DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE

Indonesia's dependence on fuel makes total gasoline imports increase. This resulted in the depletion of the country's foreign exchange reserves and state budget deficit. Therefore, there is need to look for energy from other sources especially that come from within the country. One of the...

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Main Author: Idham K.A. DR, Muhammad
Format: Final Project
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/74932
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:74932
spelling id-itb.:749322023-07-24T13:49:19ZDEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE Idham K.A. DR, Muhammad Indonesia Final Project Gasoline , Malapari and Catalytic cracking INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/74932 Indonesia's dependence on fuel makes total gasoline imports increase. This resulted in the depletion of the country's foreign exchange reserves and state budget deficit. Therefore, there is need to look for energy from other sources especially that come from within the country. One of the natural resources that can be used as an alternative material that can be converted to fuel is malapari. Malapari can produce as much as 2 tons of fatty oil / hectare / year. In addition, malapari can grow in almost all types of habitat including dry land. Malapari oil conversion to gasoline can be done in several ways such as thermal cracking, catalytic cracking and hydrocracking. The catalytic cracking reaction is more economical and efficient because it requires less heat than thermal cracking and high product conversion compared to hydrocracking. In this research, a catalytic cracking reaction was carried out in a batch reactor with a temperature of 500°C and a catalyst mass of 2.5 grams. To determine the effect of catalyst on the yield and selectivity of liquid products, variations were made between 2 different types of zeolite with catalyst ratios of 2 types successively 1:0, 0:1, 3:1, 2:3 1:1, 1:3 and 1:4. In addition, variations of WHSV were carried out to determine the effect of operating conditions on the yield, selectivity and composition of hydrocarbons in gasoline. Variation of operating conditions was carried out with a ratio of 2 types of catalyst on 1:3, while WHSV variations were 2.5, 1.5, 2 and 3 respectively. Result shows gasoline made from malapari oil has lower gasoline selectivity than gasoline made from palm oil. Results also shows variation of catalyst ratio 3:1 has higher gasoline selectivity and octane number. However, this variation hasn’t fulfill the specifications of Indonesia gasoline because it has high content of aromatic hydrocarbon. Research also shows WHSV 2,5 has optimum liquid product yield at 53,74% and high gasoline selectivity. 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 Indonesia's dependence on fuel makes total gasoline imports increase. This resulted in the depletion of the country's foreign exchange reserves and state budget deficit. Therefore, there is need to look for energy from other sources especially that come from within the country. One of the natural resources that can be used as an alternative material that can be converted to fuel is malapari. Malapari can produce as much as 2 tons of fatty oil / hectare / year. In addition, malapari can grow in almost all types of habitat including dry land. Malapari oil conversion to gasoline can be done in several ways such as thermal cracking, catalytic cracking and hydrocracking. The catalytic cracking reaction is more economical and efficient because it requires less heat than thermal cracking and high product conversion compared to hydrocracking. In this research, a catalytic cracking reaction was carried out in a batch reactor with a temperature of 500°C and a catalyst mass of 2.5 grams. To determine the effect of catalyst on the yield and selectivity of liquid products, variations were made between 2 different types of zeolite with catalyst ratios of 2 types successively 1:0, 0:1, 3:1, 2:3 1:1, 1:3 and 1:4. In addition, variations of WHSV were carried out to determine the effect of operating conditions on the yield, selectivity and composition of hydrocarbons in gasoline. Variation of operating conditions was carried out with a ratio of 2 types of catalyst on 1:3, while WHSV variations were 2.5, 1.5, 2 and 3 respectively. Result shows gasoline made from malapari oil has lower gasoline selectivity than gasoline made from palm oil. Results also shows variation of catalyst ratio 3:1 has higher gasoline selectivity and octane number. However, this variation hasn’t fulfill the specifications of Indonesia gasoline because it has high content of aromatic hydrocarbon. Research also shows WHSV 2,5 has optimum liquid product yield at 53,74% and high gasoline selectivity.
format Final Project
author Idham K.A. DR, Muhammad
spellingShingle Idham K.A. DR, Muhammad
DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
author_facet Idham K.A. DR, Muhammad
author_sort Idham K.A. DR, Muhammad
title DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
title_short DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
title_full DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
title_fullStr DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
title_full_unstemmed DEVELOPMENT OF MALAPARI OIL CATALYTIC CRACKING FOR BIO-BASED GASOLINE
title_sort development of malapari oil catalytic cracking for bio-based gasoline
url https://digilib.itb.ac.id/gdl/view/74932
_version_ 1822007533516095488