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Sludge management modeling to enhance P-recovery as struvite in wastewater treatment plants

机译:污泥管理模型可增强废水处理厂中鸟粪石的磷回收率

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摘要

Interest in phosphorus (P) recovery and reuse has increased in recent years as supplies of P are declining. After use, most of the P remains in wastewater, making Wastewater Treatment Plants (WWTPs) a vital part of P recycling. In this work, a new sludge management operation was studied by modeling in order to recover P in the form of struvite and minimize operating problems due to uncontrolled P precipitation in WWTPs. During the study, intensive analytical campaigns were carried out on the water and sludge lines. The results identified the anaerobic digester as a "hot spot" of uncontrolled P precipitation (9.5 gP/ kg sludge) and highlighted possible operating problems due to the accumulation of precipitates. A new sludge line management strategy was simulated therefore using DESASS~® software, consisting of the elutriation of the mixed sludge in the mixing chamber, to reduce uncontrolled P precipitation and to obtain a P-rich stream (primary thickener supernatant) to be used in a crystallization process. The key operating parameters were found to be: the elutriation flow from the mixing chamber to the primary thickener, the digestion flow and the sludge blanket height of the primary thickener, with optimized values between 70 and 80 m~3/d, 90-100 m~3/d and 1.4-1.5 m, respectively. Under these operating conditions, the preliminary results showed that P concentration in the primary thickener overflow significantly increased (from 38 to 100 mg PO_4-P/L), which shows that this stream is suitable for use in a subsequent crystallization reactor to recover P in the form of struvite.
机译:近年来,随着磷供应的减少,人们对磷(P)的回收和再利用的兴趣增加了。使用后,大多数磷残留在废水中,使污水处理厂(WWTP)成为磷回收的重要组成部分。在这项工作中,通过建模研究了一种新的污泥管理操作,以回收鸟粪石形式的磷,并最大程度地减少了污水处理厂中由于不受控制的磷沉淀而导致的操作问题。在研究过程中,对水和污泥管线进行了深入的分析。结果确定厌氧消化池为不受控制的P沉淀(9.5 gP / kg污泥)的“热点”,并强调了由于沉淀物的积累而可能产生的操作问题。因此,使用DESASS〜®软件模拟了一种新的污泥生产线管理策略,该软件包括在混合室中淘洗混合污泥,以减少不受控制的P沉淀并获得富P流(主要是浓稠剂上清液),用于结晶过程。发现关键的操作参数为:从混合室到初级浓缩器的淘析流量,初级浓缩器的消化流量和污泥层高度,优化值在70至80 m〜3 / d,90-100之间m〜3 / d和1.4-1.5 m。在这些操作条件下,初步结果表明,一级增稠剂溢流中的P浓度显着增加(从38 mg PO_4-P / L增至100 mg),这表明该物流适用于后续的结晶反应器中以回收P鸟粪石的形式。

著录项

  • 来源
    《Journal of Environmental Management》 |2017年第1期|340-346|共7页
  • 作者单位

    Dpto. de Ingenierfa Quimica, Universitat de València, Avinguda de la Universitat s, 46100, Burjassot, Valencia, Spain;

    Instituto* de Ingenieria del Agua y Medio Ambiente, IIAMA, Universitat Politècnica de València, CamI de Vera, s, 46022, Valencia, Spain;

    Dpto. de Ingenierfa Quimica, Universitat de València, Avinguda de la Universitat s, 46100, Burjassot, Valencia, Spain;

    Depuración de Aguas del Mediterráneo (DAM), Avenida Benjamin Franklin, 21, 46980, Parque Tecnológico, Paterna, Valencia, Spain;

    Dpto. de Ingenierfa Quimica, Universitat de València, Avinguda de la Universitat s, 46100, Burjassot, Valencia, Spain;

  • 收录信息 美国《科学引文索引》(SCI);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Nutrient recovery; Sludge treatment; Crystallization; Uncontrolled precipitation; Urban WWTP;

    机译:营养恢复;污泥处理;结晶;降雨不受控制;城市污水处理厂;

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