IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS

Fossil fuel oil has been the primary catalyst for economic and technological advancement since the 18th century industrial revolution. Hence, there is a need for renewable fuel derived from biomass.. Bio- fuelis seen as a potential substitute for fossil fuels due to its eco-friendly characteristi...

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Main Author: Tsany Hanif, Hibatullah
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/83297
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:83297
spelling id-itb.:832972024-08-07T09:54:52ZIMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS Tsany Hanif, Hibatullah Indonesia Theses catalytic cracking, biofuel, ZSM-5, Beta Zeolite INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/83297 Fossil fuel oil has been the primary catalyst for economic and technological advancement since the 18th century industrial revolution. Hence, there is a need for renewable fuel derived from biomass.. Bio- fuelis seen as a potential substitute for fossil fuels due to its eco-friendly characteristics. The cracking process is one method that can transform vegetable materials into bio-fuel. The catalytic cracking process is known for its high selectivity in producing bio-fuel. The production process necessitates the use of a catalyst for catalytic cracking. ZSM-5 and Beta zeolite are commonly utilized as catalysts.Zeolite is beneficial due to its thermal stability, selectivity, and highly organized structure. This study will use ZSM-5 catalyst and Beta zeolite to produce bio-fuel from palm oil, examining how the ratio of catalyst in the reactor bed.. The study will be conducted under operational parameters of 500°C, ambient pressure, WHSV of 2.5/hour, 5 grams total catalyst mass, and a 4-hour reaction run. Based on the findings from the experiment, it can be concluded that the ZSM-5 catalyst leads to a higher RON value than the Beta Zeolite catalyst because of the abundance of aromatic compounds in the cracked product. Three configurations were performed when preparing thesetup of the two catalysts: 5-B, B-5, and MIX. Among these three setups, it was determined that the 5-B configuration yielded the most favorable outcome, with RON results and levels of aromatic compounds both falling within the 50% range. Additionally, more research was conducted on the 5-B setup by augmenting the proportion of Beta Zeolite catalyst utilization to ratios of 1:1, 1:2, and 1:2.5.It was discovered that the ratio 1:2 was the most effective among the three ratios for achieving the research goals in product production. 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 Fossil fuel oil has been the primary catalyst for economic and technological advancement since the 18th century industrial revolution. Hence, there is a need for renewable fuel derived from biomass.. Bio- fuelis seen as a potential substitute for fossil fuels due to its eco-friendly characteristics. The cracking process is one method that can transform vegetable materials into bio-fuel. The catalytic cracking process is known for its high selectivity in producing bio-fuel. The production process necessitates the use of a catalyst for catalytic cracking. ZSM-5 and Beta zeolite are commonly utilized as catalysts.Zeolite is beneficial due to its thermal stability, selectivity, and highly organized structure. This study will use ZSM-5 catalyst and Beta zeolite to produce bio-fuel from palm oil, examining how the ratio of catalyst in the reactor bed.. The study will be conducted under operational parameters of 500°C, ambient pressure, WHSV of 2.5/hour, 5 grams total catalyst mass, and a 4-hour reaction run. Based on the findings from the experiment, it can be concluded that the ZSM-5 catalyst leads to a higher RON value than the Beta Zeolite catalyst because of the abundance of aromatic compounds in the cracked product. Three configurations were performed when preparing thesetup of the two catalysts: 5-B, B-5, and MIX. Among these three setups, it was determined that the 5-B configuration yielded the most favorable outcome, with RON results and levels of aromatic compounds both falling within the 50% range. Additionally, more research was conducted on the 5-B setup by augmenting the proportion of Beta Zeolite catalyst utilization to ratios of 1:1, 1:2, and 1:2.5.It was discovered that the ratio 1:2 was the most effective among the three ratios for achieving the research goals in product production.
format Theses
author Tsany Hanif, Hibatullah
spellingShingle Tsany Hanif, Hibatullah
IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
author_facet Tsany Hanif, Hibatullah
author_sort Tsany Hanif, Hibatullah
title IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
title_short IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
title_full IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
title_fullStr IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
title_full_unstemmed IMPROVING THE QUALITY AND YIELD OF BIO-FUEL COMBINATION CATALYST IN CATALYTIC CRACKING PROCESS
title_sort improving the quality and yield of bio-fuel combination catalyst in catalytic cracking process
url https://digilib.itb.ac.id/gdl/view/83297
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