Department of Civil, Environmental and Architectural Engineering, University of Kansas, Lawrence, KS, 66045, USA; Tertiary Oil Recovery Program, University of Kansas, Lawrence, KS, 66045, USA.
Department of Civil, Environmental and Architectural Engineering, University of Kansas, Lawrence, KS, 66045, USA.
Water Res. 2020 Mar 1;170:115362. doi: 10.1016/j.watres.2019.115362. Epub 2019 Dec 2.
Boron (B), normally present in ground water and sea water, is a vital micronutrient for plants, but is also toxic in excessive amounts. Under typical conditions, aqueous boron is present as boric acid (HBO), which is uncharged, making B particularly challenging to remove by mechanisms commonly applicable to removal of trace constituents. Adsorption of B onto aluminum hydroxide solids (Al(OH)(s)) generated using aluminum-based electrocoagulation (EC) is a promising strategy for B removal. Infrared spectroscopy analysis indicated complexation of B(OH) with aluminum hydroxide solids via surface hydroxyl groups, while X-ray and infrared spectroscopy results indicated that the structure of the Al(OH)(s) was influenced both by EC operating conditions and by water quality. A linear adsorption model predicted B removal well when initial concentrations were lower than 50 mg/L, but fit the experimental data poorly at higher initial B concentrations. The Langmuir adsorption model provided a good fit for a broader range of initial B concentrations (5-1000 mg/L). Factors affecting B adsorption during the EC process, including current intensity, Al dissolution rate, boron concentration, pH, and total dissolved solid (TDS), were investigated. Increasing current intensity initially led to a higher Al dissolution rate, and therefore higher B adsorption, but there was a limit, as further increases in current intensity caused rapid formation of Al(OH)(s) having a large particle size and a low capacity to complex B. Boron removal decreased as its concentration increased. The best removal of B occurred at pH 8, corresponding to a slightly positive zeta potential for aluminum hydroxide and a small but significant fraction of negatively charged B species. Higher TDS concentrations facilitated the use of higher current intensities, i.e., the limit on the effective Al dissolution rate increased with increasing TDS. Two real water samples (river water and oilfield produced water) spiked with B were treated using EC, resulting in up to 50% B removal from river water (C = 10 mg/L, current = 0.2 A) in 2 h, and 80% B removal from produced water (C = 50 mg/L, current = 1.0 A) in 2 h.
硼(B)通常存在于地下水和海水中,是植物必需的微量元素,但过量也会有毒。在典型条件下,水中的硼以硼酸(HBO)的形式存在,硼酸不带电荷,这使得通过通常适用于痕量成分去除的机制去除硼特别具有挑战性。使用基于铝的电凝聚(EC)生成的氢氧化铝固体(Al(OH)(s))吸附硼是去除硼的一种很有前途的策略。红外光谱分析表明,B(OH)与氢氧化铝固体通过表面羟基络合,而 X 射线和红外光谱结果表明,EC 操作条件和水质都对 Al(OH)(s)的结构产生影响。线性吸附模型在初始浓度低于 50mg/L 时很好地预测了硼的去除,但在初始硼浓度较高时拟合实验数据效果不佳。Langmuir 吸附模型对更广泛的初始硼浓度范围(5-1000mg/L)提供了很好的拟合。研究了影响 EC 过程中硼吸附的因素,包括电流强度、铝溶解速率、硼浓度、pH 值和总溶解固体(TDS)。增加电流强度最初会导致更高的铝溶解速率,从而提高硼的吸附,但存在一个限制,因为进一步增加电流强度会导致快速形成粒径较大、与硼络合能力较低的 Al(OH)(s)。随着硼浓度的增加,硼的去除率降低。在 pH 8 时,硼的去除效果最佳,此时氢氧化铝的 ζ 电位略为正,带少量但显著比例的带负电荷的硼物种。较高的 TDS 浓度有利于使用较高的电流强度,即有效铝溶解速率的限制随 TDS 的增加而增加。两种实际水样(河水和油田采出水)中添加硼后用 EC 处理,结果表明,在 2 小时内,河水(C=10mg/L,电流=0.2A)中硼的去除率高达 50%,采出水(C=50mg/L,电流=1.0A)中硼的去除率高达 80%。