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Pyrolucite fluidized-bed reactor (PFBR): A robust and compact process for removing manganese from groundwater

机译:硫铁矿流化床反应器(PFBR):一种用于去除地下水中锰的可靠而紧凑的方法

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摘要

The purpose of this paper is to introduce a pyrolucite fluidized-bed reactor (PFBR) as a potential drinking water process to treat groundwater containing high levels of dissolved manganese (Mn(Ⅱ)) (0.5-3 mg/L) and reduce its concentration to <0.02 mg/L in treated water. A pilot-scale study was conducted under dynamic conditions using synthetic groundwater (SGW), to elucidate the effect of operational conditions and groundwater composition on manganese (Mn) removal achieved by the PFBR. Results demonstrated almost complete Mn removal (close to 100%) in less than 1 min under all tested operational conditions (influent Mn concentration of 0.5-3 mg/L, calcium (Ca~(2+)) hardness of 0-200 mg CaCO_3/L, pH of 6.2-7.8, temperature of 9 & 23 ℃ and high hydraulic loading rate (HLR) of 24 -63 m/h (i.e., bed expansion of 0-30%)). Improved Mn removal profile was achieved at higher water temperature. Also, the results showed that adsorption of Mn(Ⅱ) onto pyrolucite and subsequent slower surface oxidation of sorbed Mn(Ⅱ) was the only mechanism responsible for Mn removal while direct oxidation of Mn(Ⅱ) by free chlorine did not occur even at high concentrations of Mn(Ⅱ) and free chlorine and elevated temperatures. Higher average mass transfer coefficient and consequently adsorption rate was achieved at elevated HLR. Increasing effluent free chlorine residuals from 1.0 to 2.0-2.6 mg Cl_2/L allowed increasing the operation time needed for media regeneration from 6 days to >12 days. Turbidity was maintained around 0.2 NTU during the entire test periods indicating good capture of MnO_x colloids within the PFBR.
机译:本文的目的是介绍一种热解萤石流化床反应器(PFBR),作为一种潜在的饮用水工艺,用于处理含高浓度锰(Mn(Ⅱ))(0.5-3 mg / L)的地下水并降低其浓度在处理水中至<0.02 mg / L。使用合成地下水(SGW)在动态条件下进行了中试研究,以阐明操作条件和地下水成分对PFBR去除锰(Mn)的影响。结果表明,在所有测试操作条件下(进水锰浓度为0.5-3 mg / L,钙(Ca〜(2+))硬度为0-200 mg CaCO_3),不到1分钟即可将锰几乎完全去除(接近100%)。 / L,pH值为6.2-7.8,温度为9和23℃,高水力加载速率(HLR)为24 -63 m / h(即床膨胀为0-30%)。在较高的水温下,锰去除率得到了改善。此外,结果表明,锰(Ⅱ)吸附在焦萤石上,随后缓慢的表面吸附氧化锰(Ⅱ)是造成锰去除的唯一机理,而即使在高温下也不会发生游离氯对锰(Ⅱ)的直接氧化。 Mn(Ⅱ)和游离氯的浓度和高温在升高的HLR下,获得更高的平均传质系数,从而获得更高的吸附速率。将废水中的游离氯残留量从1.0 mg Cl_2 / L增加到2.0-2.6 mg,可使培养基再生所需的操作时间从6天增加到> 12天。在整个测试期间,浊度保持在0.2 NTU附近,表明PFBR内MnO_x胶体被良好捕获。

著录项

  • 来源
    《Water Research》 |2014年第1期|475-483|共9页
  • 作者单位

    Ecole Polytechnique de Montreal, Department of Civil Engineering, NSERC - Industrial Chair on Drinking Water, Environment, C.P. 6079, Succursale Centre-Ville, Montreal, QC H3C 3A7, Canada;

    Ecole Polytechnique de Montreal, Department of Civil Engineering, NSERC - Industrial Chair on Drinking Water, Environment, C.P. 6079, Succursale Centre-Ville, Montreal, QC H3C 3A7, Canada;

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

    Drinking water; Groundwater; Treatment; Manganese; Pyrolucite; Fluidized-bed reactor;

    机译:饮用水;地下水;治疗;锰;硫铁矿;流化床反应器;

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