EP0305251B1 - Injektormischer unter Druck - Google Patents
Injektormischer unter Druck Download PDFInfo
- Publication number
- EP0305251B1 EP0305251B1 EP88402000A EP88402000A EP0305251B1 EP 0305251 B1 EP0305251 B1 EP 0305251B1 EP 88402000 A EP88402000 A EP 88402000A EP 88402000 A EP88402000 A EP 88402000A EP 0305251 B1 EP0305251 B1 EP 0305251B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- air
- mixing
- injector
- inlet
- pipe
- 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
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S261/00—Gas and liquid contact apparatus
- Y10S261/75—Flowing liquid aspirates gas
Definitions
- paper pulp undergoes numerous purification, separation and various filtration, decontamination and de-inking treatments.
- the present invention relates to devices for injecting liquid and air under pressure mixture, and in particular to devices for mixing paper pulp and air, used in decontamination and deinking cells by flotation.
- One of the known techniques of decontamination and deinking consists in injecting air into the dough to be treated, at the entry of the cell. The air traps the charges and the ink particles in bubbles, and entrains them towards the surface to form a foam which is then sucked towards a separator.
- the quality of deinking depends in particular on the quality of the mixture obtained in the injector: it is indeed necessary that the dough is very aerated in order to retain the maximum quantity of particles in the air bubbles and this aeration must be the most homogeneous and the most evenly distributed in the dough: the bubbles must be very small; and avoid even the irregular presence of large bubbles.
- Injectors are generally used comprising a pressurized liquid inlet and a nozzle-shaped outlet; between the inlet and the outlet there is an air inlet and a cylinder in which the air, sucked in by the flow of the liquid, mixes there before reaching the conical part of the outlet.
- a device of this kind is described in patent CH-A-581,493.
- injector-mixers in which the dough flows in a tubular pipe in the form of a nozzle.
- a profile of longitudinal section in the shape of a wing In the narrowest part is housed a profile of longitudinal section in the shape of a wing. The air is introduced approximately radially into the narrowest part.
- Such a device is described in patent WO-A-85 01888.
- the amount of air drawn into this type of injector is mainly a function of the supply pressure; it can for example be of the order of 150% of the volume of liquid; however, the problem is not so much to obtain a large flow of aspirated air but rather to ensure a large and constant homogeneity of the liquid-air mixture.
- the liquid flow rate accepted by an injector cannot be increased indefinitely, by enlarging the section of the mixing cylinder: there is a maximum section. For example, it turns out that for a diameter greater than about 8mm, the aeration becomes irregular: formation of large bubbles, variable air flow, lower quality inking.
- GB-A-1,582,898 describes another injection and mixing device in which the liquid supply line is divided into a plurality of small nozzles, opening into a common chamber supplied with air. Opposite each of these nozzles, there is a venturi-shaped outlet.
- this device can function as a pump, it does not give satisfactory results in this deinking: the bubbles are irregular and burst, allowing the ink to escape.
- the present invention aims to inject a liquid-air mixture at high flow rate, strong and regular aeration of the liquid and which solves the problems of clogging.
- the injector 1 is generally cylindrical in shape and comprises a plurality of parallel and preferably identical injection tubes 2: six peripheral tubes 2 regularly distributed in a ring around a central tube, each being equal distance from its immediate neighbors.
- the invention is not limited to this exemplary embodiment and the injector 1 can comprise a greater or lesser number of tubes, or even comprise only one.
- Each tube has an inlet pipe 3 for the liquid, an aeration zone 4 for mixing the liquid and the air, and an outlet pipe 5.
- the inlet pipe 3 comprises a converging truncated cone 6, followed by a cylinder 7, both of circular sections.
- the cylindrical section 7 can be very short, it can even be nonexistent, its function is to stabilize the direction of flow after the inlet cone 6.
- each tube has different frustoconical and cylindrical parts.
- the cylindrical chamber 8 is a single volume, common to all the injection tubes 2 so that the injector comprises a bundle of inlet tubes 3 which all open into the chamber 8, and a bundle of outlet tubes 5 , which leave from chamber 8 towards the outlet of injector 1.
- the chamber 8 in fact has vis-a-vis the liquid an air layer 23 which the plane jet must pass through; this blade is preferably perpendicular to the longitudinal axis 24 of the injector.
- the jet in the space of the room is thus permanently entirely surrounded by air and it can aerate as much as possible.
- the blade 23 is limited to a chamber-shaped space 8, but it is also possible not to limit the space to a chamber, by separating the inlet parts from the mixing and outlet parts , and keeping them aligned coaxially with a certain distance between them. With such a variant the jet would pass through an air space 23 not limited to the walls of a chamber.
- the diameter 13 of the mixing cylinder is greater than the outlet diameter 14 of the inlet cylinder 7 in order to accept a flow of aerated liquid, which is greater than the flow of liquid alone, and the inlet diameter 15 of the funnel centering 10 is substantially greater than the diameter 14 of the inlet cylinder 7 in order to present a large surface for receiving the jet of liquid coming from the cylinder 7.
- the air inlet pipe 9 into the chamber 8 is arranged tangentially and perpendicular to the direction of the tubes 2 in order to create a rotating movement, promoting the mixing of the air in the liquid and above all promoting the cleaning of said chamber.
- the liquid then arrives in the cylindrical part 11 of the mixing zone 4 where the air-liquid mixture is produced in the form of bubbles of very small dimensions and where the ink and the contaminants are trapped.
- the mixture enters and crosses the divergent outlet cone 12, which is a draw cone.
- Such multiple injectors provide both the advantages of large injectors (large flow) and small injectors (maximum ventilation) without having the disadvantages (significant maintenance, expensive equipment: valves, ...)
- the injector 1 is produced in two parts 20, 21 assembled one against the other by screwing 22: the input part 20 comprises the input zone 3, the output part 21 comprises the centering funnel 10, the mixing cylinder 11, and the outlet cone 12.
- a cylindrical recess is provided on one of the parts 20 or 21 (in the example it is the part 20) to form the chamber 8 which defines a cavity in the form of an air knife 23.
- a cavity is dug laterally in the hollowed out room to form the tangential air inlet 9.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Water Treatments (AREA)
- Paper (AREA)
Claims (5)
- Vorrichtung zum Mischen von Papierbrei und Luft in Form eines Druck-Injektors mit einer axialen Zufuhr von Brei unter Druck, einer seitlichen Luftzufuhr, wenigstens einem Injektorrohr (2), das nacheinander einen sich verjüngenden Einlaßkanal (7), einen Belüftungsraum (8), einen Trichter (10) zur Aufnahme und Zentrierung des Strahls, einen zylindrischen Mischkanal sowie einen sich verbreiternden Auslaß- und Abzugskanal aufweist, dessen Länge mindestens gleich der des Mischkanals ist und in dem die Zufuhr von Luft unter Atmosphärendruck erfolgt,
gekennzeichnet durch folgende Kombination:- der Belüftungsraum (8) ist eben in Form einer Kreisscheibe (23) ausgebildet, die durch die Wände (25) einer zylindrischen Kammer, deren Achse parallel zur Achse (24) des Injektors verläuft, begrenzt wird, wobei der Belüftungsraum (8) eine Weite von wenigstens 5 mm aufweist, der Einlaßkanal (7) senkrecht quer in diesen einmündet und der Belüftungsraum tangential so gespeist wird, daß ein in der Kammer umlaufender Luftstrom ausgebildet wird;- die Länge des Mischkanals (11) liegt zwischen dem 4- und 9-fachen seines Durchmessers (13), und- der Kegel-Öffnungswinkel α des Auslaßkanals liegt zwischen 1° und 3°. - Vorrichtung zum Mischen von Flüssigkeit und Luft nach Anspruch 1, dadurch gekennzeichnet, daß der Lufteinlaß (9) horizontal am unteren Teil des Injektors (1) angeordnet ist.
- Vorrichtung zum Mischen von Flüssigkeit und Luft nach Anspruch 1, dadurch gekennzeichnet, daß der Injektor (1) eine Mehrzahl von parallelen Injektorrohren (2) aufweist, die kranzförmig um ein zentrales Injektorrohr (2) herum angeordnet sind und alle die gleichen Abmessungen aufweisen.
- Vorrichtung zum Mischen von Flüssigkeit und Luft nach Anspruch 1, dadurch gekennzeichnet, daß der Einlaßdurchmesser (15) des Trichters (10) höchstens gleich dem 1,5fachen des Durchmessers des Einlaßkanals (7) und die Länge des Trichters gleich seinem Einlaßdurchmesser (15) ist.
- Vorrichtung zum Mischen von Flüssigkeit und Luft nach Anspruch 1, dadurch gekennzeichnet, daß die Weite der Belüftung höchstens 15 mm beträgt.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR8711273A FR2619023B1 (fr) | 1987-08-07 | 1987-08-07 | Injecteur melangeur sous pression |
FR8711273 | 1987-08-07 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0305251A1 EP0305251A1 (de) | 1989-03-01 |
EP0305251B1 true EP0305251B1 (de) | 1992-07-08 |
Family
ID=9354020
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP88402000A Expired - Lifetime EP0305251B1 (de) | 1987-08-07 | 1988-08-01 | Injektormischer unter Druck |
Country Status (6)
Country | Link |
---|---|
US (1) | US4842777A (de) |
EP (1) | EP0305251B1 (de) |
JP (2) | JPH01159038A (de) |
DE (1) | DE3872624T2 (de) |
ES (1) | ES2034320T3 (de) |
FR (1) | FR2619023B1 (de) |
Families Citing this family (58)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5236090A (en) * | 1990-05-30 | 1993-08-17 | Sulzer-Escher Wyss Gmbh | Flotation-deinking-device |
US5073310A (en) * | 1990-10-01 | 1991-12-17 | Water Master, Inc. | Air injector assembly |
US5160610A (en) * | 1990-11-13 | 1992-11-03 | Smith & Loveless, Inc. | Radial header for dissolved air flotation systems |
ZA919256B (en) * | 1990-11-23 | 1992-11-25 | Atomaer Pty Ltd | Gas particle formation |
DE9111657U1 (de) * | 1991-09-18 | 1991-11-14 | Anton Steinecker Entwicklungs-GmbH & Co., 8050 Freising | Belüftungsdüse für Flüssigkeiten |
US5628623A (en) * | 1993-02-12 | 1997-05-13 | Skaggs; Bill D. | Fluid jet ejector and ejection method |
US6017195A (en) * | 1993-02-12 | 2000-01-25 | Skaggs; Bill D. | Fluid jet ejector and ejection method |
FR2717192B1 (fr) * | 1994-03-11 | 1996-04-26 | Lamort E & M | Procédé de désencrage de pâte à papier et appareil pour la mise en Óoeuvre de ce procédé. |
FR2727441B1 (fr) * | 1994-11-28 | 1997-01-31 | Lamort E & M | Perfectionnements aux dispositifs d'injection d'air dans un flux de pate a papier pour en operer le desencrage |
US5746583A (en) * | 1995-01-20 | 1998-05-05 | Spear; Scott | Vacuum boost device |
FR2772399B1 (fr) | 1997-12-15 | 2000-02-11 | Lamort E & M | Procede de desencrage de la pate a papier provenant de papiers recycles |
US6113078A (en) * | 1998-03-18 | 2000-09-05 | Lytesyde, Llc | Fluid processing method |
RU2135840C1 (ru) * | 1998-04-17 | 1999-08-27 | Попов Сергей Анатольевич | Жидкостно-газовый струйный аппарат (варианты) |
FI107829B (fi) * | 1999-06-15 | 2001-10-15 | Markku Juhani Palmu | Laite kaasun imemiseksi ja sekoittamiseksi polttonesteen virtaukseen |
AT408957B (de) * | 2000-02-03 | 2002-04-25 | Andritz Ag Maschf | Verfahren und vorrichtung zum belüften von dispersionen |
KR100781820B1 (ko) | 2001-02-21 | 2007-12-03 | 시부야 코교 가부시키가이샤 | 기체액체 혼합류의 분사장치 |
FI122973B (fi) * | 2005-06-17 | 2012-09-28 | Metso Paper Inc | Flotaatiokennon injektori, flotaatiokennon injektorin suutinosa ja menetelmä kuitususpensiovirtauksen ja ilman sekoittamiseksi toisiinsa flotaatiokennon injektorissa |
US7681569B2 (en) * | 2006-01-23 | 2010-03-23 | Lytesyde, Llc | Medical liquid processor apparatus and method |
US7717096B2 (en) * | 2006-01-23 | 2010-05-18 | Lytesyde, Llc | Fuel processor apparatus and method |
US7537674B1 (en) | 2006-06-12 | 2009-05-26 | Narayanasamy Seenivasan | Closed floatation de-inking module for recycled paper |
US7544271B1 (en) | 2006-06-12 | 2009-06-09 | Narayanasamy Seenivasan | Open flotation de-inking module for recycled paper |
US7562777B1 (en) | 2006-06-12 | 2009-07-21 | Narayanasamy Seenivasan | Flotation cell injector assembly for use with open or closed flotation deinking modules for recycled paper |
GB2447677B (en) * | 2007-03-21 | 2011-11-16 | Honeywell Normalair Garrett | Jet pump apparatus |
US8028674B2 (en) * | 2007-08-07 | 2011-10-04 | Lytesyde, Llc | Fuel processor apparatus and method |
DE602007008583D1 (de) * | 2007-11-26 | 2010-09-30 | Honeywell Aerospace Bv | Flugzeugklimaanlage |
DE102008025325A1 (de) * | 2008-05-27 | 2009-04-16 | VOGT AG Feuerwehrgeräte- und Fahrzeugbau | Strahlpumpenverdichter zum Erzeugen von Druckluftschaum CAFS-(Compressed Air Foam System) |
CN105132025B (zh) | 2008-09-26 | 2018-02-06 | 俄亥俄州立大学 | 将含碳燃料转化为无碳能量载体 |
GB2471280B (en) * | 2009-06-22 | 2011-08-31 | Hydroventuri Ltd | Apparatus and method for introducing a gas into a liquid |
DE102009040317A1 (de) * | 2009-09-05 | 2011-03-10 | Voith Patent Gmbh | Mischvorrichtung |
ES2630217T3 (es) | 2009-09-08 | 2017-08-18 | The Ohio State University Research Foundation | Integración de reformación/división de agua y sistemas electromagnéticos para generación de energía con captura de carbono integrada |
CN102597173A (zh) | 2009-09-08 | 2012-07-18 | 俄亥俄州立大学研究基金会 | 具有原位co2捕集的合成燃料和化学品生产 |
CA2689729C (en) * | 2010-01-11 | 2017-01-03 | Rj Oil Sands Inc. | Fluid treatment system |
CA2770525C (en) | 2010-07-02 | 2019-09-24 | Rj Oil Sands Inc. | Method and apparatus for treatment of fluids |
GB201018721D0 (en) * | 2010-11-05 | 2010-12-22 | Transvac Systems Ltd | Improved ejector and method |
AU2011326127B2 (en) | 2010-11-08 | 2017-04-20 | Particulate Solid Research, Inc. | Circulating fluidized bed with moving bed downcomers and gas sealing between reactors |
EP2707350A4 (de) | 2011-05-11 | 2015-12-23 | Ohio State Innovation Foundation | Systeme zum umwandeln von brennstoffen |
ES2880629T3 (es) | 2011-05-11 | 2021-11-25 | Ohio State Innovation Foundation | Materiales portadores de oxígeno |
FR2975917B1 (fr) * | 2011-06-06 | 2014-02-14 | Pok | Dispositif de generation de mousse d'une lance a incendie |
JP2013248574A (ja) * | 2012-05-31 | 2013-12-12 | Yamaha Livingtec Corp | 微細気泡発生装置 |
JP5578205B2 (ja) * | 2012-07-26 | 2014-08-27 | 三菱電機株式会社 | 気液混合装置および風呂給湯装置 |
CN105358475B (zh) | 2013-02-05 | 2018-12-04 | 俄亥俄州国家创新基金会 | 用于燃料转化的方法 |
WO2014159956A1 (en) * | 2013-03-13 | 2014-10-02 | Ohio State Innovation Foundation | Distributing secondary solids in packed moving bed reactors |
WO2014152914A1 (en) | 2013-03-14 | 2014-09-25 | Ohio State Innovation Foundation | Systems and methods for converting carbonaceous fuels |
WO2015131117A1 (en) | 2014-02-27 | 2015-09-03 | Ohio State Innovation Foundation | Systems and methods for partial or complete oxidation of fuels |
JP5794338B2 (ja) * | 2014-03-31 | 2015-10-14 | 三菱電機株式会社 | 気液混合装置および風呂給湯装置 |
DE102014012666B4 (de) * | 2014-08-22 | 2016-07-21 | Rithco Papertec Gmbh | Vorrichtung und Verfahren zur Reinigung von verunreinigten Feststoff-Flüssigkeits-Gemischen und Verwendung der Vorrichtung und des Verfahrens |
FR3037084B1 (fr) | 2015-06-02 | 2020-01-10 | Coatex | Procede de desencrage de papier de recuperation |
WO2017180763A1 (en) | 2016-04-12 | 2017-10-19 | Ohio State Innovation Foundation | Chemical looping syngas production from carbonaceous fuels |
AU2018256837A1 (en) * | 2017-04-28 | 2019-12-19 | Nano Gas Technologies, Inc. | Nanogas shear processing |
CN111065459B (zh) | 2017-07-31 | 2023-09-22 | 俄亥俄州立创新基金会 | 具有不相等反应器组件运行压力的反应器系统 |
US10549236B2 (en) | 2018-01-29 | 2020-02-04 | Ohio State Innovation Foundation | Systems, methods and materials for NOx decomposition with metal oxide materials |
JP6691716B2 (ja) * | 2018-02-26 | 2020-05-13 | ウォーターナビ株式会社 | 微細気泡発生方法及び装置 |
RU189855U1 (ru) * | 2018-03-07 | 2019-06-06 | Николай Александрович Тузовский | Устройство перемешивающее струйное |
US11413574B2 (en) | 2018-08-09 | 2022-08-16 | Ohio State Innovation Foundation | Systems, methods and materials for hydrogen sulfide conversion |
CA3129146A1 (en) | 2019-04-09 | 2020-10-15 | Liang-Shih Fan | Alkene generation using metal sulfide particles |
WO2021204306A1 (en) * | 2020-04-10 | 2021-10-14 | Jetex Innovation S.R.O. | Fire extinguishing equipment with fire nozzle |
CZ309237B6 (cs) * | 2020-04-10 | 2022-06-08 | Jetex Innovation S.R.O. | Hasicí zařízení s požární proudnicí |
CA3090353A1 (en) | 2020-08-18 | 2022-02-18 | 1501367 Alberta Ltd. | Fluid treatment separator and a system and method of treating fluid |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US21416A (en) * | 1858-09-07 | Coffee-roaster | ||
BE514514A (de) * | ||||
US585064A (en) * | 1897-06-22 | Fire-ladder | ||
US2057218A (en) * | 1934-08-30 | 1936-10-13 | Pyrene Minimax Corp | Method and apparatus for producting fire extinguishing foam |
US2268063A (en) * | 1939-12-02 | 1941-12-30 | Stewart Warner Corp | Automobile heater |
GB577397A (en) * | 1944-04-27 | 1946-05-16 | Henry Alfred Ernest Talley | Improvements in or relating to apparatus for mixing gases |
GB802691A (en) * | 1955-10-26 | 1958-10-08 | Gaskell & Chambers Ltd | Liquids mixing device |
US3659962A (en) * | 1970-06-02 | 1972-05-02 | Zink Co John | Aspirator |
GB1385166A (en) * | 1973-04-25 | 1975-02-26 | Popov V F | Ejector mixer for gases and or liquids |
DE2345246C2 (de) * | 1973-09-07 | 1974-12-12 | Heinrich 6950 Mosbach Braukmann | Vorrichtung zum Vermischen von Dampf und Kaltwasser zum Erzeugen von Warmwasser |
CH581493A5 (en) * | 1974-06-24 | 1976-11-15 | Escher Wyss Ag | Static mixer for in line mixing - having sudden expansion with secondary fluid injection just prior to it |
CH585064A5 (en) * | 1974-10-08 | 1977-02-28 | Lenzburg Sauerstoffwerk Ag | Mixing nozzle for balloon gases - e.g. air and helium, having variable mixture ratio control valve |
US4134547A (en) * | 1976-12-14 | 1979-01-16 | O. Ditlev-Simonsen, Jr. | Jet pipe |
GB1582898A (en) * | 1977-07-25 | 1981-01-14 | Kamelmacher E | Jet pump or mixer and jet means therefor |
US4210166A (en) * | 1977-09-14 | 1980-07-01 | Munie Julius C | Mixing apparatus |
US4308138A (en) * | 1978-07-10 | 1981-12-29 | Woltman Robert B | Treating means for bodies of water |
FR2459679A1 (fr) * | 1979-06-27 | 1981-01-16 | Matincendie Sa | Melangeur pour l'introduction d'un produit liquide en proportion determinee dans une canalisation de liquide sous pression |
US4464314A (en) * | 1980-01-02 | 1984-08-07 | Surovikin Vitaly F | Aerodynamic apparatus for mixing components of a fuel mixture |
HU185090B (en) * | 1982-02-25 | 1984-11-28 | Debreceni Mezoegazdasagi | Foam forming head, control apparatus as well as device from these first for agricultural row marking by foam |
SE442173B (sv) * | 1983-10-27 | 1985-12-09 | Sunds Defibrator | Anordning vid flotation av fibersuspensioner |
BE901771A (nl) * | 1985-02-20 | 1985-06-17 | Studiecentrum Voor Kernerergie | Gaszuiveringsinrichting. |
SU1265404A1 (ru) * | 1985-04-22 | 1986-10-23 | Ивано-Франковский Институт Нефти И Газа | Многосопловой эжектор |
US4683122A (en) * | 1986-04-14 | 1987-07-28 | Herzog-Hart Corporation | Gas-liquid reactor and method for gas-liquid mixing |
-
1987
- 1987-08-07 FR FR8711273A patent/FR2619023B1/fr not_active Expired - Fee Related
-
1988
- 1988-08-01 ES ES198888402000T patent/ES2034320T3/es not_active Expired - Lifetime
- 1988-08-01 US US07/226,638 patent/US4842777A/en not_active Expired - Fee Related
- 1988-08-01 EP EP88402000A patent/EP0305251B1/de not_active Expired - Lifetime
- 1988-08-01 DE DE8888402000T patent/DE3872624T2/de not_active Expired - Fee Related
- 1988-08-08 JP JP63196218A patent/JPH01159038A/ja active Pending
-
1992
- 1992-03-23 JP JP1992024121U patent/JPH0730122Y2/ja not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH01159038A (ja) | 1989-06-22 |
FR2619023B1 (fr) | 1991-04-12 |
ES2034320T3 (es) | 1993-04-01 |
DE3872624D1 (de) | 1992-08-13 |
FR2619023A1 (fr) | 1989-02-10 |
US4842777A (en) | 1989-06-27 |
JPH07519U (ja) | 1995-01-06 |
EP0305251A1 (de) | 1989-03-01 |
DE3872624T2 (de) | 1993-02-25 |
JPH0730122Y2 (ja) | 1995-07-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0305251B1 (de) | Injektormischer unter Druck | |
FR2515987A1 (fr) | Appareil a injection avec point d'etranglement d'un tube melangeur situe en aval | |
EP2292321B1 (de) | Anlage zur Herstellung eines homogenen Gasgemischs aus flüssigen und gasförmigen Bestandteilen | |
FR2663318A1 (fr) | Buse distributrice de boissons et procede de melange de liquides avec cette buse. | |
FR2550469A1 (fr) | Injecteur de microbulles | |
EP0674040B1 (de) | Verfahren zum de-inken von Papierzellstoff und Vorrichtung zur Durchführung des Verfahrens | |
FR2529476A1 (fr) | Cellule de flottation | |
FR2928567A1 (fr) | Buse de pulverisation de liquide et pulverisateur de liquide comprenant une telle buse | |
FR2975917A1 (fr) | Dispositif de generation de mousse d'une lance a incendie | |
EP0191485B1 (de) | Homogenisierungsanlage für eine in einer Kanalisation transportierte Flüssigkeit | |
WO2016102701A1 (fr) | Buse optimisée d'injection d'eau pressurisée contenant un gaz dissous | |
EP0198737A1 (de) | Vorrichtung zur Dekontamination eines Faserbreis | |
FR2485399A1 (fr) | Tuyere de pulverisation en cone plein | |
FR2730941A1 (fr) | Cellule pour le traitement par flottation d'un milieu liquide | |
EP0502941A1 (de) | Vorrichtung mit einem brausekopf zur ausrüstung der brausen. | |
EP0838260B1 (de) | Vorrichtung zum Belüften und Spritzen von geladenen Flüssigkeiten | |
EP0429736B1 (de) | Spritzlanze eines Flüssigkeitsgemisches | |
FR2473349A1 (fr) | Procede pour separer le liquide d'un melange de gaz et de liquide et separateur pour la realisation de ce procede | |
FR2554738A1 (fr) | Extracteur a tourbillon et procede pour melanger un courant de fluide avec un second courant de fluide sous basse pression | |
CH554191A (fr) | Appareil pour la diffusion de gaz dans un liquide. | |
WO2006072691A1 (fr) | Crible pour bio-impacteur, bio-impacteur equipe d’un tel crible | |
BE517188A (de) | ||
BE518837A (de) | ||
FR2871392A1 (fr) | Dispositif de melange hydraulique d'un coagulant dans un courant principal de liquide | |
FR2996781A1 (fr) | Saturateur permettant l'injection d'un gaz dans un liquide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE ES FR GB IT SE |
|
17P | Request for examination filed |
Effective date: 19890208 |
|
17Q | First examination report despatched |
Effective date: 19910313 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: STORA FELDMUEHLE AKTIENGESELLSCHAFT Owner name: E. + M. LAMORT SOCIETE ANONYME DITE: |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE ES FR GB IT SE |
|
REF | Corresponds to: |
Ref document number: 3872624 Country of ref document: DE Date of ref document: 19920813 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) | ||
ITF | It: translation for a ep patent filed |
Owner name: SAIC BREVETTI S.R.L. |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2034320 Country of ref document: ES Kind code of ref document: T3 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
EAL | Se: european patent in force in sweden |
Ref document number: 88402000.9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20000725 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20000727 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20000729 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 20000804 Year of fee payment: 13 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20000828 Year of fee payment: 13 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010801 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010802 Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20010802 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20010801 |
|
EUG | Se: european patent has lapsed |
Ref document number: 88402000.9 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20020430 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20020501 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20020911 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20050801 |