Trojanowicz K, Plaza E, Trela J
a Department of Environmental Engineering , St. Pigon Krosno State College , Krosno , Poland.
b Department of Sustainable Development, Environmental Science and Engineering , Royal Institute of Technology (KTH) , Stockholm , Sweden.
Environ Technol. 2019 Apr;40(9):1079-1100. doi: 10.1080/09593330.2017.1397765. Epub 2017 Nov 9.
In the paper, the extension of mathematical model of partial nitritation-anammox process in a moving bed biofilm reactor (MBBR) is presented. The model was calibrated with a set of kinetic, stoichiometric and biofilm parameters, whose values were taken from the literature and batch tests. The model was validated with data obtained from: laboratory batch experiments, pilot-scale MBBR for a reject water deammonification operated at Himmerfjärden wastewater treatment and pilot-scale MBBR for mainstream wastewater deammonification at Hammarby Sjöstadsverk research facility, Sweden. Simulations were conducted in AQUASIM software. The proposed, extended model proved to be useful for simulating of partial nitritation/anammox process in biofilm reactor both for reject water and mainstream wastewater at variable substrate concentrations (influent total ammonium-nitrogen concentration of 530 ± 68; 45 ± 2.6 and 38 ± 3 gN/m - for reject water - and two cases of mainstream wastewater treatment, respectively), temperature (24 ± 2.8; 15 ± 1.1 and 18 ± 0.5°C), pH (7.8 ± 0.2; 7.3 ± 0.1 and 7.4 ± 0.1) and aeration patterns (continuous aeration and intermittent aeration with variable dissolved oxygen concentrations and length of aerated and anoxic phases). The model can be utilized for optimizing and testing different operational strategies of deammonification process in biofilm systems.
本文介绍了移动床生物膜反应器(MBBR)中部分亚硝化-厌氧氨氧化工艺数学模型的扩展。该模型用一组动力学、化学计量学和生物膜参数进行了校准,这些参数值取自文献和批次试验。该模型用从以下方面获得的数据进行了验证:实验室批次实验、希默菲耶尔登废水处理厂运行的用于垃圾渗滤液脱氨的中试规模MBBR,以及瑞典哈马比 Sjöstadsverk 研究设施中用于主流废水脱氨的中试规模MBBR。模拟在AQUASIM软件中进行。所提出的扩展模型被证明可用于模拟生物膜反应器中部分亚硝化/厌氧氨氧化工艺,无论是对于垃圾渗滤液还是主流废水,在可变底物浓度(垃圾渗滤液进水总铵氮浓度为530±68、45±2.6和38±3 gN/m³,以及主流废水处理的两种情况)、温度(24±2.8、15±1.1和18±0.5°C)、pH值(7.8±0.2、7.3±0.1和7.4±0.1)以及曝气模式(连续曝气和具有可变溶解氧浓度以及曝气和缺氧阶段长度的间歇曝气)下。该模型可用于优化和测试生物膜系统中脱氨工艺的不同运行策略。