Wagner Monika, Brumelis Daina, Gehr Ronald
Department of Civil Engineering, McGill University, Montreal, QC, Canada.
Water Environ Res. 2002 Jan-Feb;74(1):33-50. doi: 10.2175/106143002x139730.
The Montreal Urban Community Wastewater Treatment Plant (MUCWTP) located in Montreal. Quebec, Canada, uses physicochemical treatment processes prior to discharging wastewater into the St. Lawrence River via an outfall tunnel of 2 hours retention time. Although chlorination facilities exist, they are not being used, and the MUCWTP is seeking alternative methods for disinfection to achieve a 2- to 3-log fecal coliform reduction. Liquid chemical disinfectants were attractive options because of their low capital costs. This led to an investigation of the feasibility of using hydrogen peroxide or peracetic acid. A method for measuring peroxycompounds (hydrogen peroxide or peracetic acid plus hydrogen peroxide) was developed using the peroxidase-based oxidation of 2,2'-azino-bis(3-ethylbenz-thiazoline-6-sulfuric acid) diammonium salt (ABTS) with hydrogen peroxide. The validity of the method was confirmed using effluent from the MUCWTP. Recovery was higher than 90% for peracetic acid levels as low as 1.0 mg/L. Quenching of hydrogen peroxide was achieved with 50-mg/L catalase; quenching of peracetic acid was achieved with 100 mg/L of sodium thiosulfate, followed by 50 mg/L of catalase. Batch disinfection tests were conducted on MUCWTP effluent. Hydrogen peroxide and peracetic acid in wastewater over time could be modeled as a second-order decay, with the decay "constant" being a function of the initial concentration of peroxycompounds. This function was the same for both hydrogen peroxide and peracetic acid, possibly indicating similar decomposition pathways in wastewater matrices. Disinfection was modeled using a modified Hom equation. Required doses of hydrogen peroxide to reach the target fecal coliform levels ranged from 106 to 285 mg/L, with the higher doses occurring when ferric chloride instead of alum was used as the coagulant. Hence, hydrogen peroxide was infeasible as a disinfectant for this application. On the other hand, the peracetic acid dose needed to achieve the target fecal coliform level was only 0.6 to 1.6 mg/L. Therefore, peracetic acid seems to be a promising disinfectant for physicochemical or primary effluent, or combined sewer overflows.
位于加拿大魁北克省蒙特利尔市的蒙特利尔城市社区污水处理厂(MUCWTP),在通过一条具有2小时停留时间的排污隧道将废水排放到圣劳伦斯河之前,采用物理化学处理工艺。尽管存在氯化设施,但并未使用,MUCWTP正在寻求替代消毒方法,以实现粪便大肠菌群减少2至3个对数级。液体化学消毒剂因其较低的资本成本而成为有吸引力的选择。这导致了对使用过氧化氢或过氧乙酸可行性的研究。开发了一种基于过氧化物酶氧化2,2'-联氮-双(3-乙基苯并噻唑啉-6-磺酸)二铵盐(ABTS)与过氧化氢来测量过氧化物(过氧化氢或过氧乙酸加过氧化氢)的方法。使用MUCWTP的出水确认了该方法的有效性。对于低至1.0mg/L的过氧乙酸水平,回收率高于90%。用50mg/L过氧化氢酶实现过氧化氢的淬灭;用100mg/L硫代硫酸钠,随后用50mg/L过氧化氢酶实现过氧乙酸的淬灭。对MUCWTP的出水进行了间歇消毒试验。废水中过氧化氢和过氧乙酸随时间的变化可以模拟为二级衰减,衰减“常数”是过氧化物初始浓度的函数。过氧化氢和过氧乙酸的这个函数相同,这可能表明在废水基质中有相似的分解途径。使用修正的霍姆方程对消毒进行建模。达到目标粪便大肠菌群水平所需的过氧化氢剂量范围为106至285mg/L,当使用氯化铁而非明矾作为混凝剂时剂量较高。因此,过氧化氢作为该应用的消毒剂不可行。另一方面,实现目标粪便大肠菌群水平所需的过氧乙酸剂量仅为0.6至1.6mg/L。因此,过氧乙酸似乎是物理化学或一级出水或合流制溢流污水的一种有前景的消毒剂。