João Victor Tischler Nizer, Gabriel Scremin Correa da Cunha, Tatiane Martins de Assis, Priscila Rosseto Camiloti, Guilherme Araujo Vuitik, Thiago Edwiges, Ana Cláudia Barana
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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></p>","PeriodicalId":12009,"journal":{"name":"Environmental Technology","volume":" ","pages":"3120-3129"},"PeriodicalIF":2.2000,"publicationDate":"2025-06-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Anaerobic digestion of organic fraction from municipal solid waste with methano production as objective: acidification phase control with no chemicals.\",\"authors\":\"João Victor Tischler Nizer, Gabriel Scremin Correa da Cunha, Tatiane Martins de Assis, Priscila Rosseto Camiloti, Guilherme Araujo Vuitik, Thiago Edwiges, Ana Cláudia Barana\",\"doi\":\"10.1080/09593330.2025.2456131\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p><p>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). 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引用次数: 0
摘要
城市固体废物(USW)含有很大比例的有机物,以城市固体废物的有机组分(OFMSW)为代表,量化为挥发性固体/总固体(VS/TS)。这种有机成分可以用于能源生产。本研究提出了一种控制FOS/TAC比的创新方法(FOS:挥发性有机酸(VOAs, C2-C6);TAC:总碱性碳酸盐)厌氧消化使用连续搅拌槽反应器(CSTR)。该方法不需要添加外部碱化剂,而是依靠进料中断来促进缓冲化合物的自我恢复。通过将FOS/TAC比值、挥发性有机酸(VOA)水平、沼气和甲烷产量进行关联分析。实验采用有机负荷率(OLR)为0.5、1.0和1.5 g VS L-1 d-1,后者的VS去除率为68-91%,甲烷含量为50-75%,酸积累。FOS/TAC比值为0.5 ~ 2.0,乙酸和丙酸浓度分别达到7422 mg L-1和4596 mg L-1。当沼气产量稳定在0.06 L (L-1反应器d-1),甲烷含量为50%时,该过程停止。结果表明,在olr高达1.5 g VS L-1 d-1的情况下,厌氧消化OFMSW是一种可行的处理策略,无需化学添加剂即可实现高效的沼气生产。
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-1 d-1, 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-1 and 4,596 mg L-1, respectively. The process was halted when biogas production stabilized at 0.06 L biogas L-1 reactor d-1, 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-1 d-1, achieving efficient biogas production without the need for chemical additives.HIGHLIGHTSThe 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-1 d-1 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-1 d-1.
期刊介绍:
Environmental Technology is a leading journal for the rapid publication of science and technology papers on a wide range of topics in applied environmental studies, from environmental engineering to environmental biotechnology, the circular economy, municipal and industrial wastewater management, drinking-water treatment, air- and water-pollution control, solid-waste management, industrial hygiene and associated technologies.
Environmental Technology is intended to provide rapid publication of new developments in environmental technology. The journal has an international readership with a broad scientific base. Contributions will be accepted from scientists and engineers in industry, government and universities. Accepted manuscripts are generally published within four months.
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