SYNTHESIS AND CATALYTIC ACTIVITY EVALUATION OF POTASSIUM GLYCEROXIDE AS A TRANSESTERIFICATION CATALYST
The utilization of New and Renewable Energy (NRE) in Indonesia remains far from the energy mix target set for 2025. To achieve this target, efforts to develop NRE are essential as a strategic solution to support sustainable economic growth and minimize environmental impacts. One of the promising...
Saved in:
Main Author: | |
---|---|
Format: | Theses |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/86068 |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | The utilization of New and Renewable Energy (NRE) in Indonesia remains far from
the energy mix target set for 2025. To achieve this target, efforts to develop NRE
are essential as a strategic solution to support sustainable economic growth and
minimize environmental impacts. One of the promising alternatives is biodiesel,
given the abundance of plant-based resources in Indonesia. Biodiesel production
via transesterification requires a catalyst to accelerate the reaction, especially at
low temperatures and atmospheric pressure. On an industrial scale, base catalysts
(hydroxides and alkoxides) are commonly used as catalysts. Although these
catalysts may achieve high conversion rates in short time, there are some
drawbacks. An alternative to hydroxide and alkoxide catalysts is glyceroxide.
Glyceroxide, which can be obtained from the by-products of the biodiesel industry,
is considered superior in terms of safety, high availability, and its ability to reduce
waste. Therefore, synthesizing glyceroxide is viewed as an innovative step in
pursuing more sustainable biodiesel production.
This research focuses on potassium glyceroxide synthesis and its activity test as a
transesterification catalyst. Three parameters will be varied: the molar ratio of
KOH to glycerol (1:1, 2:1, and 3:1), catalyst concentration (0.4%, 0.8%, and
1.2%), and the methanol to oil ratio (3:1, 6:1, and 9:1). A fractional factorial design
was used, resulting in a total of 11 runs with 3 center points. Transesterification
was carried out for one hour at 60–65°C. The results showed that all three
parameters significantly affected the total glycerol and methyl ester content,
although the obtained regression model indicated aliasing. The lowest total
glycerol content (0.108%) and the highest ester content (98.877%) were obtained
in the 11th run (3:1 catalyst ratio, 1.2% catalyst amount, and 9:1 methanol ratio).
This variation was then compared with the KOH catalyst, and it was found that the
product from the potassium glyceroxide catalyst had a higher acid number and
methyl ester content, as well as lower total glycerol. |
---|