EP2146167A1 - Dispositif et procédé destinés à enlever des fluides - Google Patents

Dispositif et procédé destinés à enlever des fluides Download PDF

Info

Publication number
EP2146167A1
EP2146167A1 EP08012666A EP08012666A EP2146167A1 EP 2146167 A1 EP2146167 A1 EP 2146167A1 EP 08012666 A EP08012666 A EP 08012666A EP 08012666 A EP08012666 A EP 08012666A EP 2146167 A1 EP2146167 A1 EP 2146167A1
Authority
EP
European Patent Office
Prior art keywords
cell
opening
closure member
fluidized bed
particulate materials
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.)
Granted
Application number
EP08012666A
Other languages
German (de)
English (en)
Other versions
EP2146167B1 (fr
Inventor
Lothar Krell
Gerald Caspers
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.)
BMA Braunschweigische Maschinenbauanstalt AG
Original Assignee
BMA Braunschweigische Maschinenbauanstalt AG
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
Priority to AT08012666T priority Critical patent/ATE471493T1/de
Application filed by BMA Braunschweigische Maschinenbauanstalt AG filed Critical BMA Braunschweigische Maschinenbauanstalt AG
Priority to DE502008000807T priority patent/DE502008000807D1/de
Priority to DK08012666.7T priority patent/DK2146167T3/da
Priority to EP08012666A priority patent/EP2146167B1/fr
Priority to PCT/EP2009/058977 priority patent/WO2010007057A1/fr
Priority to US13/003,976 priority patent/US8844162B2/en
Priority to CN200980127379.XA priority patent/CN102099649B/zh
Publication of EP2146167A1 publication Critical patent/EP2146167A1/fr
Application granted granted Critical
Publication of EP2146167B1 publication Critical patent/EP2146167B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/001—Handling, e.g. loading or unloading arrangements
    • F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods

Definitions

  • the n-th cell or discharge cell provided with a discharge device, not shown, is substantially not flowed through by the fluidizing agent, so that material entering the cell without distributor bottom from above or at the inflow base 7 reaches the bottom region and via the discharge device, for example a discharge tube Screw conveyor, can be removed from the discharge cell.
  • a discharge device for example a discharge tube Screw conveyor
  • the swirl vanes 9 At its upper end, the swirl vanes 9 have a curvature of up to 35 ° to the axial component of the flow rate of the fluidizing means, to redirect the flow of the fluidizing means as well as that of the materials in the circumferential direction.
  • the swirl vanes 9 represent an extension of the walls 8, which extension may be formed with or without a gap between the swirl vanes 9 and the walls 8.
  • the swirl blades 9 may form a single or double curved surface, ie a curvature around both the axial component and a radial component to redirect the flow of the fluidizing agent and the direction of movement of the material or solids according to the requirements. Instead of a curvature, an inclination of otherwise straight-walled swirl vanes 9 can be provided for diverting the flow direction.
  • FIG. 7 represents a horizontal section along the line DD of FIG. 6
  • the entry cell 15 which is in operative connection with the entry device, not shown, for example, a screw conveyor shown, which is disposed immediately adjacent to the discharge cell 17, wherein the entry cell 15 and the discharge cell 17 are fluidly separated from each other so that an immediate transition of Material from the entry cell 15 in the discharge cell 17 is prevented.
  • Starting from the entry cell 15 is followed by a plurality of processing cells 16, which are separated by partitions 8 from each other.
  • the dividing walls 8 may be directly adjacent to the container wall or at a certain distance thereof within the annular process space 20, which is bounded on the bottom of the inflow base 7 and at the top of the underside of the swirl blades 9, suspended.
  • intermediate heating walls 18 may be arranged in order to provide additional heat energy for the drying process can.
  • the closure member has a coaxial to the shaft arranged circular segment cross-section.
  • each closure member in the n-th cell and the associated drive means are arranged outside the container, so that the shaft between the drive means and the closure member passes through the outer contour of the container.
  • Embodiments of the invention may be further characterized in that in the wall between the (n-1) -th cell and the n-th cell at least a fourth opening is arranged above the second opening, so that above the gap of particulate materials of the (n-1) th cell can enter the nth cell.
  • the walls swirl vanes are arranged, which are inclined or curved in the flow direction of the particulate materials from the first cell to the n-th cell, wherein the outer diameter of the swirl vanes is not greater than the outer diameter of the walls and the swirl vanes of an outer shell are surrounded, which does not protrude radially beyond the outer shell, which surrounds the walls.
  • first at least one closure member closes the third opening either from top to bottom or from bottom to top.
  • the invention also proposes that the process space is filled with a mixture of particulate materials in such a way and a fluidizing agent is supplied to the process space such that at least in the (n-1) -th cell the fluidized bed builds up at least up to the fourth opening.
  • the invention is therefore based on the surprising finding that during operation of the drying apparatus with a continuous feed of particulate matter to be dried and a continuous discharge of dried materials, a fluidized differential pressure gradient is formed, which on the one hand is sufficient as a driving force for transport of the the fluidized bed to be dried particulate materials from processing cell to processing cell and on the other hand ensures a continuous particle movement in front of a closure member which is necessary only between the last processing cell in which the fluidized bed propagates and the Austragszelle without fluidized bed, if the closure member not to Closing an opening of a wall between said last fluidized bed processing cell and the non-fluidized bed discharge cell is used, but for closing an opening of a gap between said the last processing cell and the discharge cell, so that there is no jamming of particles and / or an accumulation of heavy fluidizable product in front of the closure member.
  • the knowledge is used that, when the amount of supplied particulate materials of the fluidized bed is increased, the fluidized bed differential pressure increases, so that to ensure steady state process conditions in the fluidized bed with approximately constant filling and product residence time adjustment of the discharge the at least partially at least fluid-free particulate materials have to be made in dependence on said fluidized bed differential pressure.
  • This allows for a controlled amount of particulate materials in the fluidized bed, while optimizing the removal of the fluids from the particulate material. Further, even with momentary interruption or reduction of the supply of said mixture of particulate materials into the process space, it is ensured that the fluidized bed in the process space is not depleted of fluidized materials and thus maintained.
  • the transport of material in this case runs from the entry cell 15 via the processing cells 16 in the discharge cell 17, through openings in the partitions 8, such as the opening 8b in the partition wall 8a between the last processing cell 16 with distributor plate 7 and the discharge cell 17 without distributor plate.
  • materials must be able to flow out of the fluidized bed in accordance with the inflow of the materials, that is, they can leave the drying apparatus 1 through the opening 17a. This can be done in different ways.
  • the closure member 42a is made of the in FIG. 5a shown closing position in the in FIG. 5b rotated opening position, in a clockwise direction. This direction of rotation is important because it ensures that the closure member 42a sweeps past the opening 19a from bottom to top, so that coarser parts do not lead to jamming between the closure member 42a on the one hand and the wall 8a and / or the outlet bottom 7 on the other hand.
  • a plurality of closure members may be appropriate to influence the opening times.
  • the conveyor 30 may be used.
  • the closure member 42a can fully release the opening 19a for a short period of time, as in FIG. 5b shown, namely to allow the discharge of any existing coarse particles.
  • the required rotational movement of the closure members 42a, 42b also depends on the number of closure members.
  • the opening 8c acts as a stationary weir, which allows particulate materials to enter the discharge cell 17 from the processing cell 16.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Microbiology (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
  • Drying Of Solid Materials (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
EP08012666A 2008-07-14 2008-07-14 Dispositif et procédé destinés à enlever des fluides Active EP2146167B1 (fr)

Priority Applications (7)

Application Number Priority Date Filing Date Title
DE502008000807T DE502008000807D1 (de) 2008-07-14 2008-07-14 Vorrichtung und Verfahren zum Entfernen von Fluiden
DK08012666.7T DK2146167T3 (da) 2008-07-14 2008-07-14 Indretning og fremgangsmåde til fjernelse af fluider
EP08012666A EP2146167B1 (fr) 2008-07-14 2008-07-14 Dispositif et procédé destinés à enlever des fluides
AT08012666T ATE471493T1 (de) 2008-07-14 2008-07-14 Vorrichtung und verfahren zum entfernen von fluiden
PCT/EP2009/058977 WO2010007057A1 (fr) 2008-07-14 2009-07-14 Dispositif et procédé destinés à retirer des fluides et/ou des solides
US13/003,976 US8844162B2 (en) 2008-07-14 2009-07-14 Device and method for removing fluids and/or solids
CN200980127379.XA CN102099649B (zh) 2008-07-14 2009-07-14 用于排除流体和/或固体的设备和方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP08012666A EP2146167B1 (fr) 2008-07-14 2008-07-14 Dispositif et procédé destinés à enlever des fluides

Publications (2)

Publication Number Publication Date
EP2146167A1 true EP2146167A1 (fr) 2010-01-20
EP2146167B1 EP2146167B1 (fr) 2010-06-16

Family

ID=40029246

Family Applications (1)

Application Number Title Priority Date Filing Date
EP08012666A Active EP2146167B1 (fr) 2008-07-14 2008-07-14 Dispositif et procédé destinés à enlever des fluides

Country Status (7)

Country Link
US (1) US8844162B2 (fr)
EP (1) EP2146167B1 (fr)
CN (1) CN102099649B (fr)
AT (1) ATE471493T1 (fr)
DE (1) DE502008000807D1 (fr)
DK (1) DK2146167T3 (fr)
WO (1) WO2010007057A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102014106122A1 (de) 2014-04-30 2015-11-05 Bma Braunschweigische Maschinenbauanstalt Ag Wirbelschichtverdampfungstrockner

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB833232A (en) * 1955-06-06 1960-04-21 Peters Ag Claudius Improvements connected with delivery valves for silos
US3360867A (en) * 1965-11-18 1968-01-02 Komline Sanderson Eng Corp Batch-type fluidizing apparatus and process
DE1932388A1 (de) * 1968-07-01 1970-01-22 Westinghouse Brake & Signal Ventil zum Steuern der Materialabgabe aus einem Trichter
DE2421278A1 (de) * 1973-05-10 1974-11-28 Anhydro As Apparat zur behandlung fluidisierter materialien
EP0183154A2 (fr) * 1984-11-23 1986-06-04 BASF Aktiengesellschaft Procédé pour la mesure continue du degré de remplissage des appareils à poudres fluidisées
US4593477A (en) * 1982-12-16 1986-06-10 The Babcock & Wilcox Company Control system for a fluidized bed
JPH11142056A (ja) * 1997-11-10 1999-05-28 Nara Kikai Seisakusho:Kk 流動層乾燥装置の粉体排出構造
EP0955511A2 (fr) * 1998-05-07 1999-11-10 ASJ Holding ApS Appareil pour le séchage d'un matériau particulaire humide par vapeur surchauffée
EP1044732A1 (fr) * 1998-11-02 2000-10-18 Kawasaki Jukogyo Kabushiki Kaisha Classificateur a lit fluidise du type a plusieurs chambres

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1260884A (fr) * 1960-06-02 1961-05-12 English Clays Lovering Pochin Procédé de séchage d'une matière insoluble à l'état de particules, s'appliquant en particulier au séchage du kaolin
CH652940A5 (de) * 1982-01-09 1985-12-13 Sandoz Ag Verfahren zur herstellung nicht staubender granulate und vorrichtung hierfuer.
JPS61152411A (ja) * 1984-12-26 1986-07-11 Mitsubishi Gas Chem Co Inc 多層パリソン及びその製造方法
DK165290A (da) * 1990-07-09 1992-01-10 Dds Eng As Apparat til toerring af et vaeskeholdigt partikelformet materiale med overhedet damp
CN2258975Y (zh) * 1995-06-14 1997-08-06 蒋大洲 一种流化床造粒干燥装置
DE502007003463D1 (de) 2007-02-09 2010-05-27 Braunschweigische Maschb Ansta Vorrichtung zum Entfernen von Fluiden und/oder Feststoffen

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB833232A (en) * 1955-06-06 1960-04-21 Peters Ag Claudius Improvements connected with delivery valves for silos
US3360867A (en) * 1965-11-18 1968-01-02 Komline Sanderson Eng Corp Batch-type fluidizing apparatus and process
DE1932388A1 (de) * 1968-07-01 1970-01-22 Westinghouse Brake & Signal Ventil zum Steuern der Materialabgabe aus einem Trichter
DE2421278A1 (de) * 1973-05-10 1974-11-28 Anhydro As Apparat zur behandlung fluidisierter materialien
US4593477A (en) * 1982-12-16 1986-06-10 The Babcock & Wilcox Company Control system for a fluidized bed
EP0183154A2 (fr) * 1984-11-23 1986-06-04 BASF Aktiengesellschaft Procédé pour la mesure continue du degré de remplissage des appareils à poudres fluidisées
JPH11142056A (ja) * 1997-11-10 1999-05-28 Nara Kikai Seisakusho:Kk 流動層乾燥装置の粉体排出構造
EP0955511A2 (fr) * 1998-05-07 1999-11-10 ASJ Holding ApS Appareil pour le séchage d'un matériau particulaire humide par vapeur surchauffée
EP0955511B1 (fr) 1998-05-07 2003-09-10 ASJ Holding ApS Appareil pour le séchage d'un matériau particulaire humide par vapeur surchauffée
EP1044732A1 (fr) * 1998-11-02 2000-10-18 Kawasaki Jukogyo Kabushiki Kaisha Classificateur a lit fluidise du type a plusieurs chambres

Also Published As

Publication number Publication date
CN102099649A (zh) 2011-06-15
US20110162229A1 (en) 2011-07-07
EP2146167B1 (fr) 2010-06-16
WO2010007057A1 (fr) 2010-01-21
US8844162B2 (en) 2014-09-30
DE502008000807D1 (de) 2010-07-29
ATE471493T1 (de) 2010-07-15
DK2146167T3 (da) 2010-09-27
CN102099649B (zh) 2012-08-01

Similar Documents

Publication Publication Date Title
EP1956326B1 (fr) Dispositif de suppression de fluides et/ou de substances solides
EP2646160B1 (fr) Élément dynamique pour le dispositif de séparation d'un broyeur agitateur à billes
DE2330641C2 (de) Vorrichtung zum Austragen von Behandlungsgut aus einem Behandlungsraum
EP3102332B1 (fr) Broyeur à billes à agitateur
DE2820454B2 (de) Anlage zur Kühlung und Trennung von Abgüssen und Formsand
EP2316562A1 (fr) Dispositif et procédé destinés au traitement d'un produit en vrac
EP3154703B1 (fr) Centrifugeuse à vis à bol plein
EP1080786B1 (fr) Procédé, dispositif et système pour broyeur à jet à lit fluidisé
EP0541759B1 (fr) Dispositif a lit fluidise pour le traitement de matiere particulaire
EP0500561B1 (fr) Procede et dispositif pour l'agitation e le traitement thermique de particules solides
DE60118366T2 (de) Dampfschälungsverfahren
EP2146167B1 (fr) Dispositif et procédé destinés à enlever des fluides
DE19537303B4 (de) Vorrichtung zum Homogenisieren fließfähiger Stoffe
EP2429711B1 (fr) Centrifugeuse à fonctionnement continu
WO1990001985A1 (fr) Dispositif de traitement de milieux liquides ou peu visqueux
DD232844A5 (de) Verfahren und vorrichtung zum trennschleudern von feinkornmineralgemischen
DE19818270A1 (de) Verbesserungen betreffend Tabakseparatoren bzw. Tabaktrennvorrichtungen
EP1555068B1 (fr) Cloison de broyeur tubulaire et méthode de broyage utilisant un tel broyeur
DE1203734B (de) Anlage zur Extraktion von loeslichen Stoffen aus festen pflanzlichen, tierischen oder anorganischen Stoffen im Gegenstrom
DE2808011C2 (fr)
DE195740C (fr)
CH657600A5 (de) Foerderanlage.
DE7736318U1 (de) Vorrichtung zur zerlegung von schaum
EP4371668A1 (fr) Broyeur agitateur avec panier à fentes
DE102022130384A1 (de) Rührwerksmühle mit Korb mit Verdickung

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

17P Request for examination filed

Effective date: 20090729

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA MK RS

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REF Corresponds to:

Ref document number: 502008000807

Country of ref document: DE

Date of ref document: 20100729

Kind code of ref document: P

AKX Designation fees paid

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20100616

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

Ref country code: LT

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: 20100616

Ref country code: SE

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: 20100616

Ref country code: NO

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: 20100916

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20100616

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

Ref country code: FI

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: 20100616

Ref country code: HR

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: 20100616

Ref country code: LV

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: 20100616

Ref country code: SI

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: 20100616

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

Ref country code: PL

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: 20100616

Ref country code: CY

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: 20100616

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

BERE Be: lapsed

Owner name: BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT A.G.

Effective date: 20100731

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100616

Ref country code: EE

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: 20100616

Ref country code: IE

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: 20100616

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

Ref country code: SK

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: 20100616

Ref country code: MC

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

Effective date: 20100731

Ref country code: IS

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: 20101016

Ref country code: CZ

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: 20100616

Ref country code: RO

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: 20100616

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20100616

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20110331

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

Effective date: 20110317

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: 20100816

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: 20100917

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

Ref country code: BE

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

Effective date: 20100731

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502008000807

Country of ref document: DE

Effective date: 20110316

REG Reference to a national code

Ref country code: FR

Ref legal event code: D3

PGRI Patent reinstated in contracting state [announced from national office to epo]

Ref country code: FR

Effective date: 20110727

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 502008000807

Country of ref document: DE

Representative=s name: JONES DAY RECHTSANWAELTE PATENTANWAELTE, DE

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

Ref country code: MT

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: 20100616

REG Reference to a national code

Ref country code: DE

Ref legal event code: R082

Ref document number: 502008000807

Country of ref document: DE

Representative=s name: JONES DAY RECHTSANWAELTE PATENTANWAELTE, DE

Effective date: 20111122

Ref country code: DE

Ref legal event code: R081

Ref document number: 502008000807

Country of ref document: DE

Owner name: BMA BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG, DE

Free format text: FORMER OWNER: BRAUNSCHWEIGISCHE MASCHINENBAUANSTALT AG, 38122 BRAUNSCHWEIG, DE

Effective date: 20111122

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

Ref country code: HU

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: 20101217

Ref country code: LU

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

Effective date: 20100714

Ref country code: BG

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: 20100616

Ref country code: PT

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: 20101116

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

Ref country code: TR

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: 20100616

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

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

Effective date: 20120714

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: 20120731

Ref country code: CH

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

Effective date: 20120731

Ref country code: GB

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

Effective date: 20120714

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

Ref country code: BG

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: 20100916

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

Ref country code: ES

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: 20100927

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 471493

Country of ref document: AT

Kind code of ref document: T

Effective date: 20130714

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

Ref country code: AT

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

Effective date: 20130714

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 9

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 11

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

Ref country code: FR

Payment date: 20230720

Year of fee payment: 16

Ref country code: DK

Payment date: 20230724

Year of fee payment: 16

Ref country code: DE

Payment date: 20230720

Year of fee payment: 16