Treating the filtrate of mainstream anaerobic membrane bioreactor with the pilot-scale sludge-type one-stage partial nitritation/anammox process operated from 25 to 15 °C.

Ammonium Compounds Anaerobic Ammonia Oxidation Anaerobiosis Bioreactors / microbiology Denitrification Nitrogen Oxidation-Reduction Sewage Wastewater
Anammox Low temperature Municipal wastewater Nitritation One-stage Pilot-scale

Journal

Bioresource technology
ISSN: 1873-2976
Titre abrégé: Bioresour Technol
Pays: England
ID NLM: 9889523

Informations de publication

Date de publication:
May 2022
Historique:
received: 28 01 2022
revised: 20 03 2022
accepted: 22 03 2022
pubmed: 31 3 2022
medline: 14 4 2022
entrez: 30 3 2022
Statut: ppublish

Résumé

At ambient temperature condition, the one-stage partial nitritation/anammox (PNA) process has been successfully adopted to treat the filtrate from the mainstream anaerobic membrane bioreactor (AnMBR). However, there is no investigation of the performance of this process at low-temperature condition. In this study, the nitrogen removal performance of a pilot-scale PNA reactor at the temperature of 15 °C for treating the filtrate of a mainstream AnMBR was investigated. The nitrogen removal rate of 0.09 kg/m

Identifiants

DOI: 10.1016/j.biortech.2022.127062 PMID: 35351558
pubmed: 35351558
pii: S0960-8524(22)00391-1
doi: 10.1016/j.biortech.2022.127062
pii:
doi:

Substances chimiques

Ammonium Compounds 0
Sewage 0
Waste Water 0
Nitrogen N762921K75

Types de publication

Journal Article

Langues

eng

Sous-ensembles de citation

IM

Pagination

127062

Informations de copyright

Copyright © 2022 Elsevier Ltd. All rights reserved.

Auteurs

Yan Guo (Y)

Department of Environmental Engineering, School of Energy and Environmental Engineering, University of Science and Technology Beijing, Beijing 100083, PR China; Department of Civil and Environmental Engineering, Graduate School of Engineering, Tohoku University, 6-6-06 Aramaki Aza Aoba Aoba-ku, Sendai, Miyagi 980-8579, Japan.

Eli Hendrik Sanjaya (EH)

Department of Chemistry, State University of Malang (Universitas Negeri Malang), Jl. Semarang No. 5, Malang, East Java 65145, Indonesia.

Chao Rong (C)

Graduate School of Environmental Studies, Tohoku University, 6-6-06 Aramaki Aza Aoba, Aoba-ku, Sendai, Miyagi 980-8579, Japan.

Tianjie Wang (T)

Graduate School of Environmental Studies, Tohoku University, 6-6-06 Aramaki Aza Aoba, Aoba-ku, Sendai, Miyagi 980-8579, Japan.

Zibin Luo (Z)

Department of Civil and Environmental Engineering, Graduate School of Engineering, Tohoku University, 6-6-06 Aramaki Aza Aoba Aoba-ku, Sendai, Miyagi 980-8579, Japan.

Hong Chen (H)

Key Laboratory of Dongting Lake Aquatic Eco-Environmental Control and Restoration of Hunan Province, Changsha University of Science & Technology, Changsha 410004, PR China.

Hong Wang (H)

Key Laboratory of Dongting Lake Aquatic Eco-Environmental Control and Restoration of Hunan Province, Changsha University of Science & Technology, Changsha 410004, PR China.

Taira Hanaoka (T)

Solution Engineering Group, Environmental Engineering Department, Mitsubishi Kakoki Kaisha, Ltd, 1-2 Miyamae-Cho, Kawasaki-Ku, Kawasaki, Kanagawa 210-0012, Japan.

Shinichi Sakemi (S)

Solution Engineering Group, Environmental Engineering Department, Mitsubishi Kakoki Kaisha, Ltd, 1-2 Miyamae-Cho, Kawasaki-Ku, Kawasaki, Kanagawa 210-0012, Japan.

Masami Ito (M)

Global Water Recycling and Reuse System Association, Japan, 5-1, Soto-Kanda 1-Chome Chiyoda-Ku, Tokyo 101-0021, Japan.

Shigeki Kobayashi (S)

Global Water Recycling and Reuse System Association, Japan, 5-1, Soto-Kanda 1-Chome Chiyoda-Ku, Tokyo 101-0021, Japan.

Masumi Kobayashi (M)

Separation and Aqua Chemicals Department, Mitsubishi Chemical Corporation, Gate City Osaki East Tower, 11-2 Osaki 1-chome Shinagawa-Ku, Tokyo 141-0032, Japan.

Yu-You Li (YY)

Department of Civil and Environmental Engineering, Graduate School of Engineering, Tohoku University, 6-6-06 Aramaki Aza Aoba Aoba-ku, Sendai, Miyagi 980-8579, Japan; Graduate School of Environmental Studies, Tohoku University, 6-6-06 Aramaki Aza Aoba, Aoba-ku, Sendai, Miyagi 980-8579, Japan. Electronic address: gyokuyu.ri.a5@tohoku.ac.jp.

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Classifications MeSH

questionsmedicales.fr › Produits chimiques inorganiques › Composés de l'azote › Composés d'ammonium › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Phénomènes biologiques › Phénomènes écologiques et environnementaux › Cycle de l'azote › Oxydation anaérobie de l'ammonium › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Métabolisme › Anaérobiose › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Technologie, industrie et agriculture › Technologie › Biotechnologie › Bioréacteurs › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Phénomènes biologiques › Phénomènes écologiques et environnementaux › Cycle de l'azote › Dénitrification › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Produits chimiques inorganiques › Gaz › Azote › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Métabolisme › Métabolisme énergétique › Oxydoréduction › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Mélanges complexes › Eaux d'égout › Treating the filtrate of mainstream anaerobic...
questionsmedicales.fr › Environnement et santé publique › Santé publique › Pollution de l'environnement › Déchets › Eaux usées › Treating the filtrate of mainstream anaerobic...