Combined techno-economic and lifecycle analysis of renewable fuel production systems

2019 ◽  
Author(s):  
John Roles
Energies ◽  
2021 ◽  
Vol 14 (2) ◽  
pp. 295
Author(s):  
Mei Yin Ong ◽  
Saifuddin Nomanbhay ◽  
Fitranto Kusumo ◽  
Raja Mohamad Hafriz Raja Shahruzzaman ◽  
Abd Halim Shamsuddin

In this study, coconut oils have been transesterified with ethanol using microwave technology. The product obtained (biodiesel and FAEE) was then fractional distillated under vacuum to collect bio-kerosene or bio-jet fuel, which is a renewable fuel to operate a gas turbine engine. This process was modeled using RSM and ANN for optimization purposes. The developed models were proved to be reliable and accurate through different statistical tests and the results showed that ANN modeling was better than RSM. Based on the study, the optimum bio-jet fuel production yield of 74.45 wt% could be achieved with an ethanol–oil molar ratio of 9.25:1 under microwave irradiation with a power of 163.69 W for 12.66 min. This predicted value was obtained from the ANN model that has been optimized with ACO. Besides that, the sensitivity analysis indicated that microwave power offers a dominant impact on the results, followed by the reaction time and lastly ethanol–oil molar ratio. The properties of the bio-jet fuel obtained in this work was also measured and compared with American Society for Testing and Materials (ASTM) D1655 standard.


2021 ◽  
Author(s):  
Cherilyn Dignan

Canada, as one of the largest producers and consumers of fossil fuels per capita on the planet, is attempting to reduce greenhouse gas (GHG) emissions. In order to accomplish this, fuel alternatives, such as biofuel, are required. Accordingly, this study uses LCA methodology to quantify the GHG impact of a unique biofuel production model. This unique model produces biodiesel (BD), acetone, butanol and ethanol (ABE) from microalgae and assesses the process GHG impact against other microalgal BD production processes. This study’s microalgal BD and ABE production process produces 76 kgCO2e per functional unit, whereas other comparable microalgal BD production processes produce between 3.7 and 85 kgCO2e. Overall, this study clarifies that without the development of versatile infrastructure to accommodate biofuel production, LCA studies will continue to find renewable fuel production processes net GHG positive for the simple reason that fossil resources are still the primary energy source.


Fuel ◽  
2021 ◽  
pp. 122613
Author(s):  
Hao Xu ◽  
Yimeng Li ◽  
Zhaofei Li ◽  
Yang Song ◽  
Yanyan Zhang ◽  
...  

Fuel ◽  
2017 ◽  
Vol 200 ◽  
pp. 146-152 ◽  
Author(s):  
Hermawan Prajitno ◽  
Hassan Zeb ◽  
Jongkeun Park ◽  
Changkook Ryu ◽  
Jaehoon Kim

2019 ◽  
Vol 33 (2) ◽  
pp. 1659-1672 ◽  
Author(s):  
Andrea König ◽  
Kirsten Ulonska ◽  
Alexander Mitsos ◽  
Jörn Viell

2014 ◽  
Vol 16 (27) ◽  
pp. 14271-14280 ◽  
Author(s):  
William T. Gibbons ◽  
Luke J. Venstrom ◽  
Robert M. De Smith ◽  
Jane H. Davidson ◽  
Gregory S. Jackson

Zirconium-doped ceria (Ce1−xZrxO2) was synthesized through a controlled electrospinning process as a promising approach to cost-effective, sinter-resistant material structures for high-temperature, solar-driven thermochemical redox cycles.


Author(s):  
M. Gambini ◽  
M. Vellini

In this paper the overall performance of a H2/O2 cycle has been evaluated. This typology of power plants requires a material and energetic integration with hydrogen and oxygen production systems. The steam-methane reforming, for the hydrogen-rich fuel production, and the cryogenic air separation, for the oxidiser production, have been investigated, quantifying all their thermal and mechanical requirements. At first, the thermodynamic performance of this cycle has been evaluated, considering the presence of incondensable gases, owing to the processes that provide H2 from fossil fuels and O2 from air. Then, the power plant has been integrated with the oxidiser and fuel production plants as well as with the fuel compression section. Including all the material and energetic flows, the overall performance has been evaluated. The final result is not very encouraging: in fact, even if the H2/O2 cycle has relevant thermodynamic performance if the energetic requirements for oxygen and hydrogen productions are neglected — the efficiency is over 62% —, the overall performance of H2/O2 cycle power plants based on steammethane reforming is very low — the net efficiency attains only the 26%.


Sign in / Sign up

Export Citation Format

Share Document