首页> 外文期刊>Sustainable environment research >Optimization of fermentative hydrogen production from palm oil mill effluent in an up-flow anaerobic sludge blanket fixed film bioreactor
【24h】

Optimization of fermentative hydrogen production from palm oil mill effluent in an up-flow anaerobic sludge blanket fixed film bioreactor

机译:上流式厌氧污泥床固定膜生物反应器中棕榈油厂废水发酵产氢的优化

获取原文
       

摘要

Response surface methodology with a central composite design was applied to optimize fermentative hydrogen production from palm oil mill effluent (POME) in an upflow anaerobic sludge blanket fixed film?reactor. In this study, the concurrent effects of up-flow velocity (V up ) and feed flow rate (Q F ) as independent operating variables on biological hydrogen production were investigated. A broad range of organic loading rate between 10 and 60?g COD L ?1 d ?1 was used as the operating variables. The dependent parameters as multiple responses were evaluated. Experimental results showed the highest value of yield at 0.31?L H 2 g ?1 COD was obtained at V up and Q F of 0.5?m h ?1 and 1.7?L d ?1 , respectively. The?optimum conditions for the fermentative hydrogen production using pre-settled POME were Q F ?=?2.0–3.7?L?d ?1 and V up ?=?1.5–2.3?m?h ?1 . The experimental results agreed very well with the model prediction.
机译:采用中央复合设计的响应表面方法,优化了上流厌氧污泥床固定膜反应器中棕榈油厂出水(POME)的发酵产氢量。在这项研究中,研究了上流速度(V up)和进料流速(Q F)作为独立操作变量对生物制氢的同时影响。在10到60 g g COD L?1 d?1之间的宽范围有机负载率用作操作变量。评估了作为多个响应的相关参数。实验结果表明,在Vup和Q F分别为0.5?m h?1和1.7?L d?1时,在0.31?L H 2 g?1处获得了最高的COD。使用预先确定的POME进行发酵制氢的最佳条件是Q F?=?2.0–3.7?L?d?1和V up?=?1.5-2.3?m?h?1。实验结果与模型预测非常吻合。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

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