Nitrogen removal performance of municipal reverse osmosis concentrate with low C/N ratio by membrane-aerated biofilm reactor

Xiao Quan , Kai Huang , Mei Li , Meichao Lan , Baoan Li

Front. Environ. Sci. Eng. ›› 2018, Vol. 12 ›› Issue (6) : 5

PDF (738KB)
Front. Environ. Sci. Eng. ›› 2018, Vol. 12 ›› Issue (6) : 5 DOI: 10.1007/s11783-018-1047-6
RESEARCH ARTICLE
RESEARCH ARTICLE

Nitrogen removal performance of municipal reverse osmosis concentrate with low C/N ratio by membrane-aerated biofilm reactor

Author information +
History +
PDF (738KB)

Abstract

MABR exhibits excellent TN removal performance for treating ROC with low C/N ratio.

Operating conditions should be properly controlled to achieve optimal TN removal.

Denitrifying bacteria and NOB are proved notably inhibited by high salinity stress.

The TN removal rate remains over 70% when the NaCl addition amount is below 20 g/L.

A membrane-aerated biofilm reactor was employed to investigate the nitrogen removal of one typical municipal reverse osmosis(RO) concentrate with a high total nitrogen (TN) concentration and a low C/N ratio. The effects of operational conditions, including the aeration pressure, the hydraulic retention time and the C/N ratio, on the systematic performance were evaluated. The nitrogen removal mechanism was evaluated by monitoring the effluent concentrations of nitrogen contents. Furthermore, the microbial tolerance with elevated salinity was identified. The results indicated that the optimal TN removal efficiency of 79.2% was achieved of the aeration pressure of 0.02 MPa, hydraulic retention time of 24 h, and the C/N ratio of 5.8, respectively. It is essential to supplement the carbon source for the targeted RO concentrate to promote the denitrification process. The inhibitory effect of salinity on denitrifying bacteria and nitrite oxidizing bacteria was significant, revealing the limited TN removal capacity of the conditions in this work. The TN removal efficiency remained more than 70% with the addition of salt (NaCl) amount below 20 g/L. This work preliminarily demonstrated the MABR feasibility for the nitrogen removal of municipal RO concentrate with low C/N ratio and provided technical guidance for further scale-up application.

Graphical abstract

Keywords

Membrane-aerated biofilm reactor (MABR) / Salinity / Total nitrogen / Reverse osmosis concentrate

Cite this article

Download citation ▾
Xiao Quan, Kai Huang, Mei Li, Meichao Lan, Baoan Li. Nitrogen removal performance of municipal reverse osmosis concentrate with low C/N ratio by membrane-aerated biofilm reactor. Front. Environ. Sci. Eng., 2018, 12(6): 5 DOI:10.1007/s11783-018-1047-6

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

Benner J, Salhi E, Ternes T, von Gunten U (2008). Ozonation of reverse osmosis concentrate: Kinetics and efficiency of beta blocker oxidation. Water Research, 42(12): 3003–3012

[2]

Boczkaj G, Fernandes A (2017). Wastewater treatment by means of advanced oxidation processes at basic pH conditions: A review. Chemical Engineering Journal, 320: 608–633

[3]

Brindle K, Stephenson T, Semmens M J (1998). Nitrification and oxygen utilisation in a membrane aeration bioreactor. Journal of Membrane Science, 144(1–2): 197–209

[4]

Cole A C, Semmens M J, LaPara T M (2004). Stratification of activity and bacterial community structure in biofilms grown on membranes transferring oxygen. Applied and Environmental Microbiology, 70(4): 1982–1989

[5]

Deorsola A B, Camarinha G C, Carvalho D D, Jr G L (2013). Biological treatment of saline wastewaters in an aerobic sequencing batch reactor. Environmental Progress & Sustainable Energy, 32(2): 198–205

[6]

Dialynas E, Mantzavinos D, Diamadopoulos E (2008). Advanced treatment of the reverse osmosis concentrate produced during reclamation of municipal wastewater. Water Research, 42(18): 4603–4608

[7]

Downing L S, Nerenberg R (2008). Effect of oxygen gradients on the activity and microbial community structure of a nitrifying, membrane-aerated biofilm. Biotechnology and Bioengineering, 101(6): 1193–1204

[8]

Hwang J H, Cicek N, Oleszkiewicz J (2009). Effect of loading rate and oxygen supply on nitrification in a non-porous membrane biofilm reactor. Water Research, 43(13): 3301–3307

[9]

Kim I H, Lee S I, Kim D K (2016). Biological treatment of reverse osmosis concentrate from low salinity water. Desalination Water Treatment, 57(17): 7667–7678

[10]

Kumar M, Lee P Y, Fukusihma T, Whang L M, Lin J G (2012). Effect of supplementary carbon addition in the treatment of low C/N high-technology industrial wastewater by MBR. Bioresource Technology, 113(4): 148–153

[11]

LaPara T M, Cole A C, Shanahan J W, Semmens M J (2006). The effects of organic carbon, ammoniacal-nitrogen, and oxygen partial pressure on the stratification of membrane-aerated biofilms. Journal of Industrial Microbiology & Biotechnology, 33(4): 315–323

[12]

Li P, Zhao D X, Zhang Y G, Sun L Q, Zhang H M, Lian M R, Li B A (2015). Oil-field wastewater treatment by hybrid membrane-aerated biofilm reactor (MABR) system. Chemical Engineering Journal, 264: 595–602

[13]

Liu S, Yang F, Gong Z, Su Z (2008). Assessment of the positive effect of salinity on the nitrogen removal performance and microbial composition during the start-up of CANON process. Applied Microbiology and Biotechnology, 80(2): 339–348

[14]

Long D N, Schäfer A I (2006). Critical risk points of nanofiltration and reverse osmosis processes in water recycling applications. Desalination, 187(1–3): 303–312

[15]

Malaeb L, Ayoub G M (2011). Reverse osmosis technology for water treatment: State of the art review. Desalination, 267(1): 1–8

[16]

Mannina G, Cosenza A, Di Trapani D, Capodici M, Viviani G (2016). Membrane bioreactors for treatment of saline wastewater contaminated by hydrocarbons (diesel fuel): An experimental pilot plant case study. Chemical Engineering Journal, 291: 269–278

[17]

Mosquera-Corral A, González F, Campos J L, Méndez R (2005). Partial nitrification in a SHARON reactor in the presence of salts and organic carbon compounds. Process Biochemistry, 40(9): 3109–3118

[18]

Muruganandham M, Suri R, Jafari S, Sillanpää M, Lee G J, Wu J J, Swaminathan M (2014). Recent developments in homogeneous advanced oxidation processes for water and wastewater treatment. International Journal of Photoenergy,2014(2): 164–167

[19]

Nogueira R, Melo L F, Purkhold U, Wuertz S, Wagner M (2002). Nitrifying and heterotrophic population dynamics in biofilm reactors: Effects of hydraulic retention time and the presence of organic carbon. Water Research, 36(2): 469–481

[20]

Pérez-González A, Urtiaga A M, Ibáñez R, Ortiz I (2012). State of the art and review on the treatment technologies of water reverse osmosis concentrates. Water Research, 46(2): 267–283

[21]

Pradhan S, Fan L, Roddick F A (2015). Removing organic and nitrogen content from a highly saline municipal wastewater reverse osmosis concentrate by UV/H2O2-BAC treatment. Chemosphere, 136: 198–203

[22]

Rodríguez F A, Reboleiro-Rivas P, González-López J, Hontoria E, Poyatos J M (2012). Comparative study of the use of pure oxygen and air in the nitrification of a MBR system used for wastewater treatment. Bioresource Technology, 121: 205–211

[23]

Shanahan J W, Semmens M J (2004). Multipopulation model of membrane-aerated biofilms. Environmental Science & Technology, 38(11): 3176–3183

[24]

She Z L, Zhao L T, Zhang X L, Jin C J, Guo L, Yang S Y, Zhao Y G, Gao M C (2016). Partial nitrification and denitrification in a sequencing batch reactor treating high-salinity wastewater. Chemical Engineering Journal, 288: 207–215

[25]

Sliekers A O, Haaijer S C M, Stafsnes M H, Kuenen J G, Jetten M S M (2005). Competition and coexistence of aerobic ammonium- and nitrite-oxidizing bacteria at low oxygen concentrations. Applied Microbiology and Biotechnology, 68(6): 808–817

[26]

Sun L Q, Wang Z Y, Wei X, Li P, Zhang H M, Li M, Li B A, Wang S C (2015). Enhanced biological nitrogen and phosphorus removal using sequencing batch membrane-aerated biofilm reactor. Chemical Engineering Science, 135: 559–565

[27]

Syron E, Casey E (2008). Membrane-aerated biofilms for high rate biotreatment: performance appraisal, engineering principles, scale-up, and development requirements. Environmental Science & Technology, 42(6): 1833–1844

[28]

Tian H L, Liu J, Feng T T, Li H F, Wu X L, Li B A (2017). Assessing the performance and microbial structure of biofilms adhering on aerated membranes for domestic saline sewage treatment. RSC Advances, 7(44): 27198–27205

[29]

Tian H L, Zhang H M, Li P, Sun L Q, Hou F F, Li B A (2015). Treatment of pharmaceutical wastewater for reuse by coupled membrane-aerated biofilm reactor (MABR) system. RSC Advances, 5(85): 69829–69838

[30]

Vendramel S M R, Justo A, González O, Sans C, Esplugas S (2013). Reverse osmosis concentrate treatment by chemical oxidation and moving bed biofilm processes. Water Science Technology, 68(11): 2421–2426

[31]

Wang Z, Luo G, Li J, Chen S Y, Li Y, Li W T, Li A M (2016). Response of performance and ammonia oxidizing bacteria community to high salinity stress in membrane bioreactor with elevated ammonia loading. Bioresource Technology, 216: 714–721

[32]

Yang X, Wang S, Zhou L (2012). Effect of carbon source, C/N ratio, nitrate and dissolved oxygen concentration on nitrite and ammonium production from denitrification process by Pseudomonas stutzeri D6. Bioresource Technology, 104(1): 65–72

[33]

Zhao C, Gu P, Cui H, Zhang G (2012). Reverse osmosis concentrate treatment via a PAC-MF accumulative countercurrent adsorption process. Water Research, 46(1): 218–226

[34]

Zhou M H, Liu L, Jiao Y L, Wang Q, Tan Q Q (2011a). Treatment of high-salinity reverse osmosis concentrate by electrochemical oxidation on BDD and DSA electrodes. Desalination, 277(1–3): 201–206

[35]

Zhou T, Lim T T, Chin S S, Fane A G (2011a). Treatment of organics in reverse osmosis concentrate from a municipal wastewater reclamation plant: Feasibility test of advanced oxidation processes with/without pretreatment. Chemical Engineering Journal, 166(3): 932–939

RIGHTS & PERMISSIONS

Higher Education Press and Springer-Verlag GmbH Germany, part of Springer Nature

AI Summary AI Mindmap
PDF (738KB)

3230

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/