Refinery and concentration of nutrients from urine with electrodialysis enabled by upstream precipitation and nitrification

被引:55
作者
De Paepe, Jolien [1 ,2 ]
Lindeboom, Ralph E. F. [1 ,3 ]
Vanoppen, Mariolein [4 ]
De Paepe, Kim [1 ]
Demey, Dries [5 ]
Coessens, Wout [1 ]
Lamaze, Brigitte [6 ]
Verliefde, Arne R. D. [4 ]
Clauwaert, Peter [1 ]
Vlaeminck, Siegfried E. [1 ,7 ]
机构
[1] Univ Ghent, Ctr Microbial Ecol & Technol, Fac Biosci Engn, Coupure Links 653, B-9000 Ghent, Belgium
[2] Univ Autonoma Barcelona, Dept Engn Quim Biol & Ambiental, Escola Engn, Barcelona 08193, Spain
[3] Delft Univ Technol, Fac Civil Engn & Geosci, Dept Water Management, Sect Sanit Engn, Stevinweg 1, NL-2628 CN Delft, Netherlands
[4] Univ Ghent, Fac Biosci Engn, Particle & Interfacial Technol Grp PaInt, Coupure Links 653, B-9000 Ghent, Belgium
[5] QinetiQ Space, Hogenakkerhoekstr 9, B-9150 Kruibeke, Belgium
[6] ESTEC, ESA, Keplerlaan 1, NL-2200 Noordwijk, Netherlands
[7] Univ Antwerp, Dept Biosci Engn, Res Grp Sustainable Energy Air & Water Technol, Groenenborgerlaan 171, B-2020 Antwerp, Belgium
关键词
Source separation; Resource recovery; MBBR; MBR; Electrodialysis; SOURCE-SEPARATED URINE; ION-EXCHANGE MEMBRANES; NITROSOMONAS-EUTROPHA; RECOVERY; SALT; DENITRIFICATION; CLASSIFICATION; OZONATION;
D O I
10.1016/j.watres.2018.07.016
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Human urine is a valuable resource for nutrient recovery, given its high levels of nitrogen, phosphorus and potassium, but the compositional complexity of urine presents a challenge for an energy-efficient concentration and refinery of nutrients. In this study, a pilot installation combining precipitation, nitrification and electrodialysis (ED), designed for one person equivalent (1.2 L-urine d(-l)), was continuously operated for similar to 7 months. First, NaOH addition yielded calcium and magnesium precipitation, preventing scaling in ED. Second, a moving bed biofilm reactor oxidized organics, preventing downstream biofouling, and yielded complete nitrification on diluted urine (20-40%, i.e. dilution factors 5 and 2.5) at an average loading rate of 215 mg N L-1 d(-1). Batch tests demonstrated the halotolerance of the nitrifying community, with nitrification rates not affected up to an electrical conductivity of 40 mS cm(-1) and gradually decreasing, yet ongoing, activity up to 96 mS cm(-1) at 18% of the maximum rate. Next-generation 16S rRNA gene amplicon sequencing revealed that switching from a synthetic influent to real urine induced a profound shift in microbial community and that the AOB community was dominated by halophilic species closely related to Nitrosomonas aestuarii and Nitrosomonas marina. Third, nitrate, phosphate and potassium in the filtered (0.1 mu m) bioreactor effluent were concentrated by factors 43, 2.6 and 4.6, respectively, with ED. Doubling the urine concentration from 20% to 40% further increased the ED recovery efficiency by similar to 10%. Batch experiments at pH 6, 7 and 8 indicated a more efficient phosphate transport to the concentrate at pH 7. The newly proposed three-stage strategy opens up opportunities for energy- and chemical-efficient nutrient recovery from urine. Precipitation and nitrification enabled the long-term continuous operation of ED on fresh urine requiring minimal maintenance, which has, to the best of our knowledge, never been achieved before. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:76 / 86
页数:11
相关论文
共 53 条
[1]   Sodium chloride removal from urine via a six-compartment ED cell for use in Advanced Life Support Systems (Part 2:: Limiting current density behavior) [J].
Aponte, VM ;
Colón, G .
DESALINATION, 2001, 140 (02) :133-144
[2]   Effect of Elevated Salt Concentrations on the Aerobic Granular Sludge Process: Linking Microbial Activity with Microbial Community Structure [J].
Bassin, J. P. ;
Pronk, M. ;
Muyzer, G. ;
Kleerebezem, R. ;
Dezotti, M. ;
van Loosdrecht, M. C. M. .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 2011, 77 (22) :7942-7953
[3]   Effect of different salt adaptation strategies on the microbial diversity, activity, and settling of nitrifying sludge in sequencing batch reactors [J].
Bassin, Joao Paulo ;
Kleerebezem, Robbert ;
Muyzer, Gerard ;
Rosado, Alexandre Soares ;
van Loosdrecht, Mark C. M. ;
Dezotti, Marcia .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 2012, 93 (03) :1281-1294
[4]   Plant uptake of phosphorus and nitrogen recycled from synthetic source-separated urine [J].
Bonvin, Christophe ;
Etter, Bastian ;
Udert, Kai M. ;
Frossard, Emmanuel ;
Nanzer, Simone ;
Tamburini, Federica ;
Oberson, Astrid .
AMBIO, 2015, 44 :S217-S227
[5]  
Brown D. L., 1963, AMRLTDR63, P56
[6]  
Bucur B, 2006, REV ROUM CHIM, V51, P101
[7]   Nitrogen cycling in Bioregenerative Life Support Systems: Challenges for waste refinery and food production processes [J].
Clauwaert, Peter ;
Muys, Maarten ;
Alloul, Abbas ;
De Paepe, Jolien ;
Luther, Amanda ;
Sun, Xiaoyan ;
Ilgrande, Chiara ;
Christiaens, Marlies E. R. ;
Hu, Xiaona ;
Zhang, Dongdong ;
Lindeboom, Ralph E. F. ;
Sas, Benedikt ;
Rabaey, Korneel ;
Boon, Nico ;
Ronsse, Frederik ;
Geelen, Danny ;
Vlaeminck, Siegfried E. .
PROGRESS IN AEROSPACE SCIENCES, 2017, 91 :87-98
[8]   Nitrification and microalgae cultivation for two-stage biological nutrient valorization from source separated urine [J].
Coppens, Joeri ;
Lindeboom, Ralph ;
Muys, Maarten ;
Coessens, Wout ;
Alloul, Abbas ;
Meerbergen, Ken ;
Lievens, Bart ;
Clauwaert, Peter ;
Boon, Nico ;
Vlaeminck, Siegfried E. .
BIORESOURCE TECHNOLOGY, 2016, 211 :41-50
[9]   Effect of salinity on nitrification efficiency and structure of ammonia-oxidizing bacterial communities in a submerged fixed bed bioreactor [J].
Cortes-Lorenzo, C. ;
Rodriguez-Diaz, M. ;
Sipkema, D. ;
Juarez-Jimenez, B. ;
Rodelas, B. ;
Smidt, H. ;
Gonzalez-Lopez, J. .
CHEMICAL ENGINEERING JOURNAL, 2015, 266 :233-240
[10]   Effects of Salt on Microbial Populations and Treatment Performance in Purifying Saline Sewage Using the MUCT Process [J].
Cui, Youwei ;
Peng, Changyao ;
Peng, Yongzhen ;
Ye, Liu .
CLEAN-SOIL AIR WATER, 2009, 37 (08) :649-656