Tait Stephan, Clarke William P, Keller Jurg, Batstone Damien J
Advanced Water Management Centre, School of Engineering, University of Queensland, St Lucia, Queensland 4072, Australia.
Water Res. 2009 Feb;43(3):762-72. doi: 10.1016/j.watres.2008.11.008. Epub 2008 Nov 21.
Sulfate causes considerable problems in anaerobic digesters, related to generation of sulfides, loss of electrons (and hence methane), and contamination of gas streams. Removal of sulfides is generally expensive, and still results in methane losses. In this paper, we evaluate the use of precipitation for low-cost sulfate removal, in highly contaminated streams (>1 gS L(-1)). The main precipitate assessed is calcium sulfate (gypsum), though the formation of complex precipitates such as jarosite and ettringite to remove residual sulfate is also evaluated. The four main concerns in contaminated wastewater are:- high solubility, caused by high ion activity and ion pairing; slow kinetics; inhibition of nucleation; and poisoning of crystals by impurities, rendering product unsuitable for reuse as seed. These concerns were addressed through batch experiments on a landfill wastewater with a similar composition to other sulfate rich industrial wastewaters (high levels of organic and inorganic contaminants). Crystallisation rates were rapid and comparable to what is observed by others for pure solutions (2-5 h). The kinetics of crystallisation showed a 2nd order dependence on supersaturation, which have implications for crystalliser design, as discussed in the paper. No spontaneous nucleation was observed (seed was required). Seed poisoning did not occur, and product crystals were as effective as pure seed. Solubility was increased by an order of magnitude compared to a pure solution (2.6x10(-3) M2 vs. 0.22x10(-3) M2). As evaluated using equilibrium modelling, this was caused equally by non-specific ion activity, and specific ion pairing. Jarosite and ettringite could not be formed at reasonable pH and temperature levels. Given the lack of complex precipitates, and relatively high solubility, gypsum crystallisation cannot practically be used to remove sulfate to very low levels, and gas-sulfide treatment will likely still be required. It can however, be used for low-cost bulk removal of sulfate.
硫酸盐在厌氧消化池中会引发诸多问题,这些问题与硫化物的产生、电子损失(进而导致甲烷损失)以及气流污染有关。去除硫化物通常成本高昂,且仍会造成甲烷损失。在本文中,我们评估了在高污染水流(>1 gS L⁻¹)中采用沉淀法低成本去除硫酸盐的可行性。所评估的主要沉淀物是硫酸钙(石膏),不过也对诸如黄钾铁矾和钙矾石等复合沉淀物的形成进行了评估,以去除残留的硫酸盐。受污染废水中的四个主要问题是: - 高溶解度,这是由高离子活性和离子配对导致的;动力学缓慢;成核抑制;以及杂质对晶体的毒害,使得产物不适宜作为晶种回用。通过对一种成分与其他富含硫酸盐的工业废水(含有高浓度有机和无机污染物)相似的垃圾填埋场废水进行批次实验,解决了这些问题。结晶速率很快,与其他人在纯溶液中观察到的速率相当(2 - 5小时)。结晶动力学显示对过饱和度呈二级依赖关系,正如本文所讨论的,这对结晶器设计具有重要意义。未观察到自发成核现象(需要晶种)。晶种未出现中毒现象,产物晶体与纯晶种一样有效。与纯溶液相比,溶解度增加了一个数量级(2.6×10⁻³ M² 对 0.22×10⁻³ M²)。如通过平衡模型评估所示,这同样是由非特异性离子活性和特异性离子配对导致的。在合理的pH和温度水平下无法形成黄钾铁矾和钙矾石。鉴于缺乏复合沉淀物且溶解度相对较高,石膏结晶实际上无法用于将硫酸盐去除至极低水平,可能仍需要进行气体硫化物处理。然而,它可用于低成本的大量硫酸盐去除。