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Description: Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic...
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion
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Description: Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic...
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion

Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion

Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion

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Description: Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic...
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion
Abstract
CH2M is designing two installations where the thermal hydrolysis process (THP) is being used to treat waste activated sludge (WAS) and the hydrolyzed WAS will be combined with primary sludge prior to being fed to mesophilic anaerobic digestion. The technical issues for each process has proven to be different in the two case studies which are highlighted, one in Calgary, Canada and one in Singapore.The THP plant in Singapore will treat an initial flow of up to 53 metric tons of dry solids per day and is designed to be expandable to meet the ultimate requirement of 70 metric tons of dry solids per day by adding a 4th reactor. The THP system will treat both thickened and un-thickened WAS and concentrated grease waste. The thermally hydrolyzed sludge will be cooled by primary sludge and fed to 3 existing egg-shaped digesters. The total biosolids produced from these digesters to be dewatered on existing centrifuges will be 44.5 dry metric tons per day. Construction has begun in 2015 and the plant is expected to be operational in 2017.For Calgary, CH2M teamed with Stantec and completed conceptual and preliminary designs. WAS will be thickened, dewatered, and subjected to THP prior to blending with thickened primary sludge. Pre-selection of the THP equipment is in progress after which detailed design will be completed. Construction will begin in 2017. This facility will have capacity to manage an average of about 50 metric tons dry solids from a population equivalent (PE) of 1,237,000.The manuscript provides details on the decision factors associated with each project and the expected benefits and compares the technical design and operating data for each project.
CH2M is designing two installations where the thermal hydrolysis process (THP) is being used to treat waste activated sludge (WAS) and the hydrolyzed WAS will be combined with primary sludge prior to being fed to mesophilic anaerobic digestion. The technical issues for each process has proven to be different in the two case studies which are highlighted, one in Calgary, Canada and one in...
Author(s)
Todd WilliamsPeter BurrowesKim FriesColin NewberyDrury WhitlockRyan Roberts
SourceProceedings of the Water Environment Federation
SubjectResearch Article
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Apr, 2016
ISSN1938-6478
DOI10.2175/193864716821125925
Volume / Issue2016 / 3
Content sourceResiduals and Biosolids Conference
Copyright2016
Word count288

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Description: Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic...
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion
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Description: Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic...
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion
Abstract
CH2M is designing two installations where the thermal hydrolysis process (THP) is being used to treat waste activated sludge (WAS) and the hydrolyzed WAS will be combined with primary sludge prior to being fed to mesophilic anaerobic digestion. The technical issues for each process has proven to be different in the two case studies which are highlighted, one in Calgary, Canada and one in Singapore.The THP plant in Singapore will treat an initial flow of up to 53 metric tons of dry solids per day and is designed to be expandable to meet the ultimate requirement of 70 metric tons of dry solids per day by adding a 4th reactor. The THP system will treat both thickened and un-thickened WAS and concentrated grease waste. The thermally hydrolyzed sludge will be cooled by primary sludge and fed to 3 existing egg-shaped digesters. The total biosolids produced from these digesters to be dewatered on existing centrifuges will be 44.5 dry metric tons per day. Construction has begun in 2015 and the plant is expected to be operational in 2017.For Calgary, CH2M teamed with Stantec and completed conceptual and preliminary designs. WAS will be thickened, dewatered, and subjected to THP prior to blending with thickened primary sludge. Pre-selection of the THP equipment is in progress after which detailed design will be completed. Construction will begin in 2017. This facility will have capacity to manage an average of about 50 metric tons dry solids from a population equivalent (PE) of 1,237,000.The manuscript provides details on the decision factors associated with each project and the expected benefits and compares the technical design and operating data for each project.
CH2M is designing two installations where the thermal hydrolysis process (THP) is being used to treat waste activated sludge (WAS) and the hydrolyzed WAS will be combined with primary sludge prior to being fed to mesophilic anaerobic digestion. The technical issues for each process has proven to be different in the two case studies which are highlighted, one in Calgary, Canada and one in...
Author(s)
Todd WilliamsPeter BurrowesKim FriesColin NewberyDrury WhitlockRyan Roberts
SourceProceedings of the Water Environment Federation
SubjectResearch Article
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Apr, 2016
ISSN1938-6478
DOI10.2175/193864716821125925
Volume / Issue2016 / 3
Content sourceResiduals and Biosolids Conference
Copyright2016
Word count288

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Todd Williams# Peter Burrowes# Kim Fries# Colin Newbery# Drury Whitlock# Ryan Roberts. Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Web. 29 Jun. 2025. <https://www.accesswater.org?id=-279130CITANCHOR>.
Todd Williams# Peter Burrowes# Kim Fries# Colin Newbery# Drury Whitlock# Ryan Roberts. Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Accessed June 29, 2025. https://www.accesswater.org/?id=-279130CITANCHOR.
Todd Williams# Peter Burrowes# Kim Fries# Colin Newbery# Drury Whitlock# Ryan Roberts
Treatment of waste activated sludge with thermal hydrolysis and mesophilic anaerobic digestion
Access Water
Water Environment Federation
December 22, 2018
June 29, 2025
https://www.accesswater.org/?id=-279130CITANCHOR