EP1232793B1 - Farines de blé avec capacité d'absorption d'eau élevée, ainsi que procédé et appareil pour les fabriquer - Google Patents

Farines de blé avec capacité d'absorption d'eau élevée, ainsi que procédé et appareil pour les fabriquer Download PDF

Info

Publication number
EP1232793B1
EP1232793B1 EP02000504A EP02000504A EP1232793B1 EP 1232793 B1 EP1232793 B1 EP 1232793B1 EP 02000504 A EP02000504 A EP 02000504A EP 02000504 A EP02000504 A EP 02000504A EP 1232793 B1 EP1232793 B1 EP 1232793B1
Authority
EP
European Patent Office
Prior art keywords
flour
ball mill
grinding
stirring device
flours
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
EP02000504A
Other languages
German (de)
English (en)
Other versions
EP1232793A2 (fr
EP1232793A3 (fr
Inventor
Oskar Dipl.-Ing. Degant (Fh)
Dieter Dr.-Ing. Schwechten
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.)
Hosokawa Alpine AG
Original Assignee
Hosokawa Alpine 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
Application filed by Hosokawa Alpine AG filed Critical Hosokawa Alpine AG
Priority to DK02000504T priority Critical patent/DK1232793T3/da
Publication of EP1232793A2 publication Critical patent/EP1232793A2/fr
Publication of EP1232793A3 publication Critical patent/EP1232793A3/fr
Application granted granted Critical
Publication of EP1232793B1 publication Critical patent/EP1232793B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/16—Mills in which a fixed container houses stirring means tumbling the charge
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C11/00—Other auxiliary devices or accessories specially adapted for grain mills
    • B02C11/08—Cooling, heating, ventilating, conditioning with respect to temperature or water content
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/18—Details
    • B02C17/1815—Cooling or heating devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
    • B02C17/18—Details
    • B02C17/20—Disintegrating members
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C9/00—Other milling methods or mills specially adapted for grain
    • B02C9/04—Systems or sequences of operations; Plant

Definitions

  • the invention relates to wheat flour for dough preparation for the baker's Application but also for other applications inside and outside of the Food processing, a process for the production of these wheat flours and a device for carrying out the method.
  • the Dough stability is measured in minutes and is the time starting with the Reaching 500 Brabender Farinogrammtechniken until falling below 500 Brabender Farinogrammüen.
  • the dough softening is in Brabender farinogram units (FE) measured as the difference between 500 Brabender farinogram units and the value on Brabender farinogram units 12 Minutes after the start of the drop below 500 Brabender Farinogrammmaschineen.
  • FE Brabender farinogram units
  • a high water absorption or dough yield of a flour is for bakers Applications first important because they relate to the used Flour high pastry yields allowed.
  • GB-A-1 265 735 discloses a stirred ball mill having a double-walled ball mill water-cooled housing known.
  • British Patent No. 1,108,911 describes a process in which high-level flours Proportion of damaged starch. In principle, they are suitable for damage to the starch Roller mills. In the usual production of "light" flour but not at first Strength damage, but an energetically favorable and effective separation of Aspired shell ingredients, with the aim of a low-mineral flour with as possible high yield with a correspondingly low proportion of mineral-rich as possible bran and To win over products. To increase the already given Starch damage is changed in this grinding process, the roller speed. The Relative speed of the rolls of a pair of rolls to each other (overfeed) is increased, The nip is reduced, the contact pressure of the rollers is increased.
  • German Auslegeschrift DE-AS 26 22 748 relates to a method by which a Compaction of a rye flour by at least 10 percent, followed by comminution of the compacted material, an improvement of the baking properties of the flour and the To achieve freshness properties of the baked goods to be produced therefrom.
  • the Water absorption of a rye flour considerably increased.
  • Application of the procedure wheat flour affects according to the local revelations in a similar way.
  • the scored Effect was limited due to the change in the protein and the resulting resulting improvement of the adhesive properties to an increase in the Pastries volume. Data on the water absorption of untreated and treated wheat flours are not disclosed, even values for the assumed damage to starch is neither for wheat nor for Rye flours in front.
  • European patent EP 0 919 294 B1 describes a dry one Agitator ball mill for processing cereal flours. That's where it comes from the conditions used do not cause damage to the starch. These intended task is the detachment of the protein from the starch granules, which achieved with very high efficiency. The proteins can be separated by a Separate downstream sighting in high enrichment.
  • the invention relates to a novel wheat flour, which starting from a normal, by means of a conventional roller mill grinding process obtained wheat flour with a likewise claimed as invention Method was modified so that it is compared to the starting flour one order has more than 10 percentage points increased water absorption, the Dough stability and the dough softening of the dough made therefrom the corresponding values of the dough from the starting flour significantly negatively influenced or even improved.
  • flours according to the invention are also doughs with high dough yield, ie high water content, still stable and do not stick, so they despite the use the usual processing plants for an optimal pastry can be processed.
  • the influences caused by the grinding process on those in the Farinographen measured parameters (water absorption, dough stability and dough softening) a flour are not limited to the Starch damage.
  • the protein component can also be changed; here is to think about an oxidative adhesive fortification, but also a damage of the Protein by shear and temperature effects is possible.
  • the fineness of Flour particles produced also play a role.
  • different Milling systems affect the above parameters in different way. In consequence, that means that one Grinding system the strength "selectively" damaged and at the same or even leads to a higher water absorption than another milling system damaging effects on other components, e.g. Proteins and Pentosans lead to lower dough stability and higher dough softening.
  • the inventive Agitator ball mill is possible, e.g. commercial baker's flour of the type 550 to change so that compared to the starting flour an increase in the Water absorption of significantly more than the previously known 10 percentage points is reached.
  • the water absorption by up to 29 percentage points increased compared to the starting flour.
  • Table 1 shows a comparison between different flours, grinded from the same starting flour by means of pin mill (type CW) and by means of a stirred ball mill (type ATR). At about the same registered specific energy and fineness, there are clear differences in water absorption and starch damage in favor of the ground in the agitator ball mill flour. Even with significantly higher enlisted energy, the water-picking effect of the pin mill can not approach that of the ball mill. Effects of pin mill and ball mill treatment Starting flour. pin mill 1 ball mill 1 pin mill 2 ball mill 2 spec.
  • Fig. 1 shows the inventive stirred ball mill
  • Fig. 2 shows a plant scheme with continuous grinding
  • 3 shows a plant scheme with Kreislaufmahlung.
  • FIGS. 4 to 6 show the evaluations of the test results in FIG Dough stability diagrams (FIG. 4), the damaged starch (FIG Teigerweichung ( Figure 6) for test series each in an inventive Agitator ball mill (Alpine ATR) with steel balls and aluminum oxide balls (Ceramics), and a comparative test series on a pin mill (Alpine CW) According to the state of the art.
  • the mill is a continuous or discontinuous, ie batchwise dry agitator ball mill.
  • the agitator ball mill 11 is driven by a drive unit consisting of motor 7, clutch 8 and bevel gear 9 , which is arranged on a bracket 10 .
  • the drive energy of the motor 7 is introduced via the clutch 8 and the angle gear 9 in the agitator shaft 5 and transferred as grinding energy through the attached to the agitator shaft 5 agitators 6 in the foundry container 1 bed of ground material and grinding balls.
  • the stress of the ground material for comminution in the stirred ball mill 11 takes place in a complex manner by a combination of pressure, shock, shear and shear between the grinding balls. These have a size of preferably less than 7 mm, usually between 1 and 5 mm. Although even smaller grinding balls would be advantageous from a process engineering point of view (higher number of contact points), smaller balls than 1 mm are not used because economic aspects speak against it.
  • the grinding balls must be separated from the material to be ground in a separating stage following the grinding, for example in a screening machine 14 (FIGS. 2 and 3).
  • a screening machine 14 For the separation of very fine grinding balls, however, very large, fine-meshed screen surfaces are required, which are very expensive and therefore not very economical.
  • the vertical grinding vessel 1 which has a tapered lower part 2 of material to be ground and grinding balls, starting from the mill inlet 3 in the direction of the mill outlet 4 flows through evenly, with one at the end of the tapered lower part 2 of the grinding vessel 1 is a horizontal discharge screw 12 is arranged to control the residence time of the material in the grinding vessel 1 .
  • the speed of the discharge screw 12 is variably adjustable via an adjustable worm drive 13 and thus the throughput through the mill in wide ranges adjustable.
  • the speed of the agitator shaft 5 is variably adjustable via the variable motor 7 .
  • the agitator shaft and discharge screw speed determine the specific energy (kWh / t) entered into the material to be ground.
  • the material to be ground can either be placed directly on the agitator ball mill 11 , or it is - as shown - abandoned from a Mahlgutvorrat 25 via a feed screw 26 in the bucket elevator 23 .
  • the flour treated in a passage in the agitator ball mill 11 is fed by the screw discharge 12 from the lower reaches of the agitator ball mill 11 coming the sieving machine 14 and separated into a fine fraction and a coarse fraction.
  • the fine fraction is tapped off directly at the outlet material outlet 18 and represents the end product.
  • the coarse fraction consists of the balls and is returned to the collecting container 15 .
  • the balls from the collecting container 15 are combined with the newly abandoned grinding material from the ground stock 25 in the area of the bucket elevator 23 and conveyed through the bucket elevator 24 into the agitator ball mill 11 .
  • the material to be ground is first transported from a Mahlgutvorrat 25 via a feed screw 26 in the intermediate container 19 .
  • the newly added ground material is mixed in the intermediate container with recirculated coarse material and fed via a feed screw 27 via the bucket elevator 23 to the bucket elevator 24 .
  • the abandoned ground material mixture passes through the bucket elevator 24 to the mill inlet 3 of the agitating ball mill 11.
  • the flour treated in the agitating ball mill 11 is fed to the screening machine 14 after the screw discharge 12 from the underflow of the agitating ball mill 11 and into a flour fraction and a ball fraction separately.
  • the ball is again fed to the collecting tank 15 , from here the balls as well as the combined with the recirculated coarse material in the intermediate container 19 new ground material in the bucket elevator 23 of the bucket elevator 24 are promoted.
  • the flour fraction is fed coming from the screening machine 14 by means of conveying air 17 an air classifier 16 and separated there into a fine and a coarse flour fraction.
  • the coarse flour fraction is fed via the coarse material line 28 and the return screw 29 to the intermediate container 19 .
  • the air required for air classification is generated by the blower 22 and at the same time conveying air 17 for the sieved on the screening machine 14 Kreislaufgut.
  • the fine flour fraction is guided together with the classifying air into the filter 20 , deposited there and is discharged via the product outlet 21 .

Landscapes

  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Cereal-Derived Products (AREA)
  • Bakery Products And Manufacturing Methods Therefor (AREA)

Claims (16)

  1. Procédé de traitement de farines de blé par mouture à sec d'une farine de départ afin d'augmenter la capacité d'absorption d'eau, caractérisé en ce que la mouture s'opère dans un broyeur à billes-agitateur sec avec un apport d'énergie de broyage de 20 à 300 kWh par tonne de farine de départ, à une température de la farine inférieure à 60 °C, une augmentation de la capacité d'absorption d'eau de plus de 10 points étant obtenue par rapport à la farine de départ.
  2. Procédé selon la revendication 1, caractérisé en ce que l'augmentation de la capacité d'absorption d'eau représente entre 10 et 40 points par rapport à la farine de départ.
  3. Procédé selon la revendication 1 ou 2, caractérisé en ce que les farines de blé sont moulues par passage dans le broyeur à billes-agitateur.
  4. Procédé selon la revendication 1 ou 2, caractérisé en ce que les farines de blé sont moulues en circuit dans le broyeur à billes-agitateur.
  5. Procédé selon la revendication 1 à 4, caractérisé en ce que la mouture est réalisée à une température comprise entre 30 °C et 50 °C.
  6. Procédé selon la revendication 1 ou 2, caractérisé en ce que les farines de blé sont moulues dans le broyeur à billes-agitateur en mode discontinu.
  7. Procédé selon la revendication 1 à 5, caractérisé en ce qu'un produit réfrigérant est directement versé dans le contenu du broyeur à billes-agitateur.
  8. Procédé selon la revendication 1 à 5, caractérisé en ce que le broyeur à billes-agitateur fonctionne avec des billes de broyage amenées dans le circuit, qui sont refroidies par un réfrigérant.
  9. Procédé selon la revendication 7 ou 8, caractérisé en ce que le réfrigérant est de l'air, de l'azote liquide ou du dioxyde de carbone liquide/solide.
  10. Procédé selon la revendication 1 à 9, caractérisé en ce que le broyeur à billes-agitateur est pourvu d'une chemise à double paroi qui est refroidie à l'eau.
  11. Procédé selon l'une des revendications 1 à 10, caractérisé en ce que le broyeur à billes-agitateur contient des billes de broyage en oxyde d'aluminium ou en acier.
  12. Procédé selon la revendication 11, caractérisé en ce que les billes de broyage présentent un diamètre inférieur à 7 mm, de préférence compris entre 1 mm et 5 mm.
  13. Procédé selon la revendication 1 à 9, caractérisé en ce qu'il s'agit en ce qui concerne les farines de blé, de farines de type 405 ou 550.
  14. Procédé selon la revendication 13, caractérisé en ce que la farine de blé présente une capacité d'absorption d'eau supérieure à 70 % et une teneur en amidon endommagé supérieure à 8 %.
  15. Procédé selon la revendication 13, caractérisé en ce que la farine de blé présente une capacité d'absorption d'eau supérieure à 70 % et une stabilité de la pâte de plus de 1,3 min.
  16. Procédé selon la revendication 13, caractérisé en ce que la farine de blé présente une capacité d'absorption d'eau supérieure à 70 % et un ramollissement de la pâte inférieur à 130 unités Brabender de farinogramme.
EP02000504A 2001-02-16 2002-01-09 Farines de blé avec capacité d'absorption d'eau élevée, ainsi que procédé et appareil pour les fabriquer Expired - Lifetime EP1232793B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DK02000504T DK1232793T3 (da) 2001-02-16 2002-01-09 Hvedemel med foröget vandoptagelsesevne samt fremgangsmåde og indretning til fremstilling heraf

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10107885A DE10107885A1 (de) 2001-02-16 2001-02-16 Weizenmehle mit erhöhter Wasseraufnahmefähigkeit, sowie Verfahren und Vorrichtung zu deren Herstellung
DE10107885 2001-02-16

Publications (3)

Publication Number Publication Date
EP1232793A2 EP1232793A2 (fr) 2002-08-21
EP1232793A3 EP1232793A3 (fr) 2003-05-07
EP1232793B1 true EP1232793B1 (fr) 2005-04-06

Family

ID=7674690

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02000504A Expired - Lifetime EP1232793B1 (fr) 2001-02-16 2002-01-09 Farines de blé avec capacité d'absorption d'eau élevée, ainsi que procédé et appareil pour les fabriquer

Country Status (4)

Country Link
EP (1) EP1232793B1 (fr)
AT (1) ATE292521T1 (fr)
DE (2) DE10107885A1 (fr)
DK (1) DK1232793T3 (fr)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103657792A (zh) * 2013-12-03 2014-03-26 河南康隆食业有限公司 一种小麦面粉生产系统
CN109225482A (zh) * 2018-09-03 2019-01-18 马鞍山起劲磁塑科技有限公司 中心进气进水式新型化工球磨机

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB474359A (en) * 1936-04-22 1937-10-22 Gustav Gerson Haber Improvements in or relating to the grinding of grain or like cereals and storing of flour so obtained
GB1108911A (en) 1964-03-13 1968-04-10 Gordon James Baker Improvements in or relating to the milling of wheat and wheat products
GB1265735A (fr) * 1969-10-30 1972-03-08
DE2622748C2 (de) 1976-05-21 1980-01-24 Muehle Rueningen Ag, 3300 Braunschweig Behandlung von getreidemehl oder getreidekorn
JP3703148B2 (ja) * 1995-06-06 2005-10-05 寿工業株式会社 湿式撹拌ボールミルと方法
DE59701334D1 (de) 1997-11-27 2000-04-27 Hosokawa Alpine Ag & Co Verfahren zur Proteinanreicherung bei Cerealien, insbesondere Getreide und Hülsenfrüchte

Also Published As

Publication number Publication date
DE50202675D1 (de) 2005-05-12
ATE292521T1 (de) 2005-04-15
EP1232793A2 (fr) 2002-08-21
EP1232793A3 (fr) 2003-05-07
DE10107885A1 (de) 2002-09-05
DK1232793T3 (da) 2005-08-22

Similar Documents

Publication Publication Date Title
EP0335925B1 (fr) Procede de fabrication de produits cerealiers moulus et moulin a cereales
EP2313199B1 (fr) Dispositif et procédé pour produire de la farine et/ou de la semoule
EP0016442B1 (fr) Procédé et installation de préparation de chapelure ainsi qu'une chapelure
DE2442552C3 (de) Verfahren zur Verbesserung der Backeigenschaften von Weizen
WO1995004595A1 (fr) Procede et dispositif permettant de nettoyer des cereales et de les preparer en vue de leur mouture
WO1994003274A1 (fr) Procede et dispositif pour mouiller en continu des cereales et utilisation du dispositif mouille-grain
DE2454236A1 (de) Verfahren zur gewinnung von staerke, lebenswichtigem gluten und einer naehrenden mischung aus kleie, keimen und fasern
EP0544846B1 (fr) Procede pour la fabrication d'un produit sous forme de grains
EP1232793B1 (fr) Farines de blé avec capacité d'absorption d'eau élevée, ainsi que procédé et appareil pour les fabriquer
CH620708A5 (fr)
EP3009191A1 (fr) Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales
DE4494352C2 (de) Verfahren zur Herstellung eines Halbfertigprodukts, insbesondere eines Vollkornteiges, aus Getreide für Nahrungsmittel und dergleichen
CH672441A5 (fr)
DE60119265T2 (de) Verfahren zur Vermahlung von Mais
DE2919845C2 (de) Verfahren zur Herstellung von Paniermehl, eine Vorrichtung zur Durchführung dieses Verfahrens sowie ein Paniermehl
CH706010A2 (de) Verfahren zum Bereitstellen von backfähigem Mehl.
Sosulski et al. Effects of attrition milling on air classification properties of hard wheat flours
DE4443952C5 (de) Weizenmehlmischung enthaltend Weichweizenmehl und einen Anteil Hartweizenmehl und deren Verwendung zum Brotbacken
EP4344555A1 (fr) Substitut d'oeufs
DD282861A5 (de) Verfahren und Getreidemühle zur Herstellung von Getreidemahlprodukten
EP1787531B1 (fr) Procédé pour la fabrication de pâte crue pour des pâtes alimentaires
DE2604235C2 (de) Trockenes pulverförmiges Glutenprodukt, Verfahren zu seiner Herstellung und dessen Verwendung
DE102004054681A1 (de) Verfahren zur Herstellung eines kalt anrührbaren Grundstoffs zur Verwendung bei Cremes, Pasten und dergleichen
Bailey Flour Manufacture
DD266925A3 (de) Verfahren und anordnung zur herstellung proteinreichen weizenmehles

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: A2

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

RIC1 Information provided on ipc code assigned before grant

Ipc: 7B 02C 17/18 B

Ipc: 7B 02C 11/08 B

Ipc: 7B 02C 17/20 B

Ipc: 7B 02C 17/16 A

Ipc: 7B 02C 9/04 B

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Extension state: AL LT LV MK RO SI

17P Request for examination filed

Effective date: 20030403

17Q First examination report despatched

Effective date: 20030710

AKX Designation fees paid

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

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 CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

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

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: 20050406

Ref country code: GB

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: 20050406

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: 20050406

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: LUCHS & PARTNER PATENTANWAELTE

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Owner name: HOSOKAWA ALPINE AKTIENGESELLSCHAFT

Free format text: HOSOKAWA ALPINE AKTIENGESELLSCHAFT & CO. OHG#PETER-DOERFLER-STRASSE 13-25#86199 AUGSBURG (DE) -TRANSFER TO- HOSOKAWA ALPINE AKTIENGESELLSCHAFT#PETER-DOERFLER-STRASSE 13-25#86199 AUGSBURG (DE)

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: 50202675

Country of ref document: DE

Date of ref document: 20050512

Kind code of ref document: P

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

Owner name: HOSOKAWA ALPINE AKTIENGESELLSCHAFT

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: 20050706

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: 20050706

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: 20050717

NLT2 Nl: modifications (of names), taken from the european patent patent bulletin

Owner name: HOSOKAWA ALPINE AKTIENGESELLSCHAFT

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

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

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: 20050908

GBV Gb: ep patent (uk) treated as always having been void in accordance with gb section 77(7)/1977 [no translation filed]

Effective date: 20050406

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

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

Ref country code: MC

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

Effective date: 20060131

Ref country code: LU

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

Effective date: 20060131

Ref country code: BE

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

Effective date: 20060131

ET Fr: translation filed
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

Effective date: 20060110

BERE Be: lapsed

Owner name: HOSOKAWA ALPINE A.G. & CO. OHG

Effective date: 20060131

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: 20050406

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

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: 20050406

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

Ref country code: AT

Payment date: 20090127

Year of fee payment: 8

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: 20100109

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

Ref country code: FR

Payment date: 20120202

Year of fee payment: 11

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

Ref country code: DK

Payment date: 20120111

Year of fee payment: 11

Ref country code: IT

Payment date: 20120112

Year of fee payment: 11

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

Ref country code: NL

Payment date: 20120117

Year of fee payment: 11

REG Reference to a national code

Ref country code: NL

Ref legal event code: V1

Effective date: 20130801

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20130930

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: 20130801

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: 20130131

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: 20130109

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

Ref country code: DK

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

Effective date: 20130131

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

Ref country code: DE

Payment date: 20140116

Year of fee payment: 13

Ref country code: CH

Payment date: 20140114

Year of fee payment: 13

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 50202675

Country of ref document: DE

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

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: 20150131

Ref country code: CH

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

Effective date: 20150131

Ref country code: DE

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

Effective date: 20150801