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Energy Conversion and Management: X 22 (2024) 100590
Available online 12 April 2024
2590-1745/© 2024 The Author(s). Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-
nc-nd/4.0/).
Carbon-Based Nanomaterials: a Paradigm Shift in Biofuel Synthesis and
Processing for a Sustainable Energy Future
Nazia Rodoshi Khan
*
, Adib Bin Rashid
Department of Industrial and Production Engineering, Military Institute of Science and Technology (MIST), Dhaka, Bangladesh
ARTICLE INFO
Keywords:
Carbon-based nanomaterials
Biofuels production
Renewable energy
Carbon nanotubes
Graphene
Carbon nanobers
ABSTRACT
The increased demand for energy has driven researchers to concentrate on generating secure energy sources for
humanity. One advantage of inventing a biological and chemical way to generate green and efcient electrical
energy is that it eliminates dependency on soon-to-extinct fossil fuels. Biofuels are one of many emerging sectors
that are receiving major attention, all of which are alternative fuels. Carbon-based nanomaterials, due to their
larger surface area, affordability, and ability to withstand high temperatures, have been engineered to serve as
efcient electrocatalysts without the need for metals. These nanomaterials can also provide a stable structure for
metal-based electrocatalysts, enabling the conversion of biofuels into environmentally friendly energy sources.
Thus, biofuel synthesis is “greener” using its catalyst. Graphite, carbon nanoparticles, nanotubes, nanohorns, and
nanorods can be used to construct and build a wide range of biofuels. This review gives insight into how carbon-
based nanomaterials are used across all different stages of biofuel production, along with corresponding issues
and possibilities. Moreover, it emphasizes the utilization of diverse carbon-based nanomaterials and nano-
biocatalysts to enhance biofuel production by increasing its yield. Given its many possible uses, the research
in concern exhibits a seemingly indenite scope.
1. Introduction
The need for energy on a global scale is continuously increasing as a
result of growing populations and rapid industrialization. The majority
of global energy needs are addressed through the utilization of nonre-
newable resources that account for a large fraction of the human-caused
increase in atmospheric CO
2
levels. The depletion of crude oil supplies
necessitates searching for non-conventional energy sources that are both
environmentally friendly and commercially feasible [1,2]. Biofuels are
an important part of the renewable energy sector since their energy is
generated through biological carbon xation. Therefore, signicant
technological investment is needed to create methods for mass-
producing biofuel. Nanotechnology provides a potentially helpful
novel approach for dealing with the problems that have plagued con-
ventional pre-treatment, hydrolysis, and fermentation methods for a
long time. Using nanoparticles during biofuel production boosts the
fermentation response rate and improves pre-treatment and enzymatic
hydrolysis effectiveness. As of 2016, over 60 countries had initiated
national nanotechnology programs, signaling a robust commitment to
this burgeoning eld. With the backing of both governmental bodies and
the private sector, the trajectory of nanotechnology is poised for
continued expansion. The anticipated global surge in nanotechnology’s
industrial applications underscores its profound and comprehensive
inuence on nearly every economic sector. A testament to its interna-
tional reach is the array of global companies engaged in producing
nanotechnology-enabled products, as detailed in Table 1. This expan-
sion is driven by the diverse applications of nanomaterials across various
industries, including biofuels, where they enhance production efciency
and sustainability [3]. Therefore, global utilization of nanomaterials has
seen signicant growth. In addition, nanoparticles include a high
adsorption limit, durability, stability, and durability, as well as a supe-
rior degree of catalytic activity, durability, and crystallinity. Owing to
their unique properties, nano-biocatalysts have emerged as potential
materials for enhancing biofuel generation. Typically employed as
reactant specialists, chelates contribute greatly to electron transfer, s
inhibitory combinations and promoting the activity of anaerobic groups
[4–6].
Carbon nanomaterials (CNMs), a burgeoning subeld of nanotech-
nology, are making strides in diverse use ranging from drug delivery and
tissue engineering to medical transplantation. Dened by their size,
* Corresponding author.
E-mail address: naziarodoshi@iut-dhaka.edu (N. Rodoshi Khan).
Contents lists available at ScienceDirect
Energy Conversion and Management: X
journal homepage: www.sciencedirect.com/journal/energy-conversion-and-management-x
https://doi.org/10.1016/j.ecmx.2024.100590
Received 15 February 2024; Received in revised form 7 April 2024; Accepted 10 April 2024
Energy Conversion and Management: X 22 (2024) 100590
2
which ranges between 1 and 100 nm, CNMs are integral in enhancing
various properties such as surface area, refractive index, multi-
functionality, pharmaceutical delivery, durability, and immunogenicity
[7,8]. This category encompasses a variety of forms, including nano-
carbon, graphene oxide, graphene nanosheets, graphene quantum dots,
nanodiamond, and single- and multi-walled carbon nanotubes, as well as
fullerene and carbon foam [9,10].
These CNMs are particularly notable for their potential in biological
sciences, attributed to their distinct features. Their intrinsic properties
are leveraged in biofuel manufacture, where they play a critical function
in improving the synthesis process. The global biofuel sector is experi-
encing a surge in the adoption of CNMs, with carbon nanotubes, nano-
bers, and nanosheets leading the charge due to their stability and
catalytic capabilities. These materials are essential in enzyme immobi-
lization, signicantly enhancing biofuel synthesis and contributing to
the production of biogas, biodiesel, and bioethanol. This trend un-
derscores a growing recognition of the efciency and cost-effectiveness
of nanomaterials, marking a shift towards more innovative and sus-
tainable energy solutions [11–13]. This review discusses the
manufacturing of biofuels and the many process methodologies, feed-
stocks, and obstacles involved. In the present context, biofuel generation
is crucial. The concerned review provides an overview of the processes
involved in making biofuels from a wide range of feedstocks utilizing
various technological approaches utilizing carbon-based nanomaterials.
The use of fossil fuels as energy sources has peaked due to industri-
alization and globalization, posing a signicant threat to the environ-
ment. Presently, there is a shift towards sustainable alternatives such as
biofuels to meet the needs of future generations. This review examines
the application of different carbon-based nanomaterials for eco-friendly
biofuel production. The review extensively covers the use of various
carbon-based nanomaterials in biofuel synthesis, discussing the syn-
thesis, functionalization, and the circular economy of green-synthesized
CNMs in detail. The insights presented in the review aim to assist the
scientic community in adopting studies on highly efcient CNMs to
enhance the biofuel production process.
2. Overview of biofuels production
Biofuels are a category of fuels made from biomass derived from
plant-based materials processed to create a sustainable energy source.
These biofuels come in various forms, such as liquid, solid, and gaseous,
providing a wide range of fuel types for applications like heat, elec-
tricity, chemicals, and other materials. Biofuels are seen as a promising
alternative energy source that shares similarities with petroleum fuels,
particularly in transportability. This characteristic gives biofuels an
advantage over other renewable energy sources, making them a po-
tential driving force for transportation. Due to their plant-based origin,
burning biofuels does not contribute to increased atmospheric carbon
dioxide levels, as the carbon stored in biofuels was initially absorbed
through photosynthesis from the atmosphere [14–16]. Bioethanol and
biobutanol, also known as biogasoline, are widely used biofuels.
Currently, there are numerous opportunities to harness bioenergy. For
over 50 years, the gasoline industry has been the primary energy source.
However, transitioning to a biobased sector could offer a dependable
alternative energy source, leading to widespread support for promoting
biofuels in different industries. [17,18].
The classication of biofuels into different generations is based on
the origin of the biomass used in their production. This categorization
helps understand the various types of biofuels available and their po-
tential applications in the energy sector. Biofuels are classied based on
the source material used for production, with categories including rst-
generation (1G), second-generation (2G), third-generation (3G), and
fourth-generation (4G), as depicted in Fig. 1 [4].
Researchers predict that 10–50 % of the world’s energy consumption
will be derived from biomass by 2050. This estimation underscores the
critical role of biomass as a primary sustainable energy source globally.
The direct burning of biomass for energy supply has been associated
with numerous conicts and problems. This practice has played a sig-
nicant role in the emission of greenhouse gases (GHGs) and the sub-
sequent impact on climate change. However, by utilizing modern
biofuel production technologies, energy recovery from biomass holds
immense potential in addressing global energy security concerns and
balancing trade decits, as depicted in Fig. 2 (data taken from the En-
ergy Institute (EI) Statistical Review of World Energy, 2023 [19]). Bio-
fuels, generated through various technologies, offer signicant
potential. While 1st-generation biofuels have limitations, 2nd, 3rd and
4th generation biofuels show promise. In 2018, global biofuel produc-
tion reached 154 billion liters, with an expected 25 % expansion by
2024. The bioenergy sector has also created approximately 2.8 million
jobs, emphasizing its role in employment opportunities. Biofuels
continue to evolve, playing a crucial role in meeting energy demands
while promoting sustainability [20].
2.1. Biodiesel
Bio-diesel is an alternative fuel from long-chain fatty acids in mono-
alkyl esters originating from vegetable oil and animal fat. The produc-
tion of biodiesel involves trans-esterication, a chemical reaction where
oils or fats are converted into fatty acid methyl esters (FAME),
commonly known as biodiesel. The process requires an alcohol (usually
methanol) and a catalyst (such as sodium hydroxide). The by-product of
this reaction is glycerol, which can be used in other industries, adding to
the sustainability of the process [21]. Therefore, it is crucial to track
down natural sources of inexpensive feedstock. The feedstock for bio-
diesel can be diverse. Edible oils like soybean or rapeseed oil are com-
mon, but there’s a growing interest in non-edible oils from plants like
Jatropha. Waste vegetable oil and animal fats are also used to improve
economic viability and reduce waste. The choice of feedstock affects the
quality and nancial feasibility of the biodiesel, as well as its environ-
mental impact [21]. Vegetable oils are trans-esteried with methanol (or
ethanol) to produce it. Biodiesel is a sustainable energy resource since it
is made from a renewable, domestic resource, which reduces the de-
mand for petroleum fuel. It also has the added benets of being biode-
gradable and harmless [22,23]. Additionally, biodiesel offers a more
appealing combustion emission prole than petroleum-based diesel,
including minimal carbon monoxide emissions, particle matter, and
unprocessed hydrocarbons. Unlike petroleum diesel, a greater ash
point (150 ◦C) is found in biodiesel, making it more stable and more
secure to handle or carry. In light of the presence of free fatty acids, it
can also act as a lubricant and help keep engines running smoothly for
Table 1
Some global nanotechnology companies [3].
Country Company Operations
UK Applied Graphene
Materials
Develops and applies graphene
nanoplatelet dispersions
UK Advanced Material
Development
Develops 2D nanotechnologies and
metamaterial systems
USA 3 M Manufactures numerous nanomaterials
Canada CelluForce Produces a form of cellulose nanocrystals
(CelluForce NCC™)
Luxembourg OCSiAl Luxembourg Produces graphene nanotubes
Japan Zeon Corporation Manufactures single-walled carbon
nanotube
USA Cerion Manufactures metal, metal oxide, and
ceramic nanomaterials
Portugal INNOVNANO Manufactures ultra-ne nanostructured
ceramic powders
Germany RAS AG Produces and distributes of
nanomaterials
France Superbranche Develops functionalized metallic oxide
nanoparticles
Spain Nanogap Manufactures novel nanomaterials from
atomic quantum clusters
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
3
longer. Numerous cutting-edge methods have been recognized in the
study of bioenergy that have the potential to raise biodiesel output
signicantly [24]. Economically viable and readily available feedstocks
and new fabrication and purication processes are the primary research
areas presently [25,26]. Advancements in technology play a vital role in
enhancing the efciency and cost-effectiveness of biodiesel production.
These advancements include catalyst improvement, novel feedstock
processing methods, and overall production process optimization.
Additionally, research efforts are directed towards scaling up production
to meet commercial demands while ensuring minimal impact on food
supply and land use. Biodiesel offers a substantial advantage over
traditional fossil fuels by signicantly reducing carbon emissions,
thereby contributing to the mitigation of greenhouse gases. Further-
more, biodiesel is biodegradable and non-toxic, reducing the risk of
environmental contamination. Its utilization also leads to a reduction in
harmful particulate emissions, which pose a threat to human health.
Continuous research and technological progress are crucial in address-
ing challenges related to production costs, scalability, and sustainability
[21].
2.2. Bioethanol
Bioethanol, also referred to as bio-alcohol, undergoes a series of four
primary stages during its production: pretreatment, hydrolysis,
fermentation, and distillation. The production of bioethanol involves the
fermentation of carbohydrates from biomass. This process typically in-
cludes the pretreatment of biomass to release fermentable sugars, fol-
lowed by the fermentation stage, where microorganisms, such as yeast,
convert these sugars into ethanol [21]. Pretreatment aims to decompose
the complex structure of lignocellulosic biomass and increase its
accessibility for enzymatic hydrolysis. Pretreatment methods include
physical, chemical, biological, and combined techniques. Following
that, hydrolysis converts the polysaccharides (cellulose and hemicellu-
lose) in the biomass into simple sugars (glucose and xylose) using en-
zymes or acids. The general equation for the fermentation process is
represented as (C
6
H
12
O
6
→ 2C
2
H
5
OH +2CO
2
), indicating the produc-
tion of two molecules of CO
2
and ethanol for each molecule of glucose
fermented. The industrial fermentation process usually stops when
ethanol concentration reaches about 9–10 %, and the yeasts can be
Fig. 1. The categorization of biofuel feedstocks.
Fig. 2. Production and consumption of biofuels globally (2012–2022).
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
4
reused in subsequent cycles [21]. Lastly, distillation separates the
ethanol from the fermentation broth and puries it to the desired con-
centration. Distillation is an energy-intensive process that constitutes a
considerable proportion of the production expense. The ethanol yield
from glucose is between 88–95 %, with byproducts like glycerin (3–5 %)
and acetic acid. The fermented mash is distilled to increase ethanol
concentration to 94 %, making it marketable. The resultant bioethanol
can be puried through dehydration [21]. Bioethanol production is a
complex and challenging process that requires optimization of various
factors, such as feedstock selection, pretreatment method, enzyme
loading, fermentation conditions, and distillation efciency [27,28].
Bioethanol distinguishes itself from other biofuels due to its rapid
combustion rate, lower boiling point, and increased heat vaporization.
Its superiority over traditional fuels is evident, offering a multitude of
advantages. Bioethanol, in both hydrated and dehydrated forms, is used
as fuel either in pure form or blended with gasoline. It offers signicant
economic and environmental benets, such as a higher-octane number
and improved combustion efciency. Additionally, the use of ethanol in
fuels generally leads to reduced emissions of carbon monoxide (CO),
volatile organic compounds, and sulfur oxides compared to typical fossil
fuels [21]. The advantages of bioethanol over petroleum-based fuels
stem from its higher compression ratio, shorter burn time, and smaller
engine size. Bioethanol, an oxygenated fuel, contains 35 % oxygen,
reducing the emissions of nitrogen oxides (NOx) and sulfur oxides (SOx)
during combustion. Additionally, the improved ignition of bioethanol
results in a cleaner exhaust in terms of hydrocarbons and particulate
matter [4].
2.3. Biogas
Biogas, a type of renewable energy, is created through anaerobic
digestion, a process where microorganisms convert organic matter into
methane and carbon dioxide. This process occurs in different environ-
ments like marshes, landlls, and the digestive tracts of ruminants [29].
The main components of biogas are methane and carbon dioxide,
accompanied by small amounts of other gases. It can be produced from
various biomass, including carbohydrates, proteins, and fats. Biogas
production involves the decomposition of organic matter, like agricul-
tural waste, sewage sludge, and animal waste, by specic microorgan-
isms in the absence of oxygen. These microorganisms break down the
organic matter and transform it into biogas. Critical factors in biogas
production are the composition and potential of the organic matter, the
absence of harmful pathogens, and the quality of biogas for its intended
uses. The leftover residues from fermentation should also be suitable as
fertilizer for agricultural purposes. The technology for biogas production
is well-established and allows for recycling minerals and nutrients into
the soil, promoting sustainable development. Biogas can be used directly
for energy or processed in combustion engines or cars [21]. Its appli-
cations include electricity generation, heating, and cooking fuel. One of
the signicant advantages of biogas is its ability to reduce greenhouse
gas emissions since it captures and utilizes methane that would other-
wise be released into the atmosphere. Furthermore, the byproduct of
biogas production, called digestate, is a natural fertilizer that is nutrient-
rich and can enhance soil fertility. As the world strives for sustainable
and cleaner energy alternatives, biogas is vital in the transition towards
a more carbon–neutral future [30].
2.4. Bio-Hydrogen
Biohydrogens are gaining increasing attention as potential fuels for
the future due to their unique attributes in clean energy generation,
waste management, and high energy content. Biohydrogen represents a
signicant step towards achieving a sustainable and eco-friendly soci-
ety. Hydrogen has a high energy yield per mass, making it an efcient
energy carrier. The production of biohydrogens can utilize organic
waste, thus contributing to waste reduction and management [31,32].
Unlike traditional fossil fuel-based hydrogen production, biohydrogen
production, especially through biological processes, is considered
cleaner and more sustainable. It can be easily manufactured from spe-
cic biomasses, although there are several challenges in its bio-
production, such as non-condensable gas storage and transportation.
Recently, biohydrogen biosynthesis has become a signicant focus as a
fuel for the next generation, thanks to its sustainable characteristics
[33]. Overall, biohydrogen can be obtained through various biological
processes, including dark fermentation, photofermentation, and the
utilization of algal biomass. Photofermentation, carried out by photo-
synthetic bacteria (PSB), utilizes light energy to produce hydrogen by
consuming various substrates in the presence of light. On the other hand,
cyanobacteria and microalgae undergo direct and indirect biophotolysis
to produce hydrogen, using inorganic CO₂, sunlight, water, and various
substrates, including organic acids. Dark fermentation, in contrast, oc-
curs in the absence of light, where anaerobic bacteria decompose com-
plex substrate molecules into basic monomers to produce hydrogen.
Dark fermentation is a widely used method for producing biohydrogen,
with glucose, glycerol, and low organic acids being the most common
substrates. Researchers have found that combining dark fermentation
with photofermentation can create a more efcient process known as
dark-photo co-fermentation [34]. This technique is cost-effective and
environmentally friendly and utilizes renewable feedstock, making it
highly popular. In addition to traditional substrates, scientists have also
explored the use of algal biomass and residual algal biomass to enhance
the efciency of direct hydrogen production from microalgae [35,36].
3. Overview of Carbon-Based nanomaterials
Different types of nanomaterials fall under the category of “nano-
materials,” including nanosheets, nanoparticles, nanocomposites,
nanotubes, nanocrystalline materials, metal-based nanomaterials, and
carbon-based nanomaterials. These nanomaterials have been exten-
sively used in biofuel production research due to their benecial prop-
erties, such as low density, high surface area, recycling potential,
insolubility, and stability [37]. Consequently, developing nanocatalysts
for biodiesel synthesis is highly anticipated [38,39]. The ndings indi-
cate that nanocatalysts have the potential to enhance transesterication
processes and improve productivity. Consequently, numerous studies
have focused on investigating the capabilities of various nanocatalysts,
including those derived from metal oxides, supported metal oxides,
zeolites/nano-zeolites, and magnetic materials, in producing biofuels
[40–43]. Additionally, it has been discovered that heterogeneous cata-
lysts and carbon-based support materials are commonly used in catalysis
[44].
Numerous research studies have established that carbon nano-
particles, such as acid- and base-activated carbon, supported carbon
materials, and sulfonated CNTs, have signicant potential as catalysts
for producing biofuels [45,46]. Carbon-based nanomaterials mainly
consist of carbon atoms arranged in unique structures with nanoscale
dimensions that confer exceptional properties benecial in various ap-
plications. Furthermore, these catalysts offer advantages, including
excellent thermal stability, lack of metals, and ease of synthesis [39].
Nanosized carbon-based catalysts show even more tremendous promise
for biofuel synthesis due to their cost-effectiveness, wide availability,
stability at high temperatures and different chemical environments,
ability to modify hydrophobicity and polarity, and easy extraction from
reaction mixtures [37]. Consequently, these nanomaterials play a
crucial role in efciently converting biomass sources like agricultural
residues, algae, and waste into biofuels, thereby enhancing the overall
processing efciency and reducing energy consumption.
Carbon-based nanomaterials can enhance biofuel production’s
catalysis by being integrated as starting or supporting materials in the
production process. Using agricultural byproducts like fruit peels, rice
husk, and de-oiled seed cake can create catalysts through sulfonation
and high-temperature calcination. These catalysts not only make use of
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
5
the byproducts from bioreneries but also offer a partial solution to the
waste management problem. Table 2 provides a concise overview of the
research conducted on carbon-based catalysts and their application in
the biodiesel sector [47].
3.1. Synthesis and functionalization of Carbon-Based nanomaterials for
biofuels
The advancement in Carbon-based nanomaterials (CBNs) research
has led to the development of a wide range of applications, spanning
from industrial purposes such as creating strong compounds and nano-
scale electronic devices to scientic applications like enhancing tissue
scaffolds, drug delivery systems, and biosensors. Due to their excep-
tional combination of mechanical, electrical, thermal, and optical
properties, CBNs have gained popularity due to their versatility in
various elds [54]. There are diverse classications of Carbon-based
nanomaterials (CNMs), including nanocarbon, graphene quantum dots
(GQDs), graphene oxide, graphene nanosheets, nanodiamond, fullerene,
single-walled carbon nanotubes (SWCNTs), multiwalled carbon nano-
tubes (MWCNTs), and carbon foam. These CNMs exhibit unique char-
acteristics that are benecial for several biological applications.
Moreover, introducing nitrogen doping in CNMs can enhance their
properties by promoting a porous structure, increased catalytic activity,
and improved biocompatibility. Such modications allow CNMs to
adhere more effectively to cellular surfaces, ultimately leading to higher
metabolic product yields. These improved CNMs possess intrinsic fea-
tures, making them highly sought after [9]. Some CNMs have already
been extensively utilized and show promise for potential biofuel appli-
cations, as illustrated in Fig. 3 [55]. The widespread use of these CNMs
in various industries highlights their signicance and the growing in-
terest in exploring their capabilities for future innovations and ad-
vancements in the eld of biofuels.
3.1.1. Fullerenes
Fullerene, a 0-dimensional nanomaterial, may be formed into
spheres (Buckyballs), ellipsoids (Bucky tubes or CNTs), and tubes. It
wasn’t until 1970 that it was effectively synthesized in a vacuum using a
laser vaporization method. Fig. 4 depicts an analytical representation of
fullerene C
60
, which was discovered to be made of 12 pentagonal and 20
hexagonal rings with their symmetry planes aligned, similar to graphite.
Initially considered inert, their solubility in organic solvents opened up
possibilities for functionalization via addition and redox reactions. The
C
60
molecule (which has 60 carbon atoms) is popularly referred to as a
“Buckyball” (because it resembles a football) and takes its name from
Buckminster Fuller’s geodesic dome design. Fullerenes have the
following properties: (i) Fullerenes like C
76
, C
78
, C
80
, and C
84
are
fundamentally chiral due to D
2
-symmetry; (ii) C
60
lacks super-
aromaticity; (iii) fullerenes have high stability; (iv) fullerenes have
varying solubility; and (v) fullerenes’ contamination varies based on the
category, solvent functional group, and synthesis technique [8].
Following are the synthesis techniques for fullerene-.
3.1.1.1. Arc discharge. Under conditions of high temperature, the arc
discharge method is utilized as a synthesis technique. This methodology
encompasses a range of equipment such as a water-cooled trap, a
heating furnace, carbon electrodes, a high voltage pulsed-power input,
and a quartz tube. Within a temperature range of approximately 25 to
1000 ◦C, carbon clusters undergo annealing while a buffer gas is passed
through the quartz tube. To maintain a pressure of around 500 Torr, a
ow rate of 300 cm
3
s
−1
is set. To detect the presence of fullerenes,
including at low concentrations, the Performance Liquid Chromatog-
raphy (HPLC) technique is employed [56].
3.1.1.2. Laser ablation. When a high-energy laser beam is directed to-
wards a solid target material, typically graphite or a graphite rod, the
focused beam causes the target to heat rapidly, leading to vaporization.
As a result of the intense laser pulse, the target material is transformed
into vaporized carbon atoms, which subsequently condense and cool
down. These condensed carbon atoms then form clusters, eventually
evolving into structures known as fullerenes. The entire process occurs
in a controlled setting, commonly within an environment lled with
inert gases like helium or argon, which helps regulate the conditions for
forming fullerenes [57].
3.1.1.3. Chemical vapor deposition (CVD). A precursor gas with carbon
atoms is fed into a reaction chamber, which breaks down at high tem-
peratures to release carbon atoms. These carbon atoms accumulate on a
substrate surface, creating a thin lm or deposit. For fullerenes, the
precursor gas consists of carbon atoms that eventually form fullerene
structures. Various methods can be employed for chemical vapour
deposition (CVD), such as hot lament CVD, plasma-enhanced CVD, and
thermal CVD. In hot lament CVD, a heated tungsten lament dissoci-
ates the precursor gas. The temperature of the lament is carefully
regulated to aid in fullerene formation. Soot containing fullerenes is
produced as a by-product on the edges and rear surface of the substrate
holder, where diamond deposition is not favoured due to temperature
conditions. This technique enables the controlled production of fuller-
enes in a specic environment. Besides synthesis, CVD can also dope
fullerenes by introducing foreign atoms like nitrogen into the fullerene
structure. Nitrogen-doped fullerenes possess unique properties and are
applied in various elds, including optoelectronics and catalysis [58].
The free fullerene molecule’s limited solubility and hydrophobic
nature hinder its widespread use in different applications, leading re-
searchers to investigate modications that can improve its reactivity and
versatility for specic purposes. Functionalization of fullerenes can be
achieved through covalent or non-covalent methods, with covalent
changes capitalizing on C
60
′
s electrophilic properties for nucleophilic
addition. In contrast, non-covalent alterations involve hydrogen
bonding, pi-pi interactions, and coordination with metal ions. Adjusting
the fundamental characteristics of fullerene derivatives can be custom-
ized to exhibit increased lipophilicity, water solubility, and amphiphi-
licity, broadening their potential uses across various elds. An example
Table 2
Synopsis of research on carbon-based catalysts for biodiesel production.
Support/starting material Preparation method Application Yield References
D-glucose A sequence of incomplete
carbonization and sulfonation
Transesterication of used oil and
esterication of oleic acid
90 % for transesterication; 95 % for esterication [48]
Rice husk A string of carbonization and
sulfonation
Glycerol esterication with acetic acid Conversion of glycerol to triglycerides at a 90 % rate [49]
Rubber de-oiled cake Calcination promptly following direct
sulfonation
Synthetic transesterication of a non-
edible oil combination
Single-step biodiesel production yields 91.2 %,
while two-step production yields 93.7 %.
[50]
Microcrystalline cellulose
powder
A sequence of incomplete
carbonization and sulfonation
Oleic acid esterication and triolein
transesterication.
Transesterication at 98 % and esterication at 100
%
[51]
Activated carbon Wet impregnation with
Tungstophosphoric acid
Jatropha oil transesterication from
crude
87.33 % biodiesel yield [52]
Vegetable oil and
petroleum asphalt
Sulfonation of carbonized petroleum
asphalt/vegetable oil
Transesterication of used oil and
esterication of oleic acid
>80 % for both esterication and transesterication [53]
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
6
of this is the successful functionalization of Buckminsterfullerene (C
60
)
with Polyvinyl pyrrolidone (PVP) to produce a water-soluble derivative
[59].
3.1.2. Carbon nanotubes
The development of novel nanomaterials, such as carbon nanotubes,
that can be employed in various applications has recently gained much
attention. Nanoscale carbon tubes (or CNTs) are cylinders made of
carbon. CNTs are well suited for biofuel use due to their biocompati-
bility, antifouling qualities, high specic surface area, and superior
conductivity. Single-walled carbon nanotubes (SWCNTs) are nanowires
of a single enrolled graphene layer of a specic diameter and length. In
contrast, multi-walled carbon nanotubes (MWCNTs) are nanowires of
many enrolled graphene layers of varying diameters, lengths, and
chirality [60]. Carbon nanotubes can be utilized as accelerators and
catalysts because of their outstanding capabilities, superior chemical
stability, minimal toxicity, substantial surface area, and effective
structure. Several research organizations have identied carbon nano-
tubes as an essential component in various catalytic processes, including
the production of biofuels [37].
The synthesis of carbon nanotubes (CNTs) through laser ablation, arc
discharge, and chemical vapour deposition (CVD) shares similarities
with fullerene production. However, plasma-enhanced chemical vapor
deposition (PE-CVD) differs as it sources carbon from gaseous feedstocks
like methane (CH₄) and carbon monoxide (CO), eliminating the need for
solid graphite. These gases decompose into reactive carbon species
(RCS) such as C₂ and CH in the presence of an argon plasma, facilitating
product formation at lower temperatures and pressures. Thermal
Fig. 3. Carbon nanoparticles with demonstrated and potential applications in biofuels.
Fig. 4. Synthesis of Fullerene.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
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synthesis encompasses various chemical deposition methods, including
ame synthesis and CO₂ synthesis. Unlike plasma-based laser ablation
and arc discharge, thermal synthesis relies solely on a hot reaction zone
(approximately 1200 ◦C) and thermal energy. Metal catalysts like nickel,
cobalt, iron, and the carbon feedstock are often used to produce CNTs
[56].
Carbon nanotubes (CNTs) can be chemically functionalized as cata-
lysts in biodiesel production. Multi-walled carbon nanotubes (MWCNTs)
are preferred due to their cost-effectiveness compared to single-walled
carbon nanotubes (SWCNTs). For transesterication catalysts,
MWCNTs undergo specic functionalization processes [61].
3.1.2.1. Purication of CNTs. For optimal performance, CNTs must be
puried to eliminate undesirable byproducts like graphite and amor-
phous carbon, fullerenes, and metal particles. Before functionalizing
them to create catalyst supports for transesterication, MWCNTs are
puried via liquid phase oxidation and resolved in an acidic solution.
This process typically involves immersing the MWCNTs in concentrated
nitric acid (HNO
3
), a 1:1 mixture of HNO
3
and hydrochloric acid (HCl),
or a 3:1 mixture of concentrated sulfuric acid (H
2
SO
4
) and HNO
3
. The
treatment is carried out for a duration ranging from 3 to 24 h at tem-
peratures between 50 and 80 ◦C. The initial step involves sonicating the
MWCNTs in the acid solution for an hour, followed by a ltration pro-
cess where water is added until neutrality is achieved. Subsequently, the
MWCNTs are dried for 12 h at 120 ◦C. Post-treatment, the puried
MWCNTs are denoted as MWCNTs-COOH, indicating the introduction of
carboxylic functional groups to their structure [61].
3.1.2.2. Utilization of the amino groups for functionalization. The ability
of amino groups to bind onto MWCNTs has been observed, potentially
making them useful as base catalysts in transesterication reactions.
Grafting amino groups onto MWCNTs can be done in two ways: either by
thermally mixing the long-chain amine-modied MWCNTs or by intro-
ducing the amino groups into surface gaps and then reacting with carbon
monoxide in a C-C coupling reaction. The three-step direct thermal
mixing process begins with acid oxidation to generate carboxylic groups,
continues with acylation (often with thionyl chloride (SOCl
2
)), and ends
with amidation [61].
3.1.2.3. Catalytic acid functionalization. Sulfonation refers to adding a
sulfonic group (SO
3
H) to CNTs to modify their properties. Trans-
esterication using SO
3
H is effective, with substantial quantities of
biodiesel being obtained. To catalyze transesterication/esterication,
SO
3
H appears to be an excellent option for grafting onto the surface of
MWCNTs. Functionalizing MWCNTs with SO
3
H groups has been re-
ported using seven distinct sulfonation techniques, as shown in Fig. 5
[61]. Within this gure, the initial method entails functionalizing
MWCNTs using concentrated H
2
SO
4
via thermal treatment, representing
the exclusive reported sulfonation technique for transforming MWCNTs
into catalysts for biodiesel production. By treating MWCNTs with
concentrated H2SO4 at elevated temperatures, sulfonated MWCNTs are
obtained from a substantial quantity of SO
3
H groups. The second
approach involves in situ polymerization of acetic anhydride and HSO4
to generate sulfonated MWCNTs by incorporating MWCNTs-COOH
groups into a blend of H
2
SO
4
and acetic anhydride ((CH
3
-CO)
2
O). The
third tactic employs in situ polymerization of 4-styrenesulfonate to afx
SO
3
H groups onto the MWCNTs’ surface. The fourth method encom-
passes the sulfonation of MWCNTs through the thermal processing of p-
toluenesulfonic acid (TsOH) with D glucose, culminating in the creation
of carbohydrate-derived solid acid catalysts known as sulfonated
MWCNTs. The fth technique integrates the sulfonation of MWCNTs via
the thermal breakdown of (NH
4
)
2
SO
4
. Eventually, the sixth sulfonation
technique involves initiating a reaction between MWCNTs and
aminomethane-sulfonic/aminobenzenesulfonic compounds. The sev-
enth technique entails oxidizing thiol groups with hydrogen peroxide
(H
2
O
2
) to introduce sulfonic acid groups onto MWCNTs [61].
3.1.3. Sulfonated carbon nanotubes
Diminution of catalytic surface area and aggregation are the most
prominent causes of inactivation in conventional CNTs [62]. Sulfonation
is a viable option for xing this problem. Sulfonated multiwalled S-
MWCNTs, a form of carbon nanotubes, are heterogeneous acid catalysts
created for use in transesterication reactions. Numerous research
studies have been undertaken employing CNTs with sulfonic acid
functionality for the production of biodiesel from various feedstocks,
including cottonseed oil, PFAD (Palm Fatty Acid Distillate) bio-oil, tri-
laurin and PFAD, due to the benets of functionalized carbon materials
[63]. Table 3 depicts some notable research on sulfonated carbon
nanotubes and their key ndings.
Fig. 5. Sequential sulfonation techniques used in catalytic acid sulfonation.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
8
3.1.4. Graphene/Graphene Oxide-Based nanocatalysts
The exploration of graphene nanocomposites has become a pivotal
area of research. Graphene, characterized by a single atomic layer of
graphite, is the fundamental unit for fullerenes and carbon nanotubes
(CNTs), boasting a spectrum of properties including optical, mechanical,
thermal, electrical, and chemical attributes. Structurally, it is a two-
dimensional molecule composed of a tightly interlinked honeycomb
lattice of sp
2
-hybridized carbon atoms. Graphene oxide (GO), noted for
its mechanical robustness and chemical stability, draws signicant sci-
entic interest. While commonly derived from graphite and graphite
oxide, it can also be synthesized from diverse materials such as recycled
plastics and organic waste [37]. Graphene oxide (GO) is synthesized
through the exfoliation and oxidation of layered crystalline graphite in
protonated solvents. It is composed of a single layer of graphite oxide,
which can be conceptualized as individual graphene sheets adorned
with oxygen-containing functional groups such as carbonyl (C =O),
hydroxyl (–OH), carboxylic acid (–COOH), and alkoxy (C-O-C). These
oxygen functionalities make GO more soluble in water and organic
solvents, making it a valuable component in biodiesel production.
Additionally, the hydrophilic nature of GO facilitates the integration of
Brønsted acid sites during sulfonation [69].
Graphene, isolated by Geim and Novoselov in 2007, is another solid
carbon compound (SCC) utilized in biodiesel production. It features sp
2
-
hybridized carbon atoms arranged in a unique one-atom-thick, two-
dimensional honeycomb lattice, offering remarkable mechanical
strength and a high specic surface area of 2630 m
2
/g. The processing of
raw graphene presents challenges due to its intricate synthesis, limited
solubility, and propensity for aggregation through van der Waals forces
[70]. Nongbe et al. demonstrated the synthesis of cost-effective sulfo-
nated graphene from graphite, showcasing its remarkable efcacy and
durability as a catalyst for biodiesel conversion from palm oil, which can
be reused multiple times without degradation [71]. The production
process of sulfonated graphene involves two stages: the oxidation of
graphite to GO and its conversion to graphene through hydrazine-
mediated ultrasonic exfoliation, as depicted in Fig. 6 [69].
3.1.5. Carbon nanobers (CNFs)
Since their emergence in the 1960 s, carbon nanobers (CNFs) have
become pivotal in modern science and technology. Initially produced
through melt spinning from carbon precursors, polyacrylonitrile (PAN)
was the primary precursor, and it has undergone various modications
like additive incorporation, low-temperature oxidation stabilization,
and stretching during stabilization and carbonization. Vapor grown
carbon bers (VGCFs) are crafted using a catalytic chemical vapor
deposition (CVD) process. Two principal methods for synthesizing CNFs
are Catalytic decomposition of carbon precursors and Carbonization and
electrospinning of polymers. The choice of method depends on the
desired properties of the synthetic CNFs. CNFs synthesized via CVD
involve decomposing carbon-containing gases like acetylene, ethylene,
methane, and propylene, catalyzed by metal particles. CNFs’ surface
area can increase signicantly, from 300 to 400 to 1700 m2/g, when
activated with dissolved KOH, as shown in Fig. 7 [72]. Functionalization
involves modifying the surface of CNFs to introduce specic chemical
groups that can enhance their interaction with biofuel precursors. This
process consists of the introduction of functional groups to the CNFs’
surface, improving their dispersibility, reactivity, and binding capacity.
Surface characterization is pivotal in understanding the unique structure
and chemistry of CNFs, which is achieved through various techniques
like scanning probe microscopy, infrared and electron spectroscopies,
and electron microscopy. Covalent functionalization, mainly through [2
+1] cycloaddition reactions, is another method that maintains the
graphitic structure’s integrity while allowing for the attachment of
diverse functional groups [73,74]. Stellwagen et al. [75] employed a
novel method to synthesize CNFs functionalized with aryl sulfonic acid
groups using diazonium coupling reactions. These CNFs, designated as
CNF-Ar-SO
3
H, exhibited a high afnity for reactant molecules at the aryl
sulfonic acid sites, achieving a loading of 0.62 mmol/g. Utilizing these
CNFs as a catalyst in transesterifying triolein, they achieved a 72 %
conversion to methyl oleate within four hours at 120 ◦C and a molar
ratio of 1:10, with a catalyst amount of 0.75 g. Remarkably, the catalyst
maintained its efcacy for up to four cycles of transesterication,
requiring only minimal treatment for reuse. Iron (Fe), cobalt (Co), and
nickel (Ni) are the most common catalysts for CNF growth, with chro-
mium (Cr), vanadium (V), and molybdenum (Mo) also being explored.
Table 3
Overview of several investigation methodologies involving Sulfonated Carbon
Nanotubes.
Reference Methodology Key Findings
Guan et al.
[62]
An efcient S-MWCNT was
synthesized, demonstrating a
Brunauer–Emmett–Teller (BET)
surface area of 198.9 m
2
/g with
pore diameters between 5 and 35
nm. The catalytic efciency was
further investigated by studying its
ability to transesterify trilaurin in
ethanol.
•Produced 97.8 % biodiesel
from triglycerides under
optimal reaction conditions
of 20:1 ethanol to trilaurin
mass ratio, 150 ◦C reaction
temperature, 3.7 wt%
catalyst loading, and one-
hour reaction duration.
Also, transesteried tri-
glycerides are more efcient
than hydrothermal
carbonization-synthesized
sulfonated carbon and metal
oxide catalyst WO
3
/ZrO
2
.
Shuit et al.
[64]
Exhibited the way to make S-
MWCNTs by thermally
decomposing ammonium sulfate
((NH
4
)
2
SO
4
) with ultrasonication.
Through the esterication of
PFAD with methanol, S-
MWCNTs showed 84.9 %
biodiesel output.
Shu et al.
[65]
Investigated MWCNT sulfonation
with a 210 ◦C concentration of
sulfuric acid.
Found that the S-MWCNT
catalyst had an acid site density
of 3.09 mmol/g and an average
pore size of 7.48 nm.
Shuit et al.
[66]
Examined various sulfonation
procedures on MWCNTs used to
esterify PFAD in biodiesel
synthesis.
•In situ polymerization of 4-
styrene sulfonate gave 93.4
% FAME (Fatty Acid Methyl
Ester) under the following
conditions: 20:1 methanol to
oil molar ratio, 2 wt% cata-
lyst loading, 170 ◦C reaction
temperature, and 3 h reac-
tion duration.).
85.8 % was obtained
through in situ polymeriza-
tion of acetic anhydride and
sulfuric acid, while 88.0 %
was obtained through ther-
mal breakdown of ammo-
nium sulfate.
Fan et al.
[67]
This study utilized transmission
electron microscopy (TEM), X-ray
powder diffraction (XRD), Fourier-
transform infrared spectroscopy
(FT-IR), and Confocal laser
scanning microscopy (CLSM) to
examine Burkholderia cepacia
lipase (BCL)-derived MWCNTs
supported by magnetic iron oxide
and polyamidoamine dendrimers
(PAMAM).
•Encapsulated lipase was
shown to be the most
effective catalyst for
biodiesel transesterication,
yielding 92.8 %.
This catalyst can be reused
up to 20 times and retains
90 % catalytic capacity.The
catalyst (BCL-mMWCNTs-
G3)
reduced the coagulation
limitation of carbon
nanotubes in magnetic iron
oxide.
Boshagh
et al.
[68]
To observe the catalytic
performance of functionalized
multi-walled carbon nanotubes
(MWCNT-COOH) during the
transesterication process of
biohydrogen production, FT-IR
and FESEM techniques were
employed.
•In comparison to a control,
MWCNT-COOH can boost
hydrogen production rate
(HPR) by 47 % and hydrogen
yield (HY) by 5 %.
It also exhibited a high
glucose degradation capa-
bility with an efciency of
96.20 % and good bio-
catalytic and stability
properties.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
9
Fig. 6. Processing graphite into sulfonated graphene. Adapted with permission [70].
Fig. 7. (a) Typical electron image of CNF obtained by a CVD method from acetylene on the Fe/C/SiO
2
catalyst. (b) An electron micrograph shows that CNF was
treated with melted KOH modied with a 2% weight of copper. (c) Curve 1 representing the XRD patterns of CNF, while curve 2 representing the XRD patterns of
CNF activated with melted KOH. Reproduced from Ref. [73] with permission from the Royal Society of Chemistry.
Fig. 8. (a) Schematic diagram of Carbon Dot (CD) preparation via “top-down” and “bottom-up” approaches and modication, including functionalization, doping
and nanohybrids. (b) Various methods of synthesis of CD. Reproduced from Ref. [73] with permission from the Royal Society of Chemistry.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
10
Compared to other carbon nanostructures like single-walled carbon
nanotubes (CNTs), CNFs offer a cost-effective advantage for mass pro-
duction, making them an economically favourable option in producing
biofuels [72].
3.1.6. Carbon dot (CD)
The synthesis of carbon dots (CDs) encompasses a variety of
methods, including hydrothermal/solvothermal, microwave, electro-
chemical, microplasma, and chemical oxidation. Each method imparts
distinct properties to the CDs. Broadly, these techniques fall into two
categories: “top-down” and “bottom-up” approaches, as depicted in
Fig. 8(a). The top-down approach involves fragmenting bulk carbona-
ceous materials into CDs through electrochemical synthesis, chemical
oxidation, and solvent heat treatment. Conversely, the bottom-up
approach constructs CDs from molecular precursors using hydrother-
mal treatment, microwave-assisted synthesis, thermal decomposition, or
carbonization, as illustrated in Fig. 8(b). Based on their structure,
properties, and synthesis methods, CDs are classied into carbon
quantum dots (CQDs), graphene quantum dots (GQDs), and carbonized
polymer dots (CPDs). The synthesis of carbon dots (CDs) can be opti-
mized by adjusting conditions such as time, temperature, and voltage.
Following synthesis, CDs are typically puried using methods like
centrifugation, dialysis, and ltration or more complex techniques such
as electrophoresis and chromatography. The hydrothermal/sol-
vothermal method is commonly used for CD synthesis, involving the
dissolution of raw materials in a solvent, heating in a Teon-lined
autoclave, and producing CDs with high yield and the potential for
element diversication [72]. In a study by Macina et al. [45], a novel
heterogeneous carbon dot catalyst was synthesized through glycine and
citric acid hydrothermal interaction. The catalytic potential of this
catalyst was then examined for the transesterication of canola oil to
generate biodiesel. The researchers attained a biodiesel conversion rate
of 97 % under the conditions of 150 ◦C and a catalyst loading of 1 %.
Furthermore, at least ve reaction cycles have demonstrated that this
nanocatalyst maintains its catalytic efcacy without deteriorating.
Although information is scarce on these nanocatalysts, previous
research suggests they have catalytic potential in the transesterication
of diverse feedstocks. Extensive investigation into these parameters is
required to determine how effective these nanocatalysts are as catalysts
for different feedstocks and reaction circumstances [76]. Su et al. syn-
thesized multifunctional CDs that can sense temperature, detect Ni(II),
and indicate doxycycline through uorescence changes. Meanwhile,
Zhang et al. employed electrochemical carbonization to convert alcohols
into CDs, observing increased size and graphitization with higher
applied potentials. This method showcases the versatility and adapt-
ability of CD synthesis techniques [72].
3.1.7. Carbon nanohorns
Carbon nanohorns (CNHs), also known as CNHs, are enclosed
structures composed of carbon atoms bound in a sp
2
conguration.
These nanohorns typically exhibit diameters ranging from 2 to 5 nm and
lengths between 40 and 50 nm. Due to their enclosed cage construction,
they are related to a class of fullerenes with a high aspect ratio. They can,
however, be extended by oxidation to disclose more of their surface
while providing access to their internal cavity. Because of their molec-
ular similarities, tiny single-walled carbon nanotubes serve as a struc-
tural analogue despite their elongated appearance. Nanohorns are
currently under investigation as prospective substitutes for nanotubes in
various applications, such as energy conversion, gas storage, medicine
delivery, and supercapacitors [77]. Unlike nanotube synthesis, nano-
horn production does not require metal catalysts and typically yields
high-purity samples with minimal byproducts like micrometric graphite
particles, fullerenes, and carbon onions. Current methods for synthe-
sizing carbon nanohorns involve energizing a carbon source, often
graphite, to the point of vaporization and restructuring, followed by
rapid cooling in an inert gas. The purity depends on the synthesis
method, and certain impurities can be reduced by preheating the carbon
source. Many applications do not necessitate further purication beyond
a possible thermal anneal. [77]. Synthesis processes are generally
categorized into three types concerning the methodology utilized to
infuse energy into the carbon, as depicted in Fig. 9.
CNHs were rst discovered in soot byproducts from arc-discharge
fullerene production. Heating can transform them into single-walled
and multiwalled nanohorns. Pulsed arc-discharge in atmospheric air
has been used to produce high-purity CNHs directly. Submerged arc-
discharge methods, including those in liquid nitrogen or argon, have
shown promise for large-scale production. An ‘arc in water’ method
using nitrogen gas has also been efcient for producing high-purity
CNHs. Laser ablation is another standard method for synthesizing car-
bon nanohorns (CNHs). This process involves the irradiation of pure
graphite with a high-powered laser in an inert atmosphere, such as
argon, without the need for a metal catalyst. It’s known for its high
production rate and yield, typically resulting in CNHs that form radial
aggregates. The size distribution and purity of the CNHs can be
controlled by adjusting the synthesis parameters, like temperature,
pressure, and laser power. This method is valued for producing CNHs
with high purity, which are helpful in various applications, including
biofuel production [78]. Induction heating is an alternative method for
producing carbon nanohorns, which involves generating high-frequency
eddy currents in graphite rods to create Joule heating. This process heats
the rods to over 3200 ◦C, forming a carbon plasma on the surface. The
resulting nanohorn soot, carried away by argon or helium gas, forms
dahlias or bud-like structures. This technique can produce approxi-
mately 0.1 kg of dahlias per hour and has the potential for signicant
scale-up. Although not explicitly stated, the purity of the product
Fig. 9. Methods for the synthesis of Carbon nanohorns.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
11
includes some graphene sheets and minimal amorphous carbon, with
less than 4 % organic residuals [77]. The chemical functionalization of
carbon nanohorns (CNHs) is crucial for enhancing their solubility and
ease of handling in solvents, similar to other carbon nanoforms like
CNTs and graphene. There are two primary methods for modifying
CNHs chemically −covalent attachment of organic groups to the CNH
structure, creating stable bonds and noncovalent assembly of functional
molecules via
π
-
π
interactions, electrostatic forces, or attaching inor-
ganic nanoparticles. Furthermore, covalent functionalization is catego-
rized into two groups – i) Oxidizing the tips of CNHs to add oxygen-
containing groups, particularly carboxylic acids, which facilitate sub-
sequent chemical modications and ii) Directly adding functional
groups to the CNH sidewalls for additional properties or reactivity.
These modications allow for better manipulation of CNHs in various
applications [77].
3.1.8. Other Carbon-Based nanocatalysts
Nanocatalysts that are supported, doped, impregnated, or blended
all fall within the realm of possibility as catalysts. Under ideal condi-
tions, they outperform conventional heterogeneous catalysts, leading to
higher conversion and yield. As a result, nanocomposites with a large
surface area compared to their volume and a wide pore dispersion may
be a viable choice for the industrial-scale production of biodiesel.
Table 4 depicts an overview of some of the notable research involving
carbon-based nanocatalysts and their key ndings.
3.2. Properties and unique characteristics of carbon-based nanomaterials
Carbon nanomaterials are gaining prominence for their exceptional
properties that greatly benet biofuel production. Their small size pro-
vides a vast surface area that enhances catalytic efciency and optimizes
chemical reactions. These materials’ distinctive structural and electronic
properties make them powerful catalysts, thus expediting the biofuel
production process. They are resilient against the demanding conditions
of biofuel synthesis, ensuring reliable and consistent performance. The
robustness of carbon nanomaterials also allows for their reuse, which is
both cost-effective and environmentally friendly. Additionally, they play
a crucial role in improving the kinetics of biofuel production, leading to
faster and more efcient processes. In some biofuel production methods,
carbon nanomaterials are essential for electron transfer. These charac-
teristics make carbon nanomaterials an essential research focus for
developing more effective and sustainable biofuel production
technologies.
3.2.1. Surface Area, pore Size, and acid site density
The efcacy of catalytic supports in biofuel production is intrinsi-
cally linked to their surface area, which is determined by the size and
concentration of pores [83]. Supports with a high density of ultrane
micropores exhibit extensive surface areas, enhancing the catalyst’s
accessibility to reactants. However, relying on micropores alone can
introduce mass transfer limitations in liquid-phase reactions. The pres-
ence of large molecules, such as triglycerides and long-chain fatty acids,
can be particularly problematic, as they may not easily penetrate the
micropores, leading to reduced catalytic efciency. With its larger sur-
face area compared to multi-walled carbon nanotubes (MWCNTs),
activated carbon presents a viable alternative for catalyst support. Yet,
its predominant microporosity could potentially hinder its effectiveness
in transesterication reactions involving large molecules. Therefore,
selecting a catalyst support that boasts an optimal pore size distribution,
coupled with a signicant surface area, is crucial for maximizing cata-
lytic performance and ensuring a streamlined biofuel production process
[61].
3.2.2. Superior catalyst stability
Enzyme immobilization on carbon-based nanomaterials is a crucial
strategy in biofuel production. These materials, including carbon
nanotubes (CNTs), fullerenes, graphene, and carbon nanobers, provide
a robust platform for enzymes, enhancing their stability and activity.
CNTs, with their tubular structure and high surface area, allow for a high
enzyme loading, signicantly improving reaction kinetics and bio-
catalytic efciency. Functionalizing CNTs with specic functional
groups on their surfaces will enable them to be tuned to be catalytically
active, distinguishing them from other conventional transesterication
catalysts created via precipitation or penetration. In liquid-phase re-
actions, active species can leak off the solid support because they are not
bound to the solid via covalent bonds. CNTs are an excellent option for
catalyst support in transesterication/esterication because they can be
chemically altered so that functional groups can establish covalent
bonds. Strong covalent bonds between the active species and the CNTs
prevent the active species from leaching into the reaction medium, even
at the high temperatures experienced during the reaction. There have
been reports of tests in which covalently modied CNTs were utilized
without leaching issues. CNTs provide excellent replacement catalyst
support for overcoming the experienced difculty with low stability
when employing traditional transesterication catalysts; due to covalent
bonding, the catalysts are provided with superior stability, mobility, and
specicity [61]. Fullerenes are spherical molecules that can create a
unique microenvironment for enzymes, potentially protecting them
from denaturation and extending their operational life. As a one-atom-
thick planar sheet of carbon atoms, graphene offers a large surface for
enzyme attachment, which can facilitate faster reaction rates. Carbon
Nanobers can be used to immobilize multiple enzymes, which is
Table 4
Overview of several investigation methodologies involving carbon-based other
nanocatalysts.
Reference Methodology Key Findings
Ballotin
et al.[79]
Oleic acid was esteried with
methanol using sulfonated
carbon nanostructures
embedded in a bio-oil-derived
amorphous carbon matrix.
These substances have sulfonic
surface groups, and their
acidity is relatively high (up to
0.2 mmol/g).
Findings showed that 95 % oleic
acid could be converted via
esterication at 100 ◦C, a 1:10 M
oleic acid to methanol ratio, and
2.5 wt% of catalyst loading.
Dehkhoda
et al.[80]
Two novel carbon-based
catalysts (called “biochar”)
were created via sulfonating
pyrolysis with concentrated
sulfuric acid and fuming
sulfuric acid. After producing
both catalysts, they tested them
by transesterifying vegetable
oils and by esterifying FFAs
(Free fatty acids), respectively.
A sulfonated catalyst with a high
sulfuric acid concentration had
high esterication and low
transesterication activity,
indicating that it successfully
converted the feedstock in FFA.
Janaun et al.
[81]
Provided step-by-step
instructions for preparing
sulfonated carbon catalyst by
partially carbonizing D-glucose
and then sulfonating the
product with concentrated
sulfuric acid.
Obtained a 52 % increase in oleic
acid conversion by employing a
catalyst composed of sulfonated
granulated sugar.
Fu et al.
[82]
Presented the successful
production of an inexpensive
and remarkably durable
sulfonated solid catalyst. This
catalyst exhibited a substantial
concentration of active sites
(4.25 mmol/g) and a surface
area of 1 m
2
/g. The synthesis
process involved the utilization
of microalgae residue through
in situ hydrothermal
carbonization with the aid of
sulfuric acid.
The catalyst exhibited
remarkable stability and
reusability, maintaining its
activity over six consecutive
reaction cycles without any
discernible loss.
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
12
benecial for cascade reactions often required in biofuel production
processes. The immobilization of these nanomaterials improves the en-
zymes’ performance by providing extra physical support and speeds up
the reaction, making the process more efcient and sustainable. Carbon
nitride-based nanomaterials are also highlighted for their sustainable
catalyst design, which can make biodiesel production more cost-
effective and environmentally friendly [84–86].
4. Applications of CNMs
4.1. Carbon-Based nanomaterials as catalysts for biodiesel conversion
Tremendous possibilities prevail for carbon nanomaterials to in-
crease the biofuel production rate by boosting reaction kinetics due to
reductions in material cost and processing time. Utilizing nanomaterials
would help the biofuel production procedure become more viable by
lowering expenses and improving environmental outcomes. Lipase
could be used in transesterication to reduce product contamination and
enhance glycerol recovery. Commercialization of lipase-catalyzed bio-
diesel synthesis is limited owing to the higher cost and decomposition of
enzyme byproducts and substrates. Considering methanol is an acyl
acceptor, the enzyme’s biocatalytic activity diminishes when it is pre-
sent. Immobilization of enzymes on nanocarriers and other porous
substances could be a valuable technique for tackling the issues above.
Lipase-like enzymes and support materials are vital in immobilizing
enzymes for biodiesel production. SWCNT aids in boosting enzyme ac-
tivity retention. MWCNT allows for improved resolution efciency and
stability. It also promotes increased enzymatic activity and thermal
stability [87,88]. It was found that nanocatalysts with an acidic nature,
high porosity, and a large surface area have superior catalytic activity.
Table 5 shows how carbon-based nanocatalysts boost biodiesel synthesis
[89].
Moreover, Sulfonated carbon-based catalysts (SCCs) are emerging as
a superior choice for biodiesel production due to their heterogeneous
acid nature. These catalysts are known for their high surface area,
elevated acid site density, and enhanced catalytic activity. They are
particularly effective in esterication and transesterication reactions,
which are crucial for converting biomass into biodiesel, as depicted in
Table 6 [69]. Using SCCs in biodiesel production offers improved cata-
lyst activity and operation stability and aligns with environmental sus-
tainability and economic affordability [94].
4.2. Carbon-Based nanomaterials for enhancing biogas production
An attractive approach to dealing with organic waste is anaerobic
digestion (AD), conserving the environment and producing biomethane
[29,101]. Nanoparticles (NPs) have been widely studied to improve this
process’s both quantitative and qualitative performance. Carbon-based
nanomaterials, such as carbon nanotubes and graphene, have emerged
as promising agents for enhancing biogas production through their
unique properties [102]. These nanomaterials offer increased surface
area, facilitating microbial attachment and biodegradation processes,
ultimately leading to higher biogas yields. Moreover, their exceptional
electron transfer properties and ability to immobilize enzymes further
optimize anaerobic digestion, promoting stable and efcient biogas
production. Additionally, carbon-based nanomaterials can mitigate
inhibitory compounds, stabilize pH levels, and create a favourable
microenvironment for methanogens, contributing to enhanced metha-
nation efciency. As ongoing research explores their potential impact
and scalability, these nanomaterials hold the key to sustainable and
renewable energy solutions through improved biogas production tech-
niques [103].
The utilization of single-wall carbon nanotubes (SWCNTs) has the
potential to enable direct interspecies electron transfer (DIET) in the
anaerobic digestion (AD) process. The study conducted by Zhang et el.
[102] observed that introducing SWCNTs resulted in an acceleration of
feedstock consumption and methane production rates when contrasted
with the control group. However, it is important to note that the
methane production yield remained constant at approximately 14 mL
after 180 h. Indeed, the process of DIET facilitates the direct exchange of
electrons among microorganisms, bypassing the need for formate or
hydrogen transfer [101]. Considering this, it is plausible that materials
possessing electrical conduction, such as single-walled carbon nano-
tubes (SWCNTs), have the potential to function as pathways connecting
electron-accepting and electron-donating microorganisms, specically
exoelectrogenic bacteria and methanogenic archaea, in the process of
DIET [104]. Interestingly, the promotion of methane production is more
efcient when conductive materials that allow DIET are present,
compared to the consumption of H
2
or alternative electron transport
mechanisms for intraspecies exchange, as demonstrated by Park et al.
[104].
Multi-wall carbon nanotubes (MWCNT) are an additional type of
electrically conductive material that has been found to have the possi-
bility of expanding biogas and methane production rates. This is ach-
ieved through the transfer of electrons towards methanogens, as
demonstrated in the study conducted by Ambuchi et al. in 2017. The
presence of CNTs has been widely documented. To signicantly enhance
the presence of electroactive bacteria, such as Caloramator sp. or Geo-
bacter sp., as well as other bacteria or methanogenic archaea, such as
Methanosarcina, Methanosaeta, and others [105]. Ash-based nano-
materials, derived from municipal solid waste incineration, have been
identied as effective carbon-based additives for biogas production.
Research by Lo et al. demonstrated that micro/nano y ash and bottom
ash could signicantly boost biogas yields over a 90-day anaerobic
digestion period at 35 ◦C. This enhancement is likely due to the
increased microbial habitat provided by the agglomerative properties of
these nanocompounds [106]. Conversely, Nyberg et al. (2008) found
that fullerene (C60) nanoparticles did not yield any benecial effects on
biogas production when applied long-term [107].
4.3. Carbon-Based nano-additives in Diesel/Biodiesel blends
CNTs have recently piqued the interest of scientists because of the
free-metal compounds they are composed of. Compared to metal-based
nanoparticles, carbon nanotubes possess enhanced thermal and chemi-
cal properties. CNTs increase the thermal characteristics of nanouids
by acting as a catalyst, increasing the cetane number and burning rate of
the fuel [108–110]. The tramp metal ions contained in fuels are
Table 5
Summary of the involvement of carbon-based nanocatalysts in increased bio-
diesel production.
Nanocatalyst
and
Catalyst
amount
(wt%)
Feedstock
Methanol
to oil
ratio
Reaction
Time (h)
and
reaction
temp.
(◦C)
Biodiesel
yield
(%)
References
Sulfonated
biochar and
activated
carbon (AC)
(2–8)
Vegetable
oil
6:1 6/55–60 97 Kastner
et al. [90]
s-MWCNT
(0.20)
Oleic acid 5.8:1 1.5/135 95.46 Zhang et al.
[91]
Na
2
O/CNT(3) Used
cooking oil
20:1 3/65 97 Ibrahim
et al. [44]
SiC-NaOH-GO
(5)
Rapeseed
oil oleic
acid
48:1 0.1/65 96 Loy et al.
[92]
KOH loaded
MWCNTs
(3.02)
Canola oil 13.56:1 3.34/60 94.23 Omraei
et al. [93]
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
13
successfully sequestered by carbon brils in CNTs, which can then be
removed. CNTs at higher concentrations in diesel, biodiesel, or
biodiesel-diesel blends improve BTE (Brake thermal efciency)
compared to ordinary diesel. Carbon nanotubes have potential as cata-
lysts due to their higher chemical reactivity and reactive surface area.
CNT addition improves BTE even in fuels based on a water-diesel
combination compared to ordinary diesel. Since the boiling point of
water is less than that of diesel, any CNT water in the blend will quickly
evaporate when the combustion heats up. Because CNT has a greater
surface area to volume ratio, it can readily combine with diesel and air,
and the micro-explosion principle causes these CNT water droplets to
erupt on the surrounding oil layers. When CNT-combined diesel is
compared to ordinary diesel, the former has a lower BSFC (Brake-spe-
cic fuel consumption) and drops even more as the CNT dose increases.
A prospective reason for this discovery is that CNT evaporates faster
than expected owing to its catalytic potential [111,112].
Furthermore, using CNT minimizes the ignition time for the CNT
blended fuel inside the combustion chamber, avoiding a buildup of
waste gas and consequent combustion during the premixed state.
Overall, BSFC values are heavily inuenced by the viscosity and caloric
content of the mixed fuel. CNTs, on the other hand, assist in reducing
BSFC in biodiesel/biodiesel-diesel blends by increasing combustion and
carbon oxidation. It has been discovered that CNT blended diesel has
higher in-cylinder pressure than regular diesel due to the enhanced
igniting characteristics of the carbon nanotubes. The maximal HRR of
fuels coupled with CNT increases with increasing carbon nanotube dose,
and the HRR of blended fuels is greater than that of standard diesel. Due
to its high surface area-to-volume ratio and improved thermal conduc-
tivity, CNT can achieve a higher maximum HRR [113].
CNT-blended fuel is claimed to emit less CO (Carbon monoxide) than
ordinary diesel, which can be related to the secondary atomizing
properties of the entrapped CNT droplets. As a result of higher surface
area to volume ratio, uniform dispersion and mixing are facilitated
[113]. Table 7 and Table 8 provide information on the many function-
alities of employing carbon nano-additives in manufacturing biodiesels
and their inuence on engine efciency.
Table 6
Overview of catalytic performance of Sulfonated Carbon-based catalyst for biodiesel production [94].
Sulfonated Carbon-based
catalyst
Alcohol Oil Oil: alcohol
ratio
Catalyst loading
[wt%]
t [h] T
[℃]
Conversion
[%]
Biodiesel yield
[%]
Reference
Esterication
Sulfonated carbon catalyst Methanol Waste cooking oil 1:20 10 1 60 87 −[95]
Ordered mesoporous carbons Methanol Oleic acid 1:10 0.5 16 160 96.25 Selectivity: 94 [96]
Single-walled carbon
nanohorns
Methanol Palmitic acid 1:33 3 5 64 −72 [97]
Activated carbon Methanol Palmitic acid 1:33 3 5 64 −28 [97]
Carbon black Methanol Palmitic acid 1:33 3 5 64 −55 [97]
Monolithic porous carbons Ethanol Oleic acid 1:10 −10 75 71.0 −[98]
Monolithic porous carbons Ethanol Acetic acid 1:10 −10 75 94.0 −[98]
Graphitic carbon nitride Methanol Oleic acid 1:5 10 4 27 99 −[99]
Transesterication
Graphene oxide Methanol Wet microalgae
cells
1:3 5 0.67 90 84.6 −[100]
Graphene Methanol Wet microalgae
cells
1:3 5 0.67 90 50 −[100]
Active Carbon Methanol Wet microalgae
cells
1:3 5 0.67 90 0 −[100]
Monolithic porous carbons Ethanol Sunower oil 1:20 − − 75 −63 [98]
Multiwalled carbon
nanotubes
Ethanol Trilaurin 1:20 3.7 1 150 97.8 −[62]
Graphene Methanol Palm oil 1:8 10 14 100 −98 [71]
Table 7
The primary function of carbon nano-additives in diesel/biodiesel blends.
Diesel combination Blended
percentage
Nanoparticle NP’s dosage
and size
Main effect Ref
Oenothera
Lamarckian
biodiesel
20 % GO 30–90 ppm Power and EGT (Exhaust gas temperature) increased, whereas CO and UHC (Unburned
hydrocarbon) emissions decreased. However, carbon dioxide and nitrogen oxide emissions
rose marginally.
[114]
Biodiesel– ethanol 30 % CeO
2
and
CNT
25–100 ppm A 22.2 % rise in CO emissions was accompanied by 7.2 % and 47.6 % decreases in HC and
smog emissions, respectively.
[115]
Jatropha-n-Butanol 50 % GNP-
MWCNT
50 ppm NOx, CO, and UHC were reduced by 45 %, 55 %, and 50 %, respectively. [116]
Lemon and orange
peel oil
20 % CNT, CeO
2
50–100 ppm Increased BTE and decreased BSFC with reduced CO
2
and hydrocarbon emissions. [117]
Dairy scum oil
methyl ester
50 % GO 23–27 nm Signicant improvements were made, with BSFC reduced by 8.34 %, BTE elevated by 11.56
%, unburned HC reduced by 21.68 %, and smoke reduced by 24.88 %.
[118]
Table 8
Carbon nano-additives and their effect on vehicle efciency.
Diesel
combination
Nanoparticle BTE BFSC Power Reference
Cooking oil CNTs +8.12 % −7.12 % +3.67
%
[114]
Waste cooking
oil
CNT and
silver
− − 7.08 % +2% [119]
Dairy scum oil
graphene
oxide
GO +11.56
%
−8.34 % −[118]
Ailanthus
altissima
GO − − 14.48
%
+14.3
%
[120]
Cooking oil MWCNT − − 4.5 % +7.81
%
[121]
Jatropha Methyl
Ester
GO +17 % −20 % −[122]
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
14
4.4. Photocatalytic hydrogen production using various CNMs
The process of generating hydrogen through the photocatalysis of
water has been extensively researched and is currently attracting sig-
nicant interest due to its environmentally benecial characteristics
[123]. Photocatalytic hydrogen evolution involves a complex and multi-
layered combination of chemical and physical processes. Photocatalytic
solar water splitting uses a redox reaction to separate water molecules
into oxygen (O
2
) and hydrogen (H
2
). Photocatalysis begins with an
event of photo adsorption. Semiconductors must contain an acceptable
band gap to utilize solar energy efciently. According to the Nernst
equation, the minimum energy required for the water-splitting process is
1.23 electron volts (eV). Semiconductors with a band gap of around 2
electron volts (eV) are considered suitable for enhancing photocatalysis
processes. Despite several semiconductors in this eld, only a few have
been found to be suitable options for practical application in photo-
catalytic hydrogen generation. To achieve maximum efciency, it is
crucial to tackle the inherent limitations of present semiconductor
technology, such as inadequate light absorption and increased recom-
bination rates. Contemporary studies emphasize the necessity of nding
a cost-effective substitute that improves the range of light absorption
and redox potential to maximize the efciency of the photocatalytic
process [124].
Carbon-based nanomaterials (CNMs) possess distinctive character-
istics that make them highly efcient catalysts in various applications.
The photocatalytic efcacy of these materials can be ascribed to their
large surface area, suitable morphology, and chemical and thermal
durability. CNMs can be utilized for a multitude of objectives. Cao and
Yu [125] have claimed that carbon materials have numerous applica-
tions, such as supporting materials, photocatalysts, or co-catalysts
(Fig. 10). Furthermore, they can enhance the absorption capacity, in-
crease the number of active sites, electron acceptors, and transporter
channels, accelerate photosensitization, and ensure the effectiveness of
band gap narrowing. Carbon-based semiconductors offer numerous
benets that enhance the efciency of photocatalysis. Additionally, it is
feasible to optimize the effectiveness of carbon-based materials by
modications. Several modication approaches have been successfully
employed, such as doping, surface functionalization, and interface en-
gineering. Carbon-based nanomaterials, including carbon nanotubes,
graphene oxide, graphene, fullerenes, and carbon quantum dots, have
demonstrated signicant efcacy in enhancing hydrogen generation.
The current objective is to improve hydrogen production by utilizing
carbon nanomaterials (CNMs) for a more ecologically sustainable result.
Considerable studies have focused on using carbon-based materials to
facilitate the widespread application of photocatalytic hydrogen pro-
duction. Much research has been conducted on creating hydrogen (H
2
)
using carbon-based nanomaterials (CNMs) to achieve cost efciency,
identify desired features, and reduce environmental impact. Table 9
presents a thorough overview of the rates at which distinct carbon-based
nanomaterials have achieved photocatalytic hydrogen generation
[124].
4.5. Carbon-Based nanomaterials for biofuels separation and purication
Separating the biodiesel from the glycerol is the primary step in
many renement stages that follow the transesterication technique.
Because of their different densities, biodiesel and its waste glycerol may
be easily distinguished. In general, this separation is accomplished
through decanting or centrifugation. Other processes that can result in
separation include gravity settling, purication, and deposition.
Fig. 10. Carbon materials’ functions in developing enhanced photocatalytic activity for hydrogen production.
Table 9
Rate of photocatalytic hydrogen production utilizing various nanomaterials
based on carbon.
CNMs Semiconductor
/Composite
Co-catalyst H
2
Production
Rate
Reference
CNTs CdS Pt (Pt-Af-
CNT/CdS)
120.1 mmol g
-
1
h
−1
[126]
g-C
3
N
4
CNCNT 1208 µmol g
-
1
h
−1
[127]
Graphene WO
3
Graphene 288/µmol g
-
1
h
−1
[128]
TiO
2
Graphene 100 mmol g
-
1
h
−1
[129]
CdS Pt 2310 µmol g
-
1
h
−1
[130]
Graphene
Oxide
CdS Ni 8866 µmol g
-
1
h
−1
[131]
Carbon
Quantum
Dots
TiO
2
Pt 472 µmol g
-
1
h
−1
[132]
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
15
Following the elimination of glycerol, biodiesel undergoes additional
processing to eliminate contaminants such as tri-, di-, and mono-
glycerides, catalysts, soap, and alcohol residues. Biodiesel is typically
puried by ash evaporation or vacuum distillation to eliminate
alcohol, followed by wet or dry washings to separate triglycerides,
catalysts, and soap. Different variations on the wet washing approach
include using only distilled water, rst washing with acids and then
water, and last washing with an organic solvent and then water [133].
Separation technologies more generalized for biodiesel purication
include equilibrium-based, afnity-based, membrane-based, solid-
–liquid, and reaction-based processes, as depicted in Fig. 11 [134].
Thermochemical processes like combustion, pyrolysis, and gasica-
tion convert biomass into fuels with higher energy content. One specic
process, pyrolysis, involves the distillation of biomaterials in an oxygen-
free environment, resulting in compounds like biochar and bio-oil. Bio-
oil, in particular, is a valuable product obtained from biomass pyrolysis
using materials like rice straw, pine wood, rice husk, corn cob, wheat
shell, mesquite sawdust, and jatropha seed shell. These materials can be
further rened and modied to create high-value products such as
biofuels. Advanced rening methods like extraction and fractionation
are used to separate different bio-materials and their constituent
chemicals in rening natural oils. These methods aim to create a sus-
tainable technique with maximum productivity for producing high-
value bio-based materials, like the biorenery based on palm oil mills.
Presently, a wide range of extraction techniques are being employed to
purify and separate biofuels [135]. Table 10 offers a glimpse into the
diverse methods and outlines the advantages and challenges associated
with each [135].
4.6. Carbon-based micro and nanomaterials for enzymatic
immobilization
Enzyme immobilization increases the enzyme’s resistance to heat,
severe conditions, and chemicals and its ease of recovery from the re-
action mixture, making it more practical to utilize in continuous oper-
ations. Immobilizing the enzyme can typically enhance its heat stability
by maintaining its intact tertiary structure and active site. Cellulases
have extensive global usage, and their potential in biofuel production is
crucial due to the growing demand and production of biofuels. Enzyme
adsorption onto the biomass substrate is necessary for the enzymatic
hydrolysis process, wherein cellulase facilitates the breakdown of cel-
lulose. Once the enzyme moves from the liquid to the solid biomass
particles, the enzyme molecules will attach to the active sites on the
biomass particles sequentially [139,140].
Carbon nanotubes are the most often utilized carbon-based nano-
structures. Carbon nanotubes (CNTs) are well-suited for immobilizing
enzymes, particularly in biofuel synthesis, because of their improved
electrical characteristics. In the context of enzyme immobilization on
Fig. 11. Purication methods for biodiesel, categorized by their respective techniques. Adapted with permission [1 3 5].
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
16
carbon nanotubes (CNTs), noncovalent techniques are favoured over
covalent techniques due to their propensity to lessen enzyme denatur-
ation. Two forms of carbon nanotubes can be used for enzyme immo-
bilization: single-wall carbon nanotubes and multi-wall carbon
nanotubes. MWCNTs are commonly chosen for cellulase immobilization
due to their multilayered graphite composition, which allows for easier
dispersal and cost-effectiveness. Furthermore, various chemicals in
carbon-based composite nanomaterials contribute to distinct factors
that facilitate the immobilization of the enzyme or increase its activity.
Most composite nanomaterials incorporate a magnetic nanoparticle
(MNP) due to its facilitation of enzyme recycling. An enzyme’s immo-
bilization often occurs in the outside layer of a composite nanomaterial.
In contrast, the inner layers serve various purposes, such as giving the
composite functional groups, improving stability, sensitivity to tem-
perature changes, etc. Table 11 describes the numerous types of cellu-
lases and their carbon-based micro and nano supports in biofuel
production [139].
Complex polysaccharides, including lignin, cellulose, and hemicel-
lulose, comprise most of the non-edible biomass utilized to produce
biofuels. Such lignocellulosic wastes are pre-treated using various
Table 10
Methods for biofuel extraction [135].
Technique Advantages Challenges References
Water Extraction ▪ Inexpensive solvent
Sustainable solvent
Effortlessness in executing the technique
▪ Enhanced water consumption
Depending on the raw material type, the water to oil ratio can
differ.
[136]
Atmospheric
distillation
▪ The current plants have been merged effectively.
Separation is a common practice in the orthodox oil/
gas process.
▪ Greater energy consumption
High temperature
Does not apply to biomolecules that are sensitive
[137]
Organic solvent
Extraction
▪ Comprehensive and essential information through
extensive research.
Relatively well-established technique on a commer-
cial scale
Relatively Inexpensive and economical
▪ Widespread application of toxic and hazardous solvents leading
to considerable environmental damage.
Additional complexities rising from multi-stage extraction
techniques
Considerable water wastage
[137]
Supercritical
uid Extraction
▪ Simplied methodology
Environmentally sustainable
Modifying the temperature and pressure conditions
allows for better control of the properties of a
supercritical uid.
▪ Unavailability of fundamental data
Not economical
Safety risks arising from high-pressure operations posing a
signicant threat to individuals and equipment.
[138]
Steam distillation ▪ Temperature conditions below atmospheric distillation
are mandatory.
Orthodox oil and gas processing commonly involves
the separation of different components.
Substantial expenditure. [137]
Vacuum distillation ▪ Temperature conditions below atmospheric distillation
are mandatory.
Operating under reduced pressure.
Suitable for biomolecules susceptible to elevated
temperatures.
▪ Exorbitant capital as well as equipment cost
Recovery of distillate is hindered by the rapid evaporation of
vapours from the product gas, resulting in decreased yield.
High vacuum
[137]
Adsorption ▪ Inexpensive adsorbent
Simplied methodology
Lack of attentiveness towards toxic pollutants
▪ Greater energy consumption
Lack of environmental sustainability
Accumulation of secondary waste
Challenges arise when attempting to enlarge the scale of a
process, such as the inverse correlation between owrate and
adsorption capability.
Nature of amplied complexity of the technique
[137]
Molecular
distillation
▪ Temperature conditions below atmospheric distillation
are mandatory.
Suitable for biomolecules susceptible to elevated
temperatures.
Enhanced rate of distillate recovery
▪ High vacuum
Exorbitant capital as well as equipment cost
[137]
Chromatography ▪ Sorting materials based on their category.
The separated material exhibits an exceptional level of
purity.
▪ Time-intensive technique
Usage is conned to only small-scale applications
[137]
Membrane ▪ Minimal energy consumption
Simplied methodology
Seamless scalability
No requirement for extra chemicals
▪ Membrane fouling
High cost
[137]
Electrosorption ▪ Minimal energy consumption
Reversible process
No requirement for extra chemicals
Usage is conned to only small-scale applications [137]
Ionic liquid
Extraction
▪ Greater efciency
Superior thermal stability
▪ High cost
Lack of literature on ionic liquids toxicity
[137]
Table 11
Immobilization of cellulases on carbon-based nanomaterials and composites for biofuel conversion [139].
Source of Cellulase Carbon-based nanomaterial Amount of Enzyme Immobilized Reusability References
T. reesei RUT C-30 Functionalized MWCNTs 26.61 U/mL 98 % [141]
Aspergillus niger Functionalized MWCNTs 85 % 75 % [142]
Aspergillus niger Activated carbon 90.2 % 70 % [143]
Aspergillus nidulansSU04 Modied activated carbon (MAC) 4.935 mg cellulase/mg MAC 70 % [144]
Commercial Fe
3
O
4
/GO/CS 90 % 80 % [145]
Trichoderma viride GO-Fe
3
O
4
- 4arm-PEG-NH
2
132 mg/g 45 % [146]
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
17
techniques, such as physical, chemical, physicochemical, biological, or a
mix of techniques, to produce biofuels. Subsequently, the polymeric
compounds derived from pre-treatment processes, such as cellulose and
hemicellulose, undergo enzymatic hydrolysis.
5. Circular economy of green synthesized carbon-based
nanomaterials
The use of nanomaterials presents a potential risk of contamination
and exacerbates environmental pollution. As an example, carbon
nanotubes (CNTs) worsen the process of environmental deterioration
and contribute to the phenomenon of global warming [146]. Additional
negative consequences of the production and implementation of nano-
particles in energy studies encompass intricate fabrication processes,
heightened energy requirements and usage, toxicity and environmental
pollution, inadequate disposal and recyclability, and low rates of
recovering used nanomaterials [147]. The effect of heavy metals in most
nanoparticles on human health and environmental pollution is inu-
enced by their disposal, management, and biodegradability. Prolonged
contact with carbon nanotubes (CNTs) may result in skin irritation,
while inhalation or inadvertent ingestion of nanoparticles can lead to
lung inammation, heart problems, and disruption of the digestive
system. The disposal of used nanomaterials has the capacity to pollute
the soil, surface, and subsurface water sources [34]. Extensive research
has been conducted on using biomass pyrolysis to produce eco-friendly
carbon nanomaterials, which can be used in biofuel and bioenergy
generation. This proposed approach effectively utilizes the thermal
waste and residual gases generated during biomass pyrolysis to syn-
thesize nanomaterials, enhancing this process’s economic and environ-
mental advantages. The resulting products exhibit exceptional
performance in energy storage and various eco-friendly applications
[147].
5.1. Production of Three-Dimensional graphene Bubbles (3DGBs)
The production of Three-Dimensional Graphene Bubbles (3DGB)
from biomass waste requires several procedures and the use of special-
ized equipment known as the “Atmospheric Pressure Chemical Vapour
Deposition (APCVD)-catalytic purication” method. The primary input
for 3DGB production is biomass waste, which includes lignin, cellulose,
wheat straw, sawdust, and other types of organic waste. Pre-treatment
processes, such as drying and size reduction, could render it more
accessible to process biomass waste later. The rapid pyrolysis reactor is
used to rapidly heat biomass waste at extreme temperatures, often 400
to 600 ◦C, under oxygen-depleted conditions, resulting in bio-oil, syn-
gas, and charcoal. Through biomass gasication, biomass is converted
into syngas, also known as synthesis gas, which contains carbon mon-
oxide (CO), hydrogen (H₂), and other contaminants. Catalytic purica-
tion, specically Atmospheric Pressure Chemical Vapour Deposition
(APCVD)-catalytic purication, is used to clean the syngas. The puried
syngas is directed into a CVD reactor, an APCVD reactor. The syngas
decomposes at high temperatures within the CVD reactor, forming
carbon atoms on a substrate. The substrate can serve as a catalyst or a
specialized material that aids in forming 3DGB structures. The Forma-
tion of 3DGB Carbon atoms accumulates on the substrate, forming
connected graphene sheets that evolve into a three-dimensional gra-
phene foam structure. These structures offer excellent catalytic support
in the production of biofuels [148].
5.2. Production of carbon nanotubes and nanobers through microwave
pyrolysis
Microwave Pyrolysis (MAP) rapidly releases a volatile substance,
forming a highly porous biochar with a high temperature [149,150].
This process also produces Carbon nanotubes (CNTs). The production of
CNTs is inuenced by factors such as microwave irradiation, hotspot
development, volatile matter composition, and inorganic materials. The
nucleation of CNTs begins at the hotspots in the biomass-derived char
during MAP. In the initial stage of MAP, biomass particles containing
volatile organic compounds are heated, causing the volatile materials to
be expelled from the core to the surface through the particle’s pores. The
squeezed volatile matter solidies on the particle’s surface due to the
temperature difference, forming hollow-shaped CNTs. Microwave-
mediated pyrolysis is one of the methods used to synthesize Carbon
nanobers (CNF), which is a catalyst-free process that yields efcient
results. Hollow carbon nanobers (HCNF) are produced in a shorter
reaction time during MAP, which can be further utilized in the pro-
duction of biofuels [151].
5.3. Production of carbon quantum dots (CQDs)
Apart from carbon, lignocellulosic waste also consists of nitrogen
(N), hydrogen (H), and oxygen (O). These elements are renewable but
also cost-effective and eco-friendly compared to other carbon sources.
The conversion of LCB waste into CQDs through synthesis helps trans-
form worthless biomass waste into valuable and practical commodities
[152]. Zhou et al. [89] were the rst to propose an environmentally
friendly synthesis method using watermelon peel as the carbon pre-
cursor, which initiated a new trend of utilizing biomass waste for CQD
production. Subsequently, researchers further explored the use of
diverse forms of agricultural, animal, fruit, and vegetable waste in this
process. CQDs are preferred over heavy-metal-based QDs for applica-
tions involving uorescence because of their low toxicity, excellent
biocompatibility, simple manufacturing, and great uorescence stability
[153].
6. Challenges and future directives
Carbon nanomaterials have several advantages, including superior
surface characteristics, minimal size, biocompatibility (mostly), ease of
synthesis, and evident usage in various industries. However, studying
nanoparticles’ possibly hazardous effects on living beings is currently in
the limelight. However, there is still cause for concern because the long-
term effects of widespread nanoparticle use or leakage into the envi-
ronment must be adequately examined. This has raised signicant
concerns about the benets and drawbacks of employing such tiny
particles, particularly in industrial contexts such as biofuel-biodiesel
synthesis. These opposing viewpoints and prospective consequences
present a once-in-a-lifetime chance for scientists worldwide to suggest
and analyze the long-term ramications of nanomaterials and strategies
to mitigate their potential downsides [154].
The use of biofuels may adversely impact the environment and so-
ciety. Some of the signicant repercussions include air pollution,
greenhouse gas emissions, deforestation, excessive water consumption
and pollution, loss of biodiversity, threats to food security, challenges in
rural development, instability in energy supply, social disputes, and
hazards to public health. One major drawback of biofuels is that they are
obtained from biomass, which is also used as a source of food for humans
[155]. This becomes an issue when there is inadequate food to support
everyone. Biofuels need substantial quantities of fertilizer, water, and
land area, leading to competition for land utilization and a poor net
energy ratio [156]. This process may also result in ecological degrada-
tion as a consequence of adverse impacts on biodiversity.
Biofuels provide a more cost-effective and viable alternative to fossil
fuels, which are becoming more costly. As a result, biofuels are being
seen as a feasible and economically efcient substitute [157,158]. The
manufacturing of biofuel necessitates the use of organic biomass derived
from agricultural waste, municipal trash, and other sources. Neverthe-
less, more studies are required to enhance biofuel output. Efcient pre-
treatment solutions that provide good value for money are needed to
strengthen the use of lignocellulosic biomass [159,160]. Algal biomass is
used to manufacture biodiesel due to its rapid growth, carbon neutrality,
N. Rodoshi Khan and A. Bin Rashid
Energy Conversion and Management: X 22 (2024) 100590
18
and high oil content. In the future, there is a potential for it to replace
fossil fuels in the manufacture of biodiesel ultimately. Cultivating algal
biomass is exceptionally costly due to the high energy demand for lipid
extraction [161].
Further research, in the context of the study, has the potential to
surpass the current constraints on biodiesel production greatly. Devel-
oping nanocatalysts with stable active sites that can perform many
functions during the trans-esterication reaction and have low leaching
effects and establishing a strategy for the industrial use of oils derived
from non-edible feedstocks. Lu et al. [162] investigated the efciency of
multi-functionalized carbon nanotubes combined with nitrate (NH
2
) and
carboxylic acid (COOH) in the transesterication of microalgal oil
(Chlorella), followed by hydrothermal liquefaction. The experiment was
conducted in a batch reactor with a 1:1 mass ratio of CNTs-NH
2
and CNTs-
COOH at 280 ◦C. Carbon nanotubes were discovered to play an essential
role in enhancing hydrogen output while lowering oxygen, sulphur, and
nitrogen levels. At 340 ◦C, the utilization of these CNTs created a steady
condition, resulting in a considerable proportion of hydrocarbon (47 %)
in bio-oil compared to the control (28 %). Also, carbonaceous and zeolite-
based catalysts are functionalized using nanomaterials and polymeric
materials to increase their effectiveness, specicity, and longevity. Opti-
mizing the rate of the chemical reactions required to make biodiesel by
structural modication depends on the size and form of nano-based ma-
terials. For instance, nanomaterials made of graphene and graphene oxide
have lately acquired favour for capturing microalgae biomass in a sus-
tainable manner. Graphene-based nanomaterials are lipophilic materials
with unique characteristics that have numerous applications in environ-
mental and biological sciences. Graphene-based nanomaterials are
benecial in various domains, including electrochemical sensors, elec-
troanalytical chemistry, and enzyme and biomolecule immobilization,
due to their unique physiochemical properties, including electrical, me-
chanical, optical, and thermal strength. An enzyme-based biofuel cell
creates electricity through electrochemical reactions involving biomass-
derived energy carriers such as ethanol, glucose, and oils. Elahi et al.
[118] studied the effects of adding graphene oxide nanoparticles to
various quantities of dairy scum oil biodiesel. Adding graphene oxide
nanoparticles to dairy scum oil biodiesel blends signicantly reduced CO
emissions (around 38.62 % for DSOME2040) and unburned hydrocarbons
(around 21.68 % for DSOME2040) while also increasing brake thermal
efciency (11.56 % for DSOME2040) and decreasing brake specic fuel
consumption (8.34 % for DSOME2040). Further improvement is crucial to
boost reaction throughput while minimizing mass transfer resistance,
energy expenditure, and waste. Increasing the possibility of sustaining
optimum reaction conditions and, as a result, maximizing biodiesel
output [163,164].
7. Conclusion
Even though the prospect for biofuels became apparent throughout
the twentieth century, the onset of the petroleum age was widely
recognized at the turn of the century. Other options for petroleum have
sparked much debate; they could aid in sustainability worldwide by
ensuring energy access and accomplishing GHG targets (at the same
time remaining protable and cost-competitive, if achievable) while not
affecting future cultures, economies, communities, and ecosystems.
Carbon NMs and their offspring are currently the centre of extensive
research. This is reinforced by the mountain of literature devoted to
exploring this intriguing area. The optical, mechanical, chemical, and
electrical properties they exhibit make them one of the most signicant
accessible and cannot be equalled by more commonplace materials. Yet,
substantial amounts of these elements still need to be produced for the
industry. However, the strong and consistent use of these materials
across different technologies has been hindered by the absence of uni-
formity in their structures and the irregularity of their production.
Numerous studies have shown that many rst-generation biofuels
are not as environmentally friendly as their petroleum-based
counterparts regarding greenhouse gas emissions and environmental
damage. However, it is essential not to let these challenges discourage us
from exploring the potential of biofuels and biomass consumption.
Instead, we should be motivated to nd more sustainable ways to
convert low-value and waste biomass into biofuels using reliable tech-
nologies and with a thorough understanding of their environmental
impacts. Future research should prioritize optimizing their qualities,
improving existing methods, and developing new synthesis approaches.
To fully benet from nanotechnology in biofuel research, it is crucial to
support interdisciplinary and collaborative investigations into cost-
effective and sustainable production techniques. Fuel industry stake-
holders must embrace research ndings to enhance the biofuel pro-
duction value chain. The outcomes of innovative studies on
nanotechnology applications, such as biofuel production and purica-
tion, development of efcient and affordable catalysts, etc., have the
potential to revolutionize biofuel research and production. Therefore,
emphasis should be placed on advancing research and development of
carbon NMs and related compounds across various industries. To opti-
mize biofuel production, it is imperative to deploy advanced technolo-
gies such as machine learning, articial intelligence, robotics, smart
metering, modelling and simulation software, numerical and mathe-
matical apparatuses, statistical techniques, and optimization tools.
These technologies can improve production parameters, reduce pro-
duction time, minimize material wastage, and advance biofuels pro-
duction. Given the increasing demand for sustainable energy solutions,
technologies like nanotechnology that accelerate biofuel production will
continue to receive attention from researchers and stakeholders.
Without a doubt, biofuels will remain positioned as critical contributors
to the renewable energy sector and vital sustainable energy solutions.
CRediT authorship contribution statement
Nazia Rodoshi Khan: Writing – original draft, Conceptualization.
Adib Bin Rashid: Writing – original draft, Supervision,
Conceptualization.
Declaration of competing interest
The authors declare that they have no known competing nancial
interests or personal relationships that could have appeared to inuence
the work reported in this paper.
Data availability
Data will be made available on request.
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