Patent Grant
9067213
The present invention relates to the field of the production of flour and/or semolina from grain, having the features of the preambles of the independent claims.
A method and an apparatus for producing ground grain products, such as, for example, flour, semolina or middlings, according to the principle of advanced milling is disclosed by EP 0 335 925 B1. Here, the ground product is repeatedly ground, preferably twelve to twenty times, between rollers and is repeatedly sieved. In this case, the ground product is directed at least twice via double roller grinding stages without sieving between the individual stages of the double grinding and is sieved in each case following the double grinding.
These previously known apparatuses and methods have in this case the disadvantage that the material to be ground is greatly heated in the grinding arrangements during the grinding operation. This is especially disadvantageous when grinding grain into flour, since the proteins present in the grain are changed or damaged by the heat introduced into the grain. In particular, gluten is changed by the introduced heat, since gluten is thermolabile. Since gluten has a very great effect on the quality of a loaf of bread baked with the flour, changes in the gluten due to the grinding process lead to changes in the bread quality, which have to be compensated for, for example in a bakery, during the process of producing a loaf of bread from the flour produced.
A further disadvantage of the previously known method and of the apparatus for producing flour from grain is the need to use a plurality of sequential grinders for the flour production, since said grinders are costly and the operation thereof requires large amounts of energy. In addition, the use of a plurality of grinders means that large buildings are required for the mill, which further increases the costs for setting up a mill.
In addition, the previously known method and the apparatus have the disadvantage that the power required for producing flour and/or semolina from grain is considerable. For example, in the prior art, at least 25 to 27 kWh/t or even more than 33 kWh/t is required for producing flour of common fineness, i.e. common particle size.
DE 27 08 053 discloses a method for the fine and very fine comminution of ores by means of a material bed roller mill, this comminution being effected under high compressive stress, but in a limited manner for protecting from excessive compressive stresses and pressure peaks.
One object of the present invention is therefore to avoid the disadvantages of the known prior art, that is to say in particular to provide an apparatus and a method with which flour can be produced from grain with a lower input of heat during the grinding operation. Another object of the present invention is to provide an apparatus and a method with which flour can be produced from grain cost-effectively and in a favorable manner in terms of energy.
These objects are achieved by an apparatus and a method according to the characterizing part of the independent claims.
The apparatus according to the invention relates to a grinding arrangement for producing flour from grain, said grain being in particular bread wheat, durum wheat, maize or buckwheat. The grinding arrangement is characterized by at least one grinder which is designed in particular as a material bed roller mill. The grinder has at least one feed opening and at least one delivery opening. The grinding arrangement comprises at least one separating stage for separating ground products into finer ground product and coarser ground product and a return arrangement for returning at least some of the coarser ground product into the feed opening of the grinder.
Bread wheat is also referred to as Triticum aevastivum and durum wheat as Triticum durum.
Within the scope of the invention, rice is also regarded as grain.
Roller mills usually have two rollers which rotate at different speeds and between which a roller gap and thus a grinding force can be set, grain, for example, being transported through said roller gap and thus being ground. The degree of grinding, i.e. the particle size of the ground product to be achieved, is determined in particular by the size of the roller gap. The roller gap remains constant during the grinding operation. A grain to be ground is fed into this roller mill. In order to be able to grind grain using such a roller mill, the roller gap has to be set to the particle size of the grain. During such grinding, a considerable amount of heat is introduced into the grain by the mechanical grinding process and the pressure in the roller gap, in particular at small roller gap widths, and therefore the grain is heated to a considerable extent. Since the grain is fed into the roller mill, i.e. in particular as individual particles, the throughput in the case of a small roller gap, that is to say in particular in the final so-called fine grinding stages, is very small.
A material bed roller mill within the scope of the present application refers to a force-controlled roller mill. For example, mechanically preloaded springs or hydraulically coupled gas accumulators are used for generating force. A pressure is exerted on the rollers in the direction of the roller gap, such that a roller gap is set between these rollers as a function of the quantity and the type of grain to be ground in the roller gap and as a function of the set pressure. For example, a gap of about 0.5% to 2% of a roller diameter can be set. The resulting grinding gap is thus obtained when the grain is being drawn in, which in particular is dependent upon friction, by the rollers. In the process, some of the particles can be larger than the gap. Typically, however, the particles are smaller than the resulting gap. A material bed is produced in the draw-in region between the rollers when the material bed roller mill can draw in the grain from a surplus thereof, e.g. by means of a filled material shaft or funnel. The material bed comminution is based on a packed particle fill in the grinding gap. The setting of the grinding force serves to control the input of energy at the mill. The input of energy determines, depending on material and grain size, the production of finer ground product in the material and is to be set to an optimum range.
In particular, the throughput through a material bed roller mill is dependent, for example, upon the rotary speed of the rollers. A higher rotary speed generally leads to a higher throughput. For example, peripheral speeds of the rollers, i.e. the speed at the surface which is in engagement with the grain during the grinding operation, can be within the range of 1 m/s to 1.5 m/s, in particular less than 1 m/s and most particularly less than 0.1 m/s. Smaller peripheral speeds are generally set for finer ground products.
If the drawing-in of grain into the material bed roller mill is insufficient, for example on account of a lack of friction, such that fluidization phenomena occur, a compactor, e.g. a compactor screw, can be used, and this compactor conveys the grain into the roller gap, assisting the gravitational force for example.
The material bed roller mill is therefore characterized by a variable roller gap during the grinding, by setting of the pressure in the roller gap and by virtue of the fact that an increase in the grain volume in the roller gap leads to an increase in the roller gap.
The rollers of the material bed roller mill advantageously rotate at different speeds. This leads to intensified shearing of the grain in the roller gap and as a result to improved grinding into bran and semolina.
Within the scope of the application, bran also refers to a mixture of bran and husk parts of the grain.
A separating stage within the scope of the present invention means an apparatus for separating grain into various sizes, shapes or densities, wherein separation can take place either on the basis of one of these parameters or on the basis of any desired combination of these parameters. Separation can be effected, for example, first into various particle sizes of the ground grain. After that, for example, further separation into various densities of the particles of a size range is possible. For example, the ground grain can be separated in a first step into particles having particle sizes of 280 μm up to 560 μm and particles having a particle size of 560 μm up to 1120 μm. In a second stage, for example, the particles from the size range of 280 μm up to 560 μm can then be sorted according to the density and/or the shape of the particles, whereas the particles from the size range of 560 μm up to 1120 μm are ground a second time.
The expression that a ground product is separated into finer ground product and coarser ground product refers within the scope of the present application to relative separation according to particle sizes of the ground product. For example, during separation of a ground product into particles having particle sizes of 100 μm up to 200 μm and of 200 μm up to 300 μm, i.e. into two fractions, the ground product within the first size range is the finer ground product and the ground product within the second size range is the coarser ground product. Separation into two, three, four or even more fractions is also possible.
The grinding arrangement according to the invention has the advantage that the return of at least some of the coarser ground product into the feed opening of the grinder by means of the return arrangement leads to a reduction in the number or requisite grinders for achieving a defined degree of grinding, i.e. a particle size to be achieved, after the grinding operation, since the ground product is directed through the grinder again until the defined degree of grinding is achieved. This leads to a more cost-effective grinding arrangement compared with the prior art, since the number of grinders and the overall size of the entire grinding arrangement are reduced.
A further advantage of the grinding arrangement, in particular when using a material bed roller mill, is the selective grinding of the grain in the grinder, i.e. the bran is not ground to the same extent as the flour body, also called endosperm. In other words, the bran retains a larger particle size than the ground flour body, as a result of which said bran and said flour body can be more easily separated in a separating stage.
The returned ground product is mixed with grain that is not yet ground, for example before the grinding operation again in the grinder, such that a throughput of the mixture of grain and returned ground product in the grinder can be kept as constant as possible. This can be achieved, for example, by a regulating mechanism for the grain that is not yet ground.
A specific grinding force of the grinder can preferably be set in the grinding arrangement in such a way that grain is heated during the grinding operation by less than 30° C. relative to the temperature of the grain before the respective grinding. The grain is heated preferably by less than 15° C., particularly preferably by less than 10° C. and most particularly preferably by less than 5° C.
A specific grinding force S refers within the scope of the present application to the ratio of the pressure exerted in the direction of the grain, i.e. the contact force F, roller diameter D and the effective roller length L coming into engagement with the grain, according to the formula S=F/LD.
The adjustability of the specific grinding force of the grinder in such a way that the heating of the grain by the grinding operation is limited has the advantage that the change in or damage to the proteins, in particular the gluten in the grain, is reduced. This leads to enhanced reproducibility of properties of the flour produced according to the present invention. In special applications, for example, cooling of the rollers, of the grain or of the rollers and the grain can also be provided.
The specific grinding force is therefore advantageously set in such a way that the desired grinding result is achieved, i.e. production of a high proportion of finer ground product, without the grain being heated too strongly during the grinding operation. As a result, the energy consumed by the grinding plant is reduced compared with the prior art, since the grain is heated less strongly.
A grinding gap between two rollers of the grinder of the grinding arrangement is also preferably variable at a constant specific grinding force on the grain which can be introduced into the roller gap.
In this case, it is also possible to make the specific grinding force adjustable or controllable manually or by means of an open-loop or closed-loop control apparatus, e.g. as a function of the particle size, of the number of particles produced and of the heating of the grain.
The exertion of a constant specific grinding force on grain in the roller gap has the advantage that the grain is ground under constant conditions, i.e. with substantially constant input of heat into the grain by the grinding operation. This is achieved by the roller gap between the two rollers of the grinder being variable, such that, for example during an increase in the quantity of grain in the roller gap, the latter is increased and therefore the specific grinding force exerted on the grain remains constant. In the event of the quantity of grain in the roller gap being reduced, the roller gap is also reduced and the specific grinding force exerted on the grain remains constant.
However, it is also possible for the specific grinding force to increase in a defined manner when the roller gap is enlarged. This is achieved, for example when using a mechanically preloaded spring for generating force, by an increase in the roller gap leading to further extension of the spring and thus by an increased specific grinding force being set on account of the characteristic of the spring. Since the throughput through the roller gap is increased, with at the same time an increase in the specific grinding force, an input of energy per grain quantity remains approximately constant, such that the grinding conditions likewise remain constant here. If the roller gap is reduced, the specific grinding force correspondingly decreases, such that, here too, an input of energy per grain quantity remains approximately constant.
In a completely surprising manner, it has now been shown that, despite the protective grinding of the grain by limiting the input of heat into the grain compacted in the roller gap, the starch cores, i.e. the main constituent of the endosperm, are damaged. This damage can in particular be set, for example by setting the specific grinding force or also conditioning the grain.
The separating stage of the grinding arrangement is in particular preferably configured in such a way that grain having a density of less than 2 g/cm3 and in particular less than 1.5 g/cm3 can be separated into finer ground product and coarser ground product. In this case, the ground products have a density of less than 2 g/cm3 and in particular less than 1.5 g/cm3.
This has the advantage that the separating stage is adapted to the separation of grain into finer and coarser ground products and therefore better separation according to the density of the ground product is made possible. This is possible, for example, in separating stages which achieve the separation by means of air flows by the geometry of the separating stage and the air flow being adapted precisely to the density range of the material.
Furthermore, a specific grinding force of less than 3 N/mm2 is particularly preferably set in the grinding arrangement. This specific grinding force is preferably less than 2 N/mm2, particularly preferably between 1 N/mm2 and 2 N/mm2 and most particularly preferably less than 1 N/mm2.
This limiting of the specific grinding force has the advantage that the heat introduced into the grain by the grinding operation is further reduced, such that damage to or changes in the proteins, in particular gluten, are further reduced.
Furthermore, the separating stage of the grinding arrangement most particularly preferably comprises at least one apparatus from the list of the following apparatuses: zigzag sifter, semolina purifier, plan sifter, turbo sifter, distribution plate separator, crossflow separator. The separating stage comprises preferably two of these apparatuses, particularly preferably at least two of these apparatuses.
Zigzag sifters are known from the prior art, for example from GB 468 212 and DE 197 132 107 C2 or from the textbook “Prinzipien and neuere Verfahren der Windsichtung” [Principles and newer methods of air separation] by H. Rumpf and K. Leshonski (CIT 39 (1967) 21, 1261 ff.).
Semolina purifiers are known from the prior at, for example according to DE 612 639 C1, DE 34 10 573 A1 or the textbook “Maschinenkunde für Müller” [Machinery for millers] by A. W. Rohner (1986) and are obtainable, for example, from Bühler AG.
Plan sifters, which are designed as sieving apparatuses, are likewise known from the prior art, for example from the textbook “Maschinenkunde für Müller” [Machinery for millers] by A. W. Rohner (1986) and are obtainable, for example, from Bühler AG.
Turbo sifters are likewise known from the prior art, for example from the textbook “Handbuch der Verfarhrenstechnik” [Process engineering manual] by H. Schubert (Wiley-Verlag) and are offered, for example, by Hosokawa Alpine AG, Augsburg, in the Turboplex or Statoplex ranges.
This construction of the separating stage comprising at least one of the apparatuses described above has the advantage that, for the respective separation according to particle size, particle shape or density, the respectively suitable apparatus, i.e. zigzag sifter, semolina purifier, plan sifter, turbo sifter, can be integrated into the separating stage. For example, for two-stage separation, separation can be carried out first according to particle size and after that according to the density of the particles. A plan sifter, for example, is used for the first separating stage and a zigzag sifter or a semolina purifier, for example, is used for the second separating stage. In this case, the grain is first separated into finer and coarser ground products using the plan sifter and, for example, the finer ground product is thereupon separated into constituents of different densities by means of a zigzag sifter, that is to say in particular into semolina and bran. It is also possible for the plan sifter to separate the grain into a plurality of fractions and for these fractions, that is to say the coarser ground product too, to then each be conveyed into a separate zigzag sifter in which said fractions are separated according to shape and/or density.
Semolina within the scope of the application means ground grain having a small proportion of bran, i.e. substantially pure semolina.
However, it is also possible in particular for a separating stage to comprise a plan sifter and two or at least two zigzag sifters arranged one after the other.
The grinding arrangement preferably has two grinders. In particular, the grinding arrangement has three grinders, particularly preferably four grinders and most particularly preferably at least four grinders.
This has the advantage that, for example, grinders of identical construction can be arranged sequentially one after the other, and the grinding force for the grinding result to be achieved can in each case be set individually in each grinder. Furthermore, for example, grinders of different types of construction, i.e. a material bed roller mill and a roller mill having a constant roller gap, can also be combined.
In particular, the grinding arrangement preferably has two separating stages. This grinding arrangement preferably has three separating stages, particularly preferably four separating stages and most particularly preferably at least four separating stages.
This has the advantage that, for example, if the grinding arrangement has a plurality of grinders, a separating stage can be arranged downstream of each of these grinders. Furthermore, it can be advantageous for two separating stages to be arranged sequentially and for each of these separating stages to carry out separation of the ground product according to different parameters.
Furthermore, a flow-based separating stage, in particular with air flows, is most particularly preferably designed as a partly circulating-air or circulating-air separating stage, in particular containing a zigzag sifter.
This has the advantage that at least some of the air which flows through the separating stage for separating the ground product, for example according to density, i.e. separation for example into semolina and bran, is returned into the separating stage again. This leads to a reduction in the energy consumed by the separating stage since, because inter alia, the air consumed by the separating stage is reduced as a result.
In a further preferred embodiment, the grinding arrangement comprises at least one separating stage for the separate discharge of bran from the finer ground product.
This has the advantage that the bran still located, for example, in the finer ground product is removed, which is especially advantageous for the production of white flour.
In an alternative preferred embodiment, the grinder has at least one roller type according to the following list: smooth rollers, fluted rollers, profiled rollers. Profiled rollers have, for example, a defined surface roughness.
This has the advantage that the grinder can be adapted to the grain to be ground in each case and to the grinding result to be achieved. Here, it is possible for the grinder to have two smooth rollers and two fluted rollers or else also a combination of smooth, profiled and fluted rollers.
A conditioning apparatus can preferably be connected upstream and/or downstream of at least one grinder of the grinding arrangement. With this conditioning apparatus, at least one of the following parameters of the grain can be set: temperature, moisture, particle size, proportion of bran.
This has the advantage that the grain is conditioned before and/or after the grinding in the grinder in such a way that an optimum grinding result can be achieved for the respective intended use. For example, the conditioning apparatus can be designed as a grist stage in which the grain is ground by a roller mill having a constant roller gap. In the process, a ground product of bran and endosperm is produced. In the conditioning stage, some of the bran can now be separated, for example in a first step, and therefore the proportion of bran in the grain is set. Due to the setting of the grinder in the grist stage, the particle size of the grain can also be set, said grain then being conveyed into the following grinder.
The conditioning apparatus can also contain, for example, a plan sifter for separating various particle sizes or also a portion of the bran. In addition, the conditioning apparatus can also contain a temperature-regulating device for heating or cooling the grain before the grinding operation and a device for setting the moisture of the grain.
The grinding plant preferably has at least one sensor for measuring the ash content, the moisture, the temperature and/or the particle size of the ground grain, in particular of the finer ground product and/or of the coarser ground product. However, it is also possible to measure the temperature and/or the moisture of the air flowing out of the separating stage, for example out of the zigzag sifter, by means of this sensor. This at least one sensor is preferably contained in the separating stage.
This has, inter alia, the advantage that the ash content or also the moisture content of the separated ground product, i.e. of the finer ground product and/or of the coarser ground product, can be measured, for example, after the separation in the separating stage. After that, the ground product can be conditioned, for example in a conditioning apparatus, to achieve an optimum moisture content for the grinding.
A further advantage is the measurement of the temperature and/or of the moisture of the air flowing out of the separating stage. On account of this measurement, the separating stage for example, in particular the zigzag sifter, can now be adjusted to optimum conditions, i.e. optimum flow conditions for optimum separation, in the separating stage.
This sensor is in particular a near-infrared spectrometer, i.e. an NIR spectrometer, and/or a color sensor. The color sensor is in particular suitable for measuring the ash content of the ground product. The NIR spectrometer is in particular suitable for measuring the moisture of the ground product and/or of the air.
A further aspect of the invention relates to a method for producing flour from grain, preferably from bread wheat, durum wheat, maize or buckwheat. This method is carried out in particular with a grinding arrangement as described above. In a first method step, the grain is ground in a grinder, this grinder being in particular a material bed roller mill. This grinder has at least one feed opening and at least one delivery opening. The grain is ground in particular with such a specific grinding force that the grain is heated during the grinding operation by less than 30° C. relative to the temperature of the grain before the respective grinding. The grain is preferably ground with such a specific grinding force that the grain is heated during the grinding operation by less than 15° C., particularly preferably by less than 10° C. and most particularly preferably by less than 5° C. relative to the temperature of the grain before the respective grinding. The grain is ground in particular preferably with a specific grinding force of less than 3 N/mm2, preferably less than 2 N/mm2, particularly preferably between 1 N/mm2 and 2 N/mm2 and most particularly preferably less than 1 N/mm2. In a further method step, the ground grain is conveyed into a separating stage by means of a conveying arrangement. In a further step, the ground grain is separated in the separating stage into finer ground product and coarser ground product. In particular, grain having a density of less than 2 g/cm3, in particular less than 1.5 g/cm3, is separated into finer ground product and coarser ground product, the ground products having a density of less than 2 g/cm3, in particular less than 1.5 g/cm3. In a next step, at least some of the coarser ground product is returned into the feed opening of the grinder by means of the return arrangement. Furthermore, finer ground product is discharged from the separating stage.
This method is preferably carried out with the apparatus described above and therefore has all the advantages of the apparatus that are described above.
Firstly, starch damage of the grain is preferably set by the selection of the specific grinding force during the grinding in the grinder. Secondly, the input of heat into the grain is limited by this corresponding setting of the specific grinding force.
The expression “starch damage” refers within the scope of the application to damage of the starch core in the endosperm, such that the latter, for example, can absorb water in a simpler manner or is also more easily accessible for enzymes.
This adjustability of the starch damage of the grain by selecting the specific grinding force has the advantage that the starch damage of the grain can be adapted to the respective market requirements. For example, high starch damage is required for bread making in Britain since high water absorption of the flour is required for bread making in Britain. In Asia, on the other hand, low starch damage is required, such that the flour absorbs less water, since many products in Asia are sold in the dry state and therefore, after the process for producing the product, the water repeatedly absorbed due to starch damage has to be removed again, which requires large amounts of energy and is therefore expensive.
Preferably, at least 90% of the grain is ground into finer ground product by means of two passes through the grinder. In particular, the grain is ground into finer ground product by means of three passes, more preferably by means of four passes and most preferably by means of at least four passes through the grinder.
This has the advantage that, when the proportion of 90% of finer ground product is achieved with few passes, the throughput through the grinding plant is increased, although a higher specific grinding force is necessary for this purpose. This leads to greater heating of the grain during the grinding and to higher starch damage of the grain. If the grinding plant is set in such a way that a plurality of passes through the grinder are necessary in order to achieve 90% finer ground product, the throughput through the same grinding plant is reduced, although the specific grinding force is lower for the same grain to be processed. As a result, lower starch damage of the grain and lower heating of the grain during the grinding operation are achieved.
In a method step, bran is most particularly preferably substantially separated from the vegetable ground product in the separating stage.
In particular, a further grinder is preferably connected downstream of the separating stage for the further grinding of the finer ground product.
This has the advantage that, after the separation of the finder ground product, said finer ground product can be ground in a separate grinder for producing, for example, special flours.
Furthermore, a further separating stage is preferably connected downstream of the first grinding stage for the further separation of the finer ground product.
This has the advantage that each separating stage can be set to the specific separation result. For example, the separating stages can have different degrees of separation sharpness with regard to the density of the particles to be separated.
Furthermore, a detacher is preferably connected downstream of at least one grinder for detaching the grain after the grinding in the grinder. This has the advantage that, with possible compression of the grain in the grinder, the ground product is detached into individual particles by the detacher and therefore separation into finer and coarser ground products in the separating stage is then made possible.
The detachers used in practice are preferably impact detachers. However, drum detachers, agitators or also attrition mills or friction mills are used.
At least one of the following parameters of the grain is most particularly preferably set in a conditioning apparatus before and/or after the grinding: temperature, moisture, particle size, proportion of bran.
In particular, the conditioning apparatus is designed as a grist stage.
An additional aspect of the present invention relates to a zigzag sifter which is suitable in particular for carrying out the method as described above. The zigzag sifter is configured in such a way that grain having a density of less than 2 g/cm2 and in particular less than 1.5 g/cm2 can be separated into finer ground product and coarser ground product. In this case, the ground products have a density of less than 2 g/cm2 and in particular less than 1.5 g/cm2.
These zigzag sifters are preferably used in the grinding arrangement described above and therefore have all the advantages of the zigzag sifter that are described above.
An additional alternative aspect of the invention relates to a material bed roller mill which is suitable in particular for carrying out the method as described above.
This material bed roller mill is preferably used in the grinding arrangement described above and therefore has all the advantages of the grinding arrangement that are described above.
Grain can preferably be ground into finer ground product and coarser ground product in the material bed roller mill. A specific grinding force is less than 3 N/mm2, preferably less than 2 N/mm2, particularly preferably between 1 N/mm2 and 2 N/mm2 and most particularly preferably less than 1 N/mm2.
A further aspect of the present invention relates to the use of a material bed roller mill for producing flour and/or semolina from grain, in particular from bread wheat, durum wheat, maize or buckwheat.
The material bed roller mill is characterized by a variable roller gap during the grinding, by setting of the pressure in the roller gap and by virtue of the fact that an increase in the grain volume in the roller gap leads to an increase in the roller gap.
A further alternative aspect of the invention relates to the use of a zigzag sifter for separating grain, preferably bread wheat, durum wheat, maize or buckwheat. The grain is separated into finer ground product and coarser ground product after a grinding operation in a grinder.
Grain having a density of less than 2 g/cm3, in particular less than 1.5 g/cm3, is preferably separated into finer ground product and coarser ground product. The ground products have a density of less than 2 g/cm3, in particular less than 1.5 g/cm3.
The zigzag sifter is particularly preferably used for separating bran from a finer ground product and/or coarser ground product.
The invention is explained in more detail below with reference to exemplary embodiments for better understanding.
The grinding arrangement has, as grinder, a material bed roller mill 16, as shown, for example, in
Grain 20 is transported through the feed opening 3 into the material bed roller mill 16, the grain 20 being ground in the material bed roller mill 16 into coarser ground product 21, finer ground product 22 and bran 23. To this end, a maximum specific grinding force of 1 N/mm2 is set in the material bed roller mill 16, as a result of which a typical roller gap of between 1.25 mm and 5 mm forms as a function the quantity of grain 20 fed. The ground product is transported via the delivery opening 4 and the conveying arrangement 9 and through the inlet opening 6 into the separating stage 5. In the separating stage 5, the ground product is sorted in a first step according to size into coarser ground product 21 and a mixture of finer ground product 22 and bran 23. The plan sifter 15 is used for this purpose. The coarser ground product 21 is transported through one of the outlet openings 7 into the return arrangement 8 and is returned to the grinder 2 for grinding again. The mixture of finer ground product 22 and bran 23 located in the separating stage 5 is separated into bran 23 and finer ground product 22 by means of a zigzag sifter. The finer ground product 22 is discharged via the lateral outlet opening 7 and the bran 23 is discharged via the top outlet opening 7.
Here, the material bed grinding mills have rollers having a roller diameter of 250 mm and a length of 44 mm. A force of 22 kN is exerted on the rollers. The grinding is effected at a specific grinding force of 2 N/mm2 with a roller gap of a thickness of 2 mm. Here, a flour yield in the ground product is 12.5%, approximately 5.3% of bran being separated with a zigzag sifter. The specific energy consumption at the mill is only 1.6 kWh/t; accordingly, about 12.8 kWh/t has to be consumed for the production of finished flour.
Here, the grain fed to the circuit has an ash content of 0.52%, the ash content of the flour produced being 0.47%.
In contrast to the grinding arrangement, the grinding arrangement 1 according to figure has a grinder 2 having two rollers 10 which are at a fixed distance s apart. The fixed distance s can be set and is adapted to the grain size and can be, for example, 1 mm.
Here, in contrast to the method described with respect to
In contrast to the grinding plant 1 according to
The method for grinding the grain 20 and for separating the ground product of coarser ground product 21, finer ground product 22 and bran 23 is otherwise effected substantially as described in
It is also possible for the grain to be cooled between the grinding stages or else for the rollers themselves to also be cooled. The combination of both cooling means is also possible.
This grinding plant substantially corresponds to the grinding plant according to
The further method for producing flour corresponds to the method already described with respect to
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2008 040 091 | Jul 2008 | DE | national |
| 10 2008 040 100 | Jul 2008 | DE | national |
| 10 2008 043 140 | Oct 2008 | DE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2009/058345 | 7/2/2009 | WO | 00 | 4/19/2011 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2010/000811 | 1/7/2010 | WO | A |
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| Number | Date | Country |
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| 118531 | Mar 1901 | DE |
| 612639 | Apr 1935 | DE |
| 1211901 | Mar 1966 | DE |
| 1270380 | Jun 1968 | DE |
| 1407846 | Apr 1969 | DE |
| 7606402 | Jun 1977 | DE |
| 2708053 | Sep 1978 | DE |
| 3410573 | Oct 1985 | DE |
| 4239602 | May 1994 | DE |
| 4320362 | Dec 1994 | DE |
| 4334904 | Apr 1995 | DE |
| 4414367 | Oct 1995 | DE |
| 19732107 | Feb 1999 | DE |
| 19757431 | Jun 1999 | DE |
| 19819614 | Nov 1999 | DE |
| 10338430 | Mar 2005 | DE |
| 102006054598 | May 2008 | DE |
| 0037066 | Oct 1981 | EP |
| 0273198 | Jul 1988 | EP |
| 0285921 | Oct 1988 | EP |
| 0335925 | Oct 1989 | EP |
| 0406591 | Jan 1991 | EP |
| 0433498 | Jun 1991 | EP |
| 468774 | Jan 1992 | EP |
| 0686065 | Dec 1995 | EP |
| 468212 | Jun 1937 | GB |
| 739562 | Nov 1955 | GB |
| 32-9364 | Nov 1957 | JP |
| 60-175556 | Sep 1985 | JP |
| 4-48500 | Jul 1988 | JP |
| 414172 | Feb 1992 | JP |
| 6205998 | Jul 1994 | JP |
| 7185383 | Jul 1995 | JP |
| 2710039 | Feb 1998 | JP |
| 1176841 | Mar 1999 | JP |
| 3126696 | Nov 2006 | JP |
| 2007-104962 | Apr 2007 | JP |
| 0132311 | May 2001 | WO |
| 2006108577 | Oct 2006 | WO |
| Entry |
|---|
| “Prinzipien und neuere Verfahren der Windsichtung” [Principles and newer methods of air separation] by H. Rumpf and K. Leshonski (CIT 39 (1967) 21, 1261 ff.), Elsevier B.V., (English abstract). |
| Number | Date | Country | |
|---|---|---|---|
| 20110186661 A1 | Aug 2011 | US |
