Effect of the proportion of nitrite on denitrification and N2O release
FU Kunming,, JIN Yiran, LIU Fanqi, QIU Fuguo, CAO Xiuqin Key Laboratory of Urban Storm Water System and Water Environment, Ministry of Education, School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China
Abstract:Aiming at the problem of large amount of N2O release during sewage treatment, the effects of different ${\rm{NO}}_2^ - $-N ratios on the denitrification process and N2O release were studied. At the total nitrogen concentration of 100 mg·L?1, the change of ${\rm{NO}}_2^ - $-N proportion was performed to conduct batch experiment. The reactor denitrification rate and nitrogen index variations were studied. The results show that the denitrification efficiency increased with the increase of the initial ${\rm{NO}}_2^ - $-N ratio, in which the ${\rm{NO}}_2^ - $-N concentration basically increased first and then decreased. The higher the initial ${\rm{NO}}_2^ - $-N ratio, the faster the degradation rate of ${\rm{NO}}_3^ - $-N and the more ${\rm{NO}}_2^ - $-N accumulation. With the increase of the initial ${\rm{NO}}_2^ - $-N ratio, the accumulation rate, maximum accumulation value and conversion rate of N2O both gradually increased. The highest values were 18.828 mg·(g·h)?1, 22.123 mg·L?1 and 24.05%, respectively. As the initial ${\rm{NO}}_2^ - $-N ratio increased, the concentration of free nitrous acid (FNA) increased, resulting in more N2O accumulation. FNA concentration may be the cause of the large N2O accumulation. Key words:nitrite/ denitrification/ free nitrous acid(FNA)/ N2O.
图1不同初始${\bf{NO}}_2^ -$-N占比下反应器内氮素的变化 Figure1.Variations of nitrogen in the bioreactors at different initial ${\rm{NO}}_2^ - $-N concentrations
图2不同初始${\bf{NO}}_2^ - $-N占比下反应器内${\bf{NO}}_3^ - $-N的变化 Figure2.Variations of ${\rm{NO}}_3^ - $-N in the bioreactors at different initial ${\rm{NO}}_2^ - $-N concentrations
图3不同初始${\bf{NO}}_2^ - $-N占比下反应器内${\bf{NO}}_2^ - $-N的变化 Figure3.Variations of ${\rm{NO}}_2^ - $-N in the bioreactors at different initial ${\rm{NO}}_2^ - $-N concentrations
图5不同初始${\bf{NO}}_2^ - $-N占比下各反硝化酶的电子消耗速率和电子分布率 Figure5.Electron consumption rate and distribution rate of denitrification enzymes at different initial ${\rm{NO}}_2^ - $-N concentrations
表1不同初始${\rm{NO}}_2^ - $-N浓度时实验的运行条件 Table1.Operational conditions at different initial ${\rm{NO}}_2^ - $-N concentrations mg·L?1
${\rm{NO}}_x^ - $-N
${\rm{NO}}_2^ - $-N
${\rm{NO}}_3^ - $-N
FNA
100
0
100
0
100
5
95
0.003 9
100
10
90
0.007 7
100
20
80
0.015 4
100
40
60
0.030 8
100
100
0
0.076 9
${\rm{NO}}_x^ - $-N
${\rm{NO}}_2^ - $-N
${\rm{NO}}_3^ - $-N
FNA
100
0
100
0
100
5
95
0.003 9
100
10
90
0.007 7
100
20
80
0.015 4
100
40
60
0.030 8
100
100
0
0.076 9
下载: 导出CSV 表2不同初始${\bf{NO}}_2^ - $-N占比下反应器内N2O动力分析 Table2.Kinetic analysis of bioreactors at different initial ${\rm{NO}}_2^ -\text{-}{\rm{N}}$ concentrations
MONTZKA S A, DLUGOKENCKY E J, BUTLER J H. Non-CO2 greenhouse gases and climate change[J]. Nature, 2011, 476(7358): 43-50. doi: 10.1038/nature10322
[4]
RAVISHANKARA A R. Nitrous oxide (N2O): The dominant ozone-depleting substance emitted in the 21st century[J]. Science, 2009, 326(5949): 123-5. doi: 10.1126/science.1176985
[5]
IPCC. Climate change 2007: The IPCC scientific assessment[R]. Cambridge: Cambridge University Press, 2007.
[6]
PARK K Y, INAMORI Y, MIZUOCHI M, et al. Emission and control of nitrous oxide from a biological wastewater treatment system with intermittent aeration[J]. Journal of Bioscience and Bioengineering, 2000, 90(3): 247-252. doi: 10.1016/S1389-1723(00)80077-8
[7]
PARK K Y, LEE J W, INAMORI Y, et al. Effects of fill modes on N2O emission from the SBR treating domestic wastewater[J]. Water Science and Technology, 2001, 43(3): 147-150. doi: 10.2166/wst.2001.0130
[8]
ZHOU Y, PIJUAN M, J ZENG RAYMOND, et al. Free nitrous acid inhibition on nitrous oxide reduction by a denitrifying-enhanced biological phosphorus removal sludge[J]. Environmental Science & Technology, 2008, 42(22): 8260-8265.
[9]
DUAN H, WANG Q, ERLER D V, et al. Effects of free nitrous acid treatment conditions on the nitrite pathway performance in mainstream wastewater treatment[J]. Science of the Total Environment, 2018, 644: 360-370. doi: 10.1016/j.scitotenv.2018.06.346
[10]
SCHULTHESS R V, GUJER W. Release of nitrous oxide (N2O) from denitrifying activated sludge: Verification and application of a mathematical model[J]. Water Research, 1996, 30(3): 521-530. doi: 10.1016/0043-1354(95)00204-9
PAN Y, YE L, NI B, et al. Effect of pH on N2O reduction and accumulation during denitrification by methanol utilizing denitrifiers[J]. Water Research, 2012, 46(15): 4832-4840. doi: 10.1016/j.watres.2012.06.003
PAN Y, NI B J, BOND P L, et al. Electron competition among nitrogen oxides reduction during methanol-utilizing denitrification in wastewater treatment[J]. Water Research, 2013, 47(10): 3273-3281. doi: 10.1016/j.watres.2013.02.054
[20]
ALMEIDA J S, REIS M A M, CARRONDO M J T. Competition between nitrate and nitrite reduction in denitrification by pseudomonas fluorescens[J]. Biotechnology and Bioengineering, 1995, 46(5): 476-484. doi: 10.1002/bit.260460512
[21]
THOMSEN J K, GEEST T, RAYMOND P C. Mass spectrometric studies of the effect of pH on the accumulation of intermediates in denitrification by paracoccus denitrificans[J]. Applied & Environmental Microbiology, 1994, 60(2): 536-41.
GABARRó J, GONZáLEZ-CáRCAMO P, RUSCALLEDA M, et al. Anoxic phases are the main N2O contributor in partial nitritation reactors treating high nitrogen loads with alternate aeration[J]. Bioresource Technology, 2014, 163: 92-99.
[25]
WANG Q, JIANG G, YE L, et al. Heterotrophic denitrification plays an important role in N2O production from nitritation reactors treating anaerobic sludge digestion liquor[J]. Water Research, 2014, 62: 202-210. doi: 10.1016/j.watres.2014.06.003
[26]
WANG Q, YE L, JIANG G, et al. Side-stream sludge treatment using free nitrous acid selectively eliminates nitrite oxidizing bacteria and achieves the nitrite pathway[J]. Water Research, 2014, 55: 245-255. doi: 10.1016/j.watres.2014.02.029
[27]
ADOUANI N, LIMOUSY L, LENDORMI T, et al. N2O and NO emissions during wastewater denitrification step: Influence of temperature on the biological process[J]. Comptes Rendus Chimie, 2015, 18(1): 15-22. doi: 10.1016/j.crci.2014.11.005
Key Laboratory of Urban Storm Water System and Water Environment, Ministry of Education, School of Environment and Energy Engineering, Beijing University of Civil Engineering and Architecture, Beijing 100044, China Received Date: 2020-06-09 Accepted Date: 2020-09-16 Available Online: 2021-03-24 Keywords:nitrite/ denitrification/ free nitrous acid(FNA)/ N2O Abstract:Aiming at the problem of large amount of N2O release during sewage treatment, the effects of different ${\rm{NO}}_2^ - $-N ratios on the denitrification process and N2O release were studied. At the total nitrogen concentration of 100 mg·L?1, the change of ${\rm{NO}}_2^ - $-N proportion was performed to conduct batch experiment. The reactor denitrification rate and nitrogen index variations were studied. The results show that the denitrification efficiency increased with the increase of the initial ${\rm{NO}}_2^ - $-N ratio, in which the ${\rm{NO}}_2^ - $-N concentration basically increased first and then decreased. The higher the initial ${\rm{NO}}_2^ - $-N ratio, the faster the degradation rate of ${\rm{NO}}_3^ - $-N and the more ${\rm{NO}}_2^ - $-N accumulation. With the increase of the initial ${\rm{NO}}_2^ - $-N ratio, the accumulation rate, maximum accumulation value and conversion rate of N2O both gradually increased. The highest values were 18.828 mg·(g·h)?1, 22.123 mg·L?1 and 24.05%, respectively. As the initial ${\rm{NO}}_2^ - $-N ratio increased, the concentration of free nitrous acid (FNA) increased, resulting in more N2O accumulation. FNA concentration may be the cause of the large N2O accumulation.