Article(id=1314922190953341433, tenantId=1146029695717560320, journalId=1234093305789726721, issueId=1314922077824578469, articleNumber=null, orderNo=null, doi=null, pmid=null, cstr=null, oa=null, hot=null, price=null, onlineType=0, articleFormat=0, articleType=null, articleTypeStr=null, receivedDate=1752508800000, receivedDateStr=2025-07-15, revisedDate=null, revisedDateStr=null, acceptedDate=null, acceptedDateStr=null, onlineDate=1791431480396, onlineDateStr=2026-10-08, pubDate=1771516800000, pubDateStr=2026-02-20, doiRegisterDate=null, doiRegisterDateStr=null, onlineIssueDate=1791431480396, onlineIssueDateStr=2026-10-08, onlineJustAcceptDate=null, onlineJustAcceptDateStr=null, onlineFirstDate=null, onlineFirstDateStr=null, sourceXml=null, magXml=null, createTime=1791431480396, creator=13701087609, updateTime=1791431480396, updator=13701087609, issue=Issue{id=1314922077824578469, tenantId=1146029695717560320, journalId=1234093305789726721, year='2026', volume='46', issue='2', pageStart='593', pageEnd='1184', issueExtLink='null', onlineDate='null', pubDate='1771516800000', pubDateStr='2026-02-20', beforeIssueId=null, nextIssueId=null, price=null, status=1, issueComplete=1, articleOrder=1, issueType=-1, specialIssue=null, createTime=1791431453424, creator='13701087609', updateTime=1791431520751, updator='13701087609', preIssue=null, nextIssue=null, articleTotal=null, ext={EN=IssueExt(id=1314922360277398376, tenantId=1146029695717560320, journalId=1234093305789726721, issueId=1314922077824578469, language=EN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=), CN=IssueExt(id=1314922360277398377, tenantId=1146029695717560320, journalId=1234093305789726721, issueId=1314922077824578469, language=CN, specialIssueTitle=, coverIllustrator=null, specialIssueEditor=, specialIssueAbout=)}, issueFiles=null, downloadFileDto=null}, startPage=698, endPage=706, ext={EN=ArticleExt(id=1314922191137890810, articleId=1314922190953341433, tenantId=1146029695717560320, journalId=1234093305789726721, language=EN, title=Influence of system configurations and feeding modes on methanogenic performance in high-load co-digestion, columnId=1234106386360103680, journalTitle=China Environmental Science, columnName=Water Pollution Control, runingTitle=null, highlight=null, articleAbstract=

To improve the stability and methane production efficiency of an anaerobic co-digestion system treating high-load food waste (FW) and waste activated sludge (WAS), a 300-mesh metal mesh dynamic membrane bioreactor (DMBR) and an anaerobic continuous stirred tank reactor (CSTR) were operated in parallel under a high organic loading rate (OLR of 22.8g COD/(L·d)). The long-term performance and microbial community characteristics were compared between continuous and intermittent feeding modes. Results showed that at the same OLR, the continuously fed DMBR achieved a higher methane production rate of (8.86±0.29) L/(L·d) and a methane yield of (407±13) mL/g COD, representing an improvement of approximately 12% over intermittent feeding modes and 22% over the intermittently fed CSTR. It also maintained more stable pH levels and exhibited superior degradation capacity, demonstrating enhanced resistance to organic loading shocks. The dynamic membrane effectively retained and enriched key functional microorganisms, including syntrophic bacteria (Treponema, Lutispora, Syntrophomonas) and hydrogenotrophic methanogens (Methanoculleus). Their relative abundances were significantly higher than those in the conventional CSTR, which considerably accelerated the conversion of organic substrates. However, continuous feeding resulted in a lower membrane flux of 0.0079L/(m2·h) and a more rapid increase in transmembrane pressure (TMP) at 0.98kPa/h. In contrast, intermittent feeding maintained a higher membrane flux of 0.025L/(m2·h), though with slightly lower gas production efficiency. Taking into account overall system performance, including methane yield and operational stability, the DMBR system operated with continuous feeding and intermittent discharge significantly enhances methane conversion efficiency and process stability in high-load FW and WAS co-digestion. This offers an effective intensification strategy for the efficient and stable operation of practical high-load anaerobic co-digestion systems.

, authors=Yong-Xin CUI1, Yi-Fan WU1, Zi-Yi WANG1, Jia-Yi LIU1, Xiao-chang WANG1, Yu-You LI2, Rong CHEN1, Bao-Shan XING1, 2, *, authorsList=Yong-Xin CUI, Yi-Fan WU, Zi-Yi WANG, Jia-Yi LIU, Xiao-chang WANG, Yu-You LI, Rong CHEN, Bao-Shan XING, authorCompany=null, correspAuthors=Bao-Shan XING, authorNote=null, correspAuthorsNote=null, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=null, magXml=null, pdfUrl=null, pdf=null, pdfFileSize=null, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=null, mapNumber=null, fund=null), CN=ArticleExt(id=1314922191360188923, articleId=1314922190953341433, tenantId=1146029695717560320, journalId=1234093305789726721, language=CN, title=系统构型和进料方式对高负荷共消化产甲烷效能的影响, columnId=1234106386565624579, journalTitle=中国环境科学, columnName=水污染与控制, runingTitle=null, highlight=null, articleAbstract=

为提升高负荷餐厨垃圾(FW)与剩余污泥(WAS)厌氧共消化系统的稳定性及其产甲烷效能,在高有机负荷(OLR为22.8g COD/(L·d))下,平行运行300目金属网动态膜生物反应器(DMBR)和厌氧完全混合式反应器(CSTR),比较了连续与非连续进料模式的长期性能与微生物群落特征.结果表明,在相同OLR下,连续进料DMBR实现了更高的甲烷产量(8.86±0.29)L/(L·d)和甲烷产率(407±13)mL/g COD),较非连续模式提升约12%,较非连续的CSTR提升了22%,并能维持更稳定的pH值及更好的降解能力,展现出更强的抗负荷冲击能力.动态膜对关键功能微生物如互营细菌(Treponema,Lutispora,Syntrophomonas)及氢营养型产甲烷古菌(Methanoculleus)的截留与富集,使其相对丰度显著高于传统CSTR,有效加速了有机底物转化.但连续进料模式也导致膜通量较低(0.0079L/(m2·h))且跨膜压差(TMP)增长较快(0.98kPa/h);相比之下,非连续进料虽在产气效能上稍逊,但能维持较高膜通量(0.025L/(m2·h)).综合权衡系统效能(甲烷产量和稳定性),高负荷FW与WAS共消化系统采用连续进料和间歇出料运行的DMBR系统,能显著提升共消化系统的甲烷转化效率与运行稳定性,为实际高负荷厌氧共消化系统的高效稳定运行提供有效的强化策略.

, authors=崔咏新1, 吴一凡1, 王紫怡1, 刘佳怡1, 王晓昌1, 李玉友2, 陈荣1, 邢保山1, 2, *, authorsList=崔咏新, 吴一凡, 王紫怡, 刘佳怡, 王晓昌, 李玉友, 陈荣, 邢保山, authorCompany=null, correspAuthors=邢保山, authorNote=

崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

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* 责任作者,副教授,
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崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

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崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

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系统构型和进料方式对高负荷共消化产甲烷效能的影响
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崔咏新 1 , 吴一凡 1 , 王紫怡 1 , 刘佳怡 1 , 王晓昌 1 , 李玉友 2 , 陈荣 1 , 邢保山 1, 2, *
中国环境科学 | 水污染与控制 2026,46(2): 698-706
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中国环境科学 |水污染与控制 2026 , 46 (2) : 698 -706
系统构型和进料方式对高负荷共消化产甲烷效能的影响
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崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

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崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

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崔咏新1 , 吴一凡1, 王紫怡1, 刘佳怡1, 王晓昌1, 李玉友2, 陈荣1, 邢保山1, 2, *
作者信息
  • 1.西安建筑科技大学环境与市政工程学院,西北水资源与环境生态教育部重点实验室,国家城市非传统水资源开发利用国际科技合作基地,陕西省污水处理与资源化工程技术研究中心,陕西省环境工程重点实验室,陕西 西安 710055
  • 2.日本东北大学土木与环境工程系,仙台 9809579
通讯作者:
* 责任作者,副教授,
作者简介:

崔咏新(2002-),女,河南洛阳人,西安建筑科技大学硕士研究生,主要从事废物资源化技术研究.共发表2篇论文..

Influence of system configurations and feeding modes on methanogenic performance in high-load co-digestion
Yong-Xin CUI1 , Yi-Fan WU1, Zi-Yi WANG1, Jia-Yi LIU1, Xiao-chang WANG1, Yu-You LI2, Rong CHEN1, Bao-Shan XING1, 2, *
Affiliations
  • 1.Northwest China Key Laboratory of Water Resource and Environment Ecology, Ministry of Education, International Science & Technology Cooperation Center for Urban Alternative Water Resources Development, Engineering Technology Research Center for Wastewater Treatment and Reuse, Shaanxi Province, Key Laboratory of Environmental Engineering, School of Environmental & Municipal Engineering, Xi'an University of Architecture and Technology, Xi'an 710055, China
  • 2.Department of Civil and Environmental Engineering, Tohoku University, Sendai 9809579, Japan
出版时间: 2026-02-20
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为提升高负荷餐厨垃圾(FW)与剩余污泥(WAS)厌氧共消化系统的稳定性及其产甲烷效能,在高有机负荷(OLR为22.8g COD/(L·d))下,平行运行300目金属网动态膜生物反应器(DMBR)和厌氧完全混合式反应器(CSTR),比较了连续与非连续进料模式的长期性能与微生物群落特征.结果表明,在相同OLR下,连续进料DMBR实现了更高的甲烷产量(8.86±0.29)L/(L·d)和甲烷产率(407±13)mL/g COD),较非连续模式提升约12%,较非连续的CSTR提升了22%,并能维持更稳定的pH值及更好的降解能力,展现出更强的抗负荷冲击能力.动态膜对关键功能微生物如互营细菌(Treponema,Lutispora,Syntrophomonas)及氢营养型产甲烷古菌(Methanoculleus)的截留与富集,使其相对丰度显著高于传统CSTR,有效加速了有机底物转化.但连续进料模式也导致膜通量较低(0.0079L/(m2·h))且跨膜压差(TMP)增长较快(0.98kPa/h);相比之下,非连续进料虽在产气效能上稍逊,但能维持较高膜通量(0.025L/(m2·h)).综合权衡系统效能(甲烷产量和稳定性),高负荷FW与WAS共消化系统采用连续进料和间歇出料运行的DMBR系统,能显著提升共消化系统的甲烷转化效率与运行稳定性,为实际高负荷厌氧共消化系统的高效稳定运行提供有效的强化策略.

动态膜生物反应器  /  厌氧共消化  /  高有机负荷  /  进料方式  /  完全混合式反应器

To improve the stability and methane production efficiency of an anaerobic co-digestion system treating high-load food waste (FW) and waste activated sludge (WAS), a 300-mesh metal mesh dynamic membrane bioreactor (DMBR) and an anaerobic continuous stirred tank reactor (CSTR) were operated in parallel under a high organic loading rate (OLR of 22.8g COD/(L·d)). The long-term performance and microbial community characteristics were compared between continuous and intermittent feeding modes. Results showed that at the same OLR, the continuously fed DMBR achieved a higher methane production rate of (8.86±0.29) L/(L·d) and a methane yield of (407±13) mL/g COD, representing an improvement of approximately 12% over intermittent feeding modes and 22% over the intermittently fed CSTR. It also maintained more stable pH levels and exhibited superior degradation capacity, demonstrating enhanced resistance to organic loading shocks. The dynamic membrane effectively retained and enriched key functional microorganisms, including syntrophic bacteria (Treponema, Lutispora, Syntrophomonas) and hydrogenotrophic methanogens (Methanoculleus). Their relative abundances were significantly higher than those in the conventional CSTR, which considerably accelerated the conversion of organic substrates. However, continuous feeding resulted in a lower membrane flux of 0.0079L/(m2·h) and a more rapid increase in transmembrane pressure (TMP) at 0.98kPa/h. In contrast, intermittent feeding maintained a higher membrane flux of 0.025L/(m2·h), though with slightly lower gas production efficiency. Taking into account overall system performance, including methane yield and operational stability, the DMBR system operated with continuous feeding and intermittent discharge significantly enhances methane conversion efficiency and process stability in high-load FW and WAS co-digestion. This offers an effective intensification strategy for the efficient and stable operation of practical high-load anaerobic co-digestion systems.

dynamic membrane bioreactor (DMBR)  /  anaerobic co-digestion  /  high organic loading  /  feeding mode  /  continuous stirred tank reactor (CSTR)
崔咏新, 吴一凡, 王紫怡, 刘佳怡, 王晓昌, 李玉友, 陈荣, 邢保山. 系统构型和进料方式对高负荷共消化产甲烷效能的影响. 中国环境科学, 2026 , 46 (2) : 698 -706 .
Yong-Xin CUI, Yi-Fan WU, Zi-Yi WANG, Jia-Yi LIU, Xiao-chang WANG, Yu-You LI, Rong CHEN, Bao-Shan XING. Influence of system configurations and feeding modes on methanogenic performance in high-load co-digestion[J]. China Environmental Science, 2026 , 46 (2) : 698 -706 .
  • 国家自然科学基金资助项目(52570176)
  • 日本学术振兴会海外特别研究员项目(P24088)
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  • 接收时间:2025-07-15
  • 首发时间:2026-10-08
  • 出版时间:2026-02-20
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  • 收稿日期:2025-07-15
基金
国家自然科学基金资助项目(52570176)
日本学术振兴会海外特别研究员项目(P24088)
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    1.西安建筑科技大学环境与市政工程学院,西北水资源与环境生态教育部重点实验室,国家城市非传统水资源开发利用国际科技合作基地,陕西省污水处理与资源化工程技术研究中心,陕西省环境工程重点实验室,陕西 西安 710055
    2.日本东北大学土木与环境工程系,仙台 9809579

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2种不同金属材料的力学参数
科
Family
属数
Number of
genus
种数
Number of
species
占总种数比例
Percentage of
total species (%)
属
Genus
种数
Number of
species
占总种数比例
Percentage of total
species (%)
鹅膏菌科Amanitaceae 2 11 5.26 鹅膏菌属 Amanita 10 4.78
小菇科 Mycenaceae 2 12 5.74 丝盖伞属 Inocybe 5 2.39
多孔菌科 Polyporaceae 8 14 6.70 蜡蘑属 Laccaria 5 2.39
红菇科 Russulaceae 3 23 11.00 小皮伞属 Marasmius 6 2.87
小菇属 Mycena 11 5.26
光柄菇属 Pluteus 5 2.39
红菇属 Russula 17 8.13
栓菌属 Trametes 5 2.39
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