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Treatment of Groundwater Containing Methane – Combination of the Processing Stages Desorption and Filtration

Treatment of Groundwater Containing Methane – Combination of the Processing Stages Desorption and... Methane is produced under anaerobic conditions by metabolic processes in microbes and can occur in waters of the types anoxic‐anaerobic (RG 1/2) and anaerobic‐reduced (RG 2). If the concentration of methane lies below 0.2 mg/L, then no special treatment processes are required apart from dosing of oxygen and rapid sand filtration, which are performed to remove iron, manganese, and ammonium. The research results show that a higher concentration of methane must be specially treated. From the point of view of stable deferrisation, oxidation of up to 2 mg/L is tolerable in rapid sand filtration. However, an unusual increase in regrowth potential was observed. For this reason, the oxidation of methane should be reduced to 0.5 mg/L until further experiments yield results on the microbiological stability of treated water. Rapid sand filters for nitrification and demanganisation should have a maximum methane loading of 0.2 mg/L. The experiments show that nitrification first occurs at a methane concentration below 0.1 mg/L. During the working in of demanganisation, the inlet water should be free of methane. Therefore desorption is often required. If there is less than 1 mg/L to be degassed, then desorption can be achieved with overpressure in the oxidiser without any change in the carbonate‐bicarbonate equilibrium. With other systems, such as packed columns, wetted‐wall columns, or percolators, carbon dioxide is removed simultaneously. By means of the coefficients of similarity found, it was shown that methane and carbon dioxide desorb in different proportions depending on the system, and that the discharge of carbon dioxide can be reduced through a decrease in the air/water ratio. http://www.deepdyve.com/assets/images/DeepDyve-Logo-lg.png Acta hydrochimica et hydrobiologica Wiley

Treatment of Groundwater Containing Methane – Combination of the Processing Stages Desorption and Filtration

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Publisher
Wiley
Copyright
Copyright © 2000 Wiley Subscription Services, Inc., A Wiley Company
ISSN
0323-4320
eISSN
1521-401X
DOI
10.1002/1521-401X(200003)28:3<145::AID-AHEH145>3.0.CO;2-V
Publisher site
See Article on Publisher Site

Abstract

Methane is produced under anaerobic conditions by metabolic processes in microbes and can occur in waters of the types anoxic‐anaerobic (RG 1/2) and anaerobic‐reduced (RG 2). If the concentration of methane lies below 0.2 mg/L, then no special treatment processes are required apart from dosing of oxygen and rapid sand filtration, which are performed to remove iron, manganese, and ammonium. The research results show that a higher concentration of methane must be specially treated. From the point of view of stable deferrisation, oxidation of up to 2 mg/L is tolerable in rapid sand filtration. However, an unusual increase in regrowth potential was observed. For this reason, the oxidation of methane should be reduced to 0.5 mg/L until further experiments yield results on the microbiological stability of treated water. Rapid sand filters for nitrification and demanganisation should have a maximum methane loading of 0.2 mg/L. The experiments show that nitrification first occurs at a methane concentration below 0.1 mg/L. During the working in of demanganisation, the inlet water should be free of methane. Therefore desorption is often required. If there is less than 1 mg/L to be degassed, then desorption can be achieved with overpressure in the oxidiser without any change in the carbonate‐bicarbonate equilibrium. With other systems, such as packed columns, wetted‐wall columns, or percolators, carbon dioxide is removed simultaneously. By means of the coefficients of similarity found, it was shown that methane and carbon dioxide desorb in different proportions depending on the system, and that the discharge of carbon dioxide can be reduced through a decrease in the air/water ratio.

Journal

Acta hydrochimica et hydrobiologicaWiley

Published: Mar 1, 2000

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