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San Francisco Sequencing Batch Reactor Temperature Phased Anaerobic Digestion: Efficient Adaptation to Class A Biosolids

机译:旧金山测序分批反应器温度分步厌氧消化:高效适应A类生物固体

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San Francisco Public Utilities Commission (SFPUC), in collaboration with CH2M HILL,evaluated and designed the conversion of its existing high-rate mesophilic anaerobic digestionprocess at OSP to a SBR TPAD process in order to produce Class A biosolids, per USEPA Title40 Code of Federal Regulations Part 503 (40 CFR 503) Alternative 1 - Time and Temperature.Approximately 30 percent of San Francisco’s biosolids are land applied in neighboring SolanoCounty during the dry season (April through October). Recently, Solano County revised Chapter25 of its County Code biosolids regulation to requires that a portion of a utility’s biosolids betreated to Class A standards, in order to allow the utility to continue to land apply Class Bbiosolids in the county after October 2012. Pursuant to these pending requirements, SFPUCdetermined the best near-term approach to meet Class A requirements during the dry seasonrequires a solution that avoids environmental permitting delays and minimizes capitalexpenditures, while expediting construction. SFPUC staff developed a temperature-phaseddigestion approach to convert the mesophilic anaerobic digestion system to SBR TPAD (Jolis,2009) without constructing additional digester volume.SBR TPAD is phased anaerobic digestion. Phase 1 will consist of three sequentially fed,thermophilic phase digesters (TPD) (Digesters 2, 3, and 4) at 131℉/55°C in fill/hold/draw modewith the hold digester allowing a minimum of 24 hours of reaction time at 131℉ withoutadditional digester feed, to provide sufficient destruction of pathogens as required by 40 CFR503. Phase 2 will consist of one mesophilic phase digester (MPD) (Digester 1 is designated andDigester 2 is designated back-up) at 100℉/38°C in flow-through mode receiving digested solidsfrom the TPD draw, which is transferred to biosolids dewatering.
机译:旧金山公用事业委员会(SFPUC)与CH2M HILL合作, 评估并设计了其现有的高速中温厌氧消化的转换 根据USEPA标题,在OSP上将工艺流程转换为SBR TPAD工艺,以生产A类生物固体 40联邦法规第503部分(40 CFR 503)替代1-时间和温度。 旧金山约30%的生物固体被用于邻近的Solano土地 干旱季节(4月至10月)的县城。最近,索拉诺县修订了该章 县法规《生物固体》中的25条规定,公用事业的部分生物固体应为 为了使公用事业能够继续降落而申请B级,则按照A级标准进行处理 2012年10月后,该县将产生生物固体。根据这些未决要求,SFPUC 确定了在旱季满足A类要求的最佳近期方法 需要一种避免环境许可延迟并最大程度减少资本的解决方案 支出,同时加快建设。 SFPUC工作人员制定了温度阶段 消化方法将中温厌氧消化系统转化为SBR TPAD(Jolis, 2009)。 SBR TPAD是分阶段厌氧消化。第1阶段将包括三个顺序喂入的食物, 在131hold / 55°C下以填充/保持/抽取模式进行的嗜热相消化器(TPD)(消化器2、3和4) 保持消化池在131°C的条件下最少可以进行24小时的反应,而无需 额外的消化器饲料,以充分破坏40 CFR所要求的病原体 503.第2阶段将由一个中温消化池(MPD)组成(第1阶段被指定为 消化器2在100℉/ 38°C下指定为备用(流通模式),可吸收消化的固体 从TPD抽水中提取,然后转移到生物固体脱水中。

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