EP2269739A1 - Procédé de préparation de broyage de céréales - Google Patents

Procédé de préparation de broyage de céréales Download PDF

Info

Publication number: EP2269739A1
Authority: EP; European Patent Office
Prior art keywords: grain; weight; cereal; fraction; conditioning
Prior art date: 2009-07-01
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

EP09164321A

Other languages

German (de)

English (en)

Other versions

EP2269739B1 (fr

Inventor

Walter Eugster

Jürgen Winter

Uwe Schill

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.)

Buehler AG

Original Assignee

Buehler 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.)

2009-07-01

Filing date

2009-07-01

Publication date

2011-01-05

2009-07-01 Application filed by Buehler AG filed Critical Buehler AG

2009-07-01 Priority to EP09164321.3A priority Critical patent/EP2269739B1/fr

2009-07-01 Priority to EP15194089.7A priority patent/EP3009191A1/fr

2009-07-01 Priority to ES09164321.3T priority patent/ES2563042T3/es

2011-01-05 Publication of EP2269739A1 publication Critical patent/EP2269739A1/fr

2015-12-16 Application granted granted Critical

2015-12-16 Publication of EP2269739B1 publication Critical patent/EP2269739B1/fr

Status Not-in-force legal-status Critical Current

2029-07-01 Anticipated expiration legal-status Critical

Images

Classifications

- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02B—PREPARING GRAIN FOR MILLING; REFINING GRANULAR FRUIT TO COMMERCIAL PRODUCTS BY WORKING THE SURFACE
- B02B1/00—Preparing grain for milling or like processes
- B02B1/04—Wet treatment, e.g. washing, wetting, softening
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02B—PREPARING GRAIN FOR MILLING; REFINING GRANULAR FRUIT TO COMMERCIAL PRODUCTS BY WORKING THE SURFACE
- B02B3/00—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02B—PREPARING GRAIN FOR MILLING; REFINING GRANULAR FRUIT TO COMMERCIAL PRODUCTS BY WORKING THE SURFACE
- B02B3/00—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming
- B02B3/04—Hulling; Husking; Decorticating; Polishing; Removing the awns; Degerming by means of rollers
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02B—PREPARING GRAIN FOR MILLING; REFINING GRANULAR FRUIT TO COMMERCIAL PRODUCTS BY WORKING THE SURFACE
- B02B5/00—Grain treatment not otherwise provided for
- B02B5/02—Combined processes

Definitions

the invention relates to the field of milling, in particular the Mahlvor admirability of cereals.
the grain has, simplified, a triple shell structure.
the outer shell layer comprises the epidermis, longitudinal and transverse cells as well as tubular cells. This outer shell layer can make up to 5.5% by weight of the whole grain.
the next inner layer is a double layer of a so-called dye layer and a colorless layer; for this double layer, a proportion of about 2.5% by weight of the whole grain is assumed.
the next inner layer is called the aleurone layer and comprises about 7% by weight of the whole grain. In the interior of the grain is to find the germ (about 2.5 wt.% Of the total grain), as well as the actual meal body, which accounts for the rest to 100 autonomousgew.%.
DE 1 164 210 proposes a multi-stage process in which already in a first step, the shell components are replaced in an amount of 2.8 to 3.6 wt.% Of the cereal grain. In a second step another 0.4 to 2.1% by weight of the cereal grain is replaced. In total, between 3.2 and 5.7% by weight of the cereal grain are replaced cumulatively in this process.
the invention has for its object to provide a method by which both contaminated outermost layers of the grain can be reliably removed as well as the grain as much as possible can be added to a value-added use.
the method should also be as simple, efficient and inexpensive feasible.
step c) only the surface layer is removed to such an extent that contaminations such as environmental toxins and / or other impurities are removed. Surprisingly, it has been shown that for this purpose the removal of only 0.2 to 0.5% by weight is completely sufficient in order to obtain largely contamination-free cereal grains.
step e) another layer is removed which is then substantially free of contaminants and which substantially contains dietary fiber of the crop. The thus obtained, contamination-free dietary fibers can be supplied as value components of a further use.
dietary fibers are understood as meaning the total dietary fibers, determined in accordance with AOAC 985.29.
step a) The provision of grain in step a) can take place with so-called “storage moisture” or "ground moisture”.
grinding moisture is carried out with a moisture content of ⁇ 14% by weight, preferably 14 to 20% by weight, more preferably 15 to 20% by weight, particularly preferably 15 to 17% by weight, this moisture being as substantially homogeneous as possible Cereal grain is distributed, as it is optimal for the milling process.
the provision of "storage moisture” is preferably carried out with a moisture content of ⁇ 14% by weight, preferably 8 to 13.99% by weight, particularly preferably 10 to ⁇ 13.99% by weight.
the meshing of the grain in steps b) and d) can be done with very little water.
grain with the o.g. "Storage moisture” is provided, it is typically added between 0.1 to 4 wt.%, Preferably 0.2 to 2.5 wt.%, Water (based on the resulting total weight).
the conditioning in steps b) and d) can take place directly during the meshing of the grain, for example in a vortexer. However, the conditioning can also take place only partially directly during meshing (for example, in a screw conveyor, is fed into the water), in which case then a separate conditioning of the strained cereal takes place (eg. In a screw conveyor, in which no additional water is fed more ).
step b) during a period of ⁇ 1 hour, preferably for ⁇ 10 minutes, more preferably for about 5 seconds to 5 minutes, more preferably about 8 seconds to 30 seconds. This meshing is preferably done in a vortexer.
step d) it is wetted and conditioned for about 0.5 to 30 minutes, preferably 0.5 to 15 minutes, more preferably between 1 and 5 minutes.
This network is preferably carried out in a network and residence screw conveyor.
step c) While in step c) only just as much surface layer of the grain is removed that a substantially contamination-free residual grain is obtained in step e) a fraction with the highest possible dietary fiber content is obtained, the flour body should not be damaged as possible.
the proportion of the second fraction obtained in step e) in% by weight of the total grain may vary depending on the type of cereal and the contaminated layer removed in step c). However, proper control of the process can be readily determined by routine experimentation; For this purpose, the content of total food fibers of the second fraction and the content of starch (as an indication of damage to the endosperm) can be used (individually or in combination).
the second fraction removed in step e) has a total dietary fiber content of ⁇ 60% by weight, preferably ⁇ 70% by weight, particularly preferably ⁇ 80% by weight.
the second fraction removed in step e) has a starch content of ⁇ 20% by weight, preferably ⁇ 15% by weight, more preferably ⁇ 10% by weight.
starch The content of starch is determined in the context of the invention according to the Swiss Food Book SLMB (2002), chapter 3.6.1.
step e) is carried out in several substeps e 1 ) to e n ).
the fractions obtained in such sub-steps may in particular contain varying amounts of cereal (in% by weight of the total weight of the cereal used). In this way, a particularly fine approach to a maximally uncovered meal body can be achieved; In particular, the isolated fraction can be chosen the smaller, the more dietary fibers have already been removed.
the fractions or partial amounts thereof obtained in substeps e 1 ) to e n ) can be mixed with one another such that the mixture has a total dietary fiber content of ⁇ 60% by weight, preferably ⁇ 70% by weight, particularly preferably ⁇ 80 wt.%.
the first partial fractions typically have a total dietary fiber content of> 80% by weight, in particular> 85% by weight. Later partial fractions can - despite the lower content of total dietary fiber - also be isolated and mixed with the former partial fractions, if this does not fall below a desired content of total food fibers (or a maximum tolerated content of starch, see below, not exceeded).
the fractions or partial amounts thereof obtained in substeps e 1 ) to e n ) may be mixed with one another such that the mixture has a starch content of ⁇ 20% by weight, preferably ⁇ 15% by weight, more preferably ⁇ 10 wt.%.
the first partial fractions typically have a starch content of ⁇ 6% by weight, in particular of ⁇ 5% by weight. Later sub-fractions can - despite higher content of starch - also still isolated and mixed with the former sub-fractions, provided that this maximum tolerated starch content is not exceeded (or a desired content of total food fibers is not exceeded).
the meshing and conditioning takes place in steps b) and d) and, if appropriate, between substeps e 1 ) to e n ) with a swirling network or with a network and residence-screw conveyor.
a vortex setter has surprisingly been found to be particularly suitable for use in step b), whereas the net and indwelling screw conveyor has proved to be particularly effective in step d) and optionally between sub-steps e 1 ) to e n );
the sequential use of a net screw conveyor (with added water) and a subsequent residence screw conveyor (without addition of water) has proven to be particularly advantageous.
peeling is particularly advantageously achievable essentially by grain / grain friction, as already explained above in connection with the method according to the invention.
stator planar segments As processing tools can be provided on the stator planar segments; But these segments can also be equipped with baffles, cams o. The like.
knobs o As editing tools on the rotor projecting strips, knobs o. The like. Be provided.
the baskets can be adapted to the specific application (in particular to the respective type of grain) with expert routine tests, in particular in their hole dimensions.
a further aspect of the invention relates to the use of dietary fibers obtained by a method described above, in particular with a plant described above, as an additive in foods, in particular baked goods, preferably breads; cereals; Snacks, in particular bars; Beverages; Dairy products, in particular yoghurt; Food supplements; Diet food.
substantially contamination-free dietary fibers can be obtained in a particularly simple and high yield, which can thus be supplied to a further use.
the resulting, treated (freed from an outer layer of the shell components) grain material can also be further processed.
Fig. 1 In the flowchart in Fig. 1
grain from a stand-off cell (not shown) is fed to the process with a defined moisture content.
the grain first passes through a magnet 1 for sorting out metallic parts.
the grain is fed to a Wirbeletzer 2, which has a water supply 3 for meshing the grain.
the vibrator 2 is in the Bescheibung to Fig. 6 explained in more detail.
the corn is fed to a first device for peeling surface treatment of the grain, namely a so-called light peeler 4; this is related to Fig. 2 and Fig. 3 explained in more detail.
a peeler 12 can also be used; this is related to Fig. 4 and 5 explained in more detail.
the fiber fraction leaving the Light Peeler 4 (or Peeler 12) can be recycled (not shown).
the grain fraction is passed through an aspiration channel 5.
the grain is then fed to a depot 6, in which it can be stored temporarily to compensate for different capacities of the individual process stages.
a balance 7 can be ensured that the subsequent process stages defined amounts of grain are supplied, which is essential in particular for the subsequent network.
a net screw conveyor 8 the grain is wetted and promoted at the same time; the net screw conveyor 8 is fed via a water supply 9 with water.
the strained grain is then conditioned in an indwelling screw conveyor 10.
the construction of auger conveyor 8 and indwelling screw conveyor 10 is identical except for the water supply and is associated with Fig. 7 explained in more detail.
the strained grain is in turn passed to a magnet 11 to sort out any metallic contaminants.
the grain is fed to a second apparatus for peeling surface treatment of the grain, here a peeler 12; this is related to Fig. 4 and Fig. 5 explained in more detail.
a light peeler 4 can alternatively be used if a gentler treatment with less removal of shell material is desired.
the fiber fraction leaving the peeler 12 can be sent for further use (not shown).
the grain passes through another aspiration channel 13 and another magnet 14 and is then fed to the grinding process.
the Light Peeler 4 is shown in more detail.
the grain is supplied to the light peeler 4 via a product inlet 15 and reaches a feed screw 20.
the light peeler 4 has a stator 19 and a rotor 25. Between rotor 25 and stator 19 and screen plates 27 (FIG. Fig. 3 ), a treatment room 18 for the cereal is formed.
the distance between rotor 25 and stator 19 can be reduced above and below by underlaying the segments 41, in order to achieve a more intensive treatment of the process material.
the distance of the screen plates 27 to the rotor 25 can also be adjusted; a greater distance is accompanied by a gentler treatment of the process material.
the rotor 25 has a hollow shaft 26 which is driven by a motor 23.
the hollow shaft has air openings 24, via which air is supplied into the treatment chamber 18 can.
the treatment intensity in the treatment chamber 18 can be regulated by adjusting the back pressure of the grain in the Light Peeler 4. Via the outlet 16, the fiber fraction leaves the light peeler 4; the treated grain leaves the Light Peeler 4 via the outlet 17.
the Peeler 12 is shown in more detail. Parts having substantially the same function are designated by the same reference numerals as in the light peeler 4.
the cereal is supplied to the peeler 12 via a product inlet 15 and reaches a feed screw 20.
the peeler 12 has a stator 19 and a rotor 25. Between rotor 25 and stator 19 and screen plates 27 (FIG. Fig. 5 ), a treatment room 18 for the cereal is formed.
the distance between rotor 25 and stator 19 can be reduced above and below by underlaying the segments 41, in order to achieve a more intensive treatment of the process material.
the distance of the screen plates 27 to the rotor 25 can also be adjusted; a greater distance is accompanied by a gentler treatment of the process material.
the rotor 25 has a hollow shaft 26 which is driven by a motor 23.
the hollow shaft has air openings 24, via which air can be supplied by means of a fan 28 in the treatment chamber 18, whereby the separation of the shell fraction can be facilitated and completed.
the narrower in the Pealer 12 compared to the Light Peeler 4 treatment room 18 intensifies the treatment of the grain (see. Fig. 3 ).
the treatment intensity in the treatment space 18 can be regulated by adjusting the back pressure of the grain in the peeler 12. Via the outlet 16, the fiber fraction leaves the peeler 12; the treated grain leaves the peeler 12 via the outlet 17.
Fig. 6 the vertebrae setter 2 is shown in detail.
the cereal is fed to the vortexer 2 via the product inlet 34 and passed through the vortexer in a helical direction (indicated by the arrow line in the interior of the vortexer 2).
About a not shown in detail water inlet 2 water is metered supplied to the interior of the vortex network.
an upper shaft 30 and a lower shaft 31 are arranged; Paddles 32 and 33 are provided on these rotating shafts in such a geometry and arrangement as to achieve the above described helical conveying movement.
the shafts 30 and 31 are driven by a common motor 29.
the strained corn leaves the vortex network via the product outlet 35.
an indwelling screw conveyor 10 is shown in detail.
the grain is fed to the indwelling screw conveyor via a product inlet 36.
a shaft 38 is arranged, on which paddle 40 provided in such a geometry and arrangement that a conveying movement is achieved.
the grain exits the indwelling screw conveyor via the product outlet 37.
the shaft 38 is driven by the motor 39.
a net screw conveyor not shown in detail may be designed in an analogous manner, with only one water supply being provided preferably in the front part of the interior in the direction of product flow.
the netting was carried out with a Wirbeletzer 2.
the surface treatments were carried out with a Peeler 12 (MHXM-W, Bühler AG).
the Peeler 12 was always operated with the following settings: Performance product receipt: 3t / h Speed of the rotor: 335U / min Screen size: 1.1mm x 12mm Distance rotor to segment 41: 13mm Distance rotor to sieve: 8mm

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Cereal-Derived Products (AREA)

EP09164321.3A 2009-07-01 2009-07-01 Procédé de préparation de broyage de céréales Not-in-force EP2269739B1 (fr)

Priority Applications (3)

Application Number	Priority Date	Filing Date	Title
EP09164321.3A EP2269739B1 (fr)	2009-07-01	2009-07-01	Procédé de préparation de broyage de céréales
EP15194089.7A EP3009191A1 (fr)	2009-07-01	2009-07-01	Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales
ES09164321.3T ES2563042T3 (es)	2009-07-01	2009-07-01	Procedimiento para el tratamiento previo para la trituración de cereales

Applications Claiming Priority (1)

Application Number	Priority Date	Filing Date	Title
EP09164321.3A EP2269739B1 (fr)	2009-07-01	2009-07-01	Procédé de préparation de broyage de céréales

Related Child Applications (2)

Application Number	Title	Priority Date	Filing Date
EP15194089.7A Division EP3009191A1 (fr)	2009-07-01	2009-07-01	Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales
EP15194089.7A Division-Into EP3009191A1 (fr)	2009-07-01	2009-07-01	Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales

Publications (2)

Publication Number	Publication Date
EP2269739A1 true EP2269739A1 (fr)	2011-01-05
EP2269739B1 EP2269739B1 (fr)	2015-12-16

Family

ID=41353929

Family Applications (2)

Application Number	Title	Priority Date	Filing Date
EP15194089.7A Withdrawn EP3009191A1 (fr)	2009-07-01	2009-07-01	Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales
EP09164321.3A Not-in-force EP2269739B1 (fr)	2009-07-01	2009-07-01	Procédé de préparation de broyage de céréales

Family Applications Before (1)

Application Number	Title	Priority Date	Filing Date
EP15194089.7A Withdrawn EP3009191A1 (fr)	2009-07-01	2009-07-01	Utilisation de fibres nutritives obtenues lors d'un procede de preparation de broyage de cereales

Country Status (2)

Country	Link
EP (2)	EP3009191A1 (fr)
ES (1)	ES2563042T3 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
ITBO20120025A1 (it) *	2012-01-20	2013-07-21	Molini Pivetti Societa Per Azioni	Impianto e procedimento di decorticazione per l'estrazione di aleurone e prodotto farinaceo ottenuto da tale procedimento.
US8800897B2 (en)	2010-04-15	2014-08-12	Bühler AG	Process and device for producing flour
CN113262834A (zh) *	2021-05-28	2021-08-17	王倪虎	一种大米加工工艺
CN114471802A (zh) *	2022-02-16	2022-05-13	山西农业大学玉米研究所(山西省农业科学院玉米研究所)	一种基于智能自动化的藜麦高效去壳装置及方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
DE1164210B (de)	1959-01-05	1964-02-27	Theodore Earle	Verfahren zum Entfernen der Epidermis-Schicht von Getreidekoernern
DD123159A2 (fr) *	1975-12-19	1976-12-05
DE2952049A1 (de) *	1979-01-04	1980-07-17	Fortschritt Veb K	Universelles verfahren, vorzugsweise zum netzen von brotgetreide und huelsenfruechten
GB2268386A (en) *	1992-07-11	1994-01-12	Satake	A process for treating cereal grain prior to milling
EP0801984B1 (fr)	1993-08-10	2000-05-03	Bühler Ag	Procédé et appareil pour la préparation de céréales en vue de leur mouture
WO2004060564A1 (fr) *	2003-01-02	2004-07-22	Bühler AG	Procede et equipement pour monder des cereales

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
JPH09313955A (ja) *	1996-05-31	1997-12-09	Satake Eng Co Ltd	製粉前処理方法

2009
- 2009-07-01 ES ES09164321.3T patent/ES2563042T3/es active Active
- 2009-07-01 EP EP15194089.7A patent/EP3009191A1/fr not_active Withdrawn
- 2009-07-01 EP EP09164321.3A patent/EP2269739B1/fr not_active Not-in-force

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
DE1164210B (de)	1959-01-05	1964-02-27	Theodore Earle	Verfahren zum Entfernen der Epidermis-Schicht von Getreidekoernern
DD123159A2 (fr) *	1975-12-19	1976-12-05
DE2952049A1 (de) *	1979-01-04	1980-07-17	Fortschritt Veb K	Universelles verfahren, vorzugsweise zum netzen von brotgetreide und huelsenfruechten
GB2268386A (en) *	1992-07-11	1994-01-12	Satake	A process for treating cereal grain prior to milling
EP0801984B1 (fr)	1993-08-10	2000-05-03	Bühler Ag	Procédé et appareil pour la préparation de céréales en vue de leur mouture
WO2004060564A1 (fr) *	2003-01-02	2004-07-22	Bühler AG	Procede et equipement pour monder des cereales

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number	Priority date	Publication date	Assignee	Title
US8800897B2 (en)	2010-04-15	2014-08-12	Bühler AG	Process and device for producing flour
ITBO20120025A1 (it) *	2012-01-20	2013-07-21	Molini Pivetti Societa Per Azioni	Impianto e procedimento di decorticazione per l'estrazione di aleurone e prodotto farinaceo ottenuto da tale procedimento.
CN113262834A (zh) *	2021-05-28	2021-08-17	王倪虎	一种大米加工工艺
CN114471802A (zh) *	2022-02-16	2022-05-13	山西农业大学玉米研究所(山西省农业科学院玉米研究所)	一种基于智能自动化的藜麦高效去壳装置及方法
CN114471802B (zh) *	2022-02-16	2022-09-06	山西农业大学玉米研究所(山西省农业科学院玉米研究所)	一种基于智能自动化的藜麦高效去壳装置及方法

Also Published As

Publication number	Publication date
ES2563042T3 (es)	2016-03-10
EP3009191A1 (fr)	2016-04-20
EP2269739B1 (fr)	2015-12-16

Publication	Publication Date	Title
DE4345422C2 (de)	2002-09-12	Verfahren und Vorrichtung zum Scheuern von Getreide
EP0334919B1 (fr)	1993-09-15	Moulin a cylindres de fabrication de produits de ble moulu
DE69215455T3 (de)	2003-11-20	Verfahren und Anlage zum Mahlen von Mehl
DE3650406T3 (de)	2001-08-23	Anlage zur Vorbereitung der Vermahlung von Weizen sowie Verfahren und Anlage zur Weizenvermahlung.
DD299518A5 (de)	1992-04-23	Verfahren und anlage fuer die behandlung von weizenkoernern
DE69708717T2 (de)	2002-05-08	Verfahren zur Vorbehandlung von Weizenkörnern zum Mahlen von Mehl
DE68922934T2 (de)	1995-10-19	Verfahren und Vorrichtung zum Mahlen von Weizen.
DE69417669T2 (de)	1999-09-02	Vertikale Poliermaschinen und Vorrichtung zur Vorbehandlung zum Mahlen von Mehl die solche Poliermaschinen verwendet
EP0327610B1 (fr)	1991-09-25	Dispositif permettant l'epluchage et l'egrenage des grains de mais
DE1211901B (de)	1966-03-03	Verfahren und Vorrichtung zur Vermahlung von Getreide und aehnlichen Koernerfruechten
DE69611034T2 (de)	2001-03-22	Verfahren und Vorrichtung zur Herstellung von extrudierten und gekochten Nahrungsmitteln
EP2269739B1 (fr)	2015-12-16	Procédé de préparation de broyage de céréales
EP0598022A1 (fr)	1994-05-25	Procede pour l'impregnation de grains avec un liquide, ainsi que dispositif pour la realisation du procede et application du procede.
CH640750A5 (en)	1984-01-31	Method for preparing and roller-milling cereal, and device for carrying out the method
CH624020A5 (fr)	1981-07-15
DE2642628B2 (de)	1979-08-30	Verfahren zur Herstellung von Stärke und Gluten aus Weizen, Roggen oder Gerste, und Mühle zum Ausüben des Verfahrens
DE19743470A1 (de)	1999-04-08	Verfahren und Vorrichtung zum Vorkonditionieren des in einem Extruder zu verarbeitenden Produktes und dgl.
CH672441A5 (fr)	1989-11-30
EP1578534A1 (fr)	2005-09-28	Procede et equipement pour monder des cereales
DE60119265T2 (de)	2007-02-22	Verfahren zur Vermahlung von Mais
DE19733424C2 (de)	2001-05-17	Verfahren zum Vermahlen von Körnerfrüchten
DE577125C (de)	1933-05-27	Verfahren zum Reinigen, Schaelen und Aufschliessen von Brotgetreide
DE2628199C3 (de)	1979-03-29	Verfahren zur Gewinnung von Kleie, Keimsubstanz und Endosperm aus ganzen Weizenkörnern
DD282861A5 (de)	1990-09-26	Verfahren und Getreidemühle zur Herstellung von Getreidemahlprodukten
DE19758096A1 (de)	1999-07-01	Verfahren und Vorrichtung zur Bearbeitung von Korn

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