ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS

With increasing technological developments and the use of machines in industry and automotive at this time, the need for lubricants will increase. However, declining reserves of crude oil as a raw material for making lubricants and the need to reduce pollution from mineral lubricants have prompte...

Full description

Saved in:
Bibliographic Details
Main Author: Fitri, Zakiatul
Format: Theses
Language:Indonesia
Subjects:
Online Access:https://digilib.itb.ac.id/gdl/view/70064
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:70064
spelling id-itb.:700642022-12-23T14:35:25ZESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS Fitri, Zakiatul Teknik kimia Indonesia Theses bio lubricant, esterification, oleic acid, 1,2 propanediol, reaction kinetics INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/70064 With increasing technological developments and the use of machines in industry and automotive at this time, the need for lubricants will increase. However, declining reserves of crude oil as a raw material for making lubricants and the need to reduce pollution from mineral lubricants have prompted waste and pollution reduction technologies to reduce environmental problems and raw materials that can be renewed. One of the realizations is alternative lubricants called vegetable lubricants or bio-lubricants which are superior in solving environmental problems and have good lubricating properties. However, bio-lubricants have drawbacks, namely low oxidative stability and poor fluidity at low temperatures. This is due to the presence of ?-hydrogen in the glycerol molecule. Glycerol can be replaced with polyols or diols which lack ?- hydrogen such as 1,2 propanediol. In this study, the esterification reaction of oleic acid with 1,2 propanediol was carried out using sulfuric acid as a catalyst. The reaction variables carried out were catalyst weight percent and temperature with a fixed feed molar ratio. From the research, it was found that the higher the temperature of the esterification reaction, the greater the ester conversion obtained with the maximum conversion value at 150 oC at 2% sulfuric acid weight percent for 5 hours amounting to 82.7%. From the experiment, it was also determined that the esterification reaction for the production of this bio-lubricant was a triple reaction with an activation energy value of 46052 J/mol. The biolubricant product obtained had an acid number in the range of 36 - 55 mg- KOH/g-sample and a kinematic viscosity value (at 40 oC) of 20.980 cSt - 38.366 cSt. Bio-lubricant products are classified as ISO VG 22 and ISO VG 46 lubricants. 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
topic Teknik kimia
spellingShingle Teknik kimia
Fitri, Zakiatul
ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
description With increasing technological developments and the use of machines in industry and automotive at this time, the need for lubricants will increase. However, declining reserves of crude oil as a raw material for making lubricants and the need to reduce pollution from mineral lubricants have prompted waste and pollution reduction technologies to reduce environmental problems and raw materials that can be renewed. One of the realizations is alternative lubricants called vegetable lubricants or bio-lubricants which are superior in solving environmental problems and have good lubricating properties. However, bio-lubricants have drawbacks, namely low oxidative stability and poor fluidity at low temperatures. This is due to the presence of ?-hydrogen in the glycerol molecule. Glycerol can be replaced with polyols or diols which lack ?- hydrogen such as 1,2 propanediol. In this study, the esterification reaction of oleic acid with 1,2 propanediol was carried out using sulfuric acid as a catalyst. The reaction variables carried out were catalyst weight percent and temperature with a fixed feed molar ratio. From the research, it was found that the higher the temperature of the esterification reaction, the greater the ester conversion obtained with the maximum conversion value at 150 oC at 2% sulfuric acid weight percent for 5 hours amounting to 82.7%. From the experiment, it was also determined that the esterification reaction for the production of this bio-lubricant was a triple reaction with an activation energy value of 46052 J/mol. The biolubricant product obtained had an acid number in the range of 36 - 55 mg- KOH/g-sample and a kinematic viscosity value (at 40 oC) of 20.980 cSt - 38.366 cSt. Bio-lubricant products are classified as ISO VG 22 and ISO VG 46 lubricants.
format Theses
author Fitri, Zakiatul
author_facet Fitri, Zakiatul
author_sort Fitri, Zakiatul
title ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
title_short ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
title_full ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
title_fullStr ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
title_full_unstemmed ESTERIFICATION REACTION KINETICS OF THE MANUFACTURING OF TWO-BASED ESTER BASED LUBRICANTS
title_sort esterification reaction kinetics of the manufacturing of two-based ester based lubricants
url https://digilib.itb.ac.id/gdl/view/70064
_version_ 1822006203485519872