ETHYLENEDIAMINE MODIFIED CHITOSAN BEADS AS A CATALYST FOR BIODIESEL SYNTHESIS
Biodiesel is one of the renewable alternative fuels which is easily made through a transesterification reaction, between vegetable oil or animal fat with short-chain alcohol and catalyst assistance. Palm oil is a reliable producer of vegetable oil as a raw material for making biodiesel and Ind...
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Format: | Theses |
Language: | Indonesia |
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Online Access: | https://digilib.itb.ac.id/gdl/view/75566 |
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Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | Biodiesel is one of the renewable alternative fuels which is easily made through a
transesterification reaction, between vegetable oil or animal fat with short-chain
alcohol and catalyst assistance. Palm oil is a reliable producer of vegetable oil as
a raw material for making biodiesel and Indonesia is the number one producer
and exporter of palm oil in the world. Heterogeneous catalyst have the advantage
that they can be separated easily due to phase differences, are regenerative, and
can be reused in biodiesel synthesis reactions. One of the potential raw materials
is chitosan (CS), a natural polymer that is low cost and safe for the environment.
The amine groups in CS play a catalytic role in transesterification. However, CS has
limited and non-free amine groups, leading to suboptimal catalytic performance., so
modifications were made to the CS structure using ethylenediamine (EDA) as
donor of base group in the form of amines (N–H) with epichlorohydrin (ECH) as
cross-linker. This study aims to synthesis and characterization catalysts in the
form of CS, CS/ECH, and CS/ECH/EDA granules followed by testing the catalyst
performance in biodiesel synthesis under various conditions. The success of
biodiesel synthesis was analyzed using Gas Chromatography-Mass Spectrometry
(GC-MS) to determine the desired target methyl ester compound and to determine
the total area of the methyl ester formed in optimization using a Gas
Chromatography Flame Ionization Detector (GC-FID). Based on the IR spectra
of CS, CS/ECH, CS/ECH/EDA, there is an absorption band of O–H vibrations at
3415 and C–O bond vibrations at 2898
. The success of the
CS/ECH/EDA modification was observed from the appearance of absorption
wave numbers at 1655 which is the vibration of the primary N–H bond and
1566 which is the vibration of the secondary N–H bond. Where the bond
that appears comes from the added EDA. In addition, CS/ECH/EDA has a
spherical grain shape and is yellow compared to the CS and CS/ECH grain
catalysts. Determination of the CS/ECH/EDA catalyst performance test showed
that the optimum concentration of EDA addition was 5% (v/v), the reaction was at
room temperature, the ratio of oil:MeOH was 1:1 (v/v), the total volume of
oil/methanol was 10 mL, and catalyst mass of 0.75 gram. The biodiesel
synthesized using the CS/ECH/EDA catalyst exhibited a catalytic performance
that was 8 times better compared to the performance of the CS and CS/ECH
beads catalysts with the methyl ester compounds formed including palmitic acid,
methyl 9,10-octadecadienoic, oleic acid, methyl 12,13-tetradecadienoate, stearic
acid, which was confirmed using GC-MS. In addition, the success of biodiesel
synthesis can be seen from the IR characterization between palm oil and the
synthesis of biodiesel, namely, there is an absorption band at 1193 which is
the vibration of the O–CH3 bond (typical of biodiesel peak) and 1440 which
is the vibration of the CH3 bond (typical biodiesel peak). The IR characterization
of the synthesis biodiesel was also compared to commercial biodiesel where the
IR analysis results of the synthesized biodiesel using CS/ECH/EDA granular
catalysts had similar IR spectra with marketed commercial biodiesel.
Furthermore, the CS/ECH/EDA catalyst was tested for its ability to be used
repeatedly so that the results obtained in the 1st to 3rd use did not experience a
decrease in the total area of the methyl ester indicating that the synthesized
catalyst has fairly good stability. The decrease in the area of the methyl ester
occurred in the 4th application by 29% compared to the 3rd application. After
contact CS/ECH/EDA granular catalysts were characterized using IR with
spectral results similar to the IR spectra of CS/ECH/EDA granular catalysts
before contact indicating that the catalyst structure had not changed. In addition,
SEM characterization was carried out on the catalyst before and after contact,
there was no difference in the SEM image. |
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