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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2019, Vol. 13 Issue (5) : 69    https://doi.org/10.1007/s11783-019-1153-0
RESEARCH ARTICLE
Enhanced nitrification in integrated floating fixed-film activated sludge (IFFAS) system using novel clinoptilolite composite carrier
Aoshuang Jing, Tao Liu, Xie Quan(), Shuo Chen, Yaobin Zhang
Key Laboratory of Industrial Ecology and Environmental Engineering (Ministry of Education), School of Environmental Science and Technology, Dalian University of Technology, Dalian 116024, China
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Abstract

Novel carriers with favorable electrophilicity and hydrophilicity were prepared.

Novel carriers had the capability of nitrification-enhancing.

NH4+-N removal efficiency of IFFAS process rose up to 20% with novel carriers.

Nitrosomonadales and Nitrospirales were identified as the functional nitrifiers.

The population of Nitrospirales increased by 4.51%.

The integrated floating fixed-film activated sludge (IFFAS) process is an ideal preference for nitrification attributing to the longer sludge age for nitrifiers. However, as the core of this process, conventional carriers made of polymer materials usually exhibit negative charge and hydrophobicity on the surface, which is unbeneficial to nitrifying biofilm formation. In this study, novel clinoptilolite composite carriers with favorable hydrophilicity, positive charge and nitrification-enhancing capability were made and implemented in IFFAS system. In comparison with conventional carriers, the novel clinoptilolite composite carriers displayed positive charges on the surface (11.7±1.1 mV, pH 7.0) with increased hydrophilicity (surface contact angle dropped to 76.7°). The novel-carriers-based reactors achieved significantly better NH4+-N removal efficiency at different influent concentrations, dissolved oxygen (DO) levels and shock loads (NH4+-N removal efficiency rose up to 20% comparing with the control reactors filled with polyethylene (PE) carriers or activated sludge). High-throughput sequencing (HTS) results indicated the novel clinoptilolite composite carriers provided favorable niche for more types of bacteria, especially for Nitrosomonadales and Nitrospirales (the functional nitrifiers in the system). The population of Nitrospirales increased by 4.51% by using novel clinoptilolite composite carriers comparing with using PE carriers, which ensured enhanced nitrification process. This study was expected to provide a practical option for enhancing wastewater nitrification performance with the novel clinoptilolite composite carrier.

Keywords Biofilm carrier      Clinoptilolite      Integrated floating fixed-film activated sludge (IFFAS)      Microbial community      Nitrification      Wastewater     
Corresponding Author(s): Xie Quan   
Issue Date: 30 July 2019
 Cite this article:   
Aoshuang Jing,Tao Liu,Xie Quan, et al. Enhanced nitrification in integrated floating fixed-film activated sludge (IFFAS) system using novel clinoptilolite composite carrier[J]. Front. Environ. Sci. Eng., 2019, 13(5): 69.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-019-1153-0
https://academic.hep.com.cn/fese/EN/Y2019/V13/I5/69
Fig.1  Photographs of conventional carriers (a) and novel composite carriers with 1 wt%, 2 wt% and 3 wt% clinoptilolite (b, c and d).
Fig.2  Schematic diagram of reactor used in the experiment.
Carrier type Surface zeta potential Water contact angle Density
Conventional carrier -38.6 mV 95.1° 0.945 g/cm3
Novel carrier
(1 wt% clinoptilolite)
+11.7±1.1 mV 88.5° 0.972 g/cm3
Novel carrier
(2 wt% clinoptilolite)
+11.7±1.1 mV 80.9° 0.978 g/cm3
Novel carrier
(3 wt% clinoptilolite)
+11.7±1.1 mV 76.7° 0.983 g/cm3
Tab.1  Carrier surface properties
Fig.3  Variations of NH4+-N concentrations (a) and COD concentrations (b) at different influent concentrations.
Fig.4  Variations of NH4+-N concentrations (a) and COD concentrations (b) at different DO levels (Run 1: 3.0±0.5 mg/L; Run 2: 2.5±0.5 mg/L; Run 3: 1.5±0.5 mg/L).
Fig.5  Variations of NH4+-N concentrations (a) and COD concentrations (b) at different HRTs.
Fig.6  The proportion of N-compounds in effluent and nitrogen loss of each reactor.
Sample ID Sep num OTU num Shannon index ACE index Chao1 index Coverage Simpson
R1_S 51746 686 3.50 904.22 860.78 1.00 0.07
R2_B 60035 798 3.79 1144.98 1123.23 1.00 0.08
R2_S 44987 646 3.27 858.80 845 1.00 0.10
R3_B 52206 747 3.73 1234.96 1035.19 1.00 0.08
R3_S 34540 601 3.59 826.89 813.74 0.99 0.07
R4_B 44590 689 4.00 939.26 929.19 1.00 0.07
R4_S 42087 637 3.68 1057.57 878.88 0.99 0.09
R5_B 49937 776 4.24 1019.08 967.19 1.00 0.04
R5_S 38111 608 3.80 842.37 843.44 0.99 0.05
Tab.2  Richness and ɑ-diversity of suspended sludge and biofilm samples in reactors
Fig.7  Taxonomic classification of the bacterial communities at phylum level.
Fig.8  Taxonomic classification of the bacterial communities at order level.
Order Nitrosomonadales (AOB) Nitrospirales (NOB)
R1_S 0.01 0.12
R2_B 0.07 1.46
R2_S 0.04 1.07
R3_B 0.02 1.52
R3_S 0.03 0.51
R4_B 0.03 4.06
R4_S 0.02 0.65
R5_B 0.01 5.97
R5_S 0.03 0.53
Tab.3  Functional microorganisms and proportions (%) of the major orders in each sample
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