Yuanyao Ye , Juefei Ye , Zhi Xu , Jianxiong Kang , Dongqi Liu , Yongzheng Ren , Huu Hao Ngo , Wenshan Guo , Shijing Huang , Wei Jiang
{"title":"乙醇对UASB反应器中硫酸盐还原和甲烷生成的影响","authors":"Yuanyao Ye , Juefei Ye , Zhi Xu , Jianxiong Kang , Dongqi Liu , Yongzheng Ren , Huu Hao Ngo , Wenshan Guo , Shijing Huang , Wei Jiang","doi":"10.1016/j.jwpe.2025.107754","DOIUrl":null,"url":null,"abstract":"<div><div>This study evaluated the performance of an anaerobic reactor at low carbon-to-sulfate ratios with various sulfate concentrations and carbon sources. The results indicated that ethanol addition enhanced both sulfate removal and methane production, achieving 80 % sulfate removal and over 40 % methane content in the biogas. When mixed ethanol with starch hydrolysate in a weight ratio of 1, the methane content increased to 55 %. However, using 100 % ethanol reduced COD removal to <20 % and inhibited biogas production. Further analysis showed that ethanol promoted sulfate removal as sulfide in the liquid phase and altered electron flow between sulfate reducing bacteria and methanogens, with methanogens predominantly capturing the electrons. The addition of ethanol also reduced extracellular polymeric substance levels, suggesting decreased microbial stress. The addition of ethanol selectively enriched <em>Desulfovibrio</em>-based incompletely oxidizing sulfate-reducing bacteria. These microbes efficiently metabolized ethanol into acetic acid, which served as both an electron donor for sulfate reducers and a substrate for methanogens. As a result, over 50 % of the electron flow was directed toward methane generation at a carbon-to‑sulfur (C/S) ratio of 2:1, significantly increasing the methane content in the biogas to 55 %.</div></div>","PeriodicalId":17528,"journal":{"name":"Journal of water process engineering","volume":"74 ","pages":"Article 107754"},"PeriodicalIF":6.3000,"publicationDate":"2025-04-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Influence of ethanol supplementation on sulfate reduction and methanogenesis in UASB reactors\",\"authors\":\"Yuanyao Ye , Juefei Ye , Zhi Xu , Jianxiong Kang , Dongqi Liu , Yongzheng Ren , Huu Hao Ngo , Wenshan Guo , Shijing Huang , Wei Jiang\",\"doi\":\"10.1016/j.jwpe.2025.107754\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This study evaluated the performance of an anaerobic reactor at low carbon-to-sulfate ratios with various sulfate concentrations and carbon sources. The results indicated that ethanol addition enhanced both sulfate removal and methane production, achieving 80 % sulfate removal and over 40 % methane content in the biogas. When mixed ethanol with starch hydrolysate in a weight ratio of 1, the methane content increased to 55 %. However, using 100 % ethanol reduced COD removal to <20 % and inhibited biogas production. Further analysis showed that ethanol promoted sulfate removal as sulfide in the liquid phase and altered electron flow between sulfate reducing bacteria and methanogens, with methanogens predominantly capturing the electrons. The addition of ethanol also reduced extracellular polymeric substance levels, suggesting decreased microbial stress. The addition of ethanol selectively enriched <em>Desulfovibrio</em>-based incompletely oxidizing sulfate-reducing bacteria. These microbes efficiently metabolized ethanol into acetic acid, which served as both an electron donor for sulfate reducers and a substrate for methanogens. As a result, over 50 % of the electron flow was directed toward methane generation at a carbon-to‑sulfur (C/S) ratio of 2:1, significantly increasing the methane content in the biogas to 55 %.</div></div>\",\"PeriodicalId\":17528,\"journal\":{\"name\":\"Journal of water process engineering\",\"volume\":\"74 \",\"pages\":\"Article 107754\"},\"PeriodicalIF\":6.3000,\"publicationDate\":\"2025-04-28\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Journal of water process engineering\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2214714425008268\",\"RegionNum\":2,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q1\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of water process engineering","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2214714425008268","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q1","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
Influence of ethanol supplementation on sulfate reduction and methanogenesis in UASB reactors
This study evaluated the performance of an anaerobic reactor at low carbon-to-sulfate ratios with various sulfate concentrations and carbon sources. The results indicated that ethanol addition enhanced both sulfate removal and methane production, achieving 80 % sulfate removal and over 40 % methane content in the biogas. When mixed ethanol with starch hydrolysate in a weight ratio of 1, the methane content increased to 55 %. However, using 100 % ethanol reduced COD removal to <20 % and inhibited biogas production. Further analysis showed that ethanol promoted sulfate removal as sulfide in the liquid phase and altered electron flow between sulfate reducing bacteria and methanogens, with methanogens predominantly capturing the electrons. The addition of ethanol also reduced extracellular polymeric substance levels, suggesting decreased microbial stress. The addition of ethanol selectively enriched Desulfovibrio-based incompletely oxidizing sulfate-reducing bacteria. These microbes efficiently metabolized ethanol into acetic acid, which served as both an electron donor for sulfate reducers and a substrate for methanogens. As a result, over 50 % of the electron flow was directed toward methane generation at a carbon-to‑sulfur (C/S) ratio of 2:1, significantly increasing the methane content in the biogas to 55 %.
期刊介绍:
The Journal of Water Process Engineering aims to publish refereed, high-quality research papers with significant novelty and impact in all areas of the engineering of water and wastewater processing . Papers on advanced and novel treatment processes and technologies are particularly welcome. The Journal considers papers in areas such as nanotechnology and biotechnology applications in water, novel oxidation and separation processes, membrane processes (except those for desalination) , catalytic processes for the removal of water contaminants, sustainable processes, water reuse and recycling, water use and wastewater minimization, integrated/hybrid technology, process modeling of water treatment and novel treatment processes. Submissions on the subject of adsorbents, including standard measurements of adsorption kinetics and equilibrium will only be considered if there is a genuine case for novelty and contribution, for example highly novel, sustainable adsorbents and their use: papers on activated carbon-type materials derived from natural matter, or surfactant-modified clays and related minerals, would not fulfil this criterion. The Journal particularly welcomes contributions involving environmentally, economically and socially sustainable technology for water treatment, including those which are energy-efficient, with minimal or no chemical consumption, and capable of water recycling and reuse that minimizes the direct disposal of wastewater to the aquatic environment. Papers that describe novel ideas for solving issues related to water quality and availability are also welcome, as are those that show the transfer of techniques from other disciplines. The Journal will consider papers dealing with processes for various water matrices including drinking water (except desalination), domestic, urban and industrial wastewaters, in addition to their residues. It is expected that the journal will be of particular relevance to chemical and process engineers working in the field. The Journal welcomes Full Text papers, Short Communications, State-of-the-Art Reviews and Letters to Editors and Case Studies