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Biomass Gasification Process in Renewable Energy Systems

A special issue of Energies (ISSN 1996-1073). This special issue belongs to the section "A4: Bio-Energy".

Deadline for manuscript submissions: closed (20 December 2023) | Viewed by 10370

Special Issue Editors


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Guest Editor
Faculty of Engineering, University of Porto, 4200 Porto, Portugal
Interests: biomass gasification; gasification modeling; hydrogen
Special Issues, Collections and Topics in MDPI journals

E-Mail Website
Guest Editor
Faculty of Engineering, University of Porto, 4200 Porto, Portugal
Interests: thermal processes; energy conversion
Special Issues, Collections and Topics in MDPI journals
Institute of Science and Innovation in Mechanical and Industrial Engineering, 4200 Porto, Portugal
Interests: environment; circular economy; sustainability; waste-to-energy; life cycle assessment; life cycle cost; social LCA
Special Issues, Collections and Topics in MDPI journals

Special Issue Information

Dear Colleagues,

Environmental problems are forcing a rethinking of the world’s energy supply system. A fundamental shift toward greater reliance on biomass in the world’s energy system is plausible because major technological advances are ongoing that hold the promise of making the conversion of biomass into high-quality energy carriers such as electricity and gaseous or liquid fuels economically competitive with fossil fuels. Therefore, energy systems have become a paramount topic for both industry and researchers due to the interest in energy production from biomass with improved chemical and thermal efficiencies and more cost-effective systems. The market penetration of biomass-based power production systems should be analyzed from technical, political, and economical perspectives.

This Special Issue on “Biomass Gasification Process in Renewable Energy Systems” aims to publish novel advances on biomass gasification technologies for energy production from experimental and computational perspectives. Topics include but are not limited to:

  • Progress in biomass gasification technologies;
  • Biomass gasification combined heat and power systems;
  • Biomass integrated gasification combined cycle systems;
  • Grid integration of biomass gasification power systems;
  • Life-cycle cost analysis of biomass gasification systems.

Dr. Eliseu Monteiro
Dr. Abel Rouboa
Dr. Ana Ramos
Guest Editors

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Please visit the Instructions for Authors page before submitting a manuscript. The Article Processing Charge (APC) for publication in this open access journal is 2600 CHF (Swiss Francs). Submitted papers should be well formatted and use good English. Authors may use MDPI's English editing service prior to publication or during author revisions.

Keywords

  • progress in biomass gasification systems
  • biomass gasification modeling
  • biomass gasification integrated power systems
  • biomass gasification life cycle cost
  • grid integration of biomass gasification power systems

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Published Papers (4 papers)

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Research

13 pages, 1276 KiB  
Article
Residence Time Reduction in Anaerobic Reactors: Investigating the Economic Benefits of Magnetite-Induced Direct Interspecies Electron Transfer Mechanism
by Tae-Bong Kim, Jun-Hyeong Lee and Young-Man Yoon
Energies 2024, 17(2), 358; https://doi.org/10.3390/en17020358 - 10 Jan 2024
Viewed by 1034
Abstract
Existing research on direct interspecies electron transfer (DIET) has predominantly focused on the types and concentrations of conductive materials across diverse anaerobic digestion. However, insufficient understanding of the impact of residence time, a critical economic factor, prompted this investigation. Magnetite, a conductive material, [...] Read more.
Existing research on direct interspecies electron transfer (DIET) has predominantly focused on the types and concentrations of conductive materials across diverse anaerobic digestion. However, insufficient understanding of the impact of residence time, a critical economic factor, prompted this investigation. Magnetite, a conductive material, was introduced into the anaerobic digestion of food wastewater, leading to a significant increase in ultimate methane production (Bu) with 25 mM-Fe3O4 (p < 0.05). Despite a subsequent decline in methane production efficiency from 388.9% to 7.1% over the 15- to 65-day anaerobic digestion period, the initial impact of increased methane production due to magnetite addition was evident. Control’s maximum methane production rate (Rm) was 27.5 mL/day, reaching its highest point at 37.4 mL/day with 15 mM-Fe3O4, accompanied by a noteworthy 56.6% reduction in the attainment day of Rm (Rm-day), shortened to 8.2 days. Even with 100 mM-Fe3O4, while Bu showed no significant difference, Rm-day exhibited a substantial reduction of 22.8. Despite the lower overall anaerobic digestion efficiency under some magnetite input conditions, this study confirmed a substantial shortening of Rm-day, suggesting that the DIET mechanism induced by conductive materials such as magnetite could reduce the residence time in continuous-type anaerobic reactors, contributing to improved economic feasibility. Full article
(This article belongs to the Special Issue Biomass Gasification Process in Renewable Energy Systems)
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12 pages, 1922 KiB  
Article
Air-Blown Biomass Gasification Process Intensification for Green Hydrogen Production: Modeling and Simulation in Aspen Plus
by Bernardino Novais, Ana Ramos, Abel Rouboa and Eliseu Monteiro
Energies 2023, 16(23), 7829; https://doi.org/10.3390/en16237829 - 28 Nov 2023
Cited by 1 | Viewed by 2541
Abstract
Hydrogen produced sustainably has the potential to be an important energy source in the short term. Biomass gasification is one of the fastest-growing technologies to produce green hydrogen. In this work, an air-blown gasification model was developed in Aspen Plus®, integrating [...] Read more.
Hydrogen produced sustainably has the potential to be an important energy source in the short term. Biomass gasification is one of the fastest-growing technologies to produce green hydrogen. In this work, an air-blown gasification model was developed in Aspen Plus®, integrating a water–gas shift (WGS) reactor to study green hydrogen production. A sensitivity analysis was performed based on two approaches with the objective of optimizing the WGS reaction. The gasifier is optimized for carbon monoxide production (Case A) or hydrogen production (Case B). A CO2 recycling stream is approached as another intensification process. Results suggested that the Case B approach is more favorable for green hydrogen production, allowing for a 52.5% molar fraction. The introduction of CO2 as an additional gasifying agent showed a negative effect on the H2 molar fraction. A general conclusion can be drawn that the combination of a WGS reactor with an air-blown biomass gasification process allows for attaining 52.5% hydrogen content in syngas with lower steam flow rates than a pure steam gasification process. These results are relevant for the hydrogen economy because they represent reference data for further studies towards the implementation of biomass gasification projects for green hydrogen production. Full article
(This article belongs to the Special Issue Biomass Gasification Process in Renewable Energy Systems)
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14 pages, 8456 KiB  
Article
The Growth and Evolution of Biomass Soot in Partial Oxidation-Assisted Hot Gas Filtration
by Lin Tian, Zixuan Jin and Wenran Gao
Energies 2023, 16(10), 4233; https://doi.org/10.3390/en16104233 - 21 May 2023
Viewed by 1649
Abstract
At present, partial oxidation is applied in the filtration processes of biomass hot gas to aid in solving the blockage problems caused by tar and dust condensates. However, in the resulting high-temperature and oxygen-limited environment, the risk of tar polymerization forming soot is [...] Read more.
At present, partial oxidation is applied in the filtration processes of biomass hot gas to aid in solving the blockage problems caused by tar and dust condensates. However, in the resulting high-temperature and oxygen-limited environment, the risk of tar polymerization forming soot is created during the purification processes. Thus, this work established a hardware-in-the-loop simulation model using the Lagrangian method coupled with the chemical reactions on the particle surface. The model was then used to simulate the entire evolution process of soot, including its formation, growth, and interception. The simulation results confirmed that under partial oxidation conditions, the increase in tar’s conversion rate promotes the formation of soot. Further analysis indicated that the high-temperature field formed as a result of oxidation and the increase in the naphthalene/oxygen ratio are the main reasons for the soot formation. On the other hand, the growth process of soot was inhibited by partial oxidation, which is mainly reflected in the relatively smaller increasing magnitude of soot particle mass and the decrease in the soot formation rate. Although the formation and growth of biomass soot cannot be completely avoided, the growth process is beneficial to interception and the soot escape rate can be minimized by varying the premixed oxygen content. On this basis, the potential of the partial oxidation-assisted hot gas filtration method can be further investigated and analyzed. Full article
(This article belongs to the Special Issue Biomass Gasification Process in Renewable Energy Systems)
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14 pages, 4126 KiB  
Article
Development of a Biomass Gasification Process for the Coproduction of Methanol and Power from Red Sea Microalgae
by Abdulrahman A. Al-Rabiah, Jiyad N. Al-Dawsari, Abdelhamid M. Ajbar, Rayan K. Al Darwish and Omar Y. Abdelaziz
Energies 2022, 15(21), 7890; https://doi.org/10.3390/en15217890 - 24 Oct 2022
Cited by 3 | Viewed by 4167
Abstract
In this study, an algae biomass gasification process using a dual fluidized bed with combined power and methanol cogeneration was developed. The gasification process was modeled using Aspen Plus and validated using experimental data of two microalgae species (Nannochloropsis oculata and Dunaliella [...] Read more.
In this study, an algae biomass gasification process using a dual fluidized bed with combined power and methanol cogeneration was developed. The gasification process was modeled using Aspen Plus and validated using experimental data of two microalgae species (Nannochloropsis oculata and Dunaliella salina) commonly found on the western coast of Saudi Arabia. The impacts of different operating conditions, including the gasifier temperature, steam-to-biomass ratio, and algae-char split ratio, on the compositions of four main gases (CO, CO2, CH4, and H2) were investigated. The results of the parametric studies indicated that the gasification temperature has a significant effect on the composition of the synthesis gas, where 700–850 °C was the ideal operating range for gasification. Altering the ratio of biomass to steam showed a slightly smaller effect on the synthesis gas composition. The char split ratio should be kept below 75% to ensure an adequate heat supply to the process. The proposed process successfully converted 45.7% of the biomass feed to methanol at a production capacity of 290 metric tons per day. On the other hand, 38 MW of electricity capacity was generated in the combined power cycle. Full article
(This article belongs to the Special Issue Biomass Gasification Process in Renewable Energy Systems)
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