首页> 外文期刊>Energy & Environment >Feasibility of wastewater resource recovery using pilot-scale membrane reactor with long-term operation
【24h】

Feasibility of wastewater resource recovery using pilot-scale membrane reactor with long-term operation

机译:使用试验型膜反应器具有长期运行的污水资源回收的可行性

获取原文
获取原文并翻译 | 示例
       

摘要

With the growing interest in resource recovery from wastewater, research has been put forward to realize this aim using different approaches. Here, we considered several conditions necessary for the experiment, with the primary goal of recovering concentrates suitable for biogas recovery and water reuse through the pilot-scale membrane reactor (PSMR). The new concept enables the feasibility of recovering permeates and concentrates directly from the PSMR. From the results obtained, permeate chemical oxygen demand was within 20 mg/L to 38 mg/L; the total nitrogen yielded an average value of 22.14 +/- 3.53 mg/L; ammonia yielded an average value of 13.34 +/- 1.18 mg/L; and the total phosphorus presented a value of 0.46 +/- 0.32 mg/L. Permeates recovered from the experiment feature potential use for agriculture, groundwater, and lake recharge, as the chemical oxygen demand, total nitrogen, total phosphorus, and ammonia contents are low and acceptable for these purposes. Concentrates from two days of solid retention time ranged from 6050 mg/L to 10,000 mg/L, which was suitable for anaerobic digestion for biogas recovery. A further experiment is suggested to enable the removal of more ammonia, total phosphorus, and total nitrogen in permeate to enable its use for a domestic purpose.
机译:随着对废水中资源回收的兴趣日益增长,已经提出了使用不同方法实现这一目标的研究。在此,我们考虑了实验所需的几种条件,具有通过试验型膜反应器(PSMR)的沼气回收和水再利用的浓缩物的主要目标。新概念使得能够恢复渗透物的可行性,并直接从PSMR中浓缩。从得到的结果中,渗透化学氧需求在20mg / L至38 mg / L内;总氮产生平均值22.14 +/- 3.53mg / l;氨的平均值为13.34 +/- 1.18 mg / l;并且总磷呈现为0.46 +/- 0.32 mg / L.从实验特征潜在用于农业,地下水和湖泊充电的渗透物,作为化学需氧量,总氮,总磷和氨含量,这些目的是低且可接受的。从固体保留时间的两天浓缩,范围为6050mg / L至10,000 mg / L,适用于沼气消化的沼气回收。提出了进一步的实验,使得能够在渗透物中去除更多的氨,总磷和总氮,以使其用于国内目的。

著录项

  • 来源
    《Energy & Environment》 |2019年第4期|662-671|共10页
  • 作者单位

    Tsinghua Univ Sch Environm State Key Joint Lab Environm Simulat & Pollut Con Beijing 100084 Peoples R China|Univ Sci & Technol Beijing Sch Energy & Environm Engn Beijing Key Lab Resource Oriented Treatment Ind P Beijing Peoples R China;

    Tsinghua Univ Sch Environm State Key Joint Lab Environm Simulat & Pollut Con Beijing 100084 Peoples R China;

    Univ Sci & Technol Beijing Sch Energy & Environm Engn Beijing Key Lab Resource Oriented Treatment Ind P Beijing Peoples R China;

    Tsinghua Univ Sch Environm State Key Joint Lab Environm Simulat & Pollut Con Beijing 100084 Peoples R China;

    Univ Sci & Technol Beijing Sch Energy & Environm Engn Beijing Key Lab Resource Oriented Treatment Ind P Beijing Peoples R China;

  • 收录信息 美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Sewage membrane filtration; sewage concentration; resource recovery; permeate; anaerobic digestion; bioenergy;

    机译:污水膜过滤;污水浓度;资源恢复;渗透;厌氧消化;生物能源;
  • 入库时间 2022-08-18 21:48:41

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