Anaerobic digestion of organic fraction from municipal solid waste with methano production as objective: acidification phase control with no chemicals

Urban solid waste (USW) contains a significant proportion of organic matter, represented by the Organic Fraction of Municipal Solid Waste (OFMSW), quantified as Volatile Solids/Total Solids (VS/TS). This organic fraction can be leveraged for energy production. This study proposes an innovative approach to controlling the FOS/TAC ratio (FOS: Volatile Organic Acids (VOAs, C2-C6); TAC: Total Alkaline Carbonate) in anaerobic digestion using a Continuously Stirred Tank Reactor (CSTR). Instead of adding external alkalizing agents, the method relies on feed interruptions to promote self-recovery of buffering compounds. The process was analyzed by correlating the FOS/TAC ratio, volatile organic acids (VOA) levels, and biogas and methane production. Experiments utilized organic loading rates (OLR) of 0.5, 1.0, and 1.5 g VS L<sup>-1</sup> d<sup>-1</sup>, with the latter yielding a VS removal efficiency of 68-91%, methane content of 50-75%, and acid accumulation. The FOS/TAC ratio ranged from 0.5 to 2.0, with acetic and propionic acid concentrations reaching 7,422 mg L<sup>-1</sup> and 4,596 mg L<sup>-1</sup>, respectively. The process was halted when biogas production stabilized at 0.06 L biogas L<sup>-1</sup> reactor d<sup>-1</sup>, with methane content at 50%. The results demonstrate that anaerobic digestion of OFMSW is a viable treatment strategy at OLRs up to 1.5 g VS L<sup>-1</sup> d<sup>-1</sup>, achieving efficient biogas production without the need for chemical additives.<b>HIGHLIGHTS</b>The alkalinity increased, represented by FOS/TAC ratio, was positivity influenced by methane gas concentration.Programmed stops were the key-tool used to get a no acidification reator during the experimental time.The OLR of 1.5 g SV Kg<sup>-1</sup> d<sup>-1</sup> was the limited the charge where the reator was capable to recovery of acidification started, only with the programmed stop.It was possible to remain in stable condition for the reactor for 52 days, with the FOS/TAC ratio in 0.6 and OLR in 1.5 g SV Kg<sup>-1</sup> d<sup>-1.</sup>

Authors

Institutions

Publication Details

Journal
Environmental Technology
Published
2025-02-06
DOI
https://doi.org/10.1080/09593330.2025.2456131
Citations
1
Primary Topic
Anaerobic Digestion and Biogas Production
Type
article
Field-Weighted Citation Impact
1.01

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Anaerobic digestion of organic fraction from municipal solid waste with methano production as objective: acidification phase control with no chemicals

Ana Cláudia Barana, Priscila Rosseto Camiloti, Tatiane Martins de Assis, Thiago Edwiges et al.
1 citations
Environmental Technology
Anaerobic Digestion and Biogas Production
1.01
article

Anaerobic digestion of organic fraction from municipal solid waste with methano production as objective: acidification phase control with no chemicals

Ana Cláudia Barana, Priscila Rosseto Camiloti, Tatiane Martins de Assis, Thiago Edwiges, João Victor Tischler Nizer, GABRIEL DAMASCENO FERREIRA CUNHA, Guilherme Araújo Vuitik
article en
1 citations

Abstract

Urban solid waste (USW) contains a significant proportion of organic matter, represented by the Organic Fraction of Municipal Solid Waste (OFMSW), quantified as Volatile Solids/Total Solids (VS/TS). This organic fraction can be leveraged for energy production. This study proposes an innovative approach to controlling the FOS/TAC ratio (FOS: Volatile Organic Acids (VOAs, C2-C6); TAC: Total Alkaline Carbonate) in anaerobic digestion using a Continuously Stirred Tank Reactor (CSTR). Instead of adding external alkalizing agents, the method relies on feed interruptions to promote self-recovery of buffering compounds. The process was analyzed by correlating the FOS/TAC ratio, volatile organic acids (VOA) levels, and biogas and methane production. Experiments utilized organic loading rates (OLR) of 0.5, 1.0, and 1.5 g VS L<sup>-1</sup> d<sup>-1</sup>, with the latter yielding a VS removal efficiency of 68-91%, methane content of 50-75%, and acid accumulation. The FOS/TAC ratio ranged from 0.5 to 2.0, with acetic and propionic acid concentrations reaching 7,422 mg L<sup>-1</sup> and 4,596 mg L<sup>-1</sup>, respectively. The process was halted when biogas production stabilized at 0.06 L biogas L<sup>-1</sup> reactor d<sup>-1</sup>, with methane content at 50%. The results demonstrate that anaerobic digestion of OFMSW is a viable treatment strategy at OLRs up to 1.5 g VS L<sup>-1</sup> d<sup>-1</sup>, achieving efficient biogas production without the need for chemical additives.<b>HIGHLIGHTS</b>The alkalinity increased, represented by FOS/TAC ratio, was positivity influenced by methane gas concentration.Programmed stops were the key-tool used to get a no acidification reator during the experimental time.The OLR of 1.5 g SV Kg<sup>-1</sup> d<sup>-1</sup> was the limited the charge where the reator was capable to recovery of acidification started, only with the programmed stop.It was possible to remain in stable condition for the reactor for 52 days, with the FOS/TAC ratio in 0.6 and OLR in 1.5 g SV Kg<sup>-1</sup> d<sup>-1.</sup>

Environmental TechnologyVol. 46(16)
Universidade Tecnológica Federal do Paraná (BR), Universidade Estadual de Ponta Grossa (BR)
Coordenação de Aperfeiçoamento de Pessoal de Nível Superior
Sustainable cities and communities
Openalex Percentile: Top 28%
Anaerobic Digestion and Biogas Production
1.01
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.