Research of phosphate removal from water on reverse osmotic filters

M. Gomelya, I. Trus, A. Vakulenko, A. Taranenko
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Abstract

Eutrophication of natural water bodies caused by an excess of biogenic substances is one of the global environmental problems of modern times. Usually, phosphorus is a limiting biogenic element, the concentration of which determines the intensity of eutrophication processes in water bodies. Therefore, it is important to develop methods aimed at preventing excessive amounts of phosphates from entering the environment. To remove phosphates from water, typically used biological degradation technologies, which usually proceed very slowly and depend on the conditions under which the process takes place. Also, Biogenic elements can be removed by using ion exchange, reverse osmosis, and chemical methods. However, the disposal of concentrated solutions becomes an issue with these methods. Baromembrane purification methods, particularly reverse osmosis, are becoming increasingly important in the field of water treatment and purification and are essential in creating efficient and low-waste complex technologies for water purification from biogenic compounds. The study investigated the processes of removing orthophosphates from distilled and artesian water using a low-pressure reverse osmosis membrane Filmtec TW30-1812-50. The dependence of membrane productivity and selectivity on the concentration of phosphates and the degree of permeate rejection was determined. Was found that residual concentrations of phosphates in the permeate increase with the increase in the degree of permeate rejection. The lowest residual concentrations of phosphates were observed at the initial concentration of up to 10 mg/dm3. The highest residual phosphate concentrations were observed at initial concentrations above 900 mg/dm3. At the same time, the membrane productivity constantly decreased with increasing feed concentration and degree of permeate recovery due to the increased osmotic pressure on the membrane. The selectivity of the membrane was highest at an initial concentration of up to 10 mg/dm3 and slightly decreased at a rejection rate of 20-50% for initial phosphate concentrations of 100-900 mg/dm3. At the maximum degree of permeate rejection (90%), the selectivity of the membrane reached 97-99 % and decreased with an increase in phosphate concentrations, which is due to a change in the pH of the medium, hydrolysis of phosphates, hydration of ions, and concentration polarization. The membrane selectivity for phosphates in solutions in artesian water was slightly lower (95-99 %), which was due to the competing influence of chlorides, sulfates, and bicarbonates, as well as a decrease in the pH of the solution to 7.52-7.67, which promotes the hydrolysis of o-phosphates.
反渗透过滤器去除水中磷酸盐的研究
由生物物质过量引起的水体富营养化是现代全球性环境问题之一。通常,磷是一种限制性生物元素,其浓度决定了水体富营养化过程的强度。因此,制定旨在防止过量磷酸盐进入环境的方法是很重要的。为了从水中去除磷酸盐,通常使用生物降解技术,这通常进行得非常缓慢,并且取决于过程发生的条件。此外,生物源元素可以通过离子交换、反渗透和化学方法去除。然而,浓缩溶液的处理成为这些方法的一个问题。气压膜净化方法,特别是反渗透,在水处理和净化领域正变得越来越重要,并且对于创造从生物化合物中净化水的高效和低废物复杂技术至关重要。研究了使用低压反渗透膜Filmtec TW30-1812-50从蒸馏水和自流水中去除正磷酸盐的过程。测定了膜的产率和选择性与磷酸盐浓度和渗透排斥程度的关系。发现渗透液中磷酸盐残留浓度随渗透液排斥程度的增加而增加。在初始浓度高达10 mg/dm3时,观察到磷酸盐残留浓度最低。在初始浓度高于900 mg/dm3时,观察到最高残留磷酸盐浓度。同时,随着进料浓度和渗透恢复程度的增加,膜的产率不断降低,这是由于膜上渗透压的增加。当初始磷酸盐浓度为10 mg/dm3时,膜的选择性最高,当初始磷酸盐浓度为100-900 mg/dm3时,膜的拒绝率略有下降,为20-50%。在最大阻渗度(90%)时,膜的选择性达到97- 99%,并随着磷酸盐浓度的增加而降低,这是由于介质pH的变化、磷酸盐的水解、离子的水合作用和浓度极化。在自流水中溶液中,磷酸盐的膜选择性略低(95- 99%),这是由于氯化物、硫酸盐和碳酸氢盐的竞争影响,以及溶液pH降至7.52-7.67,促进了邻磷酸盐的水解。
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