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Microalgae Oil Production: A Downstream Approach to Energy Requirements for the Minamisoma Pilot Plant

Author

Listed:
  • Dhani S. Wibawa

    (Graduate School of Life and Environmental Sciences, University of Tsukuba, Ibaraki 305-8572, Japan
    Surfactant and Bioenergy Research Center (SBRC), Bogor Agricultural University, Bogor 16143, Indonesia)

  • Muhammad A. Nasution

    (Graduate School of Life and Environmental Sciences, University of Tsukuba, Ibaraki 305-8572, Japan
    Indonesian Oil Palm Research Institute (IOPRI), Medan 20158, Indonesia)

  • Ryozo Noguchi

    (Faculty of Life and Environmental Sciences, University of Tsukuba, Ibaraki 305-8572, Japan)

  • Tofael Ahamed

    (Faculty of Life and Environmental Sciences, University of Tsukuba, Ibaraki 305-8572, Japan)

  • Mikihide Demura

    (Algae Biomass and Energy System R&D Center, University of Tsukuba, Ibaraki 305-8572, Japan)

  • Makoto M. Watanabe

    (Faculty of Life and Environmental Sciences, University of Tsukuba, Ibaraki 305-8572, Japan)

Abstract

This study investigates the potential of microalgae oil production as an alternative renewable energy source, in a pilot project located at Minamisoma City in the Fukushima Prefecture of Japan. The algal communities used in this research were the locally mixed species, which were mainly composed of Desmodesmus collected from the Minamisoma pilot project. The microalgae oil-production processes in Minamisoma consisted of three stages: cultivation, dewatering, and extraction. The estimated theoretical input-energy requirement for extracting oil was 137.25 MJ to process 50 m 3 of microalgae, which was divided into cultivation 15.40 MJ, centrifuge 13.39 MJ, drum filter 14.17 MJ, and hydrothermal liquefaction (HTL) 94.29 MJ. The energy profit ratio (EPR) was 1.41. The total energy requirement was highest in the HTL process (68%) followed by cultivation (11%) and the drum filter (10%). The EPR value increased along with the yield in the cultivation process. Using HTL, the microalgae biomass could be converted to bio-crude oil to increase the oil yield in the extraction process. Therefore, in the long run, the HTL process could help lower production costs, due to the lack of chemical additions, for extracting oil in the downstream estimation of the energy requirements for microalgae oil production.

Suggested Citation

  • Dhani S. Wibawa & Muhammad A. Nasution & Ryozo Noguchi & Tofael Ahamed & Mikihide Demura & Makoto M. Watanabe, 2018. "Microalgae Oil Production: A Downstream Approach to Energy Requirements for the Minamisoma Pilot Plant," Energies, MDPI, vol. 11(3), pages 1-16, February.
    • Handle: RePEc:gam:jeners:v:11:y:2018:i:3:p:521-:d:133940
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    References listed on IDEAS

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    Cited by:

    1. Catarina Viegas & Catarina Nobre & Ricardo Correia & Luísa Gouveia & Margarida Gonçalves, 2021. "Optimization of Biochar Production by Co-Torrefaction of Microalgae and Lignocellulosic Biomass Using Response Surface Methodology," Energies, MDPI, vol. 14(21), pages 1-23, November.
    2. Makoto M. Watanabe & Andreas Isdepsky, 2021. "Biocrude Oil Production by Integrating Microalgae Polyculture and Wastewater Treatment: Novel Proposal on the Use of Deep Water-Depth Polyculture of Mixotrophic Microalgae," Energies, MDPI, vol. 14(21), pages 1-29, October.
    3. Riaru Ishizaki & Agusta Samodra Putra & Sosaku Ichikawa & Tofael Ahamed & Makoto M. Watanabe & Ryozo Noguchi, 2020. "Microalgae Oil Production Using Wastewater in Japan—Introducing Operational Cost Function for Sustainable Management of WWTP," Energies, MDPI, vol. 13(20), pages 1-19, October.
    4. Riaru Ishizaki & Ryozo Noguchi & Agusta Samodra Putra & Sosaku Ichikawa & Tofael Ahamed & Makoto M Watanabe, 2020. "Reduction in Energy Requirement and CO 2 Emission for Microalgae Oil Production Using Wastewater," Energies, MDPI, vol. 13(7), pages 1-20, April.

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