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Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter
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Description: Book cover
Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter

Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter

Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter

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Description: Book cover
Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter
Abstract
There are two basic types of denitrification filters being used in the Chesapeake Bay region to meet enhanced nutrient removal (ENR) level effluent requirements: continuously backwashing upflow sand filters (herein called “continuously backwashing denitrification filters”) (CBDF) and intermittent backwashing downflow sand filters (herein called “downflow denitrification filters”) (DDF). These types of filters can also be used as conventional effluent filters – in fact, there is little difference between the physical design of a denitrification filter and a conventional effluent filter. Primary differences are hydraulic loading rates and bed depths and in some cases media size, backwash rates, and control sequences.Although there is limited performance data for denitrification filters operating in the Chesapeake Bay watershed, common operation problems such as high influent DO levels and low influent phosphorus levels have been experienced at several facilities and have resulted in reduced treatment performance. The requirement to achieve very low total nitrogen (TN) and total phosphorus (TP) levels in the same filter requires a tool for operations staff to predict how changes in operating parameters will impact performance, especially as the flows and loads increase from startup conditions to design conditions at these facilities. A CBDF has been online at the 2.0 mgd Aberdeen Area Wastewater Treatment Plant of the Aberdeen Proving Grounds (AAWWTP-APG) since March 2006. While this facility has achieved excellent nutrient removal since startup, it is apparent that more precise process control will be required as the WWTP approaches design conditions.Additionally, CBDF equipment manufacturers propose filter sizing without providing kinetic calculations to demonstrate the performance of the filter under varying operating conditions. A modeling tool would be beneficial as more CBDFs are utilized to meet ENR level treatment.
There are two basic types of denitrification filters being used in the Chesapeake Bay region to meet enhanced nutrient removal (ENR) level effluent requirements: continuously backwashing upflow sand filters (herein called “continuously backwashing denitrification filters”) (CBDF) and intermittent backwashing downflow sand filters (herein called “downflow denitrification...
Author(s)
Scott CrosswellThor YoungDan TobocmanJohn CannonJohn StulkenDipankar SenCurtis Ball
SourceProceedings of the Water Environment Federation
SubjectSession 2 - Fixed Film/Hybrid Process Modeling & Mechanics
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2009
ISSN1938-6478
SICI1938-6478(20090101)2009:4L.166;1-
DOI10.2175/193864709793901518
Volume / Issue2009 / 4
Content sourceNutrient Removal and Recovery Symposium
First / last page(s)166 - 186
Copyright2009
Word count292
Subject keywordsDenitrification Filtersenhanced nutrient removalnitrate removalphosphorus removalprocess modeling

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Description: Book cover
Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter
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Description: Book cover
Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter
Abstract
There are two basic types of denitrification filters being used in the Chesapeake Bay region to meet enhanced nutrient removal (ENR) level effluent requirements: continuously backwashing upflow sand filters (herein called “continuously backwashing denitrification filters”) (CBDF) and intermittent backwashing downflow sand filters (herein called “downflow denitrification filters”) (DDF). These types of filters can also be used as conventional effluent filters – in fact, there is little difference between the physical design of a denitrification filter and a conventional effluent filter. Primary differences are hydraulic loading rates and bed depths and in some cases media size, backwash rates, and control sequences.Although there is limited performance data for denitrification filters operating in the Chesapeake Bay watershed, common operation problems such as high influent DO levels and low influent phosphorus levels have been experienced at several facilities and have resulted in reduced treatment performance. The requirement to achieve very low total nitrogen (TN) and total phosphorus (TP) levels in the same filter requires a tool for operations staff to predict how changes in operating parameters will impact performance, especially as the flows and loads increase from startup conditions to design conditions at these facilities. A CBDF has been online at the 2.0 mgd Aberdeen Area Wastewater Treatment Plant of the Aberdeen Proving Grounds (AAWWTP-APG) since March 2006. While this facility has achieved excellent nutrient removal since startup, it is apparent that more precise process control will be required as the WWTP approaches design conditions.Additionally, CBDF equipment manufacturers propose filter sizing without providing kinetic calculations to demonstrate the performance of the filter under varying operating conditions. A modeling tool would be beneficial as more CBDFs are utilized to meet ENR level treatment.
There are two basic types of denitrification filters being used in the Chesapeake Bay region to meet enhanced nutrient removal (ENR) level effluent requirements: continuously backwashing upflow sand filters (herein called “continuously backwashing denitrification filters”) (CBDF) and intermittent backwashing downflow sand filters (herein called “downflow denitrification...
Author(s)
Scott CrosswellThor YoungDan TobocmanJohn CannonJohn StulkenDipankar SenCurtis Ball
SourceProceedings of the Water Environment Federation
SubjectSession 2 - Fixed Film/Hybrid Process Modeling & Mechanics
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2009
ISSN1938-6478
SICI1938-6478(20090101)2009:4L.166;1-
DOI10.2175/193864709793901518
Volume / Issue2009 / 4
Content sourceNutrient Removal and Recovery Symposium
First / last page(s)166 - 186
Copyright2009
Word count292
Subject keywordsDenitrification Filtersenhanced nutrient removalnitrate removalphosphorus removalprocess modeling

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Scott Crosswell# Thor Young# Dan Tobocman# John Cannon# John Stulken# Dipankar Sen# Curtis Ball. Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Web. 3 Nov. 2025. <https://www.accesswater.org?id=-296721CITANCHOR>.
Scott Crosswell# Thor Young# Dan Tobocman# John Cannon# John Stulken# Dipankar Sen# Curtis Ball. Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Accessed November 3, 2025. https://www.accesswater.org/?id=-296721CITANCHOR.
Scott Crosswell# Thor Young# Dan Tobocman# John Cannon# John Stulken# Dipankar Sen# Curtis Ball
Full Scale Evaluation, Modeling, and Optimization of Nitrate Removal through Continuously Backwashing Denitrification Filter
Access Water
Water Environment Federation
December 22, 2018
November 3, 2025
https://www.accesswater.org/?id=-296721CITANCHOR