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Fuel
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Review article
Significant parameters and technological advancements in biodiesel
production systems
M. Erdem Günay
a
, Lemi Türker
b
, N. Alper Tapan
c,
⁎
a
Department of Energy Systems Engineering, Istanbul Bilgi University, 34060 Eyup, Istanbul, Turkey
b
Department of Chemistry, Middle East Technical University, 06800 Çankaya, Ankara, Turkey
c
Department of Chemical Engineering, Gazi University, 06570 Maltepe, Ankara, Turkey
ARTICLE INFO
Keywords:
Catalyst type
Reaction temperature
Calcination temperature
Mechanical stirring
Supercritical transesterification
Microwave transesterification
Hydrodynamic cavitation
Ultrasound technology
Future directions
ABSTRACT
Biodiesel is a mixture of fatty acid esters formed by transesterification of vegetable oil, animal fat, algae oil or
waste oil with an alcohol like methanol (CH
3
OH), ethanol (C
2
H
5
OH) or higher alcohols. There are many im-
portant catalytic variables like catalyst type and composition, support type and pretreatment conditions (i.e.
calcination temperature and time) which are utilized to achieve high yields for the transesterification reaction.
In addition, operational conditions such as reaction temperature, alcohol type, alcohol to oil molar ratio and
stirring speed have also quite high significance. Moreover, all these variables can be optimized under super-
critical conditions by novel techniques like ultrasonic and microwave irradiation or hydrodynamic cavitation. In
this work, significant catalytic and operational variables for biodiesel production are reviewed. In addition,
dominant parameters together with their limitations during the application of advanced technologies are in-
vestigated in detail. Then, it has been concluded that, for better control and higher yields of biodiesel pro-
duction, future research works should focus on addition of co-solvents, use of longer chain alcohols, bulky
structures or ionic liquids, adjustment of mode of irradiation and modification of the instrumentation or the
equipment.
1. Introduction
The world fuel consumption has been increasing since the industrial
revolution and this increase is even sharper especially in the recent
years due to the increased movement of goods, services and technology.
Although most of the fuel demand for transportation is supplied by
petroleum-based fuels, their resources are depleted year by year.
Moreover, the recovery of petroleum from new reservoirs in extreme
locations is sometimes also too difficult being too costly. Besides, ex-
cessive use of petroleum-based fuels causes air and water pollution
leading to global warming. However, biofuel production from renew-
able sources is a sustainable way to maintain the ever-growing fuel
demand, causing negligible harm to the environment due to the fast
bioenergy cycle. As a result, the world biofuel production has an in-
creasing trend in the recent years as shown in Fig. 1; such that, annual
bioethanol production increased from 13.7 billion metric ton in the year
2000 to 78.8 billion metric ton in the year 2016 (multiplied by a factor
of 5.8) while annual biodiesel production increased from 0.77 billion
metric ton to 29.8 billion metric ton in the same period of time (mul-
tiplied by a factor of 38.6) [1].
Although biodiesel is an alternative fuel that can be produced from
any edible plant-based oil or animal-based fat, this kind of 1st gen-
eration feedstocks are not preferred anymore due to the requirement of
large farm areas, competition with the food market and thus high costs
in the raw material [2]. Instead, biodiesel is recently preferred to be
made from non-edible plant-based oils with (high oil yield), waste
cooking oils and algae oil (2nd or 3rd generation feedstocks) [3].
The basic pictorial representation of biodiesel production is shown
in Fig. 2, where the main steps for the process are given. It should be
noted that the process may have some minor (or sometimes major)
differences especially in the case of application of advanced techniques.
The main reaction in biodiesel production is transesterification of any
oil with a short chain alcohol like methanol or ethanol. In fact, vege-
table oil can straightly be used as a fuel but its low fuel quality due to
high viscosity, incomplete combustion, coking etc. make it insufficient
for combustion engines. Therefore, transesterification of these types of
oils by lower boiling alcohols convert them to high quality fuels by
lowering viscosity, boiling and flash point.
The transesterification of oil (Eq. (1)) is an endothermic equilibrium
reaction requiring 3 mol of a short chain alcohol per 1 mol of oil in
https://doi.org/10.1016/j.fuel.2019.03.147
Received 27 September 2018; Received in revised form 26 March 2019; Accepted 28 March 2019
⁎
Corresponding author.
E-mail address: atapan@gazi.edu.tr (N. Alper Tapan).
Fuel 250 (2019) 27–41
0016-2361/ © 2019 Published by Elsevier Ltd.
T