Pyrolysis of engineered beach-cast seaweed: Performances and life cycle assessment

• Published in: Water research (Oxford) Vol. 222; p. 118875
• Main Authors: Wen, Yuming, Wang, Shule, Shi, Ziyi, Jin, Yanghao, Thomas, Jean-Baptiste, Azzi, Elias Sebastian, Franzén, Daniel, Gröndahl, Fredrik, Martin, Andrew, Tang, Chuchu, Mu, Wangzhong, Jönsson, Pär Göran, Yang, Weihong
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 15.08.2022
• Subjects: Beach-cast seaweed; Biochar; LCA; Negative emission; Pyrolysis; Negative emission; Pyrolysis; Beach-cast seaweed; LCA; Biochar
• ISSN: 0043-1354; 1879-2448; 1879-2448
• DOI: 10.1016/j.watres.2022.118875

•Comprehensive study on producing power or biofuel from beach-cast seaweeds.•TG, bench-scale experiments, process simulation and life cycle assessment are combined.•Pyrolysis activation energy of RS and WS was estimated to be 44.23 and 58.45 kJ/mol.•Three scenarios LCA study were conducted. The blooming of beach-cast seaweed has caused environmental degradation in some coastal regions. Therefore, a proper treating and utilizing method of beach-cast seaweed is demanded. This study investigated the potential of producing power or biofuel from pyrolysis of beach-cast seaweed and the effect of the ash-washing process. First, the raw and washed beach-cast seaweeds (RS and WS) were prepared. Thereafter, thermogravimetric analysis (TG), bench-scale pyrolysis experiment, process simulation, and life cycle assessment (LCA) were conducted. The TG results showed that the activation energies of thermal decomposition of the main organic contents of RS and WS were 44.23 and 58.45 kJ/mol, respectively. Three peak temperatures of 400, 500, and 600 °C were used in the bench-scale pyrolysis experiments of WS. The 600 °C case yielded the most desirable gas and liquid products. The bench-scale pyrolysis experiment of RS was conducted at 600 °C as well. Also, an LCA was conducted based on the simulation result of 600 °C pyrolysis of WS. The further process simulation and LCA results show that compare to producing liquid biofuel and syngas, a process designed for electricity production is most favored. It was estimated that treating 1 ton of dry WS can result in a negative cumulative energy demand of -2.98 GJ and carbon emissions of -790.89 kg CO2 equivalence. [Display omitted]