首页> 外文OA文献 >Enhancement of hydrolysis and acidification of solid organic wastenext term by a rotational drum fermentation system with methanogenic leachate recirculation
【2h】

Enhancement of hydrolysis and acidification of solid organic wastenext term by a rotational drum fermentation system with methanogenic leachate recirculation

机译:带有产甲烷渗滤液再循环的转鼓发酵系统增强了固体有机wastenext的水解和酸化

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务,本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文,但由于OA文献来源多样且变更频繁,仍可能出现获取不到、文献不完整或与标题不符等情况,如果获取不到我们将提供退款服务。请知悉。

摘要

A cascade process of a rotational drum fermentation system with leachate recirculation from a methanogenic to the acidogenic reactorwas constructed to enhance the hydrolysis and acidification of solid organic waste. Using fresh soybean meal as substrates, two processconfigurations, Cascade process 1 and 2, without and with leachate recirculation, respectively were employed to perform the experimentalestimation under mesophilic condition and a total HRT of 20 days. An apparent first-order hydrolysis rate constant of 9.0 x 10-3/dfor Cascade process 1 at pH 4.5-4.6, and 15.8 x 10-3/d for Cascade process 2 at pH 4.6-5.2 were obtained. The apparent VS degradationratios ranged from 16.5% to 21.1% and total VA (as acetic acid) from 14.5 to 16.7 g/L. Occupying ratios for ionized VA decreased from40.5% to 35.3% for Cascade process 1 and increased to 68.5% for Cascade process 2. However, occupying ratios of acetic acid decreasedfrom 96.1% to 94.3% for Cascade process 1 and to 72.6% for Cascade process 2, whereas propionic acid and butyric acid ratios increasedin acidogenesis of Cascade process 2. The leachate recirculation promoted hydrolysis of substrate in Cascade process 2, where apparenthydrolysis rate constant and VS degradation ratio were higher than that of Cascade process 1.
机译:构建了具有从产甲烷反应器到产酸反应器的渗滤液再循环的转鼓发酵系统的级联过程,以增强固体有机废物的水解和酸化。以新鲜豆粕为底物,分别采用不带浸出液再循环和带浸出液再循环的两种工艺配置,级联工艺1和2,在中温条件下进行了实验估算,总HRT为20天。对于pH 4.5-4.6的级联方法1,获得的表观一级水解速率常数为9.0 x 10-3 / d,对于pH 4.6-5.2的级联过程2,获得的表观一级水解速率常数为15.8 x 10-3 / d。表观VS降解比为16.5%至21.1%,总VA(以乙酸计)为14.5至16.7 g / L。级联过程1中离子化VA的占有率从40.5%降低到35.3%,而级联过程2中的占有率增加到68.5%。但是,乙酸的占有率从级联过程1的96.1%降低到94.3%,而级联过程1的乙酸占有率降低到72.6%。步骤2,而在级联过程2的产酸过程中,丙酸和丁酸的比例增加。在级联过程2中,渗滤液的再循环促进了底物的水解,其中表观水解速率常数和VS降解率高于级联过程1。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
代理获取

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号