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By
Y.H. Taufiq-Yap, A.N. Fitriyah and H.V. Lee
The
search for alternative and sustainable fuels has gained
more importance due to several current situations i.e.
(i) gradual depletion of world petroleum reserves, (ii)
an extremely high increase in the price of petroleum
and (iii) environmental concerns about air pollution
caused by the combustion of fossil fuels. Biodiesel,
a renewable fuel, consists of fatty acid methyl esters
(FAME) derived through the transesterification of vegetable
oils, animal fat and also recycles oil from the food
industry with methanol. Biodiesel is recognized as “green
fuel” with several advantages, i.e. safe, non-toxic
and biodegradable compared to petroleum diesel. It is
oxygenated and essentially free of sulfur and aromatics
making it a cleaner burning fuel with reduced emission
of SOx, CO, unburnt hydrocarbons and particulate matter.
Moreover,
using biodiesel as a fuel in a car can give many advantages
such as it is not harmful to the environment, does not
require an engine modification, cheap, makes the vehicle
perform better, last longer, reduces the environmental
effect of a waste product, and is energy efficient.
But, when compared with the cost of diesel obtained
by petroleum, the high cost is the main drawback in
biodiesel production. However, the cost of biodiesel
could certainly be lowered by improving the production
process. The first step in this direction could be represented
by the use of heterogeneous catalysts instead of homogeneous
ones.
Current
technology for biodiesel manufacturing employs transesterification
of triglycerides with methanol using homogeneous acid
or base catalysts. The homogeneous acid-catalyzed process
often uses hydrochloric acid and sulfonic acid as a
catalyst. The problem with this process is the costly
separation of the catalyst, is corrosive to the equipment
and toxic. Moreover, the reaction time is very long
and a high molar ratio of methanol to oil is needed
(30-150:1 mol %). Potassium hydroxide and sodium hydroxide
are usually used as a homogeneous base-catalyst. These
base catalysts show higher performance for obtaining
biodiesel but, they also react with free fatty acids
(FFA) to form unwanted soap by products in which an
expensive separation is required.
Since
the homogeneous catalysts can cause many problems and
increased the production cost, they can be replaced
by environmentally friendly heterogeneous catalysts
because of environmental constraints and simplifications
in the existing processes. Moreover, heterogeneous catalysts
can be more easily separated and give place to a higher
quality ester products and glycerol by product. In this
case, pure high grade glycerol can be obtained without
expensive refining operations. Most heterogeneous catalysts
employed for transesterification are solid bases. Solid
base catalysts have a higher activity and faster reaction
rate as compared to solid acid catalysts. But solid
base catalysts are very sensitive to the presence of
FFA and water.
In
contrast to solid bases, solid acid catalysts can be
applied to feedstock with high FFA and water. Furthermore,
by using solid acid catalyst there is no polluting by-products
formed and the catalysts do not have to be removed since
they do not mix with the product. When compared to liquid
acids that possess well-defined acid properties, solid
acid may contain a variety of acid sites. However, transesterification
using solid acids is not yet well established in the
industry, as it is more difficult to find a suitable
solid acid catalyst for long-chain acids compared to
shorter acids such as acetic acid.
Transesterification
or alcoholysis is the displacement of alcohol from an
ester by another in a process similar to hydrolysis,
except that alcohol is used instead of water. The reaction
is represented by the general equation below:

Transesterification
is a reversible reaction and proceeds essentially by
mixing the reactants. However, the presence of a catalyst
accelerates the conversion. Transesterification process
is affected by the mode of reaction condition, molar
ratio of alcohol to oil, type and amount of catalysts,
reaction time and temperature and purity of reactants.
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Prof.
Dr. Taufik Yap Yun Hin, B.Sc. (Hons)
UPM, MSc. UPM, Ph.D UMIST, UK. Email: yap@science.upm.edu.my
Get your next issue of Symbiosis for Part
2 on types of solid catalysts for transesterification,
advantages of heterogeneous catalyst and oil
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