An investigation of a process for partial nitrification and autotrophic denitrification combined desulfurization in a single biofilm reactor

2013 ◽  
Vol 24 (6) ◽  
pp. 843-853 ◽  
Author(s):  
Zhiwei Liang ◽  
Hanli Xu ◽  
Yunlong Wang ◽  
Shangyuan Yang ◽  
Ping Du
Membranes ◽  
2021 ◽  
Vol 11 (12) ◽  
pp. 911
Author(s):  
Kun Dong ◽  
Xinghui Feng ◽  
Wubin Wang ◽  
Yuchao Chen ◽  
Wei Hu ◽  
...  

Low C/N wastewater results from a wide range of factors that significantly harm the environment. They include insufficient carbon sources, low denitrification efficiency, and NH4+-N concentrations in low C/N wastewater that are too high to be treated. In this research, the membrane biofilm reactor and hydrogen-based membrane biofilm reactor (MBR-MBfR) were optimized and regulated under different operating parameters: the simulated domestic sewage with low C/N was domesticated and the domestic sewage was then denitrified. The results of the MBR-MBfR experiments indicated that a C/N ratio of two was suitable for NH4+-N, NO2−-N, NO3−-N, and chemical oxygen demand (COD) removal in partial nitrification-denitrification (PN-D) and hydrogen autotrophic denitrification for further treatment. The steady state for domestic wastewater was reached when the MBR-MBfR in the experimental conditions of HRT = 15 h, SRT = 20 d, 0.04 Mpa for H2 pressure in MBfR, 0.4–0.8 mg/L DO in MBR, MLSS = 2500 mg/L(MBR) and 2800 mg/L(MBfR), and effluent concentrations of NH4+-N, NO3−-N, and NO2−-N were 4.3 ± 0.5, 1.95 ± 0.04, and 2.05 ± 0.15 mg/L, respectively. High-throughput sequencing results revealed the following: (1) The genus Nitrosomonas as the ammonia oxidizing bacteria (AOB) and Denitratisoma as potential denitrifiers were simultaneously enriched in the MBR; (2) at the genus level, Meiothermus,Lentimicrobium, Thauera,Hydrogenophaga, and Desulfotomaculum played a dominant role in leading to NO3−-N and NO2−-N removal in the MBfR.


2010 ◽  
Vol 52 (1) ◽  
pp. 7-18 ◽  
Author(s):  
César Huiliñir ◽  
Rodrigo Romero ◽  
Carlos Muñoz ◽  
Christian Bornhardt ◽  
Marlene Roeckel ◽  
...  

2013 ◽  
Vol 217 ◽  
pp. 435-441 ◽  
Author(s):  
Qiang Kong ◽  
Jian Zhang ◽  
Mingsheng Miao ◽  
Lin Tian ◽  
Ning Guo ◽  
...  

Water ◽  
2021 ◽  
Vol 13 (18) ◽  
pp. 2484
Author(s):  
César Huiliñir ◽  
Vivian Fuentes ◽  
Carolina Estuardo ◽  
Christian Antileo ◽  
Ernesto Pino-Cortés

This work aimed to achieve partial nitrification (PN) in a Sequencing Moving Bed Biofilm Reactor SMBBR with zeolite as a biomass carrier by using sulfide pulses in the presence of organic matter as an inhibitor. Two conditions were evaluated: sulfide (HS−) = 5 mg S/L and vvm (air volume per liquid volume per minute, L of air L−1 of liquid min−1) = 0.1 (condition 1); and a HS− = 10 mg S/L and a vvm = 0.5 (condition 2). The simultaneous effect of organic matter and sulfide was evaluated at a Chemical Oxygen Demand (COD) = 350 mg/L and HS− = 5 mg S/L, with a vvm = 0.5. As a result, using the sulfide pulse improved the nitrite accumulation in both systems. However, Total Ammonia Nitrogen (TAN) oxidation in both processes decreased by up to 60%. The simultaneous presence of COD and sulfide significantly reduced the TAN and nitrite oxidation, with a COD removal yield of 80% and sulfide oxidation close to 20%. Thus, the use of a sulfide pulse enabled PN in a SMBBR with zeolite. Organic matter, together with the sulfide pulse, almost completely inhibited the nitrification process despite using zeolite.


2020 ◽  
Author(s):  
Patricia Perez ◽  
Emily Clements ◽  
Cristian Picioreanu ◽  
Robert nerenberg

<p>The membrane aerated biofilm reactor (MABR) is an emerging wastewater treatment technology that can greatly decrease energy requirements for wastewater treatment. It consists of cassettes of air-supplying, hollow-fiber membranes that can retrofit existing activated sludge processes. MABR behavior differs from conventional biofilm processes due to the counter-diffusion of the electron donor (ammonia) and acceptor (oxygen).</p> <p> </p> <p>Partial nitrification (PN), or partial nitrification Anammox (PNA), can further improve MABR energy efficiency and cost effectiveness.  To achieve this, ammonia oxidizing bacteria (AOB) must outcompete nitrite-oxidizing bacteria (NOB).  High temperatures favor AOB, but it is not feasible to heat the wastewater influent.  However, high-temperature compressed air can be supplied to the membrane lumen, increasing temperatures inside the biofilm without increasing the bulk temperatures. No previous research has addressed temperature gradients in biofilms, which can lead to gradients in  biodegradation kinetics, diffusivities, and O<sub>2</sub> solubility.</p> <p> </p> <p>The objective of this research was to explore the effect of temperature gradients in MABR biofilms, especially with respect to PN. We used a one-dimensional multi-species biofilm model, which considers the MABR physical and biochemical behavior, especially with respect to temperature. The model was implemented using COMSOL Multiphysics. We also used bench-scale experiments to explore the effect of biofilm temperature gradients on MABR nitrification and PN performances and microbial community structure.</p> <p> </p> <p>Model simulations showed that MABR biofilms exposed to a temperature gradient from 20 ºC (biofilm interior) to 10 ºC (bulk liquid) had a 60% increase in nitrification rates compared with biofilms at 10 ºC. More importantly, the model predicted a complete out competition of NOBs within the biofilm.</p> <p> </p> <p>Preliminary experimental results confirm a significant (105%) increase in nitrification fluxes with a temperature of 30ºC compared to ambient temperatures (20ºC). Future experiments will validate the model predicted effects of biofilm temperature gradients on nitrification fluxes and microbial community structure.</p>


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