Department of Civil Engineering, University of Manitoba, Winnipeg, R3T 5V6, Canada.
Water Res. 2010 Apr;44(7):2283-91. doi: 10.1016/j.watres.2009.12.022. Epub 2009 Dec 21.
Membrane biofilm reactors (MBfR) utilize membrane fibers for bubble-less transfer of gas by diffusion and provide a surface for biofilm development. Nitrification and subsequent autotrophic denitrification were carried out in MBfR with pure oxygen and hydrogen supply, respectively, in order to remove nitrogen without the use of heterotrophic bacteria. Excessive biomass accumulation is typically the major cause of system failure of MBfR. No biomass accumulation was detected in the nitrification reactor as low-level discharge of solids from the system balanced out biomass generation. The average specific nitrification rate during 250 days of operation was 1.88gN/m(2)d. The subsequent denitrification reactor, however, experienced decline of performance due to excessive biofilm growth, which prompted the implementation of periodic nitrogen sparging for biofilm control. The average specific denitrification rate increased from 1.50gN/m(2)d to 1.92gN/m(2)d with nitrogen sparging, over 190 days thus demonstrating the feasibility of stable long-term operation. Effluent suspended solids increased immediately following sparging: from an average of 2.5mg/L to 12.7mg/L. This periodic solids loss was found unavoidable, considering the theoretical biomass generation rates at the loadings used. A solids mass balance between the accumulating and scoured biomass was established based on the analysis of the effluent volatile solids data. Biofilm thickness was maintained at an average of 270microm by the gas sparging biofilm control. It was concluded that biomass accumulation and scouring can be balanced in autotrophic denitrification and that long-term stable operation can be maintained.
膜生物膜反应器 (MBfR) 利用膜纤维通过扩散进行无泡气体传递,并提供生物膜生长的表面。硝化和随后的自养反硝化分别在 MBfR 中进行,使用纯氧和氢气供应,以在不使用异养菌的情况下去除氮。过量的生物量积累通常是 MBfR 系统故障的主要原因。由于系统中低水平的固体排放与生物量生成相平衡,因此在硝化反应器中未检测到生物量积累。在 250 天的运行过程中,平均特定硝化速率为 1.88gN/m(2)d。然而,随后的反硝化反应器由于生物膜过度生长而导致性能下降,这促使实施定期氮气喷射以控制生物膜。通过氮气喷射,平均特定反硝化速率从 1.50gN/m(2)d 增加到 1.92gN/m(2)d,超过 190 天,因此证明了稳定长期运行的可行性。喷射后立即增加了出水悬浮固体:从平均 2.5mg/L 增加到 12.7mg/L。考虑到所使用负荷下的理论生物量生成率,这种周期性的固体损失是不可避免的。根据出水挥发性固体数据的分析,建立了积累和冲刷生物量之间的固体质量平衡。通过气体喷射生物膜控制,将生物膜厚度维持在平均 270μm。结论是,自养反硝化过程中可以平衡生物量积累和冲刷,并可以维持长期稳定运行。