Enhanced Biological Nutrients Removal in Modified Step-feed Anaerobic/Anoxic/Oxic Process
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Enhanced Biological Nutrients Removal in Modified Step-feed Anaerobic/Anoxic/Oxic Process
Enhanced Biological Nutrients Removal in Modified Step-feed Anaerobic/Anoxic/Oxic Process
中国化学工程学报(英文版)2009年17卷第5期 页码:840-848
Affiliations:
1. Key Laboratory of Beijing for Water Quality Science and Water Environmental Recovery Engineering, Beijing University of Technology,Beijing,China,100124
2. Beijing Municipal Engineering Professional Design Institute Co. Ltd,Beijing,China,100037
Author bio:
Funds:
Supported by the Project of Beijing Science and Technology Committee (D07050601500000);the National Key Science and Technology Special Projects (2008ZX07317-007-105)
In order to enhance phosphorus removal in traditional step-feed anoxic/oxic nitrogen removal process
a modified pilot-scale step-feed anaerobic/anoxic/oxic (SFA
2
/O) system was developed
which combined a reactor similar to UCT-type configuration and two-stage anoxic/oxic process.The simultaneous nitrogen and phosphorus removal capacities and the potential of denitrifying phosphorus removal
in particular
were investigated with four different feeding patterns using real municipal wastewater.The results showed that the feeding ratios(
Q
1
)in the first stage determined the nutrient removal performance in the SFA
2
/O system.The average phosphorus removal efficiency increased from 19.17% to 96.25% as
Q
1
was gradually increased from run 1 to run 4
but the nitrogen removal efficiency exhibited a different tendency
which attained a maximum 73.61% in run 3 and then decreased to 59.62% in run 4.As a compromise between nitrogen and phosphorus removal
run 3 (
Q
1
=0.45
Q
total
) was identified as the optimal and stable case with the maximum anoxic phosphorus uptake rate of 1.58mg·(g MLSS)
-1
·h
-1
.The results of batch tests showed that ratio of the anoxic phosphate uptake capacity to the aerobic phosphate uptake capacity increased from 11.96% to 36.85% with the optimal influent feeding ratio to the system in run 3
which demonstrated that the denitrifying polyP accumulating organisms could be accumulated and contributed more to the total phosphorus removal by optimizing the inflow ratio distribution.However
the nitrate recirculation to anoxic zone and influent feeding ratios should be carefully controlled for carbon source saving.
Abstract
In order to enhance phosphorus removal in traditional step-feed anoxic/oxic nitrogen removal process
a modified pilot-scale step-feed anaerobic/anoxic/oxic (SFA
2
/O) system was developed
which combined a reactor similar to UCT-type configuration and two-stage anoxic/oxic process.The simultaneous nitrogen and phosphorus removal capacities and the potential of denitrifying phosphorus removal
in particular
were investigated with four different feeding patterns using real municipal wastewater.The results showed that the feeding ratios(
Q
1
)in the first stage determined the nutrient removal performance in the SFA 2/O system.The average phosphorus removal efficiency increased from 19.17% to 96.25% as
Q
1
was gradually increased from run 1 to run 4
but the nitrogen removal efficiency exhibited a different tendency
which attained a maximum 73.61% in run 3 and then decreased to 59.62% in run 4.As a compromise between nitrogen and phosphorus removal
run 3 (
Q
1
=0.45
Q
total
) was identified as the optimal and stable case with the maximum anoxic phosphorus uptake rate of 1.58mg·(g MLSS)
-1
·h
-1
.The results of batch tests showed that ratio of the anoxic phosphate uptake capacity to the aerobic phosphate uptake capacity increased from 11.96% to 36.85% with the optimal influent feeding ratio to the system in run 3
which demonstrated that the denitrifying polyP accumulating organisms could be accumulated and contrib
uted more to the total phosphorus removal by optimizing the inflow ratio distribution.However
the nitrate recirculation to anoxic zone and influent feeding ratios should be carefully controlled for carbon source saving.
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