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MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS
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Description: Book cover
MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS

MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS

MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS

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Description: Book cover
MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS
Abstract
Ferric chloride addition was investigated for treatment of As-laden spent regeneration brine from ion exchange processes. Furthermore, varying conditions and calcium addition were investigated for the stabilization of the resulting As-laden solids. Arsenic, sulfate, bicarbonate, and chloride concentrations in the spent brine (300 mg/L, 605 mg/L, 305 mg/L, and 24 g/L, respectively) were orders of magnitude greater than typical drinking water treatment levels. Batch tests revealed that nearly 100% of the As in spent brine can be removed with a Fe/As molar ratio of 2 at circumneutral pH. The EPA TCLP and California WET tests were employed to determine the leachable Asin the treatment residuals. When the brine was treated using a Fe/As molar ratio of 5 and 20, the resultant As-laden sludge easily passed the TCLP and WET respectively. Addition of calcium hydroxide (Ca(OH)2) in the Ca/Fe molar ratio 1.5 decreased leachable As by 80% in the WET. Calcium addition in an optimal range decreased the chemical costs by 18% and reduced the mass of sludge produced by 20%. To further investigate the impact of calcium addition, leaching tests were performed using a landfill leachate.
Ferric chloride addition was investigated for treatment of As-laden spent regeneration brine from ion exchange processes. Furthermore, varying conditions and calcium addition were investigated for the stabilization of the resulting As-laden solids. Arsenic, sulfate, bicarbonate, and chloride concentrations in the spent brine (300 mg/L, 605 mg/L, 305 mg/L, and 24 g/L, respectively) were orders of...
Author(s)
Thomas R. SteinwinderDongye Zhao
SourceProceedings of the Water Environment Federation
SubjectSession 41: Microconstituents
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2007
ISSN1938-6478
SICI1938-6478(20070101)2007:15L.3026;1-
DOI10.2175/193864707787973662
Volume / Issue2007 / 15
Content sourceWEFTEC
First / last page(s)3026 - 3040
Copyright2007
Word count194

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Description: Book cover
MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS
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Description: Book cover
MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS
Abstract
Ferric chloride addition was investigated for treatment of As-laden spent regeneration brine from ion exchange processes. Furthermore, varying conditions and calcium addition were investigated for the stabilization of the resulting As-laden solids. Arsenic, sulfate, bicarbonate, and chloride concentrations in the spent brine (300 mg/L, 605 mg/L, 305 mg/L, and 24 g/L, respectively) were orders of magnitude greater than typical drinking water treatment levels. Batch tests revealed that nearly 100% of the As in spent brine can be removed with a Fe/As molar ratio of 2 at circumneutral pH. The EPA TCLP and California WET tests were employed to determine the leachable Asin the treatment residuals. When the brine was treated using a Fe/As molar ratio of 5 and 20, the resultant As-laden sludge easily passed the TCLP and WET respectively. Addition of calcium hydroxide (Ca(OH)2) in the Ca/Fe molar ratio 1.5 decreased leachable As by 80% in the WET. Calcium addition in an optimal range decreased the chemical costs by 18% and reduced the mass of sludge produced by 20%. To further investigate the impact of calcium addition, leaching tests were performed using a landfill leachate.
Ferric chloride addition was investigated for treatment of As-laden spent regeneration brine from ion exchange processes. Furthermore, varying conditions and calcium addition were investigated for the stabilization of the resulting As-laden solids. Arsenic, sulfate, bicarbonate, and chloride concentrations in the spent brine (300 mg/L, 605 mg/L, 305 mg/L, and 24 g/L, respectively) were orders of...
Author(s)
Thomas R. SteinwinderDongye Zhao
SourceProceedings of the Water Environment Federation
SubjectSession 41: Microconstituents
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2007
ISSN1938-6478
SICI1938-6478(20070101)2007:15L.3026;1-
DOI10.2175/193864707787973662
Volume / Issue2007 / 15
Content sourceWEFTEC
First / last page(s)3026 - 3040
Copyright2007
Word count194

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Thomas R. Steinwinder# Dongye Zhao. MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Web. 4 Jul. 2025. <https://www.accesswater.org?id=-293945CITANCHOR>.
Thomas R. Steinwinder# Dongye Zhao. MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Accessed July 4, 2025. https://www.accesswater.org/?id=-293945CITANCHOR.
Thomas R. Steinwinder# Dongye Zhao
MINIMIZING ARSENIC LEACHING FROM WATER TREATMENT PROCESS RESIDUALS
Access Water
Water Environment Federation
December 22, 2018
July 4, 2025
https://www.accesswater.org/?id=-293945CITANCHOR