Griffith School of Engineering and Build Environment, 170 Kessels Road, Griffith University, Nathan, Queensland, 4111, Australia; Advanced Water Management Centre (AWMC), Level 4, Gehrmann Bldg. (60), Research Road, University of Queensland, Brisbane, Queensland, 4072, Australia.
Advanced Water Management Centre (AWMC), Level 4, Gehrmann Bldg. (60), Research Road, University of Queensland, Brisbane, Queensland, 4072, Australia.
Water Res. 2018 Nov 15;145:660-666. doi: 10.1016/j.watres.2018.08.069. Epub 2018 Aug 31.
Recovery of phosphate from wastewater is challenging, with one of the best opportunities being recovery from sludge anaerobic digestion liquor, as struvite. However, this is limited by the proportion of total phosphorous which is soluble, due to in-digester metal ion precipitation. High-pressure anaerobic digestion may enable enhanced phosphate solubility (and hence recovery potential), without the use of added acid, due to an increased liquid phase CO concentration. This was tested at 2, 4, and 6 bar absolute (bara) vs a 1 bara control reactor, fed with activated sludge. Increased pressure significantly (p = 0.0008), increased the fraction of phosphate that was soluble, ranging from 52% at 1 bara, to 75% at 6 bara. Model based analysis indicated that the main reason for increased solubility was pH depression (down to 6.4 at 6 bara), rather than changes in ion pairing (with carbonates) or increases in ionic activity. However, biological performance was adversely impacted, with a substantial loss in VS and COD destruction (on the order of 5%-10% absolute). No organic acid accumulation was observed. Bacterial and archaeal communities were significantly impacted (p∼0.0003-0.0005), with a shift to specific organisms, including Bacteroidales Rikenellaceae within the bacteria, and a Deep Sea Euryarchaeotal Group at 2 bara, and Methanocellaceae within the archaea at 4 and 6 bara. The work indicates that high-pressure operation is a technically viable option to improve phosphate recovery, and produce a high-methane biogas product, but that the loss of overall conversion needs to be further addressed, possibly through two-stage digestion.
从废水中回收磷酸盐具有挑战性,从污泥厌氧消化液中回收鸟粪石(MgNH4PO4·6H2O)是最佳机会之一。然而,由于内消化器金属离子沉淀,总磷中可溶部分的比例有限。由于液相 CO2 浓度增加,高压厌氧消化可以在不使用外加酸的情况下提高磷酸盐的溶解度(因此提高回收潜力)。这项研究在 2、4 和 6 巴绝对压力(bara)下与 1 巴对照反应器进行了测试,进料为活性污泥。压力的增加显著(p=0.0008)提高了可溶磷酸盐的比例,从 1 巴时的 52%增加到 6 巴时的 75%。基于模型的分析表明,溶解度增加的主要原因是 pH 值降低(在 6 巴时降至 6.4),而不是离子对(与碳酸盐)的变化或离子活度的增加。然而,生物性能受到不利影响,VS 和 COD 破坏有实质性损失(绝对值为 5%-10%)。没有观察到有机酸积累。细菌和古菌群落受到显著影响(p∼0.0003-0.0005),出现了特定生物的转移,包括细菌中的拟杆菌目 Rikenellaceae 和 2 巴时的深海古菌群,以及 4 巴和 6 巴时的甲烷杆菌科。这项工作表明,高压操作是一种可行的技术选择,可以提高磷酸盐的回收效率,并生产高甲烷沼气产品,但需要进一步解决整体转化率的损失,可能需要通过两段式消化来解决。