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Converting Vegetable Oils into Aviation Fuel using CO2 as a Reactant

   

Added on  2022-10-04

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Converting vegetable oils using co2 as a reactant into aviation fuel
European Bioenergy Research Institute (EBRI), Aston University, UK

Introduction

The
inexhaustible, clean, and absence of greenhouse gas emissions are properties that
renewable energy sources have over fossil fuels. Fossils are most applied worldwide but are

not sustainable since they emit CO2 gas in the atmosphere leading to accumulation of

greenhouse gases hence climate change. Renewable friendly sources of energy such as

biofuels that are friendly to the environment are needed to be produced and applied to

improve the health of environment and make it habitable to both human, plants and

animals. One way to be rid of the negative impacts these fossil energy sources have is by

electrification. Batteries charged by renewable energy sources such as wind, hydro, solar.

Charging by non
-renewable energy sources is also plausible option as the potential harmful
emissions will be away from the dense population areas. However, planes require a lot of

power, batteries are heavy and planes need to fly. Another line of reasoning is the economic

impact, the positive correlation between the fuel quantity and the operating costs of the

aircraft. Complete electric propulsion is still being proposed, nonetheless, a hybrid system

is an approach used today. The energy from the hydrocarbon fuel and power for the aircraft

systems from the batteries (Atkinsglobal.com, 2019).

Biofuels are known as the liquid fuel generated from the biomass of dissimilar forest

materials, agricultural materials and some biodegradable wastes (Yan, 2017). It is extracted

from the vegetable oil algae, bio butanol. Vegetable oil is an upcoming major source of

biofuel generation in the whole world since they have a close energetic content to

hydrocarbon fuels for transport, but the direct use is not acceptable mainly due to the

relatively low viscosity required by the engines (
Neuling and Kaltschmitt, 2017).
Transesterification is a chemical process that converts oil into esters in the presence of a

catalyst. This conversion to biodiesel helps to reduce the viscosity of the vegetable oil and

allows use without any modification to conventional engines. Almost 400 oil crops are

potential sources for diesel engines, but aircraft engines require more specific

characteristics as defined by ASTM D1655 in terms of energy density, viscosity, lower

heating value, boiling point.

Algae
are also an upcoming source of biofuel generation as they are known to be safe, non-
competitive and grow very fast, but they have a relatively low solid content and require

more pre
-treatment steps before oil extraction (SAIFUDDIN et al., 2016).
Therefore
, exploring methods for direct production of bio kerosene is necessary. One of
these is fisher
tropsch processes which involve high-temperature gasification of biomass to
produce a syngas which is later converted catalytically to hydrocarbons. The HEFA process

is another, it is more famous and already being
commercialized. However, with the
discovery of solutions and solving problems being the sole aim of science and engineering,

there goal of this research will be to find a way to make this process more efficient (Biofuels

International, 2019
).
Methodology

This proposed research will focus mainly on the hydrothermal conversion of vegetable oils

using into aviation fuel . The yield and quality of product depend on the process conditions

and feedstock. The application of heated water works as a form of catalyst,
minimising the
formation of gaseous products from degraded oil because of the lower temperature used

relative to conventional methods. The procedure is carried out in four stages :
i) Hydrolysis
ii) Decarboxylation iii) Cracking iv) Hydrogenation.

Hydrolysis reactions can be performed using heat (thermally) as liquid
-liquid reactions or as
gas
-liquid reactions utilizing superheated steam. Another method involves the use of
lipolytic
enzymes at room temperature. Biofuel can be produced via two routes beginning
with vegetable oils or fats. In the first process, the reaction occurs in two stages. The

vegetable oil/fat is first converted into fatty acids through hydrolysis and then the fatty acid

is converted to the fuel via esterification. The second method which is the conventional

method involves transesterification of vegetable oils into biofuel in the presence of alkali
-
based catalysts (
Demirbas 2008).
Next, decarboxylation. The thermal decarboxylation of fatty acids at moderate temperatures

less than 400 degrees Celsius produces a low yield of hydrocarbons which then means it is

necessary to use a catalyst. Hydrothermal decarboxylation of fatty acids at moderate

temperatures (less than 400
°C ) gives low yields if no catalyst is used (Heimann,
Karthikeyan
, & Muthu 2016). This indicates that a catalyst is necessary to drive the reaction
and to boost the yield. Commonly used catalysts are metals such as platinum Pt, nickel Ni

and palladium
Pd (Demirbas 2008).
Following this, the large hydrocarbon molecule is broken down into smaller molecules. In

hydrothermal cracking, high temperatures as high as 750
°C are used (Boyadjian & Lefferts
2018). The pressure used is also very high (in the range of 70
atm) (Boyadjian & Lefferts
2018). It is a combined process of both thermal and catalytic cracking. The major steps in

hydrothermal cracking include:

i
) Thermal reactions break down the carbon-carbon (C-C) bonds of the alkane into free
reactive radicals.

ii) This is followed by the dissociation of the free radicals.

iii) The free radicals are then converted into hydrocarbon molecules through catalytic

hydrogenation.

The two reactions (thermal and catalytic) occur in parallel and the thermal reaction

dominates at higher reaction temperature range.

Finally, in order to meet the Jet A1 specification, the double bonds in the alkenes must be

saturated (
Demirbas 2008). The overall effect of the addition of hydrogen is the elimination
of the double bond in the alkene. Despite the fact that the reaction is exothermic, the

activation energy is quite high and the reaction cannot take place under normal conditions.

Therefore, a catalyst is normally used to lower the activation energy and to speed up the

reaction. A commonly used catalyst is
aluminium (iii) oxide Al_2 O_3.
Conclusion

This processes of generating biofuel is greener, simpler and cost
-effective hence more
sustainable. More innovations should be done on how to use the vegetable oil, forest and

agricultural products and wastes to generate more clean and friendly energy to the

environment. Algae are most preferred since they are not edible and therefore will reduce

the competition of energy generation and food industry. Generation of biofuel maintain

clean, healthy and friendly environment, reduces the levels of diseases caused by burning

fossil fuels, and also ensure sustainability. Biofuel reduced the emission of greenhouse gases

into atmosphere hence reduces global warming and climate change, therefore it will try to

solve the environmental problems and at the same time meet the need of people in terms

of energy production.

References
Atkinsglobal.com. (2019). [online] Available at: https://www.atkinsglobal.com/~/media/Files/A/Atkins-Corporate/Electrification%20White%20Paper%20-%20digital.pdf [Accessed 23 Jul. 2019].
Attaphong
, C., Do, L. & Sabatini, D., 2012. Vegetable oil-based microemulsions using carboxylate-based extended surfactants and their potential as an alternative renewable biofuel. Fuel, Volume 94, pp. 606-613. https://www.sciencedirect.com/science/article/pii/S0016236111006661.
Chiaramonti
, D. et al., 2017. Oilseed pressing and vegetable oil properties and upgrading in decentralised small scale plants for biofuel production. International Journal of Oil, Gas and Coal Technology, Volume 14, p. 91. https://www.researchgate.net/publication/312013174_
Keera, S.,
Sabagh, s. & Taman, A., 2011. Transesterification of vegetable oil to biodiesel fuel using an alkaline catalyst. Fuel, Volume 90, pp. 42-47. https://www.sciencedirect.com/science/article/pii/S0016236110004059
Lapuerta
, M., Villajos, M., Agudelo, J. & Boehman, A., 2011. Key properties and blending strategies of hydrotreated vegetable oil as biofuel for diesel engines. Fuel Processing Technology, Volume 92, pp. 2406-2411. https://www.sciencedirect.com/science/article/pii/S0378382011003171
Neuling
, U. and Kaltschmitt, M. (2017). Biokerosene from Vegetable Oils Technologies and Processes. Biokerosene, pp.475-496.
Rathore
, V. & Badoni, R., 2016. Processing of vegetable oil for biofuel production through conventional and non-conventional routes. Energy for Sustainable Development, Volume 31, pp. 24-49. https://www.researchgate.net/publication/291423239
SAIFUDDIN, N., SITI FAZLILI, A., KUMARAN, P., PEI
-JUA, N. and PRIATHASHINI, P. (2016). The Production of Biodiesel and Bio-kerosene from Coconut Oil Using Microwave Assisted Reaction. IOP Conference Series: Earth and Environmental Science, 32, p.012039.
Taylor
, T., Winter, S. & Rice, S., 2017. Biofuel and commercial aviation. International Journal of Sustainable Aviation, Volume 2, p. 217. https://www.inderscience.com/jhome.php?jcode=ijsa
Yan, X., 2017. Bio
-inspired photosystem for green energy. Green Energy & Environment, Volume 2, p. 66. http://www.jgee.org/EN/abstract/abstract43.shtml
Yigezu
, Z. & Muthukumar, K., 2014. Catalytic cracking of vegetable oil with metal oxides for biofuel production. Energy Conversion and Management, Volume 84, pp. 326-333. https://www.researchgate.net/publication/262193816
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