{"title":"High rate, low F:M anaerobic treatment of medium strength waste streams using the static granular bed reactor for renewable energy production","authors":"T. Ellis, K. M. Evans","doi":"10.2495/978-1-78466-060-4/001","DOIUrl":null,"url":null,"abstract":"A new high rate, low food to microorganism (F:M) anaerobic treatment system has been developed for maximizing the conversion efficiency of organic matter to energy in the form of methane for medium strength (1–10 g COD L –1 ) waste streams. The system, termed the static granular bed reactor (SGBR), utilizes a downflow hydraulic regime through a dense bed of active anaerobic granules that can accommodate higher suspended solids concentrations than its counterpart, the upflow anaerobic sludge blanket (UASB) reactor which is susceptible to solids washout due to the high (up to 1 m h –1 ) upflow velocities. Theoretical considerations for the SGBR are presented with results from SGBR treatment of synthetic (non-fat dry milk and sucrose) and actual (pork slaughterhouse and landfill leachate) wastewaters documenting the high efficiency (consistently greater than 90% conversion of COD) and excellent effluent characteristics (typically less than 50 mg L –1 total suspended solids and BOD5). Transient hydraulic and organic loads have relatively little effect on the SGBR as evidenced by consistent performance during an instantaneous shift in the hydraulic residence time from 36 to 5 h. In addition, results from variable reactor seeding from 25 to 100% of bed volume showed relatively little dependence of granule bed mass on effluent characteristics. This finding confirms independent results showing that a large fraction of the granule bed is substrate limited and available as reserve biomass. These results help explain the excellent treatment performance and resiliency of the SGBR regardless of hydraulic and organic loading. Fatty acid methyl ester (FAME) analysis of the granules showed distinct microbial","PeriodicalId":336954,"journal":{"name":"WIT Transactions on State-of-the-art in Science and Engineering","volume":"62 1","pages":"0"},"PeriodicalIF":0.0000,"publicationDate":"2014-12-30","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"WIT Transactions on State-of-the-art in Science and Engineering","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.2495/978-1-78466-060-4/001","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0
Abstract
A new high rate, low food to microorganism (F:M) anaerobic treatment system has been developed for maximizing the conversion efficiency of organic matter to energy in the form of methane for medium strength (1–10 g COD L –1 ) waste streams. The system, termed the static granular bed reactor (SGBR), utilizes a downflow hydraulic regime through a dense bed of active anaerobic granules that can accommodate higher suspended solids concentrations than its counterpart, the upflow anaerobic sludge blanket (UASB) reactor which is susceptible to solids washout due to the high (up to 1 m h –1 ) upflow velocities. Theoretical considerations for the SGBR are presented with results from SGBR treatment of synthetic (non-fat dry milk and sucrose) and actual (pork slaughterhouse and landfill leachate) wastewaters documenting the high efficiency (consistently greater than 90% conversion of COD) and excellent effluent characteristics (typically less than 50 mg L –1 total suspended solids and BOD5). Transient hydraulic and organic loads have relatively little effect on the SGBR as evidenced by consistent performance during an instantaneous shift in the hydraulic residence time from 36 to 5 h. In addition, results from variable reactor seeding from 25 to 100% of bed volume showed relatively little dependence of granule bed mass on effluent characteristics. This finding confirms independent results showing that a large fraction of the granule bed is substrate limited and available as reserve biomass. These results help explain the excellent treatment performance and resiliency of the SGBR regardless of hydraulic and organic loading. Fatty acid methyl ester (FAME) analysis of the granules showed distinct microbial
为了最大限度地提高中等强度(1-10 g COD L -1)废水中有机物以甲烷形式转化为能量的效率,开发了一种新型的高速率、低食物-微生物(F:M)厌氧处理系统。该系统被称为静态颗粒床反应器(SGBR),采用下流式水力机制,通过活性厌氧颗粒的密集床,可以容纳更高的悬浮固体浓度,而上流式厌氧污泥毯(UASB)反应器由于上流式速度高(高达1 m h -1)而容易受到固体冲刷。SGBR处理合成(脱脂牛奶和蔗糖)和实际(猪肉屠宰场和垃圾填埋场渗滤液)废水的结果表明,SGBR处理的理论考虑具有高效率(COD转化率始终大于90%)和优异的出水特性(通常小于50 mg L -1总悬浮固体和BOD5)。瞬态水力和有机负荷对SGBR的影响相对较小,这一点可以从水力停留时间从36小时瞬时转变为5小时期间的一致表现中得到证明。此外,从25%到100%的可变反应器播撒量的结果表明,颗粒床质量对流出物特性的依赖性相对较小。这一发现证实了独立的结果,表明颗粒床的很大一部分是底物有限的,可用作储备生物量。这些结果有助于解释无论水力和有机载荷如何,SGBR都具有出色的处理性能和弹性。脂肪酸甲酯(FAME)分析显示颗粒中有明显的微生物