EP1232793B1 - Weizenmehle mit erhöhter Wasseraufnahmefähigkeit, sowie Verfahren und Vorrichtung zu deren Herstellung - Google Patents
Weizenmehle mit erhöhter Wasseraufnahmefähigkeit, sowie Verfahren und Vorrichtung zu deren Herstellung Download PDFInfo
- 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
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 .
Description
Effekte von Stiftmühlen- und Kugelmühlenbehandlung | |||||
Ausgangsmehl. | Stiftmühle 1 | Kugelmühle 1 | Stiftmühle 2 | Kugelmühle 2 | |
spez. Energie (kWh/t) | - | 82,3 | 86,3 | 183,5 | 132,2 |
D 10 (µ) | 13,3 | 6,4 | 5,3 | 4,0 | 4,9 |
D 50 (µ) | 64,7 | 28,5 | 21,7 | 17,4 | 21,3 |
D 90 (µ) | 174,0 | 98,8 | 53,7 | 47,8 | 48,8 |
Wasseraufnahme (%) | 59,2 | 61,6 | 80,3 | 65,1 | 88,3 |
Stärkebeschädigung (%) | 6,1 | 8,0 | 9,9 | 11,4 | 12,7 |
Ausgangsmehl | behandeltes Mehl | |
Feuchte (%) | 15,0 | 9,6 |
Protein (%) | 12,7 | 12,5 |
Far.-Wasseraufnahme (%) | 59,6 | 79,8 |
Far.-Teigstabilität (min.) | 10,7 | 17,6 |
Far.-Teigerweichung (BE) | 46,0 | -16,0 |
beschädigte Stärke ICC 164 | 7,2 | 8,8 |
- 1
- Mahlgefäß
- 2
- konischer Teil
- 3
- Mühleneinlass
- 4
- Mühlenauslass
- 5
- Rührwerkswelle
- 6
- Rührorgane
- 7
- Motor
- 8
- Kupplung
- 9
- Winkelgetriebe
- 10
- Konsole
- 11
- Rührwerkskugelmühle
- 12
- Austragsschnecke
- 13
- Schneckenantrieb
- 14
- Siebmaschine
- 15
- Sammelbehälter
- 16
- Windsichter
- 17
- Förderluft
- 18
- Durchlaufgut-Auslass
- 19
- Zwischenbehälter
- 20
- Filter
- 21
- Produktauslass
- 22
- Gebläse
- 23
- Becherwerksfuß
- 24
- Becherwerk
- 25
- Mahlgutvorrat
- 26
- Aufgabeschnecke
- 27
- Zuführschnecke
- 28
- Grobgutleitung
- 29
- Rückführschnecke
Claims (16)
- Verfahren zur Behandlung von Weizenmehlen durch trockene Vermahlung eines Ausgangsmehls zur Erhöhung der Wasseraufnahmefähigkeit dadurch gekennzeichnet, dass die Vermahlung in einer trockenen Rührwerkskugelmühle unter Eintrag von 20 bis 300 kWh Mahlenergie pro Tonne Ausgangsmehl bei einer Temperatur des Mehles von weniger als 60°C durchgeführt wird, wodurch eine Erhöhung der Wasseraufnahmefähigkeit von mehr als 10 Prozentpunkten gegenüber dem Ausgangsmehl erreicht wird.
- Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass die Erhöhung der Wasseraufnahmefähigkeit zwischen 10 und 40 Prozentpunkten gegenüber dem Ausgangsmehl beträgt.
- Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass die Weizenmehle in der Rührwerkskugelmühle im Durchlauf vermahlen werden.
- Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass die Weizenmehle in der Rührwerkskugelmühle im Kreislauf vermahlen werden.
- Verfahren nach Anspruch 1 bis 4, dadurch gekennzeichnet, dass die Vermahlung bei einer Temperatur zwischen 30°C und 50°C durchgeführt wird.
- Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, dass die Weizenmehle in der Rührwerkskugelmühle batchweise vermahlen werden.
- Verfahren nach Anspruch 1 bis 5, dadurch gekennzeichnet, dass ein Kühlmittel direkt dem Rührwerkskugelmühleninhalt zugegeben wird.
- Verfahren nach Anspruch 1 bis 5, dadurch gekennzeichnet, dass die Rührwerkskugelmühle mit im Kreislauf geführten Mahlkugeln betrieben wird, die durch ein Kühlmittel gekühlt sind.
- Verfahren nach Anspruch 7 oder 8, dadurch gekennzeichnet, dass das Kühlmittel Luft, flüssiger Stickstoff oder flüssiges/festes Kohlendioxid ist.
- Verfahren nach Anspruch 1 bis 9, dadurch gekennzeichnet, dass die Rührwerkskugelmühle ein doppelwandiges wassergekühltes Gehäuse aufweist.
- Verfahren nach einem der Ansprüche 1 bis 10, dadurch gekennzeichnet, dass die Rührwerkskugelmühle Mahlperlen aus Aluminiumoxid oder Stahl beinhaltet.
- Verfahren nach Anspruch 11, dadurch gekennzeichnet, dass die Mahlkugeln einen Durchmesser kleiner als 7 mm, vorzugsweise 1 mm bis 5 mm, aufweisen.
- Verfahren nach Anspruch 1 bis 9, dadurch gekennzeichnet, dass es sich bei den Weizenmehlen um Mehle der Type 405 oder 550 handelt.
- Verfahren nach Anspruch 13, dadurch gekennzeichnet, dass das Weizenmehl eine Wasseraufnahmefähigkeit von mehr als 70% und einen Gehalt an beschädigter Stärke von mehr als 8% aufweist.
- Verfahren nach Anspruch 13 dadurch gekennzeichnet, dass das Weizenmehl eine Wasseraufnahmefähigkeit von mehr als 70% und eine Teigstabilität von mehr als 1,3 min aufweist.
- Verfahren nach Anspruch 13 , dadurch gekennzeichnet, dass das Weizenmehl eine Wasseraufnahmefähigkeit von mehr als 70% und eine Teigerweichung von weniger als 130 Brabender-Farinogrammeinheiten aufweist.
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 (de) | 2002-08-21 |
EP1232793A3 EP1232793A3 (de) | 2003-05-07 |
EP1232793B1 true EP1232793B1 (de) | 2005-04-06 |
Family
ID=7674690
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP02000504A Expired - Lifetime EP1232793B1 (de) | 2001-02-16 | 2002-01-09 | Weizenmehle mit erhöhter Wasseraufnahmefähigkeit, sowie Verfahren und Vorrichtung zu deren Herstellung |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1232793B1 (de) |
AT (1) | ATE292521T1 (de) |
DE (2) | DE10107885A1 (de) |
DK (1) | DK1232793T3 (de) |
Families Citing this family (2)
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)
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 (de) * | 1969-10-30 | 1972-03-08 | ||
DE2622748C2 (de) | 1976-05-21 | 1980-01-24 | Muehle Rueningen Ag, 3300 Braunschweig | Behandlung von getreidemehl oder getreidekorn |
EP0771591A4 (de) * | 1995-06-06 | 2000-05-31 | Kotobuki Giken Kogyo Kk | Nassrührwerkskugelmühle und verfahren |
PT919294E (pt) | 1997-11-27 | 2000-09-29 | Codrico Bv | Metodo para o enriquecimento em proteina de vegetais em grao em particular de cereais e leguminosas |
-
2001
- 2001-02-16 DE DE10107885A patent/DE10107885A1/de not_active Withdrawn
-
2002
- 2002-01-09 AT AT02000504T patent/ATE292521T1/de not_active IP Right Cessation
- 2002-01-09 DK DK02000504T patent/DK1232793T3/da active
- 2002-01-09 DE DE50202675T patent/DE50202675D1/de not_active Expired - Lifetime
- 2002-01-09 EP EP02000504A patent/EP1232793B1/de not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DE50202675D1 (de) | 2005-05-12 |
EP1232793A2 (de) | 2002-08-21 |
DK1232793T3 (da) | 2005-08-22 |
EP1232793A3 (de) | 2003-05-07 |
ATE292521T1 (de) | 2005-04-15 |
DE10107885A1 (de) | 2002-09-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0335925B1 (de) | Verfahren zur herstellung von getreidemahlprodukten und getreidemühlenanlage | |
EP2313199B1 (de) | Vorrichtung und verfahren zur herstellung von mehl und/oder griess | |
EP0016442B1 (de) | Verfahren und Vorrichtung zur Herstellung von Paniermehl sowie ein Paniermehl | |
DE69934234T2 (de) | Verfahren zur herstellung von masa-mehle | |
DE2442552C3 (de) | Verfahren zur Verbesserung der Backeigenschaften von Weizen | |
EP0662864A1 (de) | Verfahren und vorrichtung zum scheuern und mahlvorbereiten von getreide | |
WO1994003274A1 (de) | Verfahren und vorrichtung zum kontinuierlichen netzen von getreide sowie verwendung der netzvorrichtung | |
DE2454236A1 (de) | Verfahren zur gewinnung von staerke, lebenswichtigem gluten und einer naehrenden mischung aus kleie, keimen und fasern | |
EP0544846B1 (de) | Verfahren zur herstellung eines knöllchenförmigen produktes | |
EP1232793B1 (de) | Weizenmehle mit erhöhter Wasseraufnahmefähigkeit, sowie Verfahren und Vorrichtung zu deren Herstellung | |
CH620708A5 (de) | ||
EP3009191A1 (de) | Verwendung von mit einem verfahren zur mahlvorbereitung von getreide erhaltenen nahrungsfasern | |
DE4494352C2 (de) | Verfahren zur Herstellung eines Halbfertigprodukts, insbesondere eines Vollkornteiges, aus Getreide für Nahrungsmittel und dergleichen | |
CH672441A5 (de) | ||
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 (de) | Ei-ersatzstoff | |
DD282861A5 (de) | Verfahren und Getreidemühle zur Herstellung von Getreidemahlprodukten | |
EP1787531B1 (de) | Verfahren zur Herstellung von Rohteig für Teigwaren | |
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 |
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 |