Maximizing the efficiency of single‐stage partial nitrification/Anammox granule processes and balancing microbial competition using insights of a numerical model study

Granulation is an efficient approach for the rapid growth of anaerobic ammonia oxidation (Anammox) bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ) to limit the growth of nitrite-oxidizing bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> ). However, the high sensitivity of Anammox bacteria to operational conditions and the competition with other microorganisms lead to a critical challenge in maintaining sufficient <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> population. In this study, a one-dimensional steady-state model was developed and calibrated to investigate the kinetic constants of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> growth and mass transport in individual granules, including the liquid film. According to the model calibration results, the range of the maximum specific growth rate constant of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mspace></mml:mspace> <mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>μ</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {\mu}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ) was 0.033 to 0.10 d<sup>-1</sup>. In addition the other kinetic constants of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> were 0.003 d<sup>-1</sup> for decay rate constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>b</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {b}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), 0.10 mg-O<sub>2</sub>/L for oxygen half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>O</mml:mi> <mml:mn>2</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{O_2}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), 0.07 mg-N/L for ammonia half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>NH</mml:mi> <mml:mn>4</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{NH_4}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), and 0.05 mg-N/L for nitrite half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>NO</mml:mi> <mml:mn>2</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{NO_2}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ). The model simulation results showed that the dissolved oxygen of about 0.10 mg-O<sub>2</sub>/L was found to be optimal to maintain high <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> population. In addition, minimal COD concentration is required to control heterotrophs ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>H</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_H $$</mml:annotation></mml:semantics> </mml:math> ) and improve ammonia oxidation by ammonia-oxidizing bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>AOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{AOB} $$</mml:annotation></mml:semantics> </mml:math> ). It was also emphasized that moderate mixing conditions ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>L</mml:mi> <mml:mi>f</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {L}_f $$</mml:annotation></mml:semantics> </mml:math> <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 100 μm) are preferable to decrease the diffusion of oxygen to the deep layers of the granules, controlling the competition between <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> and <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> . A single-factor relative sensitivity analysis (RSA) on microbial kinetics revealed that <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>μ</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {\mu}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> is the governing factor in the efficient operation of the single-stage PN/A processes. In addition, it was found that nitrite concentration is a rate-limiting parameter on the success of the process due to the competition between <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> and <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> . These findings can be used to enhance our understanding on the importance of microbial competition and mass transport in the single-stage PN/A process. PRACTITIONER POINTS: A one-dimensional steady-state model was developed and calibrated for simulating the single-stage partial nitrification/Anammox (PN/A) granule process. Moderate liquid films ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>L</mml:mi> <mml:mi>f</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {L}_f $$</mml:annotation></mml:semantics> </mml:math> <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 100 μm) are preferable for better performance of Anammox growth in single-stage PN/A processes. Moderate dissolved oxygen (DO <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 0.10 mg-O<sub>2</sub>/L) is highly recommended for efficient growth of Anammox bacteria in single-stage PN/A granulation. Minimal COD (COD <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 0) is preferable for successful operation of the single-stage PN/A granule process. Nitrite concentration is a rate-limiting parameter on the competition between Anammox and nitrite-oxidizing bacteria in the single-stage PN/A processes.

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Water Environment Research
Published
2025-03-01
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https://doi.org/10.1002/wer.70059
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4
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Wastewater Treatment and Nitrogen Removal
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article

Maximizing the efficiency of single‐stage partial nitrification/Anammox granule processes and balancing microbial competition using insights of a numerical model study

Younggy Kim, Taeho Lee, Ahmed Elsayed
4 citations
Water Environment Research
Wastewater Treatment and Nitrogen Removal
2.01
article

Maximizing the efficiency of single‐stage partial nitrification/Anammox granule processes and balancing microbial competition using insights of a numerical model study

Younggy Kim, Taeho Lee, Ahmed Elsayed
article en
4 citations

Abstract

Granulation is an efficient approach for the rapid growth of anaerobic ammonia oxidation (Anammox) bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ) to limit the growth of nitrite-oxidizing bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> ). However, the high sensitivity of Anammox bacteria to operational conditions and the competition with other microorganisms lead to a critical challenge in maintaining sufficient <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> population. In this study, a one-dimensional steady-state model was developed and calibrated to investigate the kinetic constants of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> growth and mass transport in individual granules, including the liquid film. According to the model calibration results, the range of the maximum specific growth rate constant of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mspace></mml:mspace> <mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>μ</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {\mu}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ) was 0.033 to 0.10 d<sup>-1</sup>. In addition the other kinetic constants of <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> were 0.003 d<sup>-1</sup> for decay rate constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>b</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {b}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), 0.10 mg-O<sub>2</sub>/L for oxygen half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>O</mml:mi> <mml:mn>2</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{O_2}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), 0.07 mg-N/L for ammonia half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>NH</mml:mi> <mml:mn>4</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{NH_4}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ), and 0.05 mg-N/L for nitrite half-saturation constant ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msubsup><mml:mi>K</mml:mi> <mml:msub><mml:mi>NO</mml:mi> <mml:mn>2</mml:mn></mml:msub> <mml:mi>ANA</mml:mi></mml:msubsup> </mml:mrow> <mml:annotation>$$ {K}_{NO_2}^{ANA} $$</mml:annotation></mml:semantics> </mml:math> ). The model simulation results showed that the dissolved oxygen of about 0.10 mg-O<sub>2</sub>/L was found to be optimal to maintain high <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> population. In addition, minimal COD concentration is required to control heterotrophs ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>H</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_H $$</mml:annotation></mml:semantics> </mml:math> ) and improve ammonia oxidation by ammonia-oxidizing bacteria ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>AOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{AOB} $$</mml:annotation></mml:semantics> </mml:math> ). It was also emphasized that moderate mixing conditions ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>L</mml:mi> <mml:mi>f</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {L}_f $$</mml:annotation></mml:semantics> </mml:math> <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 100 μm) are preferable to decrease the diffusion of oxygen to the deep layers of the granules, controlling the competition between <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> and <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> . A single-factor relative sensitivity analysis (RSA) on microbial kinetics revealed that <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>μ</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {\mu}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> is the governing factor in the efficient operation of the single-stage PN/A processes. In addition, it was found that nitrite concentration is a rate-limiting parameter on the success of the process due to the competition between <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>ANA</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{ANA} $$</mml:annotation></mml:semantics> </mml:math> and <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>X</mml:mi> <mml:mi>NOB</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {X}_{NOB} $$</mml:annotation></mml:semantics> </mml:math> . These findings can be used to enhance our understanding on the importance of microbial competition and mass transport in the single-stage PN/A process. PRACTITIONER POINTS: A one-dimensional steady-state model was developed and calibrated for simulating the single-stage partial nitrification/Anammox (PN/A) granule process. Moderate liquid films ( <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics> <mml:mrow><mml:msub><mml:mi>L</mml:mi> <mml:mi>f</mml:mi></mml:msub> </mml:mrow> <mml:annotation>$$ {L}_f $$</mml:annotation></mml:semantics> </mml:math> <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 100 μm) are preferable for better performance of Anammox growth in single-stage PN/A processes. Moderate dissolved oxygen (DO <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 0.10 mg-O<sub>2</sub>/L) is highly recommended for efficient growth of Anammox bacteria in single-stage PN/A granulation. Minimal COD (COD <mml:math xmlns:mml="http://www.w3.org/1998/Math/MathML"> <mml:semantics><mml:mrow><mml:mo>≅</mml:mo></mml:mrow> <mml:annotation>$$ \cong $$</mml:annotation></mml:semantics> </mml:math> 0) is preferable for successful operation of the single-stage PN/A granule process. Nitrite concentration is a rate-limiting parameter on the competition between Anammox and nitrite-oxidizing bacteria in the single-stage PN/A processes.

Water Environment ResearchVol. 97(3)
Cairo University (EG), Pusan National University (KR), McMaster University (CA)
National Research Foundation, National Research Foundation of Korea, Natural Sciences and Engineering Research Council of Canada, Ontario Ministry of Research and Innovation
Openalex Percentile: Top 15%
Wastewater Treatment and Nitrogen Removal
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