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Description: Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic...
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis
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Description: Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic...
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis

Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis

Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis

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Description: Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic...
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis
Abstract
In this paper, process modeling was used to compare struvite and brushite based phosphorus (P) recovery alternatives with the available data which can be used for conceptual decision-making for P recovery. A model based technical and economical evaluation of struvite and brushite recovery (using BioWin™ Version 6.0) was conducted for a large Water Resource Recovery Facility (WRRF). The cost effectiveness ($/lb of Premoved) of the P recovery options was determined and sensitivity analysis was conducted to compare the options with and without the sale of the fertilizer product, for chemical cost and other key parameters. This comparative assessment focused on confirming and validating the design basis, technology providers’ estimated P recovery, and chemical needs. This paper is the first application of commercial simulator for side by side comparison of the two P recovery alternatives. Modeling results compared reasonably well with the actual WRRF data for struvite recovery. The model predicted chemical requirement for brushite recovery was similar to literature values for pilot studies. For the testing conditions modeled in this paper (20 MGD WRRF), brushite recovery appears to be slightly more cost effective in terms of $/lb Premoved. However, given the cost variations depending on the location and site specific conditions, the two alternatives appear equal in cost effectiveness.
In this paper, process modeling was used to compare struvite and brushite based phosphorus (P) recovery alternatives with the available data which can be used for conceptual decision-making for P recovery. A model based technical and economical evaluation of struvite and brushite recovery (using BioWin™ Version 6.0) was conducted for a large Water Resource Recovery Facility (WRRF). The cost effectiveness ($/lb of Premoved) of the P recovery options was determined and sensitivity analysis was conducted to compare the options with and without the sale of the fertilizer product, for chemical cost and other key parameters. This comparative assessment focused on confirming and validating the design basis, technology providers’ estimated P recovery, and chemical needs. This paper is the first application of commercial simulator for side by side comparison of the two P recovery alternatives. Modeling results compared reasonably well with the actual WRRF data for struvite recovery. The model predicted chemical requirement for brushite recovery was similar to literature values for pilot studies. For the testing conditions modeled in this paper (20 MGD WRRF), brushite recovery appears to be slightly more cost effective in terms of $/lb Premoved. However, given the cost variations depending on the location and site specific conditions, the two alternatives appear equal in cost effectiveness.
SpeakerArabi, Sara
Presentation time
08:30:00
08:50:00
Session time
08:30:00
09:30:00
SessionSidestream Phosphorus Removal and Recovery Operations
Session number515
TopicFacility Operations and Maintenance, Municipal Wastewater Treatment Design, Nutrients, Research and Innovation
TopicFacility Operations and Maintenance, Municipal Wastewater Treatment Design, Nutrients, Research and Innovation
Author(s)
S. ARABIS. ARABIM. BenischC. ByeE.A. Evans
Author(s)S. ARABI1; S. ARABI1; M. Benisch2; C. Bye3; E.A. Evans4;
Author affiliation(s)HDR, IL1; HDR Engineering Inc, OR2; EnviroSim Associates Ltd., ON3; HDR, IA4
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct 2020
DOI10.2175/193864718825157501
Volume / Issue
Content sourceWEFTEC
Copyright2020
Word count16

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Description: Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic...
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis
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Description: Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic...
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis
Abstract
In this paper, process modeling was used to compare struvite and brushite based phosphorus (P) recovery alternatives with the available data which can be used for conceptual decision-making for P recovery. A model based technical and economical evaluation of struvite and brushite recovery (using BioWin™ Version 6.0) was conducted for a large Water Resource Recovery Facility (WRRF). The cost effectiveness ($/lb of Premoved) of the P recovery options was determined and sensitivity analysis was conducted to compare the options with and without the sale of the fertilizer product, for chemical cost and other key parameters. This comparative assessment focused on confirming and validating the design basis, technology providers’ estimated P recovery, and chemical needs. This paper is the first application of commercial simulator for side by side comparison of the two P recovery alternatives. Modeling results compared reasonably well with the actual WRRF data for struvite recovery. The model predicted chemical requirement for brushite recovery was similar to literature values for pilot studies. For the testing conditions modeled in this paper (20 MGD WRRF), brushite recovery appears to be slightly more cost effective in terms of $/lb Premoved. However, given the cost variations depending on the location and site specific conditions, the two alternatives appear equal in cost effectiveness.
In this paper, process modeling was used to compare struvite and brushite based phosphorus (P) recovery alternatives with the available data which can be used for conceptual decision-making for P recovery. A model based technical and economical evaluation of struvite and brushite recovery (using BioWin™ Version 6.0) was conducted for a large Water Resource Recovery Facility (WRRF). The cost effectiveness ($/lb of Premoved) of the P recovery options was determined and sensitivity analysis was conducted to compare the options with and without the sale of the fertilizer product, for chemical cost and other key parameters. This comparative assessment focused on confirming and validating the design basis, technology providers’ estimated P recovery, and chemical needs. This paper is the first application of commercial simulator for side by side comparison of the two P recovery alternatives. Modeling results compared reasonably well with the actual WRRF data for struvite recovery. The model predicted chemical requirement for brushite recovery was similar to literature values for pilot studies. For the testing conditions modeled in this paper (20 MGD WRRF), brushite recovery appears to be slightly more cost effective in terms of $/lb Premoved. However, given the cost variations depending on the location and site specific conditions, the two alternatives appear equal in cost effectiveness.
SpeakerArabi, Sara
Presentation time
08:30:00
08:50:00
Session time
08:30:00
09:30:00
SessionSidestream Phosphorus Removal and Recovery Operations
Session number515
TopicFacility Operations and Maintenance, Municipal Wastewater Treatment Design, Nutrients, Research and Innovation
TopicFacility Operations and Maintenance, Municipal Wastewater Treatment Design, Nutrients, Research and Innovation
Author(s)
S. ARABIS. ARABIM. BenischC. ByeE.A. Evans
Author(s)S. ARABI1; S. ARABI1; M. Benisch2; C. Bye3; E.A. Evans4;
Author affiliation(s)HDR, IL1; HDR Engineering Inc, OR2; EnviroSim Associates Ltd., ON3; HDR, IA4
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct 2020
DOI10.2175/193864718825157501
Volume / Issue
Content sourceWEFTEC
Copyright2020
Word count16

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S. ARABI# S. ARABI# M. Benisch# C. Bye# E.A. Evans#. Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis. Water Environment Federation, 2020. Web. 12 Jul. 2025. <https://www.accesswater.org?id=-10028446CITANCHOR>.
S. ARABI# S. ARABI# M. Benisch# C. Bye# E.A. Evans#. Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis. Water Environment Federation, 2020. Accessed July 12, 2025. https://www.accesswater.org/?id=-10028446CITANCHOR.
S. ARABI# S. ARABI# M. Benisch# C. Bye# E.A. Evans#
Comparison of Struvite and Brushite Recovery: Model Based Technical and Economic Evaluation and Sensitivity Analysis
Access Water
Water Environment Federation
October 7, 2020
July 12, 2025
https://www.accesswater.org/?id=-10028446CITANCHOR