36 times DBT HDS activity and 1.01 times 4,6-DMDBT HDS activity than of the commercial catalyst. 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 Diesel produced from petroleum processing contains sulfur compounds that can harm the environment and human health. The Government of Indonesia has issued a Ministerial Regulation which requires sulfur in diesel used in Indonesia not to exceed 50 ppm (Euro IV standard), no later than 2021. The sulfur compound in diesel which is the most difficult to react are 4,6-DMDBT. One important factor in the reaction is the type of catalyst used. The most commonly used catalyst in diesel hydrotreating is NiMo/?-Al2O3. The method that can be used to increase the activity of the catalyst is the addition of chelating agent. Citric acid is commonly used as chelating agent in the synthesis of diesel hydrotreating catalysts. The purpose of this study was to determine the best method of adding citric acid in the synthesis of diesel hydrotreating catalysts. Citric acid was impregnated into a calcined NiMo/?-Al2O3 catalyst, then the effect of post-impregnation treatment was investigated (calcination and drying). The results of the XRD pattern analysis showed that the two types of treatment were able to provide the effects of phase redispersion of NiMoO4 and MoO3 which were the inactive phase of the catalyst. The catalyst activity test in the batch reactor using DBT (dissolved in hexadecane) as feed at 300oC and 30 bar indicates that the best post-impregnation method is calcination which is able to increase the catalyst activity up to 1.80 times the activity of NiMo/?-Al2O3 catalyst. Comparison with commercial catalysts using batch reactor at 330oC and 60 bar shows that citric acid modified NiMo/?-Al2O3 catalyst has 1.36 times DBT HDS activity and 1.01 times 4,6-DMDBT HDS activity than of the commercial catalyst.
format Final Project
author Hendra, Theodorus
spellingShingle Hendra, Theodorus
DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
author_facet Hendra, Theodorus
author_sort Hendra, Theodorus
title DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
title_short DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
title_full DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
title_fullStr DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
title_full_unstemmed DEVELOPMENT OF HYDROTREATING CATALYST FOR 4,6-DMDBT HYDRODESULFURIZATION
title_sort development of hydrotreating catalyst for 4,6-dmdbt hydrodesulfurization
url https://digilib.itb.ac.id/gdl/view/38801
_version_ 1821997606235013120