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OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS
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Description: Book cover
OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS

OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS

OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS

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Description: Book cover
OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS
Abstract
Disinfection with ozone is achieved by CT product, where “C” is residual ozone concentration and “T” is reaction time. Ozone residual is developed after ozone gas is dissolved into the water. Ozone dissolution is most often achieved by either bubble-diffuser or side-stream ozone systems.Side-stream ozone systems are different from bubble-diffuser ozone systems in many ways.Ozone addition occurs outside of the ozone contactor.Additional energy is used due to side-stream pump operation.Equipment maintenance can be completed independent of ozone contactor operation.Ozone contactor size and shape can have unique design features, such as pipeline contacting or shallow-depth basins.Side-stream ozonation is a treatment technique that is gaining in popularity at larger and larger plants. Ozone generators can now operate at elevated ozone concentration, which improves the economics for installing and operating side-stream processes. Two different side-stream arrangements are discussed in this paper. The arrangements differ with the presence or absence of a de-gas vessel. The de-gas vessel option is more expensive in terms of capital and operating cost, but might be the chosen option for particular contactor configurations. Issues and considerations for installing a de-gas vessel are discussed in this paper.
Disinfection with ozone is achieved by CT product, where “C” is residual ozone concentration and “T” is reaction time. Ozone residual is developed after ozone gas is dissolved into the water. Ozone dissolution is most often achieved by either bubble-diffuser or side-stream ozone systems.Side-stream ozone systems are different from bubble-diffuser ozone systems in many ways.
Author(s)
Kerwin L. Rakness
SourceProceedings of the Water Environment Federation
SubjectSession 12: Ozone Disinfection in Drinking Water
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2007
ISSN1938-6478
SICI1938-6478(20070101)2007:1L.697;1-
DOI10.2175/193864707787932180
Volume / Issue2007 / 1
Content sourceDisinfection and Reuse Symposium
First / last page(s)697 - 716
Copyright2007
Word count200

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Description: Book cover
OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS
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Description: Book cover
OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS
Abstract
Disinfection with ozone is achieved by CT product, where “C” is residual ozone concentration and “T” is reaction time. Ozone residual is developed after ozone gas is dissolved into the water. Ozone dissolution is most often achieved by either bubble-diffuser or side-stream ozone systems.Side-stream ozone systems are different from bubble-diffuser ozone systems in many ways.Ozone addition occurs outside of the ozone contactor.Additional energy is used due to side-stream pump operation.Equipment maintenance can be completed independent of ozone contactor operation.Ozone contactor size and shape can have unique design features, such as pipeline contacting or shallow-depth basins.Side-stream ozonation is a treatment technique that is gaining in popularity at larger and larger plants. Ozone generators can now operate at elevated ozone concentration, which improves the economics for installing and operating side-stream processes. Two different side-stream arrangements are discussed in this paper. The arrangements differ with the presence or absence of a de-gas vessel. The de-gas vessel option is more expensive in terms of capital and operating cost, but might be the chosen option for particular contactor configurations. Issues and considerations for installing a de-gas vessel are discussed in this paper.
Disinfection with ozone is achieved by CT product, where “C” is residual ozone concentration and “T” is reaction time. Ozone residual is developed after ozone gas is dissolved into the water. Ozone dissolution is most often achieved by either bubble-diffuser or side-stream ozone systems.Side-stream ozone systems are different from bubble-diffuser ozone systems in many ways.
Author(s)
Kerwin L. Rakness
SourceProceedings of the Water Environment Federation
SubjectSession 12: Ozone Disinfection in Drinking Water
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Jan, 2007
ISSN1938-6478
SICI1938-6478(20070101)2007:1L.697;1-
DOI10.2175/193864707787932180
Volume / Issue2007 / 1
Content sourceDisinfection and Reuse Symposium
First / last page(s)697 - 716
Copyright2007
Word count200

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Kerwin L. Rakness. OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Web. 7 Jun. 2025. <https://www.accesswater.org?id=-294270CITANCHOR>.
Kerwin L. Rakness. OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2018. Accessed June 7, 2025. https://www.accesswater.org/?id=-294270CITANCHOR.
Kerwin L. Rakness
OZONE SIDE-STREAM SYSTEM DESIGN OPTIONS AND OPERATING CONSIDERATIONS
Access Water
Water Environment Federation
December 22, 2018
June 7, 2025
https://www.accesswater.org/?id=-294270CITANCHOR