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Critical reviews of hydrothermal gasification for poultry litter valorization: Process yield, economic viability, environmental sustainability and safety
Poultry litter can be converted into thermal or chemical energy which can assist in meeting the energy needs. The current study focuses on a critical review of the cause-and-effect analysis of hydrothermal gasification (HTG) process yield, safety, and economic analysis. HTG batch and continuous tech...
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Published in: | Journal of cleaner production 2023-08, Vol.415, p.137876, Article 137876 |
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Main Authors: | , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Poultry litter can be converted into thermal or chemical energy which can assist in meeting the energy needs. The current study focuses on a critical review of the cause-and-effect analysis of hydrothermal gasification (HTG) process yield, safety, and economic analysis. HTG batch and continuous technologies have been investigated, each with its own set of constraints. For example, resident time in a continuous reactor ranges from a few seconds to minutes, whereas it ranges from several min to hours in a batch reactor. Process parameters temperature, pressure, resident time, and solid content also contribute to the syngas quality, but temperature has the most significant effect among all. Syngas quality can be improved by managing process parameters such as 500–550 °C, 25–28 MPa, 120–150 min resident time, and 10–20% of the solid biomass content. Catalyst application in HTG promotes more hydrogen production. HTG is environmentally sustainable as compared to direct land disposal of biomass. H2 production costs range from $ 1.94 to 7.0 per kg and an investment payback period of 3.3–5.16 years. Process safety approaches that are appropriate to conduct HTG safety analysis have been investigated, and some control measures have been proposed which can be applied to make the HTG process safer. Finally, HTG future perspective and recommendations have been given based on current work.
•Strengths and weaknesses of hydrothermal gasification process are summarized.•HTG optimum operating conditions are 500–550 °C, 25–28 MPa, 120–150 min, and 10–20% solid content.•Future perspective and recommendations are proposed for hydrothermal gasification process.•The safety and control measures of hydrothermal gasification process are analyzed.•Economic and environmental performances of hydrothermal gasification process are reviewed. |
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ISSN: | 0959-6526 1879-1786 |
DOI: | 10.1016/j.jclepro.2023.137876 |