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  5. Techno-economic and environmental assessment of hydrothermal carbonization coupled with anaerobic digestion for sewage sludge and municipal solid waste co-treatment in Chile
 
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Techno-economic and environmental assessment of hydrothermal carbonization coupled with anaerobic digestion for sewage sludge and municipal solid waste co-treatment in Chile

ISSN
1873-2909
Fecha de emisión
2025-10-01
Autor(es)
Jhosané Pagés-Díaz
Universidad de Santiago de Chile 
César Huiliñir
Universidad de Los Andes
Junior Lorenzo-Llanes
Universidad Autónoma de Chile 
Lisbeth Mailin López Gónzalez
Universidad de Sancti Spíritus José Martí Pérez
Ernesto L. Barrera
Universidad de Sancti Spíritus José Martí Pérez
Editor(es)
Biomass and Bioenergy
Resumen
This work aimed to compare the stand-alone hydrothermal carbonization process (HTC) coupled with anaerobic digestion (AD) for the treatment of HTC-process water in terms of technical, economic, and environmental performance. Three scenarios were evaluated: (i) Stand-alone HTC, (ii) HTC integrated with AD (HTC + AD_1), and (iii) HTC integrated with an improved AD that uses hydrochar (HTC + AD_2). The industrial process was designed and modeled based on experimental data previously obtained for the co-treatment of the organic fraction of municipal solid waste and sewage sludge. The results show that net thermal energy (HTC = 53 kWh/traw material, HTC + AD_1 = 120 kWh/traw material, HTC + AD_2 = 84 kWh/traw material) and net electrical energy (HTC = 149 kWh/traw material, HTC + AD_1 = 187 kWh/traw material, HTC + AD_2 = 187 kWh/traw material) increased in the integrated scenarios by up to 126 % and 26 % respectively, compared to the stand-alone HTC due to extra energy from biogas. Nevertheless, the increase in methane production (58 vs. 153 NmLCH4/gVS) owing to the hydrochar addition did not supply the contribution of direct hydrochar combustion in power plants. Compared to the stand-alone HTC, the waste treatment cost with the cogeneration unit increased by 62 % due to the annexed AD plant. The total annualized cost ranges from 101 (HTC) to 127 (HTC + AD_1) USD/traw material, which is expected to decrease in all scenarios (up to 31 USD/traw material) by increasing the plant capacity (up to 100,000 t/year). The integrated configurations reduce the total environmental impact points (up to 85 %) compared to the stand-alone HTC due to the valorization of the HTC-process water and the replacement of coal fuel.
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