MX2010003655A - Metodo y planta para el tratamiento de efluentes que contienen nitrogeno en un reactor por lotes en secuencia. - Google Patents

Metodo y planta para el tratamiento de efluentes que contienen nitrogeno en un reactor por lotes en secuencia.

Info

Publication number
MX2010003655A
MX2010003655A MX2010003655A MX2010003655A MX2010003655A MX 2010003655 A MX2010003655 A MX 2010003655A MX 2010003655 A MX2010003655 A MX 2010003655A MX 2010003655 A MX2010003655 A MX 2010003655A MX 2010003655 A MX2010003655 A MX 2010003655A
Authority
MX
Mexico
Prior art keywords
stage
during
nonaerated
ammonium
batch reactor
Prior art date
Application number
MX2010003655A
Other languages
English (en)
Inventor
Adriana Gonzalez Ospina
Original Assignee
Degremont
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Degremont filed Critical Degremont
Publication of MX2010003655A publication Critical patent/MX2010003655A/es

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/006—Regulation methods for biological treatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/301—Aerobic and anaerobic treatment in the same reactor
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/302—Nitrification and denitrification treatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/16—Nitrogen compounds, e.g. ammonia
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/001—Upstream control, i.e. monitoring for predictive control
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/003—Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/05—Conductivity or salinity
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/14—NH3-N
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/22—O2
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/40—Liquid flow rate
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Treating Waste Gases (AREA)

Abstract

Se describe un m?todo para el tratamiento de efluentes que contienen nitr?geno en forma de amonio, de acuerdo con lo cual: un volumen del efluente que va a ser tratado en un ciclo completo se introduce dentro del reactor por lotes en fracciones de volumen sucesivas, cada fracci?n de volumen es tratada durante un ciclo secundario: cada ciclo secundario comprende una fase de alimentaci?n con una fracci?n de volumen y, de una manera alternativa, dos etapas de tratamiento, es decir, una primera etapa aireada, durante la cual se lleva a cabo una oxidaci?n completa o parcial del amonio de manera que genera nitritos, seguido por una segunda etapa no aireada, durante la cual los nitritos producidos y el amonio se convierten a nitr?geno gaseoso. Durante la primera etapa de aireado, la concentraci?n de ox?geno disuelta en el reactor por lotes se mantiene entre 0.1 mgO2 71 y 0.6 mgO2/l; la relaci?n N-N2: N-N4 se ajusta de manera que se encuentre entre 0.9 y 1.5 al inicio de la etapa no aireada; y la fase no aireada se lleva a cabo por desamonificaci?n, sin el suministro de un sustrato basado en carbono.
MX2010003655A 2007-10-09 2008-10-06 Metodo y planta para el tratamiento de efluentes que contienen nitrogeno en un reactor por lotes en secuencia. MX2010003655A (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0707080A FR2921917B1 (fr) 2007-10-09 2007-10-09 Procede et installation de traitement d'effluents contenant de l'azote dans un reacteur biologique sequentiel.
PCT/FR2008/001394 WO2009080912A2 (fr) 2007-10-09 2008-10-06 Procede et installation de traitement d'effluents contenant de l'azote dans un reacteur biologique sequentiel

Publications (1)

Publication Number Publication Date
MX2010003655A true MX2010003655A (es) 2010-05-17

Family

ID=39370864

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2010003655A MX2010003655A (es) 2007-10-09 2008-10-06 Metodo y planta para el tratamiento de efluentes que contienen nitrogeno en un reactor por lotes en secuencia.

Country Status (9)

Country Link
US (1) US8298422B2 (es)
EP (1) EP2197800B1 (es)
CN (1) CN101821207B (es)
BR (1) BRPI0817713B1 (es)
CA (1) CA2701786C (es)
ES (1) ES2567568T3 (es)
FR (1) FR2921917B1 (es)
MX (1) MX2010003655A (es)
WO (1) WO2009080912A2 (es)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2952932B1 (fr) 2009-11-20 2012-11-09 Otv Sa Procede de traitement d'eau au sein d'un reacteur biologique sequentiel comprenant une mesure en ligne de la concentration en nitrites a l'interieur dudit reacteur
CN102276103B (zh) * 2010-09-06 2014-02-12 中国环境科学研究院 一体化原位脱氮养殖废水生物处理装置及处理方法
FR2966146A1 (fr) * 2010-10-18 2012-04-20 Veolia Water Solutions & Tech Procede de traitement d'eau au sein d'un reacteur biologique sequentiel comprenant une mesure en ligne de la concentration en nitrites
CA2852298A1 (en) * 2011-11-16 2013-05-23 Evoqua Water Technologies Llc Using continuous nitrate measurement to control aeration in an aerated-anoxic process
KR101380406B1 (ko) * 2012-04-05 2014-04-10 주식회사 포스코 붕소 회수 장치, 붕소 회수 방법 및 붕소 회수 시스템
RU2640767C2 (ru) * 2012-09-13 2018-01-11 Ди.Си. УОТЕР ЭНД СЬЮЭР ОТОРИТИ Способ и устройство для удаления азота при обработке сточных вод
SE536972C2 (sv) * 2012-09-25 2014-11-18 Boliden Mineral Ab Ett förfarande och en apparat för samtidigt avlägsnande av tiosalt och kväveföreningar i avloppsvatten
FR3001212B1 (fr) 2013-01-18 2016-09-16 Degremont Procede de traitement d'effluents contenant de l'azote sous forme d'ammonium, et installation pour la mise en oeuvre de ce procede
MX2015011828A (es) * 2013-03-14 2016-01-08 D C Water & Sewer Authority Metodo y aparato para maximizar la eliminacion de nitrogeno de aguas residuales.
ITRM20130346A1 (it) * 2013-06-17 2014-12-18 Chemitec S R L Metodo ed apparato di controllo di un processo di trattamento biologico di acque reflue di origine civile
CN103449659B (zh) * 2013-07-23 2014-12-24 宁波清天地环境工程有限公司 短程硝化反硝化生物脱氮装置
WO2015011213A1 (en) * 2013-07-24 2015-01-29 Universitat Autonoma De Barcelona A method and a system for enhancing nitrogen removal in a granular sequencing batch reactor (gsbr) and a computer program product
FR3024726B1 (fr) * 2014-08-08 2023-05-05 Degremont Procede batch sequence pour reduire la teneur en azote dans les eaux residuaires
JP6448382B2 (ja) * 2015-01-19 2019-01-09 水ｉｎｇ株式会社 窒素含有廃水の脱窒方法及び脱窒装置
NL2018967B1 (en) * 2017-05-23 2018-12-04 Haskoningdhv Nederland Bv Controlled simultaneous nitrification and denitrification in wastewater treatment
KR101962566B1 (ko) 2018-01-04 2019-07-17 두산중공업 주식회사 연속회분식 반응조를 활용한 저 에너지 혐기성 암모늄 산화 시스템 및 이 시스템을 위한 선행 스케줄링 방법
TR201818516A2 (tr) * 2018-12-04 2020-06-22 Tuerkiye Bilimsel Ve Teknolojik Arastirma Kurumu Tuebitak Anaerobi̇k amonyum oksi̇dasyonu bakteri̇si̇ni̇n otomati̇k kontrollü kesi̇kli̇ reaktörde zengi̇nleşti̇ri̇lmesi̇ i̇çi̇n bi̇r yöntem
CN111995083B (zh) * 2020-08-25 2022-05-06 浙江京禾水务科技有限公司 一种用于厌氧氨氧化反应工艺的智能实时曝气控制方法
BR112023018476A2 (pt) 2021-03-12 2023-11-14 Bernhard Wett Método e aparelho para multi-seleção em tratamento de águas residuais
CN113526658A (zh) * 2021-06-01 2021-10-22 青岛大学 一种快速短程反硝化处理污水的装置和方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO970550D0 (no) * 1997-02-06 1997-02-06 Hifo Tech As Biologisk nitrogenfjerning fra avlöpsvann
DE19827877A1 (de) * 1998-06-23 2000-01-20 Michael Bongards Prozeßoptimierung einer nach dem Belebungsverfahren arbeitenden Kläranlage
AU2435401A (en) * 1999-12-16 2001-06-25 Robert G. Whiteman Fermentation system, methods, and apparatus
FR2889180B1 (fr) * 2005-08-01 2008-04-04 Suez Environnement Sa Procede et installation de traitement d'effluents concentres en azote dans un reacteur biologique sequentiel a cycles fractionnes
JP5177802B2 (ja) * 2009-03-25 2013-04-10 株式会社日立プラントテクノロジー 廃水処理方法及び廃水処理装置

Also Published As

Publication number Publication date
ES2567568T3 (es) 2016-04-25
US8298422B2 (en) 2012-10-30
WO2009080912A2 (fr) 2009-07-02
BRPI0817713A2 (pt) 2015-03-31
WO2009080912A3 (fr) 2009-08-20
EP2197800B1 (fr) 2016-01-13
CA2701786A1 (fr) 2009-07-02
CN101821207B (zh) 2013-08-14
EP2197800A2 (fr) 2010-06-23
CN101821207A (zh) 2010-09-01
US20100303695A1 (en) 2010-12-02
FR2921917B1 (fr) 2011-04-08
CA2701786C (fr) 2013-01-08
FR2921917A1 (fr) 2009-04-10
BRPI0817713B1 (pt) 2019-03-19

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