ES2026546T3 - Control de regimen de aumento de filtros de medio granular de lecho pulsatorio. - Google Patents

Control de regimen de aumento de filtros de medio granular de lecho pulsatorio.

Info

Publication number
ES2026546T3
ES2026546T3 ES198787307949T ES87307949T ES2026546T3 ES 2026546 T3 ES2026546 T3 ES 2026546T3 ES 198787307949 T ES198787307949 T ES 198787307949T ES 87307949 T ES87307949 T ES 87307949T ES 2026546 T3 ES2026546 T3 ES 2026546T3
Authority
ES
Spain
Prior art keywords
bed
vibration
solids
liquid
liquid level
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
ES198787307949T
Other languages
English (en)
Inventor
Gary August Garzonetti
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
US Filter Zimpro Inc
Original Assignee
Zimpro Passavant Environmental Systems Inc
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 Zimpro Passavant Environmental Systems Inc filed Critical Zimpro Passavant Environmental Systems Inc
Application granted granted Critical
Publication of ES2026546T3 publication Critical patent/ES2026546T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/02—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration
    • B01D24/20—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof with the filter bed stationary during the filtration the filtering material being provided in an open container
    • B01D24/22—Downward filtration, the filter material being supported by pervious surfaces
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/38—Feed or discharge devices
    • B01D24/40—Feed or discharge devices for feeding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/46—Regenerating the filtering material in the filter
    • B01D24/4631—Counter-current flushing, e.g. by air
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
    • B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
    • B01D24/4869—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration by level measuring

Landscapes

  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Filtration Of Liquid (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Control Of Heat Treatment Processes (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Lock And Its Accessories (AREA)
  • Networks Using Active Elements (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Mushroom Cultivation (AREA)
  • Polymerisation Methods In General (AREA)
  • Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)

Abstract

UN METODO DE CONTROL DE LA VIBRACION DE UN FILTRO (1) DE MEDIO GRANULAR ES PRESENTADO BASADO EN LA DETERMINACION DEL PODER DE INCLINACION DEL NIVEL DE LIQUIDO EN EL TANQUE DE FILTRO (3) SOBRE ELMEDIO DE FILTRACION (1). UN SISTEMA DE VIBRACION ES ACTIVADO POR MEDIO DEL CUAL UNA VIBRACION; EN EL CUAL FLUJOS SUB - FLUIDOS DE UN FLUIDO NO DIRIGIDO DE FORMA ASCENDENTE A TRAVES DEL MEDIO DE FILTRO (1) DESDE UNA MATERIA DE ORIFICIOS (7), ES INICIADA CUANDO EL FONDO DE INCLINACION DEL NIVEL DE LIQUIDO DETERMINADO ALCANZA UN VALOR PREDETERMINADO. LOS FLUJOS DE VIBRACIONES DESALOJAN SOLIDOS DE LA SUPERFICIE (11) DEL LECHO (1) Y PROVOCAN QUE UNA PARTE DE LOS SOLIDOS SEAN ALMACENADOS DENTRO DEL LECHO EN UN LUGAR DETERMINADO, DE ESTA MANERA DISMINUYE LA RESISTENCIA DEL LECHO Y REDUCE EL FONDE DE INCLINACION DEL NIVEL DEL LIQUIDO. LA FRECUENCIA DE REMOLINOS NECESARIA ES OPTIMIZADA, POR CONSIGUIENTE SOBRE UN ANCHO RANGO DE LA CANTIDAD DE SOLIDOS, CANTIDAD DE LIQUIDO Y OTROS FACTORES QUE AFECTA LA FILTRACION. LOS REMOLINOS PUEDEN SER INICIADOS DESPUES DE UN DETERMINADO NUMERO DE VIBRACIONES, DESPUES DE QUE UN TIEMPO DE FILTRACION FIJADO PREVIAMENTE HAY TRANSCURRIDO O CUANDO EL NIVEL DE LIQUIDO EN EL TANQUE (3) ALCANCE UN VALOR ALTO PERFILADO.
ES198787307949T 1987-01-28 1987-09-09 Control de regimen de aumento de filtros de medio granular de lecho pulsatorio. Expired - Lifetime ES2026546T3 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US07/008,020 US4693831A (en) 1987-01-28 1987-01-28 Rise-rate control of pulsed-bed granular medium filters

Publications (1)

Publication Number Publication Date
ES2026546T3 true ES2026546T3 (es) 1992-05-01

Family

ID=21729391

Family Applications (1)

Application Number Title Priority Date Filing Date
ES198787307949T Expired - Lifetime ES2026546T3 (es) 1987-01-28 1987-09-09 Control de regimen de aumento de filtros de medio granular de lecho pulsatorio.

Country Status (10)

Country Link
US (1) US4693831A (es)
EP (1) EP0279975B1 (es)
JP (1) JPS63185417A (es)
KR (1) KR960001376B1 (es)
AT (1) ATE69392T1 (es)
AU (1) AU589028B2 (es)
CA (1) CA1305073C (es)
DE (1) DE3774564D1 (es)
ES (1) ES2026546T3 (es)
NO (1) NO167190C (es)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2371192A1 (es) * 2009-12-17 2011-12-28 Ohl Medio Ambiente, Inima, S.A.U. Filtro de pretratamiento y acondicionamiento de agua del tipo de lecho granular cerrado a presion con medios de lavado a contracorriente.

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818414A (en) * 1988-03-25 1989-04-04 Zimpro/Passavant Inc. Slime control for primary filtration systems
DE3828821A1 (de) * 1988-08-25 1990-03-01 Bayer Ag Verfahren zur erkennung der ueberflutung einer oberflaeche
US4976873A (en) * 1989-12-14 1990-12-11 Zimpro/Passavant Inc. Pulsing portions of a filter cell to extend a filter run
FR2670682B1 (fr) * 1990-12-21 1993-10-15 Toulouse Inst Nal Sciences Appli Procede et reacteur de traitement d'eau utilisant un lit granulaire adapte pour assurer une filtration ou une filtration associee a une epuration biologique de l'eau.
US5089147A (en) * 1991-05-01 1992-02-18 Zimpro Passavant Environmental Systems, Inc. Underdrain for granular medium filter
DE4302321C1 (de) * 1993-01-28 1994-03-17 Envicon Klaertech Verwalt Becken zur Elimination von Schwebeteilchen aus Abwässern
US5534202A (en) * 1994-04-05 1996-07-09 Roberts Filter Manufacturing Company Air grid for underdrains and similar systems
EA001562B1 (ru) * 1996-08-19 2001-04-23 Вольфганг Шенк Гмбх Биореактор
US5759387A (en) * 1996-09-26 1998-06-02 Essef Corporation Grey water filter tank recovery system and filter backwashing system
AU747192B2 (en) * 1998-10-02 2002-05-09 Dennis Aldo Tull Pump strainer cleaning apparatus
JP2002119807A (ja) * 2000-10-17 2002-04-23 Sumitomo Heavy Ind Ltd 濾過装置の逆洗方法
DE10106322B4 (de) * 2001-02-09 2005-11-17 Inka-Holding Und Immobilien Gmbh & Co. Kg Wasserfilter
US7045067B2 (en) * 2004-08-05 2006-05-16 Eco-Tec Limited Method and apparatus for increasing filter contaminant loading capacity
CN100412003C (zh) * 2006-09-25 2008-08-20 山东建筑大学 曝气生物滤池
US9718004B2 (en) 2011-10-03 2017-08-01 Ishigaki Company Limited Filter medium layer and filter device provided with same
CN103316511B (zh) * 2013-07-08 2015-05-20 山东金博士环境科技有限公司 一种o型滤池
US20160045844A1 (en) * 2014-08-13 2016-02-18 Samuel N. Tyler Pulsed Backwash Method and Apparatus
AU2015327754A1 (en) * 2014-10-01 2017-04-06 Nexus Ewater Pty Ltd Method of filtering waste water
US11185800B2 (en) * 2017-08-15 2021-11-30 Conopco, Inc. Apparatus and method for filtering aqueous liquid
EP3727627B1 (en) 2017-12-22 2024-05-29 Ozono Polaris, S.A. DE C.V. Process for back-and-forth washing of adsorptive media
CN112915641B (zh) * 2021-03-18 2022-06-14 上海威派格智慧水务股份有限公司 一种滤池反冲洗控制方法
SE545635C2 (en) * 2022-02-24 2023-11-21 Zeo Concept Ece Ab A filter system for purification of a fluid comprising an acoustic wave creating arrangement

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR349450A (fr) * 1904-12-01 1905-05-29 Frank Candy Filtre à courant montant
BE471545A (es) * 1946-10-16
GB966394A (en) * 1962-01-30 1964-08-12 Candy Filter Company Ltd Improvements relating to gravity filters
US3459302A (en) * 1967-04-25 1969-08-05 Hydro Clear Corp Apparatus and method of filtering solids from a liquid effluent
US3717251A (en) * 1970-09-03 1973-02-20 Q Hampton Method and apparatus for filtering solids
US3817378A (en) * 1971-06-22 1974-06-18 Hydro Clear Corp Method and apparatus for filtering solids from a liquid effluent
US4019985A (en) * 1975-07-30 1977-04-26 Texaco Inc. Methods for fluidizing a filter media
US4627923A (en) * 1984-09-20 1986-12-09 International Tectonics Incorporated Apparatus and method of filtering solids from a liquid effluent

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2371192A1 (es) * 2009-12-17 2011-12-28 Ohl Medio Ambiente, Inima, S.A.U. Filtro de pretratamiento y acondicionamiento de agua del tipo de lecho granular cerrado a presion con medios de lavado a contracorriente.

Also Published As

Publication number Publication date
NO873747D0 (no) 1987-09-08
JPS63185417A (ja) 1988-08-01
NO873747L (no) 1988-07-29
NO167190C (no) 1991-10-16
CA1305073C (en) 1992-07-14
EP0279975A1 (en) 1988-08-31
AU589028B2 (en) 1989-09-28
ATE69392T1 (de) 1991-11-15
DE3774564D1 (de) 1991-12-19
KR890006278A (ko) 1989-06-12
US4693831A (en) 1987-09-15
NO167190B (no) 1991-07-08
EP0279975B1 (en) 1991-11-13
AU7670087A (en) 1988-08-04
KR960001376B1 (ko) 1996-01-26

Similar Documents

Publication Publication Date Title
AU589028B2 (en) Rise-rate control of pulsed-bed granular medium filters
SG87049A1 (en) An apparatus for the separation of solids from flowing liquids
US3841485A (en) Automatically backwashed gravity filter
JPS5684603A (en) Oil-water separating method by grain coarsening
EP0102767A3 (en) Granular media filter
ATE91913T1 (de) Leichtfluessigkeitsabscheider.
EP0589573A3 (en) Float for a device operated by the level.
WO1995013124A1 (en) Dynamic sand filter
JPS627336B2 (es)
EP0091600A3 (en) Device for automatically adjusting the level of a pumping tank
ATE382412T1 (de) Filterelement mit einem auf einen stützkörper aufgebrachten filtermedium
SE8300797D0 (sv) Backventil
SU909343A1 (ru) Входное устройство насоса
KR860002291A (ko) 고형물이 포함된 유체의 처리장치
HK52796A (en) Filter device for aquarium tank
DE69210623D1 (de) Flüssigkeitsbehälter
SU381366A1 (ru) •5срсоюзнаь '
ATE149374T1 (de) Abscheideanlage
KR970005694Y1 (ko) 바이패스 통로를 갖춘 유니언죠인트
ATE231737T1 (de) Unter wasser gesetzter, belüfteter filter
JPS63256827A (ja) 汚泥沈降界面検出器
JPH0244880Y2 (es)
EP0030803A1 (en) Apparatus and method for treating an aqueous effluent which contains suspended oil particles
JPS61164698A (ja) 水処理物質のインジエクタ
Bhole et al. Berry Seed Shell as Filter Media

Legal Events

Date Code Title Description
FG2A Definitive protection

Ref document number: 279975

Country of ref document: ES