首页> 外文期刊>Water Science and Technology >Dissolved oxygen, COD, nitrogen and phosphorus profiles in a continuous sand filter used for WWTP effluent reclamation
【24h】

Dissolved oxygen, COD, nitrogen and phosphorus profiles in a continuous sand filter used for WWTP effluent reclamation

机译:在用于污水处理厂废水回收的连续式砂滤器中溶解的氧气,COD,氮和磷分布

获取原文
获取原文并翻译 | 示例
           

摘要

Continuous sand filtration (CSF) offers interesting potential for the extensive treatment of wastewater treatment plant (WWTP) effluents for water reclamation and/or restrictive discharge. Research on concentration profiles over the height of the CSF shows that most bacteriological conversions are restricted to the lower part of the filter bed. Dissolved oxygen (DO) rapidly decreases to below 1 mg/L in the first 0.4 m of the filter bed, applying hydraulic velocities of 12.9 ? 14.9 m/h and 10 ? 20 mm/min sand velocities, independent of the methanol dosage. The DO decrease agrees with the observed decrease in chemical oxygen demand (COD). At the given operational conditions, NOx-N and N-total removal is dedicated to the first 0.9 m of the filter bed. Results show that by optimising the CSF operational conditions the very restrictive effluent N and P values of 2.2 and 0.15 mg/L, respectively, as described in the European Water Framework Directive, can be met.
机译:连续砂滤(CSF)为废水处理厂(WWTP)废水的广泛处理提供了有趣的潜力,可用于水的回收和/或限制排放。对CSF高度范围内浓度分布的研究表明,大多数细菌转化仅限于滤床的下部。在最初的0.4 m滤床中,溶解氧(DO)迅速降至1 mg / L以下,水力速度为12.9? 14.9 m / h和10? 20 mm / min的砂速,与甲醇用量无关。 DO的减少与观察到的化学需氧量(COD)的减少相符。在给定的运行条件下,NOx-N和N的总去除量专用于滤床的前0.9 m。结果表明,通过优化CSF操作条件,可以满足欧洲水框架指令中所述的限制性N和P值分别为2.2和0.15 mg / L的要求。

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