TY - JOUR
T1 - Characteristics of DO, organic matter, and ammonium profile for practical-scale DHS reactor under various organic load and temperature conditions
AU - Nomoto, Naoki
AU - Ali, Muntjeer
AU - Jayaswal, Komal
AU - Iguchi, Akinori
AU - Hatamoto, Masashi
AU - Okubo, Tsutomu
AU - Takahashi, Masanobu
AU - Kubota, Kengo
AU - Tagawa, Tadashi
AU - Uemura, Shigeki
AU - Yamaguchi, Takashi
AU - Harada, Hideki
N1 - Funding Information:
This study was supported by the Science and Technology Research Partnership for Sustainable Development (SATREPS) in Japan and also supported by Japan International Cooperation Agency and Japan Science and Technology Agency.
Funding Information:
This study was supported by the Science and Technology Research Partnership for Sustainable Development (SATREPS) in Japan and also supported by Japan International Cooperation Agency and Japan Science and Technology Agency. The authors are grateful to the National River Conservation Directorate (NRCD); Ministry of Environment, Forest and Climate Change (MOEF); the Indian government; and the Uttar Pradesh Jal Nigam (UPJN) for extending various forms of assistance. The authors also thank Mr A. Noori and Mr P. Shekhar for contributing to the experiments in India.
Publisher Copyright:
© 2017 Informa UK Limited, trading as Taylor & Francis Group.
PY - 2018/4/3
Y1 - 2018/4/3
N2 - Profile analysis of the down-flow hanging sponge (DHS) reactor was conducted under various temperature and organic load conditions to understand the organic removal and nitrification process for sewage treatment. Under high organic load conditions (3.21–7.89 kg-COD m−3day−1), dissolved oxygen (DO) on the upper layer of the reactor was affected by organic matter concentration and water temperature, and sometimes reaches around zero. Almost half of the CODCr was removed by the first layer, which could be attributed to the adsorption of organic matter on sponge media. After the first layer, organic removal proceeded along the first-order reaction equation from the second to the fourth layers. The ammoniacal nitrogen removal ratio decreased under high organic matter concentration (above 100 mg L−1) and low DO (less than 1 mg L−1) condition. Ammoniacal nitrogen removal proceeded via a zero-order reaction equation along the reactor height. In addition, the profile results of DO, CODCr, and NH3-N were different in the horizontal direction. Thus, it is thought the concentration of these items and microbial activities were not in a uniform state even in the same sponge layer of the DHS reactor.
AB - Profile analysis of the down-flow hanging sponge (DHS) reactor was conducted under various temperature and organic load conditions to understand the organic removal and nitrification process for sewage treatment. Under high organic load conditions (3.21–7.89 kg-COD m−3day−1), dissolved oxygen (DO) on the upper layer of the reactor was affected by organic matter concentration and water temperature, and sometimes reaches around zero. Almost half of the CODCr was removed by the first layer, which could be attributed to the adsorption of organic matter on sponge media. After the first layer, organic removal proceeded along the first-order reaction equation from the second to the fourth layers. The ammoniacal nitrogen removal ratio decreased under high organic matter concentration (above 100 mg L−1) and low DO (less than 1 mg L−1) condition. Ammoniacal nitrogen removal proceeded via a zero-order reaction equation along the reactor height. In addition, the profile results of DO, CODCr, and NH3-N were different in the horizontal direction. Thus, it is thought the concentration of these items and microbial activities were not in a uniform state even in the same sponge layer of the DHS reactor.
KW - developing country
KW - Down-flow hanging sponge
KW - high organic load
KW - nitrification
KW - sewage treatment
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U2 - 10.1080/09593330.2017.1316319
DO - 10.1080/09593330.2017.1316319
M3 - Article
C2 - 28387149
AN - SCOPUS:85017702511
SN - 0959-3330
VL - 39
SP - 907
EP - 916
JO - Environmental Technology (United Kingdom)
JF - Environmental Technology (United Kingdom)
IS - 7
ER -