Biological Removal of Nitrogen to Improve the Quality of Reclaimed Wastewater for Groundwater Recharge
Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was used to eliminate ammonia, nitrate and nitrite from a secondary wastewater effluent. The first stage of the process consisted of an aerobic...
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Published in | Acta biotechnologica Vol. 23; no. 2-3; pp. 131 - 140 |
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Main Authors | , , , , |
Format | Journal Article |
Language | English |
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WILEY-VCH Verlag
01.01.2003
WILEY‐VCH Verlag |
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Abstract | Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was used to eliminate ammonia, nitrate and nitrite from a secondary wastewater effluent.
The first stage of the process consisted of an aerobic upflow bioreactor with an autotrophic nitrifying population for ammonia oxidation, which was grown on silica sand granules and produced during the growth process nitrite and nitrate. During the second stage, these oxidised forms of nitrogen were successfully reduced to nitrogen gas in an anoxic denitrification fluidised bed reactor. At this stage, methanol was added as an external carbon source for the heterotrophic organisms growing on a silica sand support.
The optimum nitrification efficiency was 91% for the highest ammonia concentration at the influent (51 mg NH3‐N/l) and a retention time of 3.7 hours. With a lower ammonia concentration (23 mg NH3‐N/l), the highest nitrification efficiency was 95% corresponding to 1.1 mg NH3‐N/l in the nitrified effluent. In the denitrification process, a 95% removal efficiency of nitrite and nitrate for 55 mg NOx‐N/l at 2.3 hours and a concentration of microorganisms in the reactor of approx. 6,000 mg VSS/l was obtained. As a complementary stage of the nitrogen removal process, a silica sand and powderactivated carbon filter was installed in order to improve the quality of the final effluent in terms of other properties like turbidity, colour and the content of organic matter. |
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AbstractList | Abstract
Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was used to eliminate ammonia, nitrate and nitrite from a secondary wastewater effluent.
The first stage of the process consisted of an aerobic upflow bioreactor with an autotrophic nitrifying population for ammonia oxidation, which was grown on silica sand granules and produced during the growth process nitrite and nitrate. During the second stage, these oxidised forms of nitrogen were successfully reduced to nitrogen gas in an anoxic denitrification fluidised bed reactor. At this stage, methanol was added as an external carbon source for the heterotrophic organisms growing on a silica sand support.
The optimum nitrification efficiency was 91% for the highest ammonia concentration at the influent (51 mg NH
3
‐N/l) and a retention time of 3.7 hours. With a lower ammonia concentration (23 mg NH
3
‐N/l), the highest nitrification efficiency was 95% corresponding to 1.1 mg NH
3
‐N/l in the nitrified effluent. In the denitrification process, a 95% removal efficiency of nitrite and nitrate for 55 mg NO
x
‐N/l at 2.3 hours and a concentration of microorganisms in the reactor of approx. 6,000 mg VSS/l was obtained. As a complementary stage of the nitrogen removal process, a silica sand and powderactivated carbon filter was installed in order to improve the quality of the final effluent in terms of other properties like turbidity, colour and the content of organic matter. Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was used to eliminate ammonia, nitrate and nitrite from a secondary wastewater effluent. The first stage of the process consisted of an aerobic upflow bioreactor with an autotrophic nitrifying population for ammonia oxidation, which was grown on silica sand granules and produced during the growth process nitrite and nitrate. During the second stage, these oxidised forms of nitrogen were successfully reduced to nitrogen gas in an anoxic denitrification fluidised bed reactor. At this stage, methanol was added as an external carbon source for the heterotrophic organisms growing on a silica sand support. The optimum nitrification efficiency was 91% for the highest ammonia concentration at the influent (51 mg NH sub(3)-N/l) and a retention time of 3.7 hours. With a lower ammonia concentration (23 mg NH sub(3)-N/l), the highest nitrification efficiency was 95% corresponding to 1.1 mg NH sub(3)-N/l in the nitrified effluent. In the denitrification process, a 95% removal efficiency of nitrite and nitrate for 55 mg NO sub(x)-N/l at 2.3 hours and a concentration of microorganisms in the reactor of approx. 6,000 mg VSS/l was obtained. As a complementary stage of the nitrogen removal process, a silica sand and powderactivated carbon filter was installed in order to improve the quality of the final effluent in terms of other properties like turbidity, colour and the content of organic matter. Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was used to eliminate ammonia, nitrate and nitrite from a secondary wastewater effluent. The first stage of the process consisted of an aerobic upflow bioreactor with an autotrophic nitrifying population for ammonia oxidation, which was grown on silica sand granules and produced during the growth process nitrite and nitrate. During the second stage, these oxidised forms of nitrogen were successfully reduced to nitrogen gas in an anoxic denitrification fluidised bed reactor. At this stage, methanol was added as an external carbon source for the heterotrophic organisms growing on a silica sand support. The optimum nitrification efficiency was 91% for the highest ammonia concentration at the influent (51 mg NH3‐N/l) and a retention time of 3.7 hours. With a lower ammonia concentration (23 mg NH3‐N/l), the highest nitrification efficiency was 95% corresponding to 1.1 mg NH3‐N/l in the nitrified effluent. In the denitrification process, a 95% removal efficiency of nitrite and nitrate for 55 mg NOx‐N/l at 2.3 hours and a concentration of microorganisms in the reactor of approx. 6,000 mg VSS/l was obtained. As a complementary stage of the nitrogen removal process, a silica sand and powderactivated carbon filter was installed in order to improve the quality of the final effluent in terms of other properties like turbidity, colour and the content of organic matter. |
Author | Nevárez-Moorillón, G. V. Keer-Rendón, A. Bautista-Margulis, R. Manzanares-Papayanópoulos, L. I. Espino-Valdés, M. S. |
Author_xml | – sequence: 1 givenname: M. S. surname: Espino-Valdés fullname: Espino-Valdés, M. S. email: luiza.manzanares@cimav.edu.mx organization: Centro de Investigación en Materiales Avanzados, Miguel de Cervantes 120, Complejo Industrial, Chihuahua, Chih., Mexico – sequence: 2 givenname: L. I. surname: Manzanares-Papayanópoulos fullname: Manzanares-Papayanópoulos, L. I. organization: Centro de Investigación en Materiales Avanzados, Miguel de Cervantes 120, Complejo Industrial, Chihuahua, Chih., Mexico – sequence: 3 givenname: G. V. surname: Nevárez-Moorillón fullname: Nevárez-Moorillón, G. V. organization: Universidad Autónoma de Chihuahua, Facultad de Ciencias Químicas, Apdo. Postal 1542-C, Chihuahua, Chih., Mexico – sequence: 4 givenname: A. surname: Keer-Rendón fullname: Keer-Rendón, A. organization: Universidad Juárez Autónoma de Tabasco, División Académica de Ciencias Biológicas, Km 0.5 Carretera Villahermosa-Tabasco, Villahermosa, Tabasco, Mexico – sequence: 5 givenname: R. surname: Bautista-Margulis fullname: Bautista-Margulis, R. organization: Universidad Juárez Autónoma de Tabasco, División Académica de Ciencias Biológicas, Km 0.5 Carretera Villahermosa-Tabasco, Villahermosa, Tabasco, Mexico |
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Cites_doi | 10.1016/S0043-1354(97)00109-7 10.2166/wst.2000.0417 10.2166/wst.2000.0188 10.1016/S0043-1354(00)00016-6 10.2166/wst.2000.0249 10.1016/S0065-2911(08)60112-5 10.2166/wst.1990.0153 10.2166/wst.2000.0418 10.2166/wst.2000.0242 10.1080/09593339409385424 10.2166/wst.1987.0196 10.2166/wst.2000.0419 |
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Technol. – volume: 47 start-page: 727 issue: 4 year: 1975 end-page: 740 article-title: Nitrogen removal in a pilot plant publication-title: JWPCF – volume: 55 start-page: 221 year: 1983 end-page: 228 article-title: Nitrification facilities start‐up and initial operation publication-title: JWPCF – volume: 41 start-page: 131 issue: 9 year: 2000 end-page: 138 article-title: Technical solutions for upgrading high rate and medium loaded activated sludge plants for nutrient removal publication-title: Water Sci. Technol. – volume: 51 start-page: 1824 year: 1979 end-page: 1840 article-title: Control strategy for biological nitrification systems publication-title: JWPCF – volume: 41 start-page: 5 issue: 4–5 year: 2000 end-page: 12 article-title: Suspended carrier technology allows upgrading high‐rate activated sludge plants for nitrogen removal via process intensification publication-title: Water Sci. 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Technol. doi: 10.2166/wst.2000.0417 contributor: fullname: Chen J. – volume: 55 start-page: 221 year: 1983 ident: e_1_2_1_28_2 article-title: Nitrification facilities start‐up and initial operation publication-title: JWPCF contributor: fullname: Bailey W.F. – volume: 41 start-page: 131 issue: 9 year: 2000 ident: e_1_2_1_10_2 article-title: Technical solutions for upgrading high rate and medium loaded activated sludge plants for nutrient removal publication-title: Water Sci. Technol. doi: 10.2166/wst.2000.0188 contributor: fullname: Chudova P. – volume: 46 start-page: 937 issue: 5 year: 1974 ident: e_1_2_1_15_2 article-title: Plastic medium trickling filters for biological nitrogen control publication-title: JWPCF contributor: fullname: Duddles G.A. – volume: 53 start-page: 176 issue: 2 year: 1981 ident: e_1_2_1_9_2 article-title: Nitrification and denitrification of an industrial wastewater publication-title: JWPCF contributor: fullname: Sutton P.M. – ident: e_1_2_1_13_2 doi: 10.1016/S0043-1354(00)00016-6 – volume: 41 start-page: 101 issue: 12 year: 2000 ident: e_1_2_1_20_2 article-title: Simultaneous removal of nitrogen and phosphorus in a two‐biofilter system publication-title: Water Sci. Technol. doi: 10.2166/wst.2000.0249 contributor: fullname: Pak D. – ident: e_1_2_1_2_2 – ident: e_1_2_1_5_2 doi: 10.1016/S0065-2911(08)60112-5 – volume: 12 start-page: 551 issue: 5 year: 1980 ident: e_1_2_1_11_2 article-title: Influencing parameters on the nitrification‐denitrification performance of a single stage activated sludge plant publication-title: Progr. Wat. Tech. contributor: fullname: Matsché N. – volume: 46 start-page: 181 issue: 1 year: 1974 ident: e_1_2_1_8_2 article-title: Full‐scale testing of a water reclamation system publication-title: JWPCF contributor: fullname: Horstkotte G.A. – volume: 43 start-page: 2059 year: 1971 ident: e_1_2_1_7_2 article-title: Nitrification and denitrification in activated sludge systems publication-title: JWPCF contributor: fullname: Mulbarger M.C. – volume: 47 start-page: 727 issue: 4 year: 1975 ident: e_1_2_1_16_2 article-title: Nitrogen removal in a pilot plant publication-title: JWPCF contributor: fullname: Ericsson B. – volume: 47 start-page: 46 year: 1975 ident: e_1_2_1_25_2 article-title: Packed‐bed reactors for secondary effluent BOD and ammonia removal publication-title: JWPCF contributor: fullname: Young J.C. – volume: 22 start-page: 273 issue: 1 year: 1990 ident: e_1_2_1_19_2 article-title: New developments in complete nitrogen removal with biological aerated filters publication-title: Water Sci. Technol. doi: 10.2166/wst.1990.0153 contributor: fullname: Rogalia F. – volume: 41 start-page: 5 issue: 4 year: 2000 ident: e_1_2_1_14_2 article-title: Suspended carrier technology allows upgrading high‐rate activated sludge plants for nitrogen removal via process intensification publication-title: Water Sci. Technol. doi: 10.2166/wst.2000.0418 contributor: fullname: Münch E. – volume: 42 start-page: 65 issue: 12 year: 2000 ident: e_1_2_1_22_2 article-title: Organic and nitrogen removal with minimal COD requirement by integration of sequestered denitrification and separated nitrification in a low‐loaded activated sludge process publication-title: Water Sci. Technol. doi: 10.2166/wst.2000.0242 contributor: fullname: Shin H‐S. – ident: e_1_2_1_24_2 – ident: e_1_2_1_23_2 – ident: e_1_2_1_17_2 doi: 10.1080/09593339409385424 – volume: 51 start-page: 1032 year: 1979 ident: e_1_2_1_26_2 article-title: Nitrification treatability study for Carrollton, G.A publication-title: JWPCF contributor: fullname: Reinhart D.R. – volume: 47 start-page: 2045 year: 1975 ident: e_1_2_1_6_2 article-title: Pilot‐scale, high‐rate biological denitrification publication-title: JWPCF contributor: fullname: Jeris J.S. – volume: 19 start-page: 139 year: 1987 ident: e_1_2_1_18_2 article-title: Design considerations for a nitrification/denitrification process using two fixed‐bed reactors in series publication-title: Water Sci. Technol. doi: 10.2166/wst.1987.0196 contributor: fullname: Jiménez B. – volume: 41 start-page: 13 issue: 4 year: 2000 ident: e_1_2_1_21_2 article-title: Pilot testing and preliminary design of moving bed biofilm reactors for nitrogen removal at the FREVAR wastewater treatment plant publication-title: Water Sci. Technol. doi: 10.2166/wst.2000.0419 contributor: fullname: Rusten B. – volume: 51 start-page: 1824 year: 1979 ident: e_1_2_1_27_2 article-title: Control strategy for biological nitrification systems publication-title: JWPCF contributor: fullname: Young J.C. |
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Snippet | Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The system was... Abstract Nitrogen removal was studied in a pilot scale continuous flow system consisting of two reactors in series for nitrification and denitrification. The... |
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Title | Biological Removal of Nitrogen to Improve the Quality of Reclaimed Wastewater for Groundwater Recharge |
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