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Ozone Disinfection of Combined Industrial and Municipal Secondary Effluents. Part I — Laboratory Studies CARL NEBEL PAUL C. UNANGST RONALD D. GOTTSCHLING Ozone Systems Division The Welsbach Corporation Philadelphia. Pennsylvania INTRODUCTION The current demand for water quality improvement has resulted in a search for new and improved economically feasible treatment methods. As standards are raised and water re-use becomes more and more likely, tertiary treatment procedures become necessary. Recent investigations (1,2) have indicated that secondary effluents disinfected with chlorine are toxic to aquatic life. A viable alternative to the use of chlorine is ozone for disinfection and concurrent tertiary treatment. Ozone, 03, is an unstable gas naturally occurring in the upper atmosphere. It is responsible for the characteristic sweet odor in the air immediately following an electrical storm. Because ozone is unstable it cannot be effectively stored or shipped and must be generated on-site. Commercial ozonators mimic nature by generating ozone by electrical discharge through air or oxygen. The process produces ozone as a mixture with either air or oxygen, and the exit gas from the ozonator typically contains 1 percent ozone from air feed or 1.7 percent ozone using oxygen feed. Other concentrations are possible, but are less efficient economically. The ozonized gas can then be dispersed into the water to be treated either by various injection methods or by forcing the pressurized gas through a porous disperser at the bottom of a treatment tank. A variety of laboratory studies (3,4,5,6,7,8,9,10) initially demonstrated the effectiveness of ozone in secondary effluent disinfection and contaminant removal; however, the lack of uniformity in experimental techniques and methods has made comparison of data difficult. The goal of this work was to establish the degree of treatment possible with various ozone dosage levels. Additional information has been obtained in pilot-scale studies in the cities of London (England) (11), Chicago (12), and Washington, D.C. (13), where water of potable quality has been produced by ozonization of a variety of effluents. A pilot study was also recently completed at the Louisville, Ky., Fort Southworth Sewage Treatment Plant. Previous work has established that ozone treatment of sewage can be considered at several dosage levels: 1) as a treatment for primary sewage and storm water overflow (ozone dosages of 10-100 mg/1 required); 2) as a tertiary treatment to convert secondary effluent to water of potable quality (ozone dosages >50 mg/1 required); and 3) as a replacement for chlorine for disinfection whereby a certain degree of tertiary treatment is concurrently observed (ozone dosages of 5-15 mg/1 required). In this study we have attempted to more accurately elucidate the ozone dosages required for disinfection and to determine the effectiveness of removal of specific contaminants in the effluent. EXPERIMENTAL METHODS Secondary effluents obtained from the Millville, New Jersey (contact stabilization), Hatboro, Penna. (standard activated sludge), and Northeast Philadelphia, Penna. (pilot plant oxygen enriched activated sludge), sewage treatment plants were ozonized in a 6.5 in. 1039
Object Description
Purdue Identification Number | ETRIWC197289 |
Title | Ozone disinfection of combined industrial and municipal secondary effluents. Part I, Laboratory studies |
Author |
Nebel, Carl Unangst, Paul C. Gottschling, Ronald D. |
Date of Original | 1972 |
Conference Title | Proceedings of the 27th Industrial Waste Conference |
Conference Front Matter (copy and paste) | http://earchives.lib.purdue.edu/u?/engext,20246 |
Extent of Original | p. 1039-1055 |
Series | Engineering extension series no. 141 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Date Digitized | 2009-06-08 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Resolution | 300 ppi |
Color Depth | 8 bit |
Description
Title | page1039 |
Collection Title | Engineering Technical Reports Collection, Purdue University |
Repository | Purdue University Libraries |
Rights Statement | Digital object copyright Purdue University. All rights reserved. |
Language | eng |
Type (DCMI) | text |
Format | JP2 |
Capture Device | Fujitsu fi-5650C |
Capture Details | ScandAll 21 |
Transcript | Ozone Disinfection of Combined Industrial and Municipal Secondary Effluents. Part I — Laboratory Studies CARL NEBEL PAUL C. UNANGST RONALD D. GOTTSCHLING Ozone Systems Division The Welsbach Corporation Philadelphia. Pennsylvania INTRODUCTION The current demand for water quality improvement has resulted in a search for new and improved economically feasible treatment methods. As standards are raised and water re-use becomes more and more likely, tertiary treatment procedures become necessary. Recent investigations (1,2) have indicated that secondary effluents disinfected with chlorine are toxic to aquatic life. A viable alternative to the use of chlorine is ozone for disinfection and concurrent tertiary treatment. Ozone, 03, is an unstable gas naturally occurring in the upper atmosphere. It is responsible for the characteristic sweet odor in the air immediately following an electrical storm. Because ozone is unstable it cannot be effectively stored or shipped and must be generated on-site. Commercial ozonators mimic nature by generating ozone by electrical discharge through air or oxygen. The process produces ozone as a mixture with either air or oxygen, and the exit gas from the ozonator typically contains 1 percent ozone from air feed or 1.7 percent ozone using oxygen feed. Other concentrations are possible, but are less efficient economically. The ozonized gas can then be dispersed into the water to be treated either by various injection methods or by forcing the pressurized gas through a porous disperser at the bottom of a treatment tank. A variety of laboratory studies (3,4,5,6,7,8,9,10) initially demonstrated the effectiveness of ozone in secondary effluent disinfection and contaminant removal; however, the lack of uniformity in experimental techniques and methods has made comparison of data difficult. The goal of this work was to establish the degree of treatment possible with various ozone dosage levels. Additional information has been obtained in pilot-scale studies in the cities of London (England) (11), Chicago (12), and Washington, D.C. (13), where water of potable quality has been produced by ozonization of a variety of effluents. A pilot study was also recently completed at the Louisville, Ky., Fort Southworth Sewage Treatment Plant. Previous work has established that ozone treatment of sewage can be considered at several dosage levels: 1) as a treatment for primary sewage and storm water overflow (ozone dosages of 10-100 mg/1 required); 2) as a tertiary treatment to convert secondary effluent to water of potable quality (ozone dosages >50 mg/1 required); and 3) as a replacement for chlorine for disinfection whereby a certain degree of tertiary treatment is concurrently observed (ozone dosages of 5-15 mg/1 required). In this study we have attempted to more accurately elucidate the ozone dosages required for disinfection and to determine the effectiveness of removal of specific contaminants in the effluent. EXPERIMENTAL METHODS Secondary effluents obtained from the Millville, New Jersey (contact stabilization), Hatboro, Penna. (standard activated sludge), and Northeast Philadelphia, Penna. (pilot plant oxygen enriched activated sludge), sewage treatment plants were ozonized in a 6.5 in. 1039 |
Resolution | 300 ppi |
Color Depth | 8 bit |
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