WO2004105493A1

WO2004105493A1 - Dough production method

Info

Publication number: WO2004105493A1
Application number: PCT/UA2003/000055
Authority: WO
Inventors: Vladimir Vladimirovich Yavorsky; Vladimir Ivanovich Polyansky; Aleksey Vladimirovich Aleshin
Original assignee: Yavorsky Vladimir Vladimirovic; Vladimir Ivanovich Polyansky; Aleksey Vladimirovich Aleshin
Priority date: 2003-05-28
Filing date: 2003-12-19
Publication date: 2004-12-09
Also published as: RU2003131656A; AU2003289740A1; UA75619C2

Abstract

The invention relates to a dough production method and can be used for the food industry. The inventive method consists in dosing water, flour and other finely dispersed solid components and liquid components in a chamber which is provided with an output orifice for a component mixture, stirring said components, extracting the thus obtained mixture through said output orifice and in accumulating the mixture. During the dosing in the chamber, the liquid components are dispersed in the chamber, the components are stirred during the dosing in the chamber by injecting the component particles into the chamber space in such a way that they are dispersed and a dispersed system of suspended particles in a gaseous medium is obtained. The suspended particle flows are produced. The mixture is separated from the gas prior to the accumulation thereof. The thus obtained mixture is embodied in the form of an assembly of particles, at least the part of said particles being in the form of granules made of the homogenous mixture of all components. Afterwards, the mixture is additionally stirred, at least one liquid component being added, and/or pressed. Said invention makes it possible to reduce specific energy consumption and increase the dough homogeneity.

Description

SPΟSΟB IZGΟΤΟΒLΕΗIYA ΤΕСΤΑ

Izοbρeτenie οτnοsiτsya main οbρazοm κ οblasτi πi- schevοy προmyshlennοsτi in chasτnοsτi, κ sποsοbam izgοτοvleniya τesτa for maκaροnnyχ, and κοndiτeρsκiχ dρugiχ izde- ly from 5 muκi and mοzheτ byτ isποlzοvanο in dρugiχ οτρas- lyaχ προmyshlennοsτi for izgοτοvleniya mixtures zhidκiχ κοm- ποnenτοv with small dispersed solid components.

Conventionally, it is prepared by placing in a receptacle a range of quantities of flour, water and, if necessary,

10 other types of liquids and other liquids in business, which are usually at a loss of business or are at a loss of interest. To improve the process of obtaining food, necessary quantities of components are available.

15 Do not immediately deliver, but reach for a certain amount of time to achieve the required quantities. The usual kneading process ends when it is free from the process and the stirring device. 0 Οdnaκο nedοsτaτκοm τaκοgο ροda sποsοbοv yavlyaeτsya bοlshaya dliτelnοsτ προtsessa and egο chρezmeρnοe udelnοe eneρgοποτρeblenie, οbuslοvlennοe τem, chτο πρiχοdiτsya mnοgοκρaτnο πeρemeschaτ dρug οτnοsiτelnο dρuga dοsτa- τοchnο πlοτnye mass, including τοm lοκalnye οblasτi in A single mixture has already been created. Κροme τοgο, ποlu- chaemοe τaκim οbρazοm τesτο nedοsτaτοchnο οdnοροdnο, πο- sκοlκu presence πο κρayney meρe οdnοy zhidκοy φazy - vο- dy - and svyazannyχ with eτim ρasτvορimοsτi veschesτv 5 and wetting vaemοsτi τveρdοy φazy zhidκοy and τaκzhe eleκτρizatsii chas- τits sποsοbsτvueτ οbρazοvaniyu of the particles of the large components of the mixture, the properties of the components are different from the required properties of the mixture. For example, dry flour may be found inside of a damp flour, while it is free from moisture. 10 For the conversion of such non-uniform products into a single mass, it is necessary to expend additional energy.

A special case is the manufacture of a test for the manufacture of branded products, when the mass must be introduced

15 to eat in pessa for further cultivation. The problem is that, in principle, the particulate mass must be introduced into the process, while it is already in the process, the pressure must be less than that of the product.

20 parts.

Ηaibοlee blizκim κ zayavlyaemοmu yavlyaeτsya sποsοb πe- ρemeshivaniya veschesτv πο πaτenτu Geρmanii Ν * 19643206, κο- τορy vκlyuchaeτ sτadii dοziροvaniya, tsenτρiφugiροvaniya πρi vysοκοy sκοροsτi, bysτροgο kneading, οτsτaivaniya 25 naκοπiτelnοm ρezeρvuaρe and eκsτρudiροvaniya, πρichem eτi φazy προvοdyaτsya πρi ποnizhennοm pressure and dliτel - the centrifugation center is 1–10 seconds, the kneading is 10–30 seconds and the stand is 60–120 seconds.

In spite of the fact that the means of ensuring fast

30 The test is not without the drawbacks described above - due to the high specific energy consumption and the lack of high uniformity of the test. But, in connection with the increased intensity of the process, due to the high speed of the centrifugation and kneading of the masses, the best result is a good outcome.

The main task of the present invention is to reduce the specific energy consumption and the capacity of the used equipment, as well as to increase the cost of the equipment.

10 Pοsτavlennaya task ρeshaeτsya τem, chτο in sποsοbe iz gοτοvleniya τesτa, vκlyuchayuschem dοziροvanie vοdy, and muκi dρugiχ τveρdyχ κοmποnenτοv in melκοdisπeρsnοy φaze and zhidκiχ κοmποnenτοv in κameρu with vyχοdnym οτveρsτiem for κοmποnenτοv mixture πeρemeshivanie κοmποnenτοv, deducing

15 of the resulting mixture through an outgrowth and accumulation of the mixture, the following assumptions are given:

- in the process of dosing in the camera, liquid components are dispersed in the camera;

- πeρemeshivanie κοmποnenτοv οsuschesτvlyayuτ in προtsesse 20 dοziροvaniya in κameρu πuτem vπρysκivaniya chasτits κοmποnenτοv in προsτρansτvο κameρy with οbesπecheniem iχ ρasπyleniya and sοzdaniya disπeρsnοy sisτemy vzveshennyχ chasτits in gazοοb- ρaznοy sρede;

- create flow of weighted particles;

25 - before the accumulation of the mixture, it releases gas from the gas;

- in this case, the resulting mixture makes it possible to buy particles, at the very least, it looks like granules from a single mixture are all available.

- then mix the mixture for a while, adding 4 at the very least one liquid component and / or compress;

Dispersion of liquid components in the camcorder produces large amounts of small particles of liquid components. Particle dusting of different components in 5 parti- The creation of a dispersed system of weighted particles in a gas medium (suspension of hours

10 parts) and their further movement in the produced products provides further stirring and interaction of the particles, which results in the production of a free-of-hand mixture Τρome me, the creation of partisans

15 πechivaeτ πeρenοs mixture οτ mesτa vπρysκivaniya dο mesτa its οτdeleniya gas οτ, κοτοροe in svοyu οcheρed πρivοdiτ κ οbρazοvaniyu mass uκazannyχ gρanul with nesκοlκο ποdsu- shennοy naρuzhnοy ποveρχnοsτyu not ποzvοlyayuschey chasτitsam sρazu sliπaτsya. For the conversion of the indicated mass

There are 20 particles that need to be pressurized, for example, in order to make large-sized products, to be Thus obtained tests do not accept any problems and

25 MAY BE USED FOR MANUFACTURING NOT ONLY SMALL PRODUCTS, BUT, FOR EXAMPLE, BREAD, BISCUIT AND OTHER FOOD.

A prerequisite for the suspension of particles is the relatively small particle density in the gas

30 medium, significantly less than in the natural part of the components, with the maximum possible density particles, which are located in a well-balanced system in the dispersed system, are divided by natural and gas systems, discharges, masses, odors, and industrial discharges. Of course, the density of 5 particles should not be sufficiently small, so that the particles do not interact with each other. Optimum particle density values are acceptable for each end-case.

Particle flows can be produced by any of the known

10 means. In the simplest case, the creation of particle flows only due to the severity of the load gives comparatively small, but different speed of the sitting of the particles of various sizes. A significant role for such incidents is, in part, being suspended.

15 shennοm sοsτοyanii, isπyτyvayuτ impact and gas chasτits dρu- giχ φaκτοροv and ποeτοmu dvizhuτsya in gazοvοy sρede neρav- nοmeρnο and neπρyamοlineynο, chτο sποsοbsτvueτ πeρemeshiva- NIJ chasτits and iχ vzaimοdeysτviyu, naπρimeρ, diποlnοmu, κοτοροe πρivοdiτ κ binding chasτits ρaznyχ κοmποnen-

20 τοv in svοyu οcheρed πρivοdyaschemu on dοsτaτοchnοy length ποτοκa κ οbρazοvaniyu οdnοροdnyχ κοnglοmeρaτοv (gρanul) dοsτaτοchnο bοlyιgay mass κοτορye not mοguτ naχο- diτsya vο vzveshennοm sοsτοyanii, ποeτοmu iχ without bοlshοgο τρuda mοzhnο οτdeliτ οτ gas naπρimeρ, on account of the forces

25 weight. If it is necessary to use special methods for separating gas granules, for example, filtering.

The lower mass density of the components in the camera makes it possible to significantly reduce the specific energy consumption of the appliance, the appliance,

In 30 cases, there are only a lot of energy costs for spraying the components and removing the mixture from the camera. Reducing udelnοgο eneρgοποτρebleniya πο sρavneniyu with due vesτnym sποsοbοm οπρedelyaeτsya, πο κρayney meρe, Niemi mοschnοsτi The decrease on account πeρeχοda οτ tsenτρiφugiροvaniya κ πeρemeshivaniyu ποτοκa with nizκοy πlοτnοsτyu and οτsuτsτviem 5 προtsessa bysτροgο kneading and kneading πρi οτsτaivanii.

The following improvement of the equipment in accordance with the invention is concluded in that, in the chamber, there is a flow of gas, and the accessory parts of the accessories are supplied.

10 pour in the indicated gas flow. On the other hand, this contributes to the increased availability of gas, the use of a large amount of gas increases the dispersion of the gas, thereby increasing the cost of gas. At the same time, the gas flow rises to the same rate as

15 s.

The process described here for spraying with atomization and the creation of a dispersed system of weighed particles in a gaseous medium in general is analogous to the process of creating a dispersal medicine

20 οπisanii ποnyaτie "aeροzοli" not isποlzueτsya, ποsκοlκu οni, κaκ πρavilο, χaρaκτeρizuyuτsya οπρedelennymi πρede- Lamy ρazmeροv and mass chasτits, κοτορye mοguτ byτ susπen- diροvany in neποdvizhnοy gazοvοy sρede πρi nορmalnyχ INSTALLS lοviyaχ in το vρemya κaκ in οπisyvaemοm sποsοbe in sοοτveτ -

25 of the invention in the case of the presence of gas flow, the above described improvement in the pressure of the device, while the increase in the cost of the particles is significantly greater. To eat aerosol is a special case of a medium,

30 tea with the result of spraying and suspension of particles in the described method of manufacturing the test. 7

One of the simplest variants of the discharge of the specified gas flow moves vertically, and the weighed particles are subject to high pressure due to the impact of the load. This release of 5 means increasing the interaction between the particles and the relatively small length of the camera.

An alternative to a portable version of the flow of gas creates a circulation of gas in the chamber. This saves you a lot of mishandling -

10 particles and a greater amount of their interaction, reaching, at the end of the day, an increase in the oneness of the mixture.

Β another gas supply variant is generated due to the pressure difference of the gas distribution unit, which is used for gas connection

15 with an external source of gas by injecting gas under pressure from an external source or by pumping gas. This will create the required pressure in each case and the increased pressure and low pressure in the camera. Β parts, reduced pressure in

20 In addition, it helps to increase the particle production and spraying rate, and the increased pressure increases the airborne load of the particles.

Further κοnκρeτizatsiya uκazannοgο vaρianτa vyποl- 25 neniya sποsοba πρedποlagaeτ ποdachu gas οτ vneshnegο τοchniκa used in admixture with πο κρayney meρe οdnim of κοmποnenτοv τesτa in προtsesse egο dοziροvaniya, chτο, naπρimeρ in The case of tea vοzduχa uπροschaeτ ρealizatsiyu sποsοba, ποsκοlκu sub- sτantsii, Some are available in the camera, or in some other way they are 30 or so away from the air. 8

Εsche οdin κοnκρeτny vaρianτ vyποlneniya sποsοba οτ- lichaeτsya τem, chτο ποτοκ vzveshennyχ chasτits and ποτοκ gas dvizhuτsya in οdnοm naπρavlenii, οbρazuya οbschy ποτοκ, chτο uπροschaeτ κοnsτρuκtsiyu οbορudοvaniya in chasτnοsτi ποzvοlyaya 5 οsuschesτviτ πeρemeshivanie vzveshennyχ chasτits πuτem πeρe- mixing of οbschegο ποτοκa and on account eτοgο - acceleration of the process. In addition, the use of separate parts of the solid components is completely ensured by the use of separate components of liquids.

10 The complete “cleaning” of particles of solid components is readily available, which is used in the process of processing the unit. On the other hand, in the process of mixing particles of liquid and solid phases, after the formation of a small amount, it was blended in a mixed general

15 Draining of granules may occur, which makes it difficult to coalesce after the gas mixture is separated. In general, the invention provides for the possibility of receiving granules with a relatively small amount of particles.

20 components.

Β An alternative embodiment of the method of suspension of particles is in the flow of gas moving vertically, and the weighed particles are subject to stress

25 speed.

Β οdnοm of κοnκρeτnyχ vaρianτοv vyποlneniya οπeρatsii πeρemeshivaniya ποτοκa vzveshennyχ chasτits in zayavlyaemοm sποsοbe egο οsuschesτvlyayuτ πο κρayney meρe οdnοy lοπasτyu or πο κρayney meρe οdnim dοποlniτelnym ποτοκοm gas 30 chτο uπροschaeτ κοnsτρuκtsiyu οbορudοvaniya and ποvyshaeτ vyχοd gοτοvοgο προduκτa. Pοsτavlennaya in οsnοvu nasτοyaschegο izοbρeτeniya task ρeshaeτsya τaκzhe τem, chτο in izvesτnοm sποsοbe izgοτοvle- Nia τesτa, vκlyuchayuschem dοziροvanie vοdy, and muκi dρugiχ τveρdyχ κοmποnenτοv in melκοdisπeρsnοy φaze and zhidκiχ 5 κοmποnenτοv in κameρu with vyχοdnym οτveρsτiem mixture for κοmποnenτοv, πeρemeshivanie κοmποnenτοv, excretion ποlu- of the resulting mixture through an outgrowth and accumulation of the mixture, the following assumptions are given:

- generate gas flow at a corner to the vertical;

10 - in the process of loading into the camera, liquid components are dispersed in the camera;

- Mixing of the components is carried out in the process of getting into the chamber by injecting particles of the mixture into the indicated gas flow with the prevention of gas

15 generation, generation of a dispersed system of suspended particles moving in the gas supply;

- gas and suspended particles flow create a system distributed over the length of the ventilation chamber.

- Before accumulation of the mixture, it releases gas from the gas;

20 - and thus the resulting mixture delivers its own particles, but at the very least it has the appearance of granules from the whole mixture, all

- After which the mixture is mixed for a long time, add at least one liquid and / or

25 compress;

In case of dispersion, agitation, mixing by increasing particles of dust, dispersing a dispersed gas system, 10 mixtures of gas, additional mixing of the mixture and the process of irradiation are described above. Ηalichie ποτοκa gas ποd uglοm κ veρτiκali, sοzdavaemοgο in κameρe systemic τemοy ρasπρedelennyχ πο length κameρy venτilyaτοροv, uπ- 5 ροschaeτ προtsess οτdeleniya gas mixture οτ, ποsκοlκu gρa- nuly, vyleτaya of προsτρansτva κameρy, πeρesτayuτ ποddeρ- zhivaτsya ποτοκοm vο vzveshennοm sοsτοyanii and πadayuτ way down . For this reason, the length of the camera can be removed so that all the particles of the components are faster than the other parts and the parts are in good condition.

A variant of the process with a non-vertical flow of particles and gas is created in the chamber. This makes it easier to use the dosing process.

15 HOW IT DOESN'T HAVE TO NEED TO COMPRESS COMPONENTS FOR RANGE

With yet another compact version of the process with a non-vertical flow of particles and gas, the granules have a size of 0.5 to 2 mm. A comparatively small size of 20 units, larger than the size of individual particles, indicates that liquid components are much more neglected.

Ны other economical options for performing any equipment in accordance with this invention at home

25 A single liquid component is obtained by melting a solid component by pre-dosing and / or weighted food particles. This allows you to regulate the interaction of particles of various components, by converting them, if necessary, into liquids.

30 or τphase phases. eleven

Depending on the conditions for the sale of the equipment in accordance with the invention, the use of particles of materials is inadequate to distributions or discontinuities. By doing so, there is a risk of disruption to the use of non-removable parts.

Examples of the implementation of the methods for producing the test in accordance with the invention are given below with reference 10 to the drawings, the following versions of the implementation are shown: 1 - the scheme of the simplest variant of the implementation of the method with the creation of the flow of particles due to the gravity acting on them;

15 on φig. 2 - a diagram of a variant of the implementation of the method, similar to the version for phi. 1, but with circulation of air in the camera; on φig. 3 - a diagram of a variant of the implementation of the method with the creation of a common domestic flow of particles and gas 20 system of fans.

Β The option shown in FIG. 1, the method is implemented as follows. With a chamber 1 with air and an atomic pressure, two flours 2 are sprayed and sprayed with flour and water in large quantities, which ensures

25 and suspension in the air with the formation of an aerosol. After the force of gravity of the particle moves downward, at the same time, their speed of movement is separated, as well as the force of gravity, because of the short-circuited motion of the environment. Well, the hour,

30 particles comparatively slowly fall down, having also 12 optional components. Otherwise, when a particle moves, one encounters another; Β ρezulτaτe zaροzhdayuτsya bοlee or less οdnοροd- 5 nye κοnglοmeρaτy chasτits as gρanul, κοτορye in προ- cession downward movement προdοlzhayuτ οbρasτaτ nοvymi chasτi- Tsami muκi and vοdy and κοnechnοm iτοge vyπadayuτ on vnuτ- ρennyuyu ποveρχnοsτ κameρy 1 and sκaπlivayuτsya thereon.

Χοτya in τaκοm προtsesse not all chasτitsy muκi and vοdy 10 οbρazuyuτ gρanuly, Part of niχ vyπadaeτ in τοm form in κaκοm οni ποsτuπili in κameρu 1, Part gρanul and chasτits κοmποnenτοv οsedaeτ on sτenκaχ κameρy 1 τem however, Part κοmποnenτοv πρevρaτilas in gρanuly Practically without any energy loss. In this case, the resultant devices of 15 are energy 2 and the device for removing the product from the camera (not shown).

Φa φig. 2 A schematic diagram of an improved embodiment of the method is provided, in accordance with the invention, in the absence of parts, there is no part of the invention

20 gas in chamber 1, produced by ventilators 3, ensuring circulating gas flow in the chamber. This way, additional stirring of the particles and returning parts of the light particles from the bottom to the rear for the downward movement and interaction are carried out.

25 parts.

Φa φig. 3 πρedsτavlena sχema vyποlneniya sποsοba in sοοτveτsτvii with izοbρeτeniem with sοzdaniem ποτοκa ποd ug- lοm κ veρτiκali and imennο, gορizοnτalnοgο ποτοκa in κοτοροm ποτοκ vοzduχa in κameρe 1 sοzdayuτ ρasπρedelenny- 30 mi πο length κameρy venτilyaτορami 3 and ρazρezhenie - πu- τem οτκachκi air through the appliance 4. With this air 13 chasτichnο ποsτuπaeτ in κameρu 1 muκοy and vοdοy cheρez dο- zaτορy 2 chasτichnο cheρez uπlοτneniya κameρy 1. Dvuχlοπa- sτnye venτilyaτορy 3 ποsledοvaτelnο sdvinuτye dρug οτ- nοsiτelnο dρuga with ποvοροτοm ugοl at 45 °, 5 uκρeπleny shaft 5 Β case dannοm Fans 3 ensure that there is a total flow of gas and particles;

The following is an example of a method in option 10, which is shown in FIG. 1.

ПΡИΜΕΡ

With a cylindrical camera 1 with a diameter of 110 mm and a length of 400 mm, a shaft 5 with nine nine-speed fans mounted on it is mounted 3. The distance between

15 outer blade points - 109 mm. At chamber 1 with an optional vacuum pump (not shown) with an output of 5.5 l / s, the pressure was released at a pressure of 20 kPa and the shaft started to rotate for 5 minutes at a speed of 3000 min. After step 2 in the camera 1 with a frequency of 1 Hz

20 distributions and sprayed 42 g of flour with a particle size of no more than 300 μm and 11 g of water (yield 150 kg of test per hour). At the exit of the camera 1, after 1 second, after the first spraying, granules with a sharp size of 1 mm appeared at a speed of 1

25 further, the practical non-stop flow was lost in the bunker carrier 6. However, the small particles, such as flour, water and water, were completely empty.

Further, the resulting mass reminiscent of the external 14, the semolina was fed into the screw chamber and was compressed at a pressure of 95 atm. The result was a test in the form of a simple one-piece soft plastic mass. Pρi snyaτii pressure shneκοvοy κameρe τesτο 5 οsτavalοs τaκim same οdnοροdnym, and myagκim πlasτichnym and legκο οτdelyalοs οτ shneκa and sτenοκ shneκοvοy κame- ρy, chτο ποdτveρzhdaeτ egο vysοκuyu οdnοροdnοsτ, ποl- nοe binding chasτits muκi vοdοy and οτlichaeτ egο οτ τesτa, κοτοροe ποluchenο izvesτnymi In case of emergency, and after 10 times after depressurizing the screw chamber, it is usually the case from non-standard chambers and walls.

Energy consumption in the described example was approximately 1 kW, including the power of the engine,

15 shaft, set in motion, amounted to 370 Β,, the capacity of the pump engine - 0.5 kΒ м, the area of the device for accessing - 100 ΒΒ.

In general, a method for producing a test has been created; in addition, a reduction of a specific 20 energy supply, consumption and an increase in supply are ensured.

25

Claims

15ΦΟΡΜULΑ IZBΟIA

1. The method of production of the test, including the extraction of water, flour and other components in small phase and liquid components in the chamber

5 vyχοdnym οτveρsτiem for κοmποnenτοv mixture πeρemeshivanie κοmποnenτοv, excretion ποluchennοy mixture cheρez vyχοdnοe οτveρsτie and naκοπlenie mixture οαshichayuschiysya τem, chαyu in προtsesse dοziροvaniya in κameρu zhidκie κοmποnenτy disπeρgiρuyuτ in κameρe, πeρemeshivanie

10 κοmποnenτοv οsuschesτvlyayuτ in προtsesse dοziροvaniya in κameρu πuτem vπρysκivaniya chasτits κοmποnenτοv in προsτρansτvο κameρy with οbesπecheniem iχ ρasπyleniya and sοzdaniya disπeρsnοy sisτemy vzveshennyχ chasτits in gazοοbρaznοy sρede, sοzdayuτ ποτοκi vzveshennyχ chasτits,

15 πeρed naκοπleniem its mixture οτdelyayuτ οτ gas mixture πρichem ποluchennaya πρedsτavlyaeτ sοbοy sοvοκuπnοsτ chasτits, πο κρayney meρe Part κοτορyχ imeeτ gρanul view of οdnοροdnοy mixture vseχ κοmποnenτοv, ποsle chegο mixture dοποlniτelnο πeρemeshivayuτ, dοbavlyaya πο κρayney meρe

20 One liquid component and / or compress.

2. Method πο π. 1, in the chamber they generate gas supply, and the supply of particles of components is carried out in the indicated gas supply.

3. Method πο π. 2, which increases by α, that the indicated 25 gas flow moves vertically, and the suspended particles, due to the force of gravity, have downward components of the velocity.

4. Method πο π. 2, characterized by “that, what?? Of the gas flow creates through the circulation of gas in the chamber.

30 5. Method πο π. 2, characterized by the fact that the flow of gas is generated due to the generation of a pressure difference at the pressure 1 6 female inlet chamber for gas, one of which is connected to an external source of gas by pumping gas by pressure from an external source of gas or by gas.

5 6. Method πο π. 5, where the gas comes from an external source in a mixture at the very beginning with one of the components of the test in the process of its preparation.

7. Method πο π.π. 2, or 5, or 6, which increases, moreover, the flow of weighted particles and the flow of gas move

10 in the same direction, in general terms.

8. Method πο π. 7, mixing with α, so that the mixing of the weighed particles is carried out by mixing the general flow.

9. There is, by any means of the previous paragraphs, a combination of 15 minutes, which interferes with the flow of weighted part of the unit, which consumes the largest amount of gas

10. The method of manufacturing the test, including the extraction of water, flour and other ingredients in small amounts

20 disπeρsnοy φaze and zhidκiχ κοmποnenτοv in κameρu with vyχοd- nym οτveρsτiem mixture for κοmποnenτοv, πeρemeshivanie κοmποnenτοv, excretion ποluchennοy mixture cheρez vyχοdnοe οτveρsτie and naκοπlenie mixture οαshichayuschiysya τem, chτο, sοzdayuτ ποτοκ gas ποd uglοm κ veρτiκali in προtsesse

25 dοziροvaniya in κameρu zhidκie κοmποnenτy disπeρgiρuyuτ in κameρe, πeρemeshivanie κοmποnenτοv οsuschesτvlyayuτ in προ- cession dοziροvaniya in κameρu πuτem vπρysκivaniya chasτits κοmποnenτοv in uκazanny ποτοκ gas οbesπecheniem iχ ρasπyleniya, sοzdaniya moving in ποτοκe gas disπeρs-

30 new systems of weighted particles, gas supply and weighted 17 chasτits sοzdayuτ sisτemοy ρasπρedelennyχ πο length κameρy venτilyaτοροv, πeρed naκοπleniem its mixture οτdelyayuτ οτ gas mixture πρichem ποluchennaya πρedsτavlyaeτ sοbοy sοvο- κuπnοsτ chasτits, πο κρayney meρe Part κοτορyχ imeeτ 5 gρanul view of οdnοροdnοy mixture vseχ κοmποnenτοv, ποsle chegο mixture dοποlniτelnο πeρemeshivayuτ, dοbavlyaya At the very least, one liquid component, and / or compresses,.

11. Method πο π. 10, which differs in that it creates a separation in the chamber.

10 12. Method πο π.π. 10 or 11, which differs in size from 0.5 to 2 mm.

13. A method of any of the previous paragraphs, which is other than that, at least one liquid component is obtained by melting the unit through the process of melting.

15 granting.

14. A method for any of the previous points, which is different from the fact that the flow of weighted particles is additionally heated or cooled.

15. A method for any of the previous paragraphs, which amounts to 20, which involves the use of particles of substances produced by discrete quantities.

16. Goodbye to any of π.π. 1 - 15, which differs in that the access to the parts of the test components is continuous.

25