Laura André , Joel Awinzure Agumah , Flavien Picard , Xiaojun Liu , Thomas Moreau , Alain Magis , Olivier Bernat , Nabil Mabrouk , Florian Routhier , Antoine Brunet , Patrick Billette , André Pauss , Thierry Ribeiro
{"title":"Thermophilic and mesophilic two-phase co-digestion of the organic fraction of municipal solid waste with sewage sludge and equine manure","authors":"Laura André , Joel Awinzure Agumah , Flavien Picard , Xiaojun Liu , Thomas Moreau , Alain Magis , Olivier Bernat , Nabil Mabrouk , Florian Routhier , Antoine Brunet , Patrick Billette , André Pauss , Thierry Ribeiro","doi":"10.1016/j.biteb.2026.102614","DOIUrl":null,"url":null,"abstract":"<div><div>This study aimed to evaluate the feasibility of treating a unique mixture of substrates through two-phase anaerobic digestion at reduced retention times. Sewage sludge was co-digested with organic fraction of municipal solid waste and straw-rich equine manure in 20 L laboratory-scale anaerobic digesters operated under thermophilic and mesophilic conditions. Despite short hydraulic retention times (HRT) of 2 d in the thermophilic reactor followed by 12 or 15 d in the mesophilic reactor, no apparent process inhibition was observed. The system operated under high organic loading rates in the mesophilic phase (6.7 and 5.3 g<sub>VS</sub>·L<sup>−1</sup>·d<sup>−1</sup>). Under these conditions, methane yields of approximately 235–245 NL<sub>CH₄</sub>·kg<sub>VS</sub><sup>−1</sup> were achieved, corresponding to nearly 80% of the biochemical methane potential of the co-digested substrate (301 NL<sub>CH₄</sub>·kg <sub>VS</sub><sup>−1</sup>). The methanogenic reactor also showed good resilience, with gas production improving over the course of the experiment, with the volumetric methane production rate reaching 1.60 NL<sub>CH₄</sub>·L<sup>−1</sup> reactor d<sup>−1</sup> at an HRT of 12 days and 1.27 NL<sub>CH₄</sub>·L<sup>−1</sup> reactor·d<sup>−1</sup>) at 15 days. The addition of strawed equine manure improved the C/N ratio and avoided potential inhibition by ammonia, reducing ammoniacal nitrogen concentrations from 4.7 g·L<sup>−1</sup> to 2.6 g·L<sup>−1</sup>. The laboratory results indicated a strong potential for scale-up, because the system exhibited consistent performance and adaptability. These results were subsequently used in the design of a pilot plant processing 2–3 t·d<sup>−1</sup>, which is currently operational.</div></div>","PeriodicalId":8947,"journal":{"name":"Bioresource Technology Reports","volume":"34 ","pages":"Article 102614"},"PeriodicalIF":0.0000,"publicationDate":"2026-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Bioresource Technology Reports","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2589014X26000721","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"2026/2/3 0:00:00","PubModel":"Epub","JCR":"Q1","JCRName":"Environmental Science","Score":null,"Total":0}
引用次数: 0
Abstract
This study aimed to evaluate the feasibility of treating a unique mixture of substrates through two-phase anaerobic digestion at reduced retention times. Sewage sludge was co-digested with organic fraction of municipal solid waste and straw-rich equine manure in 20 L laboratory-scale anaerobic digesters operated under thermophilic and mesophilic conditions. Despite short hydraulic retention times (HRT) of 2 d in the thermophilic reactor followed by 12 or 15 d in the mesophilic reactor, no apparent process inhibition was observed. The system operated under high organic loading rates in the mesophilic phase (6.7 and 5.3 gVS·L−1·d−1). Under these conditions, methane yields of approximately 235–245 NLCH₄·kgVS−1 were achieved, corresponding to nearly 80% of the biochemical methane potential of the co-digested substrate (301 NLCH₄·kg VS−1). The methanogenic reactor also showed good resilience, with gas production improving over the course of the experiment, with the volumetric methane production rate reaching 1.60 NLCH₄·L−1 reactor d−1 at an HRT of 12 days and 1.27 NLCH₄·L−1 reactor·d−1) at 15 days. The addition of strawed equine manure improved the C/N ratio and avoided potential inhibition by ammonia, reducing ammoniacal nitrogen concentrations from 4.7 g·L−1 to 2.6 g·L−1. The laboratory results indicated a strong potential for scale-up, because the system exhibited consistent performance and adaptability. These results were subsequently used in the design of a pilot plant processing 2–3 t·d−1, which is currently operational.