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Sulfate removal from wastewater using ettringite precipitation: Magnesium ion inhibition and process optimization

机译:用钙矾石沉淀去除废水中的硫酸盐:抑制镁离子和优化工艺

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摘要

One of the main challenges in industrial wastewater treatment and recovery is the removal of sulfate, which usually coexists with Ca~(2+) and Mg~(2+). The effect of Mg~(2+) on sulfate removal by ettringite precipitation was investigated, and the process was optimized in the absence and presence of Mg~(2+). In the absence of Mg~(2+), the optimum conditions with sulfate removal of 99.7% were obtained at calcium-to-sulfate ratio of 3.20, aluminum-to-sulfate ratio of 1.25 and pH of 11.3 using response surface methodology. In the presence of Mg~(2+), sulfate removal efficiency decreased with increasing Mg~(2+) concentration, and the inhibitory effect of Mg~(2+) matched the competitive inhibition Monod model with half maximum inhibition concentration of 57.4 mmol/L X-ray diffraction and Fourier transform infrared spectroscopy analyses of precipitates revealed that ettringite was converted to hydrotalcite-type (HT) compound in the presence of Mg~(2+). The morphology of precipitates was transformed from prismatic crystals to stacked layered crystals, which confirmed that Mg~(2+) competes with Ca~(2+) for Al~(3+) to form HT compound. A two-stage process was designed with Mg~(2+) removal before ettringite precipitation to eliminate the inhibitory effect, and is potential to realize sludge recovery at the same time of effective removal of sulfate and hardness.
机译:工业废水处理和回收中的主要挑战之一是去除硫酸盐,硫酸盐通常与Ca〜(2+)和Mg〜(2+)共存。研究了Mg〜(2+)对钙矾石沉淀去除硫酸盐的影响,并在不存在和存在Mg〜(2+)的条件下优化了工艺。在不存在Mg〜(2+)的条件下,采用响应面法得到钙硫酸盐比为3.20,铝硫酸盐比为1.25,pH为11.3时,硫酸盐去除率为99.7%的最佳条件。在Mg〜(2+)存在下,硫酸盐去除效率随Mg〜(2+)浓度的增加而降低,并且Mg〜(2+)的抑制作用与竞争抑制Monod模型相匹配,最大抑制浓度为57.4 mmol。沉淀物的/ L X射线衍射和傅里叶变换红外光谱分析表明,在Mg〜(2+)存在下,钙矾石转化为水滑石型(HT)化合物。析出物的形态从棱柱形晶体转变为叠层晶体,这证实Mg〜(2+)与Ca〜(2+)竞争Al〜(3+)形成HT化合物。设计了钙镁矿沉淀前去除Mg〜(2+)的二级工艺,以消除抑制作用,在有效去除硫酸盐和硬度的同时,有望实现污泥的回收。

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  • 来源
    《Journal of Environmental Management》 |2017年第1期|518-526|共9页
  • 作者单位

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    Jiangsu Hairong Thermal & Environmental Engineering Co., Ltd, 10 Sanmiao Village, Xingren Town, Tongzhou District, Nantong, Jiangsu 226371, China;

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    College of Environmental and Chemical Engineering, Shanghai University of Electric Power, 2S88 Changyang Road, Shanghai 200090, China;

    Jiangsu Hairong Thermal & Environmental Engineering Co., Ltd, 10 Sanmiao Village, Xingren Town, Tongzhou District, Nantong, Jiangsu 226371, China;

  • 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
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