Use of surfactants for efficient removal of calcium phosphate particles from water

V. Radovenchyk, Kateryna Hordiienko, Yaroslav Radovenchyk, T. Krysenko
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Abstract

Today, softening of water in offices and private homes is mainly carried out by the ion exchange method, despite its significant negative impact on the hydrosphere. The development of alternative safe technologies in this field is extremely relevant today. Such an alternative can be considered the use of effective reagents that transfer hardness ions into the solid phase. The use of phosphates as such reagents allows, depending on the conditions, to reduce the residual hardness of water to the level of 0.1 mg-eq/dm3 or less. An important problem of this technology is the efficiency of separating the solid phase from the mother liquor. This step can be implemented by advocating or filtering. Using model calcium solutions treated with appropriate doses of sodium phosphate and flocculants, the most effective of them in settling processes were selected. As flocculants, polyacrylamide was used - as a nonionic flocculant, Magnofloc - 336 from Ciba - as an anionic flocculant, Zetag - 7692 from Ciba - as a cationic flocculant. The flocculant Magnofloc - 336 turned out to be the most effective in settling highly dispersed particles of calcium phosphate. At a flocculant concentration of 30 mg/dm3 for 10 min of settling, the apparent volume of the solid phase decreases to 30 % of the initial volume of the suspension and stabilizes at this value. Other types of flocculants and other doses were less effective. A somewhat different situation is observed when separating the solid phase by filtration. The greatest influence on the filtration rate is caused by the temperature, the hydrogen index and the ratio between the components. Only temperatures below 20 °C significantly affect the rate of filtration. This is especially noticeable at a temperature of 5 °C. At this temperature, the volume of filtrate is 8-20 minutes behind the volume of filtrate of distilled water. At 15 °C, this difference is smaller, and at temperatures above 20 °C, the curves generally overlap. In the pH range of 5-9, there is no significant effect on the filtration rate. Only in a strongly alkaline environment do the necessary filtering times increase significantly, which, in our opinion, is due to the formation of a significant number of amorphous particles of various composition, which can block the pores of the filters. With the stoichiometric ratio of the components, the curve of the change in the filtration rate practically coincides with the curve of the change in the filtration rate of distilled water under the same conditions. When the ratio changes both downward and upward, the conditions for filtering the suspension deteriorate. And the more the ratio differs from stoichiometry, the more developed the structure of the solid phase is and the worse its separation from the liquid phase is. As the ratio between the components changes, so does the pH of the zero charge of the solid particles. If the stoichiometric ratio of the components is at pH 8.15, then when the ratio decreases to 0.5, it decreases to pH 7.41, and when it increases to 2, it increases to pH 8.64. A change in the ratio of components affects not only the sign of the surface charge, but also its magnitude, which cannot help but affect the efficiency of solid phase separation. The type and dosage of flocculants determined to be most effective in settling do not always provide the same effect in filtration. Suspensions without the addition of flocculants have the highest filtration speed. The study of the effect of flocculants at their concentrations of 10 and 30 mg/dm3 showed that none of its different types and at their different concentrations contributes to an increase in the filtration rate. Obviously, significant doses of flocculants contribute to the rapid calming of the porous medium of the filters and cause a decrease in the rate of transport of the liquid phase. The obtained results make it possible to determine effective reagents for removing calcium ions from natural waters and the optimal conditions for their use and serve as a basis for the development of effective and environmentally safe technologies for softening natural waters.
使用表面活性剂有效地去除水中的磷酸钙颗粒
今天,办公室和私人住宅的水软化主要是通过离子交换法进行的,尽管它对水圈有重大的负面影响。在这一领域开发替代安全技术是当今极为重要的。这种替代方案可以考虑使用将硬度离子转移到固相中的有效试剂。使用磷酸盐作为这样的试剂,可以根据条件将水的残余硬度降低到0.1 mg-eq/dm3或更低的水平。该技术的一个重要问题是固相与母液的分离效率。这一步可以通过倡导或过滤来实现。采用适当剂量的磷酸钠和絮凝剂处理模型钙溶液,选择最有效的沉降工艺。絮凝剂选用聚丙烯酰胺为非离子型絮凝剂,汽巴生产的magnnofloc - 336为阴离子型絮凝剂,汽巴生产的Zetag - 7692为阳离子型絮凝剂。结果表明,絮凝剂magnnofloc - 336对高度分散的磷酸钙颗粒的沉降效果最好。当絮凝剂浓度为30 mg/dm3,沉降10 min时,固相表观体积降至悬浮液初始体积的30%,并稳定在此值。其他类型的絮凝剂和其他剂量的效果较差。当用过滤分离固相时,观察到的情况有些不同。对过滤速率影响最大的因素是温度、氢指数和各组分之间的比例。只有低于20°C的温度才会显著影响过滤速度。这在5°C的温度下尤其明显。在此温度下,滤液体积比蒸馏水的滤液体积少8-20分钟。在15°C时,这种差异较小,在20°C以上的温度下,曲线通常重叠。在5 ~ 9的pH范围内,对过滤速率无显著影响。只有在强碱性环境中,必要的过滤次数才会显著增加,我们认为,这是由于形成了数量可观的各种组成的非晶态颗粒,这些颗粒会堵塞过滤器的孔隙。随着各组分化学计量比的增大,过滤速率变化曲线与相同条件下蒸馏水过滤速率变化曲线基本一致。当比值上下变化时,过滤悬浮液的条件变差。比值与化学计量差越大,固相结构越发达,与液相分离越差。随着组分之间的比例变化,固体颗粒的零电荷的pH值也会变化。如果各组分的化学计量比在pH为8.15时,当该比减小到0.5时,pH值减小到7.41,当该比增大到2时,pH值增大到8.64。组分比例的变化不仅影响表面电荷的符号,而且影响电荷的大小,从而影响固相分离的效率。被确定为最有效的沉降絮凝剂的类型和剂量并不总是在过滤中提供相同的效果。未添加絮凝剂的悬浮液过滤速度最高。对絮凝剂浓度为10和30 mg/dm3时的效果进行了研究,结果表明,不同类型的絮凝剂和不同浓度的絮凝剂均无助于提高过滤速率。显然,大剂量的絮凝剂有助于过滤器多孔介质的快速镇静,并导致液相传输速率的降低。所得结果为确定天然水中钙离子去除的有效试剂及其最佳使用条件提供了可能,并为开发有效且环保的天然水软化技术奠定了基础。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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