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Comparison of temperature-phased, two phase, and single stage anaerobic co-digestion of municipal solid waste and primary wastewater solids

机译:城市固体废物和主要废水固体的温度分阶段,两阶段和单阶段厌氧消化的比较

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摘要

The objective of this research was to evaluate the application of the temperature-phased process for the co-digestion of the organic fraction of municipal solid waste (OFMSW) and primary wastewater solids (PS) and to compare the process performance with both two phase and single stage anaerobic digestion. The temperature-phased (TPAD) and two phase (2P) processes both consisted of a thermophilic reactor operated at 55°C followed by a mesophilic reactor operated at 35°C. The pH of the thermophilic stage of the 2P system was controlled at 5.6, while the thermophilic stage of the TPAD system was operated at a neutral pH range. The single stage system (SS) was a single reactor operated at 35°C;The experiment was conducted by incrementally increasing the OFMSW percentage in the feed from 0, 20, 40, 60 to 80 percent. The performance of both the TPAD and 2P systems were greater than the SS system when the feed contained 60 and 80 percent OFMSW, due to increasing hydrolysis limitations. The TPAD, 2P, and SS systems had maximum methane yields of 0.42, 0.34, and 0.37 L/g VS fed, respectively. Maintaining syntrophic relationships between acidogenic, acetogenic, and methanogenic bacteria in the first stage of the TPAD system led to superior system performance when feeding 0, 20, and 40 percent OFMSW as compared to the both 2P and SS systems. The superior performance was characterized from VS removal and methane production. When the OFMSW content of the feed was 60 and 80 percent, the difference between the performance of the TPAD and 2P systems was less evident;Hydrolysis rates were determined from particulate chemical oxygen demand (PCOD) in operating temperature-phased and two phase systems. Methanogenic first-order rates were determined using batch tests with inocula from operating TPAD and 2P systems. The first stage of the TPAD system had higher hydrolysis rates than the first stage of the 2P system at all conditions tested. The temperature phased system had specific hydrolysis rates ranging from 0.048 to 0.285 g PCOD/g VS.d. The two phase system had specific hydrolysis rates ranging from 0.063 to 0.190 g PCOD/g VS.d.
机译:这项研究的目的是评估温度分段工艺在城市生活垃圾(OFMSW)和主要废水固体(PS)的有机部分共消化中的应用,并比较两相和二相的工艺性能。单级厌氧消化。温度分阶段(TPAD)和两阶段(2P)过程均由在55°C下运行的嗜热反应器,然后是在35°C下运行的中温反应器组成。 2P系统的高温阶段的pH控制在5.6,而TPAD系统的高温阶段在中性pH范围内运行。单级系统(SS)是在35°C下运行的单个反应器;通过将进料中的OFMSW百分比从0%,20%,40%,60%逐渐增加到80%进行实验。当进料中含有60%和80%的OFMSW时,由于水解限制的增加,TPAD和2P系统的性能均优于SS系统。 TPAD,2P和SS系统进料的最大甲烷产量分别为0.42、0.34和0.37 L / gVS。与2P和SS系统相比,在TPAD系统的第一阶段保持产酸细菌,产乙酸细菌和产甲烷细菌之间的同养关系,在饲喂0、20和40%的OFMSW时,系统性能优越。 VS去除和甲烷生成具有卓越的性能。当进料的OFMSW含量分别为60%和80%时,TPAD和2P系统的性能差异不明显;水解速率由在温度阶段和两相系统中的颗粒化学需氧量(PCOD)确定。产甲烷的一级速率是通过使用批次TPAD和2P系统中的接种物进行批次测试确定的。在所有测试条件下,TPAD系统的第一阶段的水解速率均高于2P系统的第一阶段。该温度相系统的比水解速率为0.048至0.285g PCOD / gVS.d。两相体系的比水解速率为0.063至0.190g PCOD / gVS.d。

著录项

  • 作者

    Schmit, Kathryn Healy;

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  • 年度 1998
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  • 原文格式 PDF
  • 正文语种 en
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