EP0307318B1 - Dispositif notamment pour répartir uniformément des particules solides et/ou liquides et ensemble comportant un tel dispositif - Google Patents

Dispositif notamment pour répartir uniformément des particules solides et/ou liquides et ensemble comportant un tel dispositif Download PDF

Info

Publication number
EP0307318B1
EP0307318B1 EP88402268A EP88402268A EP0307318B1 EP 0307318 B1 EP0307318 B1 EP 0307318B1 EP 88402268 A EP88402268 A EP 88402268A EP 88402268 A EP88402268 A EP 88402268A EP 0307318 B1 EP0307318 B1 EP 0307318B1
Authority
EP
European Patent Office
Prior art keywords
frame
shaft
primary
ring
rotation
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
EP88402268A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0307318A1 (fr
Inventor
Francis Pillon
Michel Andriot-Ballet
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to AT88402268T priority Critical patent/ATE93744T1/de
Publication of EP0307318A1 publication Critical patent/EP0307318A1/fr
Application granted granted Critical
Publication of EP0307318B1 publication Critical patent/EP0307318B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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
    • B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
    • B01F25/74—Spray-mixers, e.g. for mixing intersecting sheets of material with rotating parts, e.g. discs
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/40—Mixers with rotor-rotor system, e.g. with intermeshing teeth
    • B01F27/41—Mixers with rotor-rotor system, e.g. with intermeshing teeth with the mutually rotating surfaces facing each other
    • B01F27/411—Mixers with rotor-rotor system, e.g. with intermeshing teeth with the mutually rotating surfaces facing each other provided with intermeshing elements

Definitions

  • the present invention relates to a device in particular for uniformly distributing solid and / or liquid particles in order to deposit regular, precise and uniform layers of pulverulent products, or to make mixtures of pulverulent products, of liquid products or of pulverulent products in liquid products.
  • the invention also relates to an assembly comprising such a device.
  • a device for bringing fluid bodies and / or solid bodies into mutual contact, which comprises a turntable, on different surfaces of which two veins of fluid bodies and / or solid bodies are accelerated and repressed, under the effect of centrifugal force, on the periphery of the plate so as to come into contact with each other. It is preferable to use the opposite surfaces of the same tray.
  • one of the veins is constituted by a solid body in the form of powder, which is brought, by a downward movement, onto the upper surface of a tray with horizontal centrifugal pallets, while the other vein is formed by a gas and directed towards the lower face of the plate whose diameter is much greater than that of the supply conduits of each vein.
  • the gas stream rises around the periphery of the plate, taking with it, towards a fluidizing section located at the top of the device, the powder leaving the upper surface of the plate at this periphery.
  • solid-solid or solid-liquid mixers comprise a central vertical tube, or fixed primary shaft which opens into a first chamber delimited by a primary crown driven in rotation around the fixed central tube and by an anvil rotating in the same direction as the primary crown and having a diameter much greater than that of the central tube.
  • the products fall into the central tube and strike the anvil in its central part, so that they are rejected towards the periphery in a second chamber determined by an upper disc rotating in the same direction as the primary crown and a disc lower turning in opposite direction.
  • the first chamber is completely included in the second, which is directly located under a hopper filled with solid products.
  • the edges of the lower and upper discs have studs arranged in staggered rows: the mixed products are ejected through baffles formed by these studs and are recovered for later use.
  • One of the aims of the present invention is therefore to provide a device in particular for uniformly distributing solid and / or liquid particles which can also simultaneously make it possible to produce homogeneous mixtures and / or to reduce the size of the particles.
  • Another object of the invention is to provide such an apparatus which is energy efficient and easy to maintain.
  • a device in particular for uniformly distributing solid and / or liquid particles which is characterized, according to the present invention, by the fact that it comprises, on the one hand, a primary shaft, vertical and hollow, which is rotated and whose lower end comprises a substantially horizontal primary crown whose lower face is provided with vertical teeth arranged in concentric circles, and, on the other hand, a secondary, vertical and hollow shaft, inside which said primary shaft is coaxially arranged, which is rotated in a direction opposite to the direction of rotation of said primary shaft, and the lower end of which comprises a cylindrical cage constituted by a secondary crown, integral with said lower end and of greater width than said primary crown and by a disc connected to the lower face of said secondary crown by at least three bars, said disc comprising at its upper face, which is opposite the lower face of said secondary crown, on the one hand, vertical teeth arranged concentrically and staggered with respect to those which comprises said primary crown which is located inside of said cylindrical cage, and, on
  • the diameter of the anvil is at least equal to that of the primary shaft.
  • the material is introduced into a removable tube arranged coaxially inside said primary shaft of which it is integral in rotation and the circular anvil has a diameter at least equal to that of said removable tube.
  • the removable tube has a screw over its entire height which is rotated.
  • the removable tube is arranged inside the primary shaft of which it is integral in rotation, and its lower end describes a crown above the circular anvil, the diameter of which is at least equal to the diameter outside of the crown thus described.
  • This device can be mounted on a horizontal plate which it crosses and to the lower face of which is fixed a cylindrical-conical skirt which widens towards the cylindrical cage and the lower edge of which is substantially lower than the disk of said cage.
  • this skirt has in its cylindrical part an area of large openings, and the secondary shaft in an area located under this area of large openings, comprises a propeller consisting of at least two blades rotating in the space delimited by this secondary shaft and the cylindrical part of this skirt.
  • a means for stopping the particles is located on the underside of the horizontal plate; it consists of a set of square frames of the same axis as the secondary shaft, on each of which are hung hanging screens whose surface is proportional to the distribution on the ground of solid particles.
  • these screens are arranged symmetrically with respect to the diagonals of all the frames and to the perpendicular bisectors on each side of these frames.
  • this set consists of five frames, numbered from 1 to 5 from the center, the width of the half-screen located at the corner of the fifth frame being defined by an angle at the center of ⁇ / 72, that of the screen located on the fourth frame by an angle at the center of ⁇ / 45, that of the screen located on the third frame by an angle at the center of ⁇ / 60, that of the screen located on the second frame by an angle at the center of ⁇ / 90, that of the screen located on the first frame being defined by an angle of ⁇ / 180 and that of the half-screen located on the fifth frame being defined by an angle at the center of ⁇ / 72, all these angles at the center being contiguous, this pattern thus defined being repeated twice without discontinuity.
  • the disc of the cylindrical cage has a central opening and the circular anvil is arranged on fins determining between them passages for the flow of the product sucked through the central opening.
  • the present invention also relates to an assembly which is constituted by a truncated-pyramidal enclosure the upper face of which is constituted by the horizontal plate provided with the device described above comprising a cylindro-conical skirt and a propeller, and the underside of which is open above a means for collecting the treated product.
  • the device comprises, on the one hand, a primary shaft 1, vertical and hollow and on the other hand, a secondary shaft 2 vertical and hollow in which is disposed coaxially the primary shaft 1.
  • a primary shaft 1 vertical and hollow
  • a secondary shaft 2 vertical and hollow in which is disposed coaxially the primary shaft 1.
  • the primary shaft 1 has at its lower end a substantially horizontal primary ring 4 whose lower face is provided with vertical teeth 5. These are arranged in concentric circles. This primary shaft 1 is rotated by a first motor 6 thanks to a belt 7 cooperating with a pulley 8 secured to the upper end of the primary shaft 1.
  • the secondary shaft 2 has at its lower part a cylindrical cage 10 enclosing the primary crown 4.
  • This cylindrical cage 10 is constituted by a secondary crown 11 secured to the lower end of the secondary shaft 2 and of greater width than the primary crown 4, and by a disc 12 connected to the underside of the secondary crown 11 by four bars 13 in the present exemplary embodiment.
  • This disc 12 has on its upper face, that is to say facing the lower face of the secondary crown 11, vertical teeth 14 which are arranged concentrically and staggered with respect to the teeth 5 of the primary crown 4: during the rotation in the opposite direction of the two primary 1 and secondary 2 shafts, the teeth of a crown describe circles arranged between those described by the teeth of the other crown.
  • the disc 12 has at its center a circular anvil 15 of the same axis as it: this anvil 15 is located at the top of a rod 16.
  • the device also comprises a removable tube 20 which is arranged coaxially inside the primary shaft 1 of which it is integral in rotation.
  • the lower end of this removable tube 20 opens out above the circular anvil 15, the diameter of which is barely greater than that of the removable tube 20.
  • the removable tube 20 includes a funnel 21 located under the lower opening 22 of a frustoconical hopper 23 containing the product or products to be treated. These are introduced into this hopper 23 by one or more feed troughs 24.
  • the opening 22 is open, the pulverulent products fall into the removable tube 20 which is in rotation just like the primary 1 and secondary 2 shafts : thanks to the suction created by this rotation, the descent of the products is facilitated.
  • the funnel 21 and / or the hopper 23 have an air inlet.
  • this removable tube 20 is not essential, the same result would be obtained by using the primary shaft 1 as a tube, but because of its removable nature, the removable tube 20 allows greater flexibility of use, as well as the will have easily understood the skilled person.
  • FIG. 2 This figure also relates to an alternative embodiment for the removable tube 20.
  • the latter is constituted by a coaxial obviouslye20 party and a lower portion 20 b vertical and with an axis parallel to the axis of the primary shaft 1. Consequently, during its rotation, the lower part 20 b describes a cylinder: therefore the product falls according to a crown 46 on the circular anvil 15.
  • cylindrical-conical skirt 27 which is fixed to a horizontal plate 28 through which the device passes.
  • This plate 28 can be the upper wall of an enclosure 47, the lower part of which is open above a device 48 for collecting the treated product.
  • the cylindrical-conical skirt 27 widens towards the cylindrical cage 10 and its lower edge is situated in a plane slightly lower than that of the disc 12.
  • the device comprises a propeller 29 whose blades are fixed on the secondary shaft 2 and outside.
  • the cylindrical part 27 a of the cylindrical-conical skirt has large openings in its zone situated above the propeller 29 so as to allow gas circulation as shown in FIG. 3.
  • the tronco-pyramidal enclosure 47 has a square cross-section and in fact constitutes a relaxation chamber.
  • This mist is deposited by gravity on a means 48 intended to collect the products thus treated.
  • This means 48, on which the products are therefore perfectly spread and in a determined quantity, is generally a conveyor belt.
  • an assembly 30 consisting of metal frames in a plane slightly greater than that of the secondary crown 11.
  • this assembly consists of five frames 31 to 35, on which are hung screens 36 whose length increases from the inner frame, or first frame 31, to the outer frame or fifth frame 35. These screens make it possible to stop the particles expelled from the cylindrical cage 10 and have a surface proportional to the distribution surface on the ground, constituted by the means 48 for collecting the treated product.
  • the five frames 31 to 35 are square and have as axis of symmetry the axis of rotation of the device. They are suspended under the horizontal plate 28 by known means, the latter being part of the enclosure 47 already described.
  • the screens are arranged symmetrically with respect to the diagonals and the perpendicular bisectors on each side of these frames. On a half-side, the following pattern is repeated twice continuously: a half-side therefore has three patterns.
  • the width of the first half-screen 37 located at the corner of the fifth frame 35 is defined by an angle at the center of ⁇ / 72; that of the screen 38 located on the fourth frame 34 is defined by an angle at the center of ⁇ / 45; that of the screen 39 located on the third frame 33 is defined by an angle at the center of ⁇ / 60; that of the screen 40 located on the second frame 32 is defined by an angle at the center of ⁇ / 90; that of the screen 41 located on the first frame 31 is defined by an angle at the center of ⁇ / 180; and that of the second half-screen 42 located on the fifth frame 35 is defined by an angle at the center of ⁇ / 72.
  • FIG 6 there is shown a cylindrical cage 10 more particularly suitable for mixing liquids or liquids and solids.
  • the disc 12 has a central opening 43 externally limited by a cylindrical wall 44.
  • the circular anvil 15 is mounted on fins 45 determining between them passages for the flow of the fluid sucked through the opening 43.

Landscapes

  • Chemical Kinetics & Catalysis (AREA)
  • Chemical & Material Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Manufacturing Of Micro-Capsules (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Crushing And Grinding (AREA)
  • Fertilizers (AREA)
  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Lubricants (AREA)
  • Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Detergent Compositions (AREA)
EP88402268A 1987-09-08 1988-09-08 Dispositif notamment pour répartir uniformément des particules solides et/ou liquides et ensemble comportant un tel dispositif Expired - Lifetime EP0307318B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT88402268T ATE93744T1 (de) 1987-09-08 1988-09-08 Vorrichtung, insbesondere zum gleichmaessigen verteilen fester teilchen oder/und fluessigkeiten, und apparat mit einer solchen vorrichtung.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8712441A FR2620044B1 (fr) 1987-09-08 1987-09-08 Procede et dispositif pour epandre ou melanger des pulverulents par depot de particules en suspension dans l'air
FR8712441 1987-09-08

Publications (2)

Publication Number Publication Date
EP0307318A1 EP0307318A1 (fr) 1989-03-15
EP0307318B1 true EP0307318B1 (fr) 1993-09-01

Family

ID=9354703

Family Applications (1)

Application Number Title Priority Date Filing Date
EP88402268A Expired - Lifetime EP0307318B1 (fr) 1987-09-08 1988-09-08 Dispositif notamment pour répartir uniformément des particules solides et/ou liquides et ensemble comportant un tel dispositif

Country Status (16)

Country Link
US (1) US4883363A (da)
EP (1) EP0307318B1 (da)
JP (1) JPH01159044A (da)
AT (1) ATE93744T1 (da)
AU (1) AU619757B2 (da)
CA (1) CA1327885C (da)
DE (1) DE3883669T2 (da)
DK (1) DK496288A (da)
ES (1) ES2046321T3 (da)
FI (1) FI96493C (da)
FR (1) FR2620044B1 (da)
IE (1) IE62264B1 (da)
MC (1) MC1979A1 (da)
NO (1) NO174137C (da)
PT (1) PT88428B (da)
ZA (1) ZA886673B (da)

Families Citing this family (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5495986A (en) * 1993-05-12 1996-03-05 Davenport; Ricky W. Method for providing a fuel mixture
US5863305A (en) * 1996-05-03 1999-01-26 Minnesota Mining And Manufacturing Company Method and apparatus for manufacturing abrasive articles
CA2251796A1 (en) * 1996-05-03 1997-11-13 Minnesota Mining And Manufacturing Company Method of making a porous abrasive article
JP2000509663A (ja) * 1996-05-03 2000-08-02 ミネソタ・マイニング・アンド・マニュファクチャリング・カンパニー 不織研磨製品
SE9804442D0 (sv) * 1998-12-21 1998-12-21 Global Powder Ab Anordning och metod för kontinuerlig blandning
EP1060786B1 (en) * 1999-06-15 2004-04-14 Pfaudler Werke GmbH Charging assembly for mixing vessel
DE20002920U1 (de) * 2000-02-18 2000-04-20 Schröder & Boos Misch- und Anlagentechnik GmbH & Co. KG, 27578 Bremerhaven Homogenisator
JP4766634B2 (ja) * 2001-04-09 2011-09-07 栄司 西本 汚染液体処理装置
FI114299B (fi) * 2001-06-25 2004-09-30 Conenor Oy Menetelmä eri materiaalien käsittelemiseksi ja materiaalinkäsittelylaite
US6712496B2 (en) * 2001-07-26 2004-03-30 The Procter & Gamble Company Auger fed mixer apparatus and method of using
FR2834652B1 (fr) * 2002-01-11 2004-02-27 Atofina Dispositif d'agitation en particulier pour la dispersion ou l'emulsification de deux liquides non miscibles
US20030227817A1 (en) * 2002-04-11 2003-12-11 Mobius Technologies, Inc., A California Corporation Mixer
US6860289B2 (en) * 2002-04-11 2005-03-01 Robert Donald Villwock Surge tank
US7029162B2 (en) * 2002-04-11 2006-04-18 Mobius Technologies, Inc. Process and apparatus for continuous mixing of slurry with removal of entrained bubbles
US20030233937A1 (en) * 2002-04-11 2003-12-25 Mobius Technologies, Inc., A California Corporation Apparatus and method for continuously removing air from a mixture of ground polyurethane particles and a polyol liquid
US6994464B2 (en) * 2002-04-11 2006-02-07 Mobius Technologies, Inc Control system and method for continuous mixing of slurry with removal of entrained bubbles
CN1230242C (zh) * 2002-04-26 2005-12-07 丁楠 旋转冲击式细、均、乳化装置
NO317083B1 (no) * 2002-09-27 2004-08-02 Catalyst Services Inc Fremgangsmate for fylling av partikulaert materiale i vertikale ror
CA2602955C (en) * 2005-03-25 2013-07-02 Catalyst Services, Inc. Filling tubes with catalyst and/or other particulate
US20110235460A1 (en) * 2005-07-22 2011-09-29 Schlumberger Technology Corporation Method and apparatus to optimize the mixing process
ATE437694T1 (de) * 2006-03-29 2009-08-15 Hebold Mixing & More Gmbh Homogenisator
JP4819615B2 (ja) * 2006-08-09 2011-11-24 三井化学株式会社 固液混合流体の分割方法
DE102006045088A1 (de) * 2006-09-21 2008-03-27 Basf Ag Verfahren zum Durchmischen einer in einem im wesentlichen abgeschlossenen Behälter befindlichen Flüssigkeit oder Mischung aus einer Flüssigkeit und einem feinteiligen Feststoff
US8025472B2 (en) * 2007-06-01 2011-09-27 Catalyst Services, Inc. Catalyst loading system
BRPI1003166B1 (pt) * 2010-08-04 2020-04-28 Kraft Foods Global Brands Llc aparelho e método para encaminhamento de uma mistura seca
JP2013132573A (ja) * 2011-12-26 2013-07-08 Jtekt Corp 混合分散装置
CN103372491B (zh) * 2012-04-24 2015-11-25 徐正才 一种粉碎机
US10895114B2 (en) 2012-08-13 2021-01-19 Schlumberger Technology Corporation System and method for delivery of oilfield materials
US8979356B2 (en) * 2012-12-18 2015-03-17 Feldmeier Equipment, Inc. Dual agitator mixer with sanitary tank
US10633174B2 (en) 2013-08-08 2020-04-28 Schlumberger Technology Corporation Mobile oilfield materialtransfer unit
US10150612B2 (en) 2013-08-09 2018-12-11 Schlumberger Technology Corporation System and method for delivery of oilfield materials
US12102970B2 (en) 2014-02-27 2024-10-01 Schlumberger Technology Corporation Integrated process delivery at wellsite
US10137420B2 (en) * 2014-02-27 2018-11-27 Schlumberger Technology Corporation Mixing apparatus with stator and method
US11819810B2 (en) 2014-02-27 2023-11-21 Schlumberger Technology Corporation Mixing apparatus with flush line and method
US11453146B2 (en) 2014-02-27 2022-09-27 Schlumberger Technology Corporation Hydration systems and methods
CN104549106B (zh) * 2015-01-04 2016-06-01 安徽新中远化工科技有限公司 一种合成塔
BR112017023312B1 (pt) 2015-04-29 2022-10-04 Clpros, Llc Aparelho para amortecer e carregar uniformemente um material particulado dentro de um tubo vertical e método para preencher um material particulado em um tubo
CN106422888A (zh) * 2016-10-28 2017-02-22 无锡龙翔印业有限公司 一种丝印油墨的混合装置
CN109337785A (zh) * 2018-11-27 2019-02-15 灵参生物科技（大连）有限公司 一种用于保健酒生产的杀菌装置及方法
CN118236888B (zh) * 2024-05-23 2024-07-30 河南力启重工有限公司 起重机控制加料系统

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1068670B (de) * 1959-11-12 Schriesheim bei Heidelberg Hermann Mehne Einrichtung zum Vermischen von pulverförmigem oder kornigem. Gut mit zähen Flüssigkeiten
US211576A (en) * 1879-01-21 Improvement in bran-dusters
US412321A (en) * 1889-10-08 Walfrid burkman
FR958346A (da) * 1950-03-07
US894753A (en) * 1908-02-21 1908-07-28 Harry F Smith Apparatus for purifying gas.
US2324018A (en) * 1940-02-27 1943-07-13 Smidth & Co As F L Flotation cell
US2516455A (en) * 1945-12-27 1950-07-25 George W Edwards Means for preparing and homogenizing emulsions, mixtures, and the like
US2577095A (en) * 1946-10-25 1951-12-04 American Well Works Apparatus for dispersing material in a fluid stream
FR950579A (fr) * 1947-07-23 1949-09-30 Separation Sa Franc Pour La Perfectionnements aux procédés, dispositifs et installations mettant en jeu des opérations de pulvérisation et d'atomisation
US2619330A (en) * 1949-09-09 1952-11-25 Willems Peter Mixing and dispersing device
US2639901A (en) * 1951-11-20 1953-05-26 Nat Gypsum Co Pin mixer
US2717703A (en) * 1953-09-30 1955-09-13 Allwood Inc Device for storing pourable solid stock such as shavings, fibers, shreds, and the like
DE1178042B (de) * 1957-08-15 1964-09-17 Du Pont Vorrichtung zum Mischen von Fluessigkeiten
FR1311922A (fr) * 1961-10-27 1962-12-14 Perfectionnements aux mélangeurs
US3457047A (en) * 1962-02-20 1969-07-22 Shikoku Chem Apparatus for producing cellulose derivatives and the like
DE1442951A1 (de) * 1964-12-28 1970-03-26 Mukai Kiyoka Verfahren und Vorrichtung zum Herbeifuehren einer Mischung und/oder Reaktion
FR1539950A (fr) * 1967-08-11 1968-09-20 Stein & Roubaix Mélangeur continu
US3934859A (en) * 1973-11-02 1976-01-27 Combustion Engineering, Inc. Mixing apparatus
DE2627600C2 (de) * 1976-06-19 1982-02-18 Draiswerke Gmbh, 6800 Mannheim Vorrichtung zum diskontinuierlichen Mischen von mindestens zwei Stoffen
US4217996A (en) * 1978-09-27 1980-08-19 Good Lewis D Material storage and feeding device
US4384787A (en) * 1979-06-28 1983-05-24 Yasuro Ito Method and apparatus for adjusting the quantity of liquid deposited on fine granular materials and method of preparing mortar or concrete
EP0048312A1 (en) * 1980-09-19 1982-03-31 Nemo Ivarson Method and apparatus for continuously mixing a liquid and powder
US4342345A (en) * 1980-12-09 1982-08-03 Union Carbide Corporation Method and apparatus for filling bulk material containers

Also Published As

Publication number Publication date
AU2202888A (en) 1989-03-09
PT88428B (pt) 1994-03-31
MC1979A1 (fr) 1989-11-23
FI884118A (fi) 1989-03-09
ATE93744T1 (de) 1993-09-15
AU619757B2 (en) 1992-02-06
DE3883669D1 (de) 1993-10-07
PT88428A (pt) 1989-07-31
DK496288D0 (da) 1988-09-06
NO174137B (no) 1993-12-13
FI96493B (fi) 1996-03-29
US4883363A (en) 1989-11-28
FR2620044A1 (fr) 1989-03-10
DK496288A (da) 1989-03-09
JPH01159044A (ja) 1989-06-22
DE3883669T2 (de) 1994-03-31
FI96493C (fi) 1996-07-10
IE882705L (en) 1989-03-08
NO883975L (no) 1989-03-09
IE62264B1 (en) 1995-01-11
ZA886673B (en) 1989-06-28
ES2046321T3 (es) 1994-02-01
CA1327885C (fr) 1994-03-22
FI884118A0 (fi) 1988-09-07
NO883975D0 (no) 1988-09-07
EP0307318A1 (fr) 1989-03-15
FR2620044B1 (fr) 1989-12-22
NO174137C (no) 1994-03-23

Similar Documents

Publication Publication Date Title
EP0307318B1 (fr) Dispositif notamment pour répartir uniformément des particules solides et/ou liquides et ensemble comportant un tel dispositif
CH654741A5 (fr) Appareil pour appliquer un revetement sur des comprimes.
CH659196A5 (fr) Machine de granulation et revetement.
FR2508154A1 (fr) Sechoir melangeur granulateur
EP0075500A1 (fr) Machine permettant l'épluchage et le nettoyage de produits alimentaires en particulier de légumes tels que les oignons
FR2625426A1 (fr) Pressoir pour exprimer le jus de vegetaux
CA2066737C (fr) Machine et procede pour le traitement en continu de surface d'articles de grosseur reduite
FR2824315A1 (fr) Dispositif doseur de poudres
FR2628009A1 (fr) Appareil de pulverisation centrifuge a flux d'air cyclonique
EP0299059A1 (en) Apparatus and method for applying a uniform coating to food
FR2605207A1 (fr) Appareil emulsionneur pour preparations culinaires
CH269173A (fr) Procédé pour mélanger des matières, notamment des matières granuleuses ou pulvérisées, et installation pour la mise en oeuvre de ce procédé.
WO2016146141A1 (fr) Dispositif d'enrobage de matériau particulaire
BE633521A (da)
CA2649957A1 (fr) Appareil pour agiter des substances
BE898014A (fr) Machine de granulation et d'enrobage.
FR2529473A1 (fr) Perfectionnements aux broyeurs rotatifs a billes
FR2607724A1 (fr) Dispositif de traitement de matieres, notamment pour le melange, le malaxage, la fibrillation et la desintegration de matieres solides
FR2725636A3 (fr) Dispositif pour melanger un materiau pulverulent dans un liquide
FR2523474A1 (fr) Dispositif diviseur et melangeur de materiaux pulverulents secs ou legerement humides
FR2461650A1 (fr) Dispositif pour le remplissage automatique d'une boite de conserve ou de tout autre contenant par un ou plusieurs produits alimentaires
FR3083720A1 (fr) Separateur de solides
FR2539325A1 (fr) Dispositif d'alimentation en poudre pour appliquer des revetements resistant a l'usure sur des objets
WO1994007627A1 (fr) Installation de regeneration par traitement mecanique de particules enrobees d'une gangue
FR2639263A1 (fr) Dispositif pour le lavage de recipients de reaction

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): AT BE CH DE ES FR GB GR IT LI LU NL SE

17P Request for examination filed

Effective date: 19890907

17Q First examination report despatched

Effective date: 19910409

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19930901

REF Corresponds to:

Ref document number: 93744

Country of ref document: AT

Date of ref document: 19930915

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3883669

Country of ref document: DE

Date of ref document: 19931007

ITF It: translation for a ep patent filed
GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 19931202

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2046321

Country of ref document: ES

Kind code of ref document: T3

EPTA Lu: last paid annual fee
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: 88402268.2

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19970809

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19970811

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19970902

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: LU

Payment date: 19970904

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 19970910

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 19970911

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19970915

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19970929

Year of fee payment: 10

Ref country code: AT

Payment date: 19970929

Year of fee payment: 10

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980908

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980908

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980908

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: 19980909

Ref country code: ES

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 19980909

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980930

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980930

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19980930

BERE Be: lapsed

Owner name: ANDRIOT-BALLET MICHEL

Effective date: 19980930

Owner name: PILLON FRANCIS

Effective date: 19980930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990401

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19980908

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

EUG Se: european patent has lapsed

Ref document number: 88402268.2

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19990401

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: 19990701

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20001204

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20040915

Year of fee payment: 17

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

Effective date: 20050908

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: 20060531

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20060531