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Description: Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using...
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources
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Description: Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using...
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources

Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources

Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources

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Description: Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using...
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources
Abstract
Over the past few year’s Ostara has developed an alternative chemistry that has demonstrated an improvement in the economics of operating a Pearl® nutrient recovery system. A full-scale trial with one of the three Pearl® 500 reactors at HRSD’s (Hampton Roads Sanitation District) Nansemond site has been running since June 2018, demonstrating a cost reduction in chemicals purchases of over 60%. Over the course of the trial the system has achieved comparable ortho-phosphorous removal, production efficiency, and product quality to MgCl2 and NaOH operation. In addition, this change has allowed for the capacity of the existing Pearl® system to be increased. The reduction in chemical cost was accomplished by switching from the use of soluble reagents (magnesium chloride and sodium hydroxide) to a sparingly soluble slurry of magnesium oxide as the primary reagent.
Over the past few year’s Ostara has developed an alternative chemistry that has demonstrated an improvement in the economics of operating a Pearl® nutrient recovery system. A full-scale trial with one of the three Pearl® 500 reactors at HRSD’s (Hampton Roads Sanitation District) Nansemond site has been running since June 2018, demonstrating a cost reduction in chemicals purchases of over 60%. Over the course of the trial the system has achieved comparable ortho-phosphorous removal, production efficiency, and product quality to MgCl2 and NaOH operation. In addition, this change has allowed for the capacity of the existing Pearl® system to be increased. The reduction in chemical cost was accomplished by switching from the use of soluble reagents (magnesium chloride and sodium hydroxide) to a sparingly soluble slurry of magnesium oxide as the primary reagent.
SpeakerVerigin, Mikaela
Presentation time
09:10:00
09:30:00
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)
M. VeriginM. VeriginJ. SparksR. JonesR. PrasadS. Goy
Author(s)M. Verigin1; M. Verigin1; J. Sparks2; R. Jones2; R. Prasad1; S. Goy2;
Author affiliation(s)Ostara Nutrient Recovery Technologies, BC1; HRSD, VA2
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct 2020
DOI10.2175/193864718825157503
Volume / Issue
Content sourceWEFTEC
Copyright2020
Word count17

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Description: Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using...
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources
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Description: Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using...
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources
Abstract
Over the past few year’s Ostara has developed an alternative chemistry that has demonstrated an improvement in the economics of operating a Pearl® nutrient recovery system. A full-scale trial with one of the three Pearl® 500 reactors at HRSD’s (Hampton Roads Sanitation District) Nansemond site has been running since June 2018, demonstrating a cost reduction in chemicals purchases of over 60%. Over the course of the trial the system has achieved comparable ortho-phosphorous removal, production efficiency, and product quality to MgCl2 and NaOH operation. In addition, this change has allowed for the capacity of the existing Pearl® system to be increased. The reduction in chemical cost was accomplished by switching from the use of soluble reagents (magnesium chloride and sodium hydroxide) to a sparingly soluble slurry of magnesium oxide as the primary reagent.
Over the past few year’s Ostara has developed an alternative chemistry that has demonstrated an improvement in the economics of operating a Pearl® nutrient recovery system. A full-scale trial with one of the three Pearl® 500 reactors at HRSD’s (Hampton Roads Sanitation District) Nansemond site has been running since June 2018, demonstrating a cost reduction in chemicals purchases of over 60%. Over the course of the trial the system has achieved comparable ortho-phosphorous removal, production efficiency, and product quality to MgCl2 and NaOH operation. In addition, this change has allowed for the capacity of the existing Pearl® system to be increased. The reduction in chemical cost was accomplished by switching from the use of soluble reagents (magnesium chloride and sodium hydroxide) to a sparingly soluble slurry of magnesium oxide as the primary reagent.
SpeakerVerigin, Mikaela
Presentation time
09:10:00
09:30:00
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)
M. VeriginM. VeriginJ. SparksR. JonesR. PrasadS. Goy
Author(s)M. Verigin1; M. Verigin1; J. Sparks2; R. Jones2; R. Prasad1; S. Goy2;
Author affiliation(s)Ostara Nutrient Recovery Technologies, BC1; HRSD, VA2
SourceProceedings of the Water Environment Federation
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Oct 2020
DOI10.2175/193864718825157503
Volume / Issue
Content sourceWEFTEC
Copyright2020
Word count17

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M. Verigin# M. Verigin# J. Sparks# R. Jones# R. Prasad# S. Goy#. Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources. Water Environment Federation, 2020. Web. 1 Oct. 2025. <https://www.accesswater.org?id=-10028648CITANCHOR>.
M. Verigin# M. Verigin# J. Sparks# R. Jones# R. Prasad# S. Goy#. Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources. Water Environment Federation, 2020. Accessed October 1, 2025. https://www.accesswater.org/?id=-10028648CITANCHOR.
M. Verigin# M. Verigin# J. Sparks# R. Jones# R. Prasad# S. Goy#
Reducing Phosphorus Recovery Operating and Capital Costs at Nansemond WWTP by Using Low Solubility Magnesium Sources
Access Water
Water Environment Federation
October 7, 2020
October 1, 2025
https://www.accesswater.org/?id=-10028648CITANCHOR