EP 3541757 A1 20190925 - METHOD FOR DISINFECTING AND CLEANING LIQUID MEDIA AND METHOD FOR SEPARATING SOLID AND LIQUID CONSTITUENTS OF A SOLID-LIQUID MIXTURE AND APPARATUS FOR IMPLEMENTING THE METHOD
Title (en)
METHOD FOR DISINFECTING AND CLEANING LIQUID MEDIA AND METHOD FOR SEPARATING SOLID AND LIQUID CONSTITUENTS OF A SOLID-LIQUID MIXTURE AND APPARATUS FOR IMPLEMENTING THE METHOD
Title (de)
VERFAHREN ZUR ENTKEIMUNG UND REINIGUNG VON FLÜSSIGEN MEDIEN SOWIE VERFAHREN ZUM SEPARIEREN FESTER UND FLÜSSIGER BESTANDTEILE EINER FEST-FLÜSSIG-MISCHUNG UND VORRICHTUNG ZUR UMSETZUNG DER VERFAHREN
Title (fr)
PROCÉDÉ DE STÉRILISATION ET DE PURIFICATION DE MILIEUX LIQUIDES ET PROCÉDÉ DE SÉPARATION DE CONSTITUANTS SOLIDES ET LIQUIDES D'UN MÉLANGE SOLIDE-LIQUIDE ET DISPOSITIF POUR LA MISE EN OEUVRE DES PROCÉDÉS
Publication
Application
Priority
- EP 2016001908 W 20161116
- EP 2017001102 W 20170919
Abstract (en)
[origin: US2020055759A1] The invention relates to a method for cleaning and/or disinfecting liquid and/or aqueous media, comprising the following method steps: cavitation treatment of the medium, in particular by means of jet cavitation, at a negative pressure <1 bar, preferably 0.3 to 0.7 bar; subsequent treatment of the medium in a hydrodynamic reactor having a a rotating magnetic field and magnetic and/or magnetisable elements, in particular having ferromagnetic needles or a rotating cutting mechanism at a negative pressure <1 bar, preferably 0.3 to 0.7 bar; subsequent separation, in particular sedimentation of the treated medium by means of sludge separation at a negative pressure of <1 bar, preferably 0.3 to 0.7 bar. The invention further relates to an apparatus having the following features: a cavitator formed in particular as a jet cavitator, which is equipped with a negative pressure generator, a hydrodynamic reactor having a rotating magnetic field and magnetic and/or magnetisable elements, in particular having ferromagnetic needles and/or a rotating cutting mechanism, a unit for separation, in particular for sedimentation, preferably combined with a sludge separation apparatus.
IPC 8 full level
C02F 9/00 (2006.01); C02F 1/32 (2006.01); C02F 1/34 (2006.01); C02F 1/36 (2006.01); C02F 1/48 (2006.01); C02F 1/52 (2006.01); C02F 1/66 (2006.01); C02F 1/74 (2006.01); C02F 1/78 (2006.01); C02F 11/10 (2006.01); C02F 103/20 (2006.01)
CPC (source: EP US)
C02F 9/00 (2013.01 - EP US); C02F 1/004 (2013.01 - EP US); C02F 1/32 (2013.01 - EP); C02F 1/325 (2013.01 - US); C02F 1/34 (2013.01 - EP); C02F 1/36 (2013.01 - EP US); C02F 1/38 (2013.01 - US); C02F 1/481 (2013.01 - EP); C02F 1/485 (2013.01 - US); C02F 1/488 (2013.01 - EP); C02F 1/5245 (2013.01 - EP US); C02F 1/66 (2013.01 - EP); C02F 1/74 (2013.01 - EP); C02F 1/78 (2013.01 - EP US); C02F 11/10 (2013.01 - EP US); C02F 2001/007 (2013.01 - US); C02F 2103/20 (2013.01 - EP US); C02F 2103/22 (2013.01 - EP); C02F 2103/32 (2013.01 - US); C02F 2103/343 (2013.01 - US); C02F 2209/005 (2013.01 - EP US); C02F 2209/03 (2013.01 - US); C02F 2301/063 (2013.01 - EP); C02F 2303/04 (2013.01 - US); C02F 2303/24 (2013.01 - EP); C02F 2303/26 (2013.01 - US); C02F 2305/023 (2013.01 - EP US)
Citation (search report)
See references of WO 2018091118A1
Designated contracting state (EPC)
AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR
Designated extension state (EPC)
BA ME
DOCDB simple family (publication)
US 2020055759 A1 20200220; EP 3541757 A1 20190925; RU 2019117891 A 20201217
DOCDB simple family (application)
US 201716461429 A 20170919; EP 17783388 A 20170919; RU 2019117891 A 20170919