• 主题
高级搜索  >
历史搜索 清空历史
首页> 外文期刊>Separation and Purification Technology >Long-term operation of a pilot-scale anaerobic membrane bioreactor (AnMBR) treating high salinity low loaded municipal wastewater in real environment
【24h】

Long-term operation of a pilot-scale anaerobic membrane bioreactor (AnMBR) treating high salinity low loaded municipal wastewater in real environment

机译：试验型厌氧膜生物反应器（ANMBR）的长期运行处理真实环境中高盐度低负载的城市废水

获取原文
获取原文并翻译 | 示例
           
页面导航
  • 摘要
  • 著录项
  • 相似文献
  • 相关主题

摘要

Long term operation of an anaerobic membrane bioreactor (AnMBR) treating municipal wastewater was investigated in a real seawater intrusion spot in Falconara Marittima (Central Italy) on the Adriatic coastline. Changes in biological conversion and system stability were determined with respect to varying organic loading rate (OLR) and high salinity conditions. At an OLR of 1 kg COD m(3-1) d(-1), biogas production was around 0.39 +/- 0.2 L d(-1). The increase of the OLR to 2 kg COD m(3-1) d(-1) resulted in increase of biogas production to 2.8 +/- 1.5 L d(-1) (with 33.6% +/- 10.5% of CH4) with methanol addition and to 4.11 +/- 3.1 L d(-1) (with 29.7% +/- 11.8% of CH4) with fermented cellulosic sludge addition. COD removal by the AnMBR was 83% +/- 1% when the effluent COD concentration was below 100 mg O-2 L-1. The addition of the fermented sludge affected the membrane operation and significant fouling occurred after long-term filtration, where the trans-membrane pressure (TMP) reached up to 500 mbar. Citric acid solution was applied to remove sealants and the TMP reached the initial value. High saline conditions of 1500 mgCl(-) L-1 adversely affected the biogas production without deteriorating the membrane operation. The treated effluent met the EU quality standards of the D.M. 185/2003 and the new European Commission Resolution for reuse in agriculture.
机译：在亚得里亚海海岸线的Falconara Marittima（意大利中部）的真正海水入侵点中，研究了治疗城市废水的厌氧膜生物反应器（ANMBR）的长期运作。相对于不同的有机加载速率（OLR）和高盐度条件，确定生物转化和系统稳定性的变化。在1kg COD m（3-1）d（-1）的OLR，沼气产量约为0.39 +/- 0.2 L D（-1）。 OLR至2kg COD m（3-1）D（-1）的增加导致沼气产量增加到2.8 +/- 1.5 L D（-1）（CH4的33.6％+/- 10.5％）加入甲醇加入和4.11 +/- 3.1 L D（-1）（CH4的29.7％+/-11.8％），加入发酵纤维素污泥。当流出物COD浓度低于100mg O-2 L-1时，ANMBR的COD除去83％+/- 1％。发酵污泥的添加影响了长期过滤后发生的膜操作和显着的污垢，其中跨膜压力（TMP）达到500毫巴。施用柠檬酸溶液以除去密封剂，TMP达到初始值。高盐水条件为1500 mgCl（ - ）L-1对沼气产生产生不利影响，而不会恶化膜操作。治疗的污水符合下午的欧盟质量标准。 185/2003和新的欧洲委员会决议在农业中重用。

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