An Oxic–Hydrolytic–Oxic Process at the Nexus of Sludge Spatial Segmentation, Microbial Functionality, and Pollutants Removal in the Treatment of Coking Wastewater
Chaohai Wei, Chaohai Wei, Zemin Li, Jianxin Pan, Bingbing Fu, Jingyue Wei, Ben Chen, Xingzhou Yang, Guojie Ye, Cong Wei, Cong Wei, Pei Luo, Chaofei Wu, Guanglei Qiu, Haizhen Wu
Abstract
Toxic inhibition and wash-out of nitrifying bacteria in traditional single-activated sludge processes frequently cause instability of nitrification in industrial wastewater treatment and limit the total nitrogen (TN) removal efficiency. A novel oxic–hydrolytic–oxic (O/H/O) process based on a three-sludge regime was developed to treat coking wastewater with a high C/N ratio and biological toxicity. The results demonstrated that high COD removal (89.6%, 91.3%, 90.4%, and 87.1% in four different modes) was achieved with the complete elimination of phenol, sulfide, total cyanide, and thiocyanate. TN removal varied from 14.0% to 88.7% at an influent flow of 1.6–2.0 kg of COD m–3 day–1, depending on prenitrification, internal recycling, and the presence of a sufficient carbon source for denitrification. The first oxic (O1) and hydrolytic (H) reactors made predominant contributions to the removal of organic and toxic pollutants. The removal of these pollutants guaranteed a stable and favorable environment for nitrification in the second oxic (O2) reactor, in which high ammonium removal was observed because of the predominance of Nitrosomonas and Nitrospira. The O/H/O process has the potential to become a promising industrial wastewater treatment process because it promotes functions that are independent of microbial and process stability with respect to the removal of pollutants, especially nitrogen.