RU2104657C1 - Method of producing macaroni goods - Google Patents

Abstract

FIELD: food industry. SUBSTANCE: method includes transferring at least a part of components into accumulation tanks by means of pneumatic conveyor, while simultaneously aspirating air, accumulation tanks being connected with aspiration unit. In this case, desired area of filter surface is formed with variable carrying capacity depending on dispersity of fed component. Filter surface area of at least one tank is formed with excess over the area of corresponding air-transparent region of surface of this tank in the range from 1.002 to 230 reduced diameters of this region. Filter surface is shaped as three-dimensional shell with fixed or variable curvature or combined configuration being at maximum distance from plane apex coinciding with at least one nonlinear section of air-transparent region outline or at distance from the plane of horizontal projection of corresponding air- transparent region constituting 0.62 to 78 reduced diameters of air- transparent region. EFFECT: lowered loss of raw material and speeded up production process because of its more rhythmic organization. 89 cl, 12 dwg

Description

 The invention relates to the food industry, and in particular to a method for producing pasta.

 A known method for producing pasta, which provides for the pneumatic conveying of flour and / or grains to the silos of a flour warehouse with simultaneous suction of air supplied by pneumatic conveying through the filters of an aspiration unit, mixing flour in flour mixers, sifting the flour mixture, kneading dough, forming a semi-finished product, drying, cutting and packaging . (see Nazarov N.I. Technology of pasta, 1978, p. 21).

 The disadvantages of the method include large losses of flour during the production process associated with the insufficiently high quality of the aspiration process.

 Closest to the invention in terms of the problem to be achieved and the result achieved is the known method for producing pasta adopted for the closest analogue, which provides for pneumatic conveying of at least part of the flour and / or grains and / or other loose components to the main and / or reserve storage tanks equipped with lids, while aspirating the air supplied by pneumatic conveying by connecting at least part of the containers for feeding flour and / or grains, and / or other loose components with with a spiral installation and / or with each other with the possibility of combining and / or selective switching and the formation of a predetermined filter area, having transmittance differentiated depending on the degree of dispersion of the component supplied by pneumatic conveying, container surfaces, preparation of raw materials and water for kneading, kneading the dough with its subsequent evacuation in the chambers of screw presses, molding the semi-finished product by passing the dough through the molding matrix, drying the molded semi-finished product in the dryer a chamber with climatic zones equipped with an air conditioning system, a condensate collector, communication for condensate drainage and forced removal of moist air from the drying chamber, stabilization of dried pasta, sorting, packing and packaging, (see RU, patent, 2052956, cl. A 23 L 1/16, 01/27/96).

 The disadvantages of the method include the loss of feedstock caused by insufficient reliability and quality of suction operations.

 The objective of the invention is to reduce the loss of feedstock by optimizing the area and configuration of the filtering surfaces of the containers used during the aspiration process, as well as accelerating and simplifying the method of obtaining pasta by enabling more rhythmic organization of production, which allows to speed up and reduce the cost of the process of obtaining pasta .

 The problem is solved due to the fact that in the method for producing pasta, which provides for pneumatic conveying of at least part of the flour, and / or grains, and / or other bulk components into the main and / or storage containers equipped with lids, while feeding pneumatic transport of air by connecting at least part of the containers for supplying flour, and / or grains, and / or other loose components with an aspiration unit and / or with each other with the possibility of a combination and / or selective switching and the formation of a given filter area, having a transmittance differentiated depending on the degree of dispersion of the component supplied by pneumatic conveying, container surfaces, preparation of raw materials and water for kneading, kneading dough followed by evacuation in the chambers of screw presses, forming a semi-finished product by passing the test through a molding matrix, drying molded semi-finished product in a drying chamber with climatic zones, equipped with air conditioning system, condensate collector, comm In order to remove condensate and forcefully remove moist air from the drying chamber, stabilize the dried pasta, sort them, fill and pack, the filter surface area of at least one container is formed in excess of the area of the corresponding air-transparent surface section of this container in the range from 1.002 to 230 reduced diameters of the area of the translucent section and the formation of the shape of the filtering surface in the form of a spatial shell of constant and / or variable curvature or combined configuration with the maximum distance of its apex from the plane, combined with at least one non-linear segment of the contour of the air-transparent section or from the horizontal plane of the projection of the corresponding air-transparent section at a distance of 0.02 to 78 reduced diameters of the air-transparent section.

 At the same time, during the aspiration process, at least one air-filter insert can be used as a filter surface, which is installed in the lid cavity of the main and / or reserve storage tanks, or at least one air-filter membrane is used as a filter surface, serving at the same time as the cover of the main and / or reserve storage tank, or at least one insert for filtering the supplied air is used as a filter surface the open one is installed in the upper part of the wall of at least one main and / or reserve storage tank, in which case the insert for filtering the supplied air is made in the form of a fragment of a cylindrical surface, or double curvature, or in the form of a concave or convex-concave polyhedron, or convex relative to the surface of the walls of the tank, or in a combined form from a combination of straight and / or curved sections, or in the form of a continuous ring or discrete shell.

 When carrying out the aspiration process, at least one air-filtering element can be used as a filter surface, which is made in the form of a removable shell, while in the upper part of at least one main and / or reserve storage tank, a cut is made in which a shell with an air-filtering element, the cut-out area being at least 1% of the cross-sectional area of the corresponding container with a multifaceted configuration or at least 2.3% of the cross-sectional area the value of the corresponding capacity of cylindrical or variable curvature, or a combined configuration.

 When carrying out the aspiration process, at least two air filter inserts, air filter membranes, inserts for filtering the supplied air and air filter elements can be used as a filter surface, while the area ratio of any two filter elements is 1: 1 - 15.

 To seal the main and backup storage tanks, any filtering elements that make up the filter surface can be connected to the tanks by means of clamps with sealants, and at least some of the connections are detachable.

 For carrying out preventive or repair work during the aspiration process, the main and / or reserve storage tanks can additionally be equipped with airtight membranes, which are installed to ensure complete cessation of air supply to the replaceable filter element.

 An air filter insert, or an air filter membrane, or an insert for filtering the supplied air, or an air filter element can be made in the form of a shell containing at least one double curvature section, or at least one single curvature section, or combinations thereof, or from combinations of curvilinear and / or straight sections.

 In the process of aspiration, air can be injected to form a shell shape containing at least one cylindrical or half-cylindrical section formed by at least two joints with fragments of cylinders of constant and variable curvature, interconnected directly or by means of internal diaphragms, or with the formation of a shell shape containing at least one conical or polyconic section formed from fragments of conical and / or polyconic curvature, interconnected directly either by means of internal diaphragms, or with the formation of a shell shape containing at least one cylindrical or multicylindrical section formed from fragments of cylindrical and / or polycylinder curvature connected directly to each other or by means of internal diaphragms, or with the formation of a shell shape containing at least one cylindrical and / or conical and / or spherical and / or spheroidal and / or ellipsoidal and / or parabolic and / or hypovoid and / or toroidal portion.

 The shell may be provided with an inner frame.

 The filtering surface can be made of high-strength woven or fibrous non-woven material, moreover, for example, overcoat cloth is used as high-strength woven material, and, for example, felt is used as a fibrous non-woven fabric.

The design for aspiration with a filter surface can be made of at least two filter layers with different strength and transmittance, which are arranged in order to increase their strength and transmittance, or fastened together to form cavities into which a powdery and / or granular filler is introduced, at the same time, the differentiated throughput in at least one layer is formed to provide a pressure differential between its internal and external surfaces in the interval e from 0.1 to 0.2 mPas at operating speeds Suction suspended in an air stream of dispersed particles and the minimum sectional area of the receiving holes of at least 60 microns ² in the filter surface.

 The filtering surface can be subjected to vibrational influences, ensuring the restoration of its transmission capacity, which can create by the pressure drop in the tank.

 To carry out the aspiration process, additional containers can be installed that are equipped with filters and connected to the general aspiration system with additional air ducts.

 Evacuation and molding of the dough can be carried out with forced cooling, which can be carried out by introducing the corresponding forced cooling systems into the screw presses and molding dies.

 They can use screw presses with air cooling of traction electric motors.

 Air cooling of traction electric motors can be carried out using fans with an impeller, the blades of which are made of a heat-resistant material or composition containing a metal base and at least one layer of thermoplastic or ceramic.

 The impeller may have two or three blades, may have four to nine blades, or twelve or more blades.

 The impeller blades can have a variable angle along the radius and / or along the arc of a circle of inclination relative to a plane normal to the axis of the impeller. The front and rear edges of the impeller blades can perform with a radial configuration. The external impeller blades can be coupled without kinks with the formation of a crescent-shaped contour that smoothly passes into a crescent-shaped contour that has less curvature in the projection onto a plane normal to the axis of the impeller.

 The blades can give a hypovaroid twist.

 The blades may have an angular clearance of 0.1-0.3 angular alignment formed by the front and rear edges of the blades.

 For air cooling of traction motors, an additional impeller can be installed with the possibility of rotation in the opposite direction or with the possibility of fixation.

The filter surface can be made differentiated depending on the degree of dispersion of the component supplied by the pneumatic conveyor, with a transmittance that allows to separate the air from the particles of the supplied component of at least 10 microns in size, and control the load of the conveyor of the raw waste products and, in case of overheating of the engine, stop and stop the screw press and attachments or attachments, and forced removal from the drying chamber is subjected to air with a temperature of 30-95 ^o C and relative humidity 62-83%, which is diverted by the air duct outside the premises or into the atmosphere.

The water prepared for mixing can be fed into a storage tank, which is connected to the communication to drain condensate from the drying chamber with the possibility of completely draining the prepared water through a pipeline equipped with a valve, and air with a temperature of 30-95 ^o C is forced to be removed from the drying chamber and relative humidity 62-83%, which is diverted by the air duct outside the premises or into the atmosphere.

To knead the dough, you can use prepared water with a temperature of 20-45 ^o C, while the vacuum depth is maintained within the range of 0.07-0.08 MPa, and the humidity of the test is 29-31%.

The formation of the semi-finished product by passing the test through the molding matrix can be carried out at a pressure of 10.0-11.5 MPa, and the temperature of the semi-finished product at the exit of the matrix is not more than 42 ^o C.

 Semi-finished product can be dried in a drying chamber having at least eleven climatic zones, with differentially maintained air temperature and humidity.

 Drying of the semi-finished product can be carried out by successively increasing and decreasing the temperature and relative humidity in the climatic zones of the drying chamber, while raising the temperature is carried out in the first and seventh zones, and decreasing in the eighth and eleventh.

The temperature increase in the first to sixth climatic zones is carried out sequentially with an increase in temperature between each adjacent climate zone of not more than 7 ^o C, while the temperature in the first zone is 55 ^o C.

The temperature increase in the sixth and seventh climatic zones is carried out by no more than 5 ^o C, while the temperature in the seventh climatic zone is 95 ^o C and is maximum.

The temperature between the seventh and eighth climatic zones is reduced by no more than 5 ^o C, between the eighth and tenth zones, respectively, by no more than 15 ^o C, and between the tenth and eleventh zones by no more than 20 ^o C, which ensures the temperature of the dried semi-finished product.

 An increase in relative air humidity from a 50% source is carried out with zones lagging relative to a relative temperature increase, and the humidity reaches its maximum, namely 81-83%, in the ninth climatic zone, after which it is reduced to 65% to the eleventh climatic zone.

 The necessary temperatures and humidity in climatic zones can be maintained by conditioning with forced ventilation, thermostating and humidification of the supplied air, including using a refrigeration unit.

 Forced removal from the drying chamber can be subjected to air with maximum relative humidity.

 An air duct for forced removal of air with maximum relative humidity is provided with a heat exchanger or economizer for the selection of waste heat, which is then returned for use in the air conditioning system.

 Vitamins and / or microelements and / or oxidative improvers can be added to flour. Vitamins and / or trace elements and / or oxidative improvers can be added to flour during the grinding process. Vitamins and / or trace elements and / or oxidative improvers can be introduced into the flour in the process of feeding it to the pre-storage containers. Vitamins and / or trace elements and / or oxidative improvers can be introduced into the flour in the process of feeding it into the main and / or reserve storage tanks.

 When mixing in the dough, flavoring agents can be added. When kneading, vitamins and / or microelements and / or surfactants can be added to the dough. As surfactants, sucrose and fatty acid esters, polyoxyethylene and sorbitol esters, glycerol monoesters with fatty acids, ethylene oxide condensation products with glycerol and fatty acid esters and monoglycerides of fatty acids, aliphatic acids and glycerin, sorbitol, propylene glycol can be used and sugars.

 Drying the molded semi-finished product can be carried out on bastunas, or in tray cassettes, or on drying surfaces.

 Before packing, dried pasta can be cut, and the waste generated during the cutting process is sent to grinding and return to production.

 Pasta can be made filamentary.

 Filamentary pasta can be made short, 2 to 20 cm long, longer than 20 cm long, and their diameter is 0.45 to 3.0 mm.

 Filamentary pasta can be made with unequal cross-section. Hanging a long thread-like product with an unequal cross-section on the bastion can be carried out by orienting the larger axis of the cross-section of the product parallel to the axis of the bastion.

 Filamentary pasta can be made with a cross-sectional configuration in the form of an ellipsoid, or an oval, or a combined profile, including smooth and / or with a kink of conjugation of curved sections with straight sections. The ratio of the larger and smaller axes of the cross section of the product can be 2 - 25: 1, and the absolute value of the major axis is 1.5 - 12.0 mm.

 Filamentary pasta can be made with a cross section in the form of at least one double truncated truncated ellipsoid, or a double truncated ovoid, or a joint of truncated or double truncated circular cylindrical elements, and / or ovals, and / or as a combination of the above forms.

 Pasta can be made in the form of ribbon-like products. The width of the product can be at least 1.5 mm, the thickness is not more than 2 mm, while the products are made short, 2 to 20 cm long and long - more than 20 cm.

 The cross section of the product may have the configuration of a flat polyhedron and / or combined unequal profile.

 Hanging a long ribbon-like product on the bastion can carry out the larger axis of the product parallel to the axis of the bastion.

 Pasta can be made tubular in the form of pasta, horns and feathers. The outer diameter of the products can be 2.0-30.0 mm, the products are made short, 1.5-30 cm long, and long - more than 30 cm.

 The product can be made with a cross-sectional shape, round, or square, or grooved, or elliptical, or combined. The product can be made with unequal cross-section. In the manufacture of products with a corrugated cross-sectional shape, the corrugation can be performed externally and / or internally. Products may be curved or straight. Products can give a spiral axial twist.

 Pasta can be made curly of any shape and size, while the maximum thickness of any part of the product on the fracture should not exceed 1.5 - 3.0 mm.

 Long pasta can be dried in bastoons.

Pasta can be produced with a moisture content of 12 - 13% and a content, wt.%: Protein 11.1 - 11.8, fat 1.5 - 1.8, carbohydrates 64.4 - 66.5, potassium 0.189 - 0.253, calcium 0.025 - 0.033, phosphorus 0.136 - 0.186, as well as vitamins B ₁ , B ₂ and PP - the rest, while the energy value of 100 g of the finished product is 327 - 333 kcal.

 In the manufacture of pasta such as "Canteen" for kneading can use wheat flour of the first or second grade of durum "Durum".

 In the manufacture of pasta type "New" for kneading, you can use a mixture of wheat flour of the first or second grade of durum durum wheat and premium wheat flour of soft wheat with a mass ratio of the mixture, respectively, 0.9 - 1: 0.9 - 1.

 The arches obtained as a result of cutting long pasta dried on bastunas can be separated from crumbs and sent to packaging as commercial products.

 Pasta can be packaged on a filling machine, which includes a proximity sensor mounted on the scales of the filling machine and having a generator, a signal amplifier and a key made on a transistor and a resistor, while a diode is connected in parallel with the latter, and a resistance is connected in series with the transistor base.

 Packaging can be carried out on an automated packaging line "Zamboni".

 Pasta can be packaged on an automated packaging line that has a metering device with an adjusting element and a dispenser, which includes a bucket elevator, while the number of buckets of the latter is increased by at least eight and the total number of buckets is increased to at least forty, which extends the upper horizontal section of the elevator having a broken configuration with at least one horizontal and at least one vertical section, and for more accurate dosing, I increase maximum allowable dissipation power value adjusting member via a parallel connection of two transistors.

 Arches can be packed on an automated packaging machine, which is installed under the upper horizontal section of the bucket elevator.

 As an automated packaging machine can use the automated packaging machine "Pavan".

 Packaging can be carried out in hard or soft containers. As a soft container can use a film of polyethylene, or polyethylene terephthalate, or prolipropylene, or in the form of an adjacent composition of these materials, taken in any combination.

 Packaging can be carried out in a layered composition, the surfaces of which are metallized by spraying or applications with aluminum.

 The packaging can be carried out in a layered composition that does not transmit ultraviolet rays and the visible part of the solar spectrum, and having at least one liner made of aluminum foil or aluminized materials.

 Packaging in hard or soft containers can be carried out with the filling of the internal volume of the latter with nitrogen.

 At least one layer of the layered composition can be impermeable to ultraviolet rays and other rays of the solar spectrum.

 As an automated packaging machine can use the automated packaging machine "Pavan".

 Flour carriers may contain at least two containers that are installed on a car platform. Tanks can be installed on a railway platform. Capacities can be fixed permanently, or with the possibility of changing the spatial orientation, or with the possibility of vibration of the housing.

 A flour truck can be fed to the unloading area using a cable and a winch.

 The technical result provided by the specified set of features is that during the production of pasta, the loss of feedstock at all stages of the use of pneumatic conveying is reduced due to the adoption of the optimal area and shapes of the used filter surfaces during the air aspiration process, which increases the reliability of the aspiration process and allows accelerate and reduce the cost of the process of pasta production by providing the possibility of a more rhythmic organization of production.

 In FIG. 1 shows a fragment of a container with a filter surface exceeding the area of the corresponding air-transparent surface portion of this container; in FIG. 2 - filtering surface in the form of a spatial shell of constant curvature; in FIG. 3 - the same, in the form of a spatial shell of variable curvature; in FIG. 4 - the same, combined configuration; in FIG. 5 - a container with a lid having one air filter insert; in FIG. 6 - the same, with an insert located in the upper part of the tank wall; in FIG. 7 - insert in the form of a convex-concave polyhedron, in a perspective view, an embodiment; in FIG. 8 - insert in the form of an annular shell in a perspective view, an embodiment; in FIG. 9 - a container with a cutout in which a shell with an air-filtering element is installed; in FIG. 10 - filter surface in the form of several air-filtering membranes; in FIG. 11 - a shell with an inner frame; in FIG. 12 - main and additional containers with filters and additional air ducts.

 A method of producing pasta according to the invention is as follows.

 At least part of the flour and / or grains and / or other bulk components is fed into the main and / or reserve storage tanks 1, equipped with lids 2, while air is supplied by pneumatic conveying by connecting at least part of the containers 1 for feeding flour, and / or grains, and / or other loose components with an aspiration unit (not shown in the drawings) and / or with each other with the formation of a given area of the filter surface 3, differentiated depending on the degree of dispersion of the feed the transmission capacity of the component.

 The connection is carried out with the possibility of combining and / or selective switching by at least one additional duct 4, and the area of the filter surface 3 of at least one container is performed in excess of the area of the corresponding air-transparent portion 5 of the surface of this container 1 in the range from 1.002 to 230 reduced diameters the area of the air-transparent section, and the shape of the filtering surface in the form of a spatial shell of constant and / or variable 7 curvature or a combined configuration of 8 with max the total distance of its top from a plane aligned with at least one non-linear segment of the contour of the air-transparent section 5 or from the horizontal projection plane of the corresponding air-transparent section 5 at a distance of 0.02 to 78 reduced diameters of the area of the air-transparent section 5.

 When carrying out the aspiration process, at least one air filter insert 9 can be used as a filter surface, which is installed in the lid cavity of the main and / or backup storage containers, or at least one air filter membrane serving simultaneously is used as a filter surface. with the cover of the main and / or reserve storage tank, or at least one insert 10 for filtering the supply air, which at least one main and / or reserve storage tank is installed in the upper part of the wall 11, in which case the insert for filtering the supplied air is made in the form of a fragment of a cylindrical surface (not shown in the drawings), or double curvature (not shown in the drawings), or in the form of a concave polyhedron (not shown in the drawings), or convex-concave 12, or convex relative to the surface of the walls of the container, or in a combined form from a combination of straight and / or curved sections (not shown), and and an annular continuous or discrete shell 13 (not shown).

 When carrying out the aspiration process, at least one air-filtering element can be used as a filter surface, which is made in the form of a removable shell, while in the upper part of at least one main and / or reserve storage tank, a cutout 14 is made in which the casing is installed 15 with an air-filtering element 16, the cut-out area being at least 1% of the cross-sectional area of the corresponding container with a multifaceted configuration or at least 2.3% of the transverse area cross-section of the corresponding capacity of circular cylindrical or variable curvature or combined configuration.

 When carrying out the aspiration process, at least two air filter inserts, air filter membranes 17, inserts for filtering the supplied air and air filter elements can be used as a filter surface, while the area ratio of any two filter elements is 1: 1 - 15.

 To seal the main and backup storage tanks, any filtering elements that make up the filter surface can be connected to the tanks by means of clamps with sealant, and at least some of the connections are detachable.

 For carrying out preventive or repair work during the aspiration process, the main and / or reserve storage tanks can additionally be equipped with airtight membranes, which are installed to ensure complete cessation of air supply to the replaceable filter element.

 An air filter insert, or an air filter membrane, or an insert for filtering the supplied air, or an air filter element can be made in the form of a shell containing at least one double curvature section, or at least one single curvature section, or combinations thereof, or from combinations of curvilinear and / or straight sections.

 In the process of aspiration, air can be injected to form a shell shape containing at least one cylindrical or poly-cylindrical section formed by at least two jointed fragments of cylinders of constant and variable curvature, interconnected directly or by means of internal diaphragms, or with the formation of a shell shape containing no less than one conical or polyconic section formed from fragments of conical and / or polyconic curvature directly connected to each other either indirectly or by means of internal diaphragms, or with the formation of a shell shape containing at least one cylindrical or poly-cylindrical section formed from fragments of cylindrical and / or poly-cylindrical curvature interconnected directly or by means of internal diaphragms, or with the formation of a shell shape containing at least one cylindrical and / or conical and / or spherical and / or spheroidal and / or ellipsoidal and / or parabolic and / or hypovoid and / or toroidal ASTK.

 The shell may be provided with an inner frame 18.

 The filtering surface can be made of high-strength woven or fibrous non-woven material, moreover, for example, overcoat cloth is used as high-strength woven material, and, for example, felt is used as a fibrous non-woven fabric.

The design for aspiration with a filter surface can be made of at least two filter layers with different strength and transmittance, which are arranged in order to increase their strength and transmittance, or fastened together to form cavities into which a powdery and / or granular filler is introduced, in this case, a differentiated throughput is formed in at least one layer, providing a pressure differential between its internal and external surfaces in the interval from 0.1 to 0.2 MPa at the working air supply rates of dispersed particles suspended in the air flow, and the minimum cross-sectional area of the holes in the filter surface is taken to be at least 60 μm ² .

 The filtering surface can be subjected to vibrational influences, ensuring the restoration of its transmission capacity, which can create by the pressure drop in the tank.

 To carry out the aspiration process, additional containers 19 can be installed, which are equipped with filters and connected to the general aspiration system with additional air ducts 20.

 Prepare raw materials and water for kneading, kneading the dough and then evacuating it in the chambers of screw presses (not shown in the drawings), molding the semi-finished product by passing the dough through the molding matrix (not shown in the drawings), and drying the molded semi-finished product in the drying chamber (not shown in the drawings shown) with climatic zones equipped with an air conditioning system, a condensate collector (not shown in the drawings), communication for condensate drainage and forced removal of moist air (in the drawings e shown) from the drying chamber, the dried pasta stabilization, their grading, packing and packaging.

 Evacuation and molding of the dough can be carried out with forced cooling. Forced cooling is carried out by introducing into the screw presses and molding dies the corresponding forced cooling systems. They can use screw presses with air cooling of traction electric motors.

 Air cooling of traction motors can be carried out using fans with an impeller, the blades of which are made of heat-resistant material or composition containing a metal base and at least one layer of thermoplastic or ceramic.

 The impeller has two or three blades, or four to nine blades, or twelve or more blades.

 The impeller blades can have a variable angle along the radius and / or along the arc of a circle of inclination relative to a plane normal to the axis of the impeller. The front and rear edges of the impeller blades can perform with a radial configuration. The external impeller blades can be coupled without kinks with the formation of a crescent-shaped contour that smoothly passes into a crescent-shaped contour that has less curvature in the projection onto a plane normal to the axis of the impeller.

 The blades can give a hypovaroid twist. The blades may have an angular clearance of 0.1 - 0.3 angular alignment formed by the front and rear edges of the blades.

 For air cooling of traction motors, an additional impeller can be installed with the possibility of rotation in the opposite direction or with the possibility of fixation.

The filter surface can be made differentiated depending on the degree of dispersion of the component supplied by the pneumatic conveyor, with a transmittance that allows to separate the air from the particles of the supplied component of at least 10 microns in size, and control the load of the conveyor of the raw waste products and, in case of overheating of the engine, stop and stop the screw press and attachments or attachments, and forced removal from the drying chamber is subjected to air with a temperature of 30 - 95 ^o C and relative humidity 62 - 83%, which is diverted by the air duct outside the premises or into the atmosphere.

The water prepared for mixing can be fed into a storage tank, which is connected to the communication to drain condensate from the drying chamber with the possibility of completely draining the prepared water through a pipeline equipped with a valve, and air with a temperature of 30 - 95 ^o C is forced to be removed from the drying chamber and relative humidity 62 - 83%, which is removed by the air duct outside the premises or into the atmosphere.

To knead the dough using prepared water with a temperature of 20 - 45 ^o C, while the depth of the vacuum support within the range of 0.07 - 0.09 MPa, and the humidity of the test 29 - 31%.

The formation of the semi-finished product by passing the test through the molding matrix is carried out at a pressure of 10.0 to 11.5 MPa, and the temperature of the semi-finished product at the exit of the matrix is not more than 42 ^o C.

The drying of the semi-finished product is carried out in a drying chamber having at least eleven climatic zones with differentially maintained air temperature and humidity, or the drying of the semi-finished product is carried out by successively increasing and decreasing the temperature and relative humidity in the climatic zones of the drying chamber, while the temperature is increased in the first - the seventh zone, and the decline - in the eighth - eleventh. Moreover, the temperature increase in the first to sixth climatic zones is carried out sequentially with an increase in temperature between each adjacent climatic zone of not more than 7 ^o C, while the temperature in the first zone is 55 ^o C.

The temperature increase in the sixth and seventh climatic zones is carried out by no more than 5 ^o C, while the temperature in the seventh climatic zone is 95 ^o C and is maximum.

The temperature is reduced between the seventh and eighth climatic zones by no more than 5 ^o C, between the eighth and tenth zones, respectively, by no more than 15 ^o C, and between the tenth and eleventh zones by no more than 20 ^o C, which ensures the temperature dried semi-finished product.

 An increase in relative air humidity from a 50% initial temperature can be made by lagging in zones from a relative temperature increase and reaches a maximum, namely 81 - 83%, in the ninth climatic zone, after which it is reduced to 65% to the eleventh climatic zone.

 The necessary temperature and humidity in climatic zones are maintained by conditioning with forced ventilation, thermostating and humidification of the supplied air, including using a refrigeration unit.

 Forced removal from the drying chamber is subjected to air with maximum relative humidity.

 An air duct for forced removal of air with maximum relative humidity is provided with a heat exchanger or economizer for the selection of waste heat, which is then returned for use in the air conditioning system.

 Vitamins and / or micronutrients and / or oxidizing improvers can be added to flour, and vitamins and / or micronutrients and / or oxidizing improvers can be introduced into flour during the grinding process.

 Vitamins and / or trace elements and / or oxidative improvers can be introduced into the flour in the process of feeding it to the pre-storage containers.

 Vitamins and / or trace elements and / or oxidative improvers can be introduced into the flour in the process of feeding it into the main and / or reserve storage tanks.

 When mixing in the dough, flavoring agents can be added.

 When kneading, vitamins and / or microelements and / or surfactants can be added to the dough.

 As surfactants, sucrose and fatty acid esters, polyoxyethylene and sorbitol esters, glycerol monoesters with fatty acids, ethylene oxide condensation products with glycerol and fatty acid esters and monoglycerides of fatty acids, aliphatic acids and glycerin, sorbitol, propylene glycol can be used and sugars.

 Drying the molded semi-finished product can be carried out on bastunas, or in tray cassettes, or on drying surfaces.

 Before packaging, dried pasta is subjected to cutting, and the waste generated during cutting is sent to grinding and return to production.

 Pasta can be made filamentary. Filamentary pasta is made short, 2 to 20 cm long, long - more than 20 cm, while their diameter is 0.45 - 3.0 mm.

 Filamentary pasta can be made with unequal cross-section.

 Hanging a long thread-like product with an unequal cross-section on the bastion is carried out by orienting the major axis of the cross-section of the product parallel to the axis of the bastion.

 Filamentary pasta can be made with a cross-sectional configuration in the form of an ellipsoid, or an oval, or a combined profile, including smooth and / or with a kink of conjugation of curved sections with straight sections.

 The ratio of the major and minor axes of the cross section of the product is 2 - 25: 1, and the absolute value of the major axis is 1.5 - 12.0 mm.

 Filamentary pasta can be made with a cross section in the form of at least one double truncated truncated ellipsoid, or a double truncated ovoid, or a joint of truncated or double truncated circular cylindrical elements, and / or ovals, and / or as a combination of the above forms.

 Pasta can be made in the form of ribbon-like products.

 The width of the product is not less than 1.5 mm, thickness - not more than 2 mm; at the same time, products are made short with a length of 2 to 20 cm and long - more than 20 cm.

 The cross section of the product may have the configuration of a flat polyhedron and / or combined unequal profile.

 Hanging a long ribbon-like product on the bastion is carried out by the larger axis of the product parallel to the axis of the bastion.

 Pasta is made tubular in the form of pasta, horns and feathers.

 The outer diameter of the products is 2.0 - 3.0 mm, the products are made short, 1.5 - 30 cm long, and long - more than 30 cm.

 Products are made with a cross-sectional shape of round, or square, or corrugated, or elliptical, or combined, or the product is made with an unequal cross-section.

 In the manufacture of products with a corrugated sectional shape, the corrugation can be carried out external and / or internal.

 Products may be curved or straight.

 Products can give a spiral axial twist.

 Pasta can be made curly of any shape and size, while the maximum thickness of any part of the product on the fracture should not exceed 1.5 - 3.0 mm.

 Long pasta can be dried in bastoons.

Pasta is made with a moisture content of 12 - 13%, content, wt. %: protein 1.1 - 11.8, fat 1.5 - 1.8%, carbohydrates 64.4 - 66.5%, potassium 0.189 - 0.253%, calcium 0.025 - 0.033%, phosphorus 0.136 - 0.186%, and also vitamins B ₁ , B ₂ and PP - the rest, while the energy value of 100 g of the finished product is 327 - 333 kcal.

 In the manufacture of pasta such as "Canteen" for kneading use wheat flour of the first or second grade of durum durum wheat.

 In the manufacture of pasta type "New" for kneading using a mixture of wheat flour of the first or second grade from soft wheat with a mass ratio of the mixture, respectively, 0.9 - 1: 0.9 - 1.

 The arches obtained as a result of cutting long pasta dried on bastunas are separated from the crumbs and sent for packaging as commercial products.

 Pasta can be packaged on a filling machine, which includes a proximity sensor mounted on the scales of a filling machine and having a generator, a signal amplifier and a key made on a transistor and a resistor, while a diode is connected in parallel with the latter, and a resistance is connected in series with the transistor base.

 Packaging can be carried out on an automated packaging line "Zambani".

 Pasta can be packaged on an automated packaging line that has a metering device with an adjustment element and a dispenser, which includes a bucket elevator, while the number of buckets of the latter is increased by at least eight and the total number of buckets is increased to at least forty, which extends the upper horizontal section of the elevator having a broken configuration with at least one horizontal and at least one vertical section and for more accurate dosing increase the maximum permissible value of the dissipation power of the control element by means of the parallel connection of two transistors.

 The arches are packed on an automated packaging machine, which is installed under the upper horizontal section of the bucket elevator.

 As an automated packaging machine can use the automated packaging machine "Pavan".

 Packaging can be carried out in hard or soft containers.

 As soft containers can use a film of polyethylene, or polyethylene terephthalate, or prolipropylene, or in the form of an adjacent composition of these materials, taken in any combination.

 Packaging can be carried out in a layered composition, the surfaces of which are metallized by spraying or by application of aluminum.

 Packaging can be carried out in a layered composition that does not transmit ultraviolet rays and the visible part of the solar spectrum and having at least one liner made of aluminum foil or aluminized materials.

 Packaging in hard or soft containers can be carried out with the filling of the internal volume of the latter with nitrogen.

 At least one layer of the layered composition can be impermeable to ultraviolet rays and other rays of the solar spectrum.

 Flour carriers may contain at least two containers that are installed on a car platform.

 Tanks can be installed on a railway platform.

 Capacities are fixed stationary, or with the possibility of measuring spatial orientation, or with the possibility of vibration of the housing.

 A flour truck can be fed to the unloading area using a cable and a winch.

 Example 1. To obtain special pasta “New” for kneading, a mixture of wheat flour of the first grade from durum wheat (durum) and wheat flour of the highest grade from durum wheat, taken in a mass ratio of 1: 1, the filtering surface of the container, in which is supplied with an air-to-air mixture, is assigned to exceed the area of the corresponding air-transparent portion of the surface of this container in 100 given diameters of the area of the air-transparent portion, the filter surface being made in the form of a spatial shell combined configuration with maximum distance from its top plane, combined with at least one rectilinear segment of the contour portion aeroprozrachnogo a distance equal to 50 listed aeroprozrachnogo diameter portion area.

 The capacity is connected by an additional duct to the suction unit.

 In this case, the filtering surface is a filtering layer bonded to each other with the formation of cavities into which granular filler is introduced, which ensures complete separation of air from the flour mixture with a particle size of at least 30 μm.

Kneading the test is carried out with a humidity of 30%, while the temperature of the water for kneading is 30 ^o C, and the depth of the vacuum test 0.07 MPa. After kneading, the semi-finished product is formed by passing the dough at a pressure of 10.0 MPa through the forming matrix, which ensures the temperature of the formed semi-finished product at 45 ^o C. After this, the semi-finished product is hung on bastuns and sent to the drying chamber.

Drying is carried out to standard humidity at a temperature and air humidity in the first zone of 55 ^° C and 50%, in the second zone of 62 ^° C and 53%, in the third zone of 69 ^° C and 55%, in the fourth zone of 76 ^° C and 55%, in the fifth zone of 83 ^o C and 55%, in the sixth zone of 90 ^o C and 55%, in the seventh zone of 95 ^o C and 62%, in the eighth zone of 90 ^o C and 65%, in the ninth zone of 75 ^o C and 82%, in the tenth zone of 50 ^o C and 70% and in the eleventh zone of 30 ^o C and 65%. Moreover, upon reaching an air temperature of 90 ^o C and a humidity of 65%, it is forcibly removed from the premises.

 Dried convenience food is cut into temples and long pasta. Long pasta is sent for packaging in a soft container made of polyethylene, and the temples are separated from the crumbs and sent for packaging in a container made of cardboard.

 Thus, they receive special "New" pasta with the following quality indicators.

Chemical composition and energy value of 100 g of product:
Protein, g - 11.3
Fats, g - 1.5
Carbohydrates, g - 67.8
Minerals, kg
Potassium - 190.0
Calcium - 26.0
Phosphorus - 138.0
Vitamins mg
Thiamine (B ₁ ) - 0.28
Riboflavin (B ₂ ) - 0.08
Niacin (PP) - 2.95
Humidity, g - 12.0 g
Energy value, kcal - 337
In production, losses of raw materials were reduced by 0.2 kg per ton of finished products and due to the acceleration of the aspiration process, the total production time was reduced by 2.7%.

 Example 2. To obtain long pasta "Canteen" for kneading serves wheat flour of the second grade from durum wheat (durum), then the method is carried out according to example 1.

 Thus, special "Canteen" pasta is obtained with the following quality indicators.

Chemical composition and energy value of 100 g of product:
Proteins, g - 12.0
Fats, g - 1.8
Carbohydrates, g - 65.2
Minerals, mg
Potassium - 256
Calcium - 33
Phosphorus - 187
Vitamins mg
Thiamine (B ₁ ) - 0.38
Riboflavin (B ₂ ) - 0.12
Niacin (PP) - 4.67
Humidity, g - 12.0
Energy value, kcal - 332
Upon receipt of pasta, the loss of raw materials was reduced by 0.21 kg per ton of finished products, and due to the acceleration of the aspiration process, the total production time was reduced by 2.7%.

Claims (87)

 1. A method for producing pasta, which provides for pneumatic conveying of at least a portion of flour, and / or grains, and / or other loose components into main and / or reserve storage tanks equipped with lids, while simultaneously aspirating the air supplied by pneumatic conveying by connecting at least parts of containers for supplying flour, and / or grains, and / or other loose components with an aspiration unit and / or with each other with the possibility of combining and / or selective switching and the formation of a predetermined filtering area having a differentiated depending on the degree of dispersion of the component supplied by pneumatic conveying capacity of the surface of the container, preparing raw materials and water for kneading, kneading the dough and then evacuating it in the chambers of screw presses, molding the semi-finished product by passing the dough through the molding matrix, drying the molded semi-finished product in the dryer a chamber with climatic zones equipped with an air conditioning system, a condensate collector, communication for the removal of air conditioning sate and forced removal of moist air from the drying chamber, stabilization of dried pasta, sorting, packing and packaging, characterized in that the filtering surface of at least one container is formed in excess of the area of the corresponding air-transparent surface area of this container within 1.002 230.0 the given diameters of the area of the air-transparent section and the formation of the shape of the filtering surface in the form of a spatial shell of constant and / or variable curvature or combination hydrochloric configuration with its maximum distance from the top plane, combined with at least one rectilinear segment of the contour portion aeroprozrachnogo or the horizontal projection plane corresponding aeprozrachnogo portion by a distance of 0.02 78.0 aeroprozrachnogo reduced diameter portion area.  2. The method according to claim 1, characterized in that when carrying out the aspiration process, at least one air-filter insert is used as a filter surface, which is installed in the lid cavity of the main and / or reserve storage tanks, or at least one is used as a filter surface one air-filtering membrane serving simultaneously as the cover of the main and / or reserve storage tank, or at least one filter insert is used as a filter surface air, which is installed in the upper part of the wall of at least one main and / or reserve storage tank, and in this case the insert for filtering the supplied air is made in the form of a fragment of a cylindrical surface or double curvature, or in the form of a concave or convex or convex polyhedron relative to the surface of the walls of the tank, or in a combined form from a combination of straight and / or curved sections, or in the form of a continuous ring or discrete shell.  3. The method according to claim 1, characterized in that when carrying out the aspiration process, at least one air-filtering element is used as a filter surface, which is made in the form of a removable shell, while in the upper part of at least one main and / or backup storage containers make a cutout in which a shell with an air-filtering element is installed, the cut-out area being at least 1% of the cross-sectional area of the corresponding container with a multifaceted configuration or at least 2, 3% of the cross-sectional area of the corresponding capacity of circular cylindrical or variable curvature or combined configuration.  4. The method according to claim 1, characterized in that when carrying out the aspiration process, at least two air filter inserts, air filter membranes, inserts for filtering the supplied air and air filter elements are used as a filter surface, while the area ratio of any two filter elements is 1 1 15.  5. The method according to one of claims 1 to 4, characterized in that for sealing the main and backup storage tanks, any filter elements included in the filter surface are connected to the tanks by means of clamps with sealant, and at least some of the connections are detachable .  6. The method according to one of claims 1 to 4, characterized in that for maintenance or repair work during the suction process, the main and / or backup storage tanks are additionally equipped with airtight membranes, which are installed to ensure complete cessation of air supply to the filtering element to be replaced.  7. The method according to one of paragraphs.2 to 6, characterized in that the air filter insert, or air filter membrane, or insert for filtering the supplied air, or air filter element is made in the form of a shell containing at least one double curvature section, or at least one section single curvature, or combinations thereof, or from combinations of curved and / or straight sections.  8. The method according to claim 7, characterized in that during the aspiration process air is injected with the formation of a shell shape containing at least one cylindrical or poly-cylindrical section formed by at least two articulated fragments of cylinders of constant and variable curvature, interconnected directly or by internal diaphragms, or with the formation of a shell shape containing at least one conical or polyconic section formed from fragments of conical and / or polyconic curvature, soy dyed directly between each other or by means of internal diaphragms, or with the formation of a shell shape containing at least one cylindrical or multicylindrical section formed from fragments of cylindrical or polycylindered curvature, interconnected directly or through internal diaphragms, or with the formation of a shell shape containing at least one cylindrical and / or conical and / or spherical and / or spheroidal and / or ellipsoidal and / or parabolic and / or hyparo idnogo and / or toroidal portion.  9. The method according to claim 7 or 8, characterized in that the shell is provided with an internal frame.  10. The method according to one of claims 1 to 9, characterized in that the filtering surface is made of high-strength woven or fibrous non-woven material, moreover, for example, overcoat fabric is used as high-strength woven material, and for example, felt as a fibrous non-woven fabric. 11. The method according to one of claims 1 to 10, characterized in that the design for aspiration with a filter surface is made of at least two filter layers with different strength and transmittance, which are arranged in order to increase their strength and transmittance or fastened together the formation of cavities into which a powdered and / or granular filler is introduced, while the differentiated throughput in at least one layer is formed to provide a pressure differential between the internal it and its external surfaces in the range of 0.1 to 0.2 MPa at operating speeds of pneumatic delivery of dispersed particles suspended in the air flow, and the minimum cross-sectional area of the holes in the filtering surface is at least 60 μm ² .  12. The method according to one of claims 1 to 11, characterized in that the filtering surface is subjected to vibrational influences, ensuring the restoration of its transmittance.  13. The method according to p. 12, characterized in that the vibrational effects create by differential pressure in the tank.  14. The method according to one of claims 1 to 13, characterized in that for carrying out the aspiration process, additional containers are installed, which are equipped with filters and connected to a common aspiration system with additional air ducts.  15. The method according to p. 1, characterized in that the evacuation and molding of the test is carried out with forced cooling.  16. The method according to p. 15, characterized in that the forced cooling is carried out by introducing into the screw presses and molding matrixes of the corresponding forced cooling systems.  17. The method according to claim 1, characterized in that they use screw presses with air cooling of traction motors.  18. The method according to 17, characterized in that the air cooling of the traction electric motors is carried out using fans with an impeller, the blades of which are made of a heat-resistant material or composition containing a metal base and at least one layer of thermoplastic or ceramic.  19. The method according to p. 18, characterized in that the impeller has two or three blades.  20. The method according to p, characterized in that the impeller of the fan has four nine blades.  21. The method according to p. 18, characterized in that the fan impeller has twelve or more blades.  22. The method according to p. 18, characterized in that the impeller blades have a variable angle along the radius and / or along an arc of a circle of inclination relative to a plane normal to the axis of the impeller.  23. The method according to p. 18, characterized in that the front and rear edges of the impeller blades perform with a radial configuration.  24. The method according to p. 18, characterized in that the outer impeller blades are conjugated without kinks with the formation of a crescent-shaped contour that smoothly passes into a crescent-shaped contour having a lower curvature in the projection onto a plane normal to the axis of the impeller.  25. The method according to p. 18, characterized in that the blades give a hypovaroid twist.  26. The method according to p. 18, characterized in that the blades are arranged with an angular gap of 0.1 to 0.3 angular alignment formed by the front and rear edges of the blade.  27. The method according to p. 18, characterized in that for air cooling of the traction motors, an additional impeller is installed with the possibility of rotation in the opposite direction or with the possibility of fixation. 28. The method according to one of claims 1 to 17, characterized in that the filtering surface is differentiated depending on the degree of dispersion of the component supplied by the pneumatic conveyor with a throughput capacity that allows air to be separated from the particles of the supplied component of at least 10 microns in size, and the load of the raw conveyor motor is controlled waste and in case of overheating of the engine, it stops and stops the screw press and attachment or attachments, and forced removal from the drying chamber s is subjected to air at a temperature of 30 95 ^o C and a relative humidity of 62 83% which duct is removed from the manufacturing facility or to the atmosphere. 29. The method of claim 1, wherein the water prepared for the batch is fed into a storage tank, which is connected to the communication to drain condensate from the drying chamber with the possibility of completely draining the prepared water through a pipeline equipped with a valve, and forced removal from the drying chambers expose air with a temperature of 30 95 ^o C and a relative humidity of 62 83% which is diverted by the air duct outside the premises or into the atmosphere. 30. The method according to p. 1, characterized in that for kneading the dough using prepared water with a temperature of 20 45 ^o C, while the depth of the vacuum support within 0.07 0.08 MPa, and the humidity of the test 29 31%
31. The method according to claim 1, characterized in that the molding of the semi-finished product by passing the test through the molding matrix is carried out at a pressure of 10.0 to 11.5 MPa, and the temperature of the semi-finished product at the exit of the matrix is not more than 42 ^o C.  32. The method according to claim 1, characterized in that the drying of the semi-finished product is carried out in a drying chamber having at least eleven climatic zones, with differentially maintained air temperature and humidity.  33. The method according to p, characterized in that the drying of the semi-finished product is carried out by sequentially raising and lowering the temperature and relative humidity in the climatic zones of the drying chamber, while increasing the temperature is carried out in the first seventh zones, and the decrease in the eighth eleventh. 34. The method according to p. 33, characterized in that the temperature increase in the first sixth climatic zones is carried out sequentially with an increase in temperature between each adjacent climatic zone of not more than 7 ^o C, while the temperature in the first zone is 55 ^o C. 35. The method according to p. 33, characterized in that the temperature increase in the sixth and seventh climatic zones is carried out by no more than 5 ^o C, while the temperature in the seventh climatic zone is 95 ^o C and is maximum. 36. The method according to p. 33, characterized in that the temperature is reduced between the seventh and eighth climatic zones by no more than 5 ^o C, between the eighth tenth zones, respectively, by no more than 15 ^o C, and between the tenth and eleventh zone no more than 20 ^o With that provides the temperature of the dried semi-finished product.  37. The method according to p. 33, characterized in that the increase in relative humidity from 50% of the original occurs with a gap in the zones from the relative increase in temperature and reaches a maximum, namely 81 83% in the ninth climatic zone, after which it is reduced up to 65% to the eleventh climatic zone.  38. The method according to one of paragraphs 32 to 37, characterized in that the required temperature and humidity in the climatic zones is maintained by conditioning with forced ventilation, thermostating and humidification of the supplied air, including using a refrigeration unit.  39. The method according to claim 1 or 37, characterized in that the forced removal from the drying chamber is subjected to air with maximum relative humidity.  40. The method according to one of claims 1, 38 and 39, characterized in that the air duct for forced removal of air with maximum relative humidity is equipped with a heat exchanger or economizer to select the waste heat, which is then returned for use in the air conditioning system.  41. The method according to claim 1, characterized in that vitamins and / or trace elements and / or oxidizing improvers are introduced into the flour.  42. The method according to paragraph 41, wherein the vitamins and / or trace elements and / or oxidative improvers are introduced into the flour during the grinding process.  43. The method according to paragraph 41, wherein the vitamins and / or trace elements and / or oxidative improvers are introduced into the flour in the process of feeding it to the pre-storage container.  44. The method according to paragraph 41, wherein the vitamins and / or trace elements and / or oxidative improvers are introduced into the flour in the process of feeding it into the main and / or reserve storage tanks.  45. The method according to claim 1, characterized in that when kneading, vitamins and / or microelements and / or surfactants are added to the dough.  46. The method according to item 45, wherein the surface-active substances are esters of sucrose and fatty acids, esters of polyoxyethylene and sorbitol, glycerol monoesters with fatty acids, condensation products of ethylene oxide with esters of glycerol and fatty acids and monoglycerides fatty acids, aliphatic acids and glycerin, sorbitol, propylene glycol and sugars.  47. The method according to claim 1, characterized in that the drying of the molded semi-factory is carried out on bastunas, or in tray cassettes, or on drying surfaces.  48. The method according to claim 1, characterized in that before packing the dried pasta is subjected to cutting, and the waste generated during the cutting process is sent to grinding and return to production.  49. The method according to claim 1, characterized in that the pasta is made filamentary.  50. The method according to 49, characterized in that the filamentary pasta is made short 2 20 cm long, longer than 20 cm long, while their diameter is 0.45 3.0 mm  51. The method according to p. 50, characterized in that the filamentary pasta is made with unequal cross-section.  52. The method according to one of paragraphs.47, 50 and 51, characterized in that the hanging of a long thread-like product with an unequal cross-section on the bastion is carried out by orienting the major axis of the cross-section of the product parallel to the axis of the bastion.  53. The method according to p. 50, characterized in that the filamentary pasta is made with a cross-sectional configuration in the form of an ellipsoid, or an oval, or a combined profile, including smooth and / or with a break in the coupling of curved sections with straight sections.  54. The method according to paragraph 52, wherein the ratio of the larger and smaller axes of the cross section of the product is 2 25 1, and the absolute value of the major axis is 1.5 12.0 mm  55. The method according to item 50, wherein the filamentary pasta is made with a cross section in the form of at least one double truncated ellipsoid, or double truncated svid, or articulation of truncated or doubly truncated round cylindrical elements, and / or ovals, and / or as a combination of the listed forms.  56. The method according to claim 1, characterized in that the pasta is made in the form of ribbon-like products.  57. The method according to p, characterized in that the width of the product is not less than 1.5 mm, the thickness is not more than 2 mm, while the products are made short 2 20 cm long and longer than 20 cm long.  58. The method according to clause 57, wherein the cross-section of the product has the configuration of a flat polyhedron and / or combined unequal profile.  59. The method according to one of paragraphs.47, 57 and 58, characterized in that the hanging of a long ribbon-like product on the bastion is carried out by the larger axis of the product parallel to the axis of the bastion.  60. The method according to claim 1, characterized in that the pasta is made tubular in the form of pasta, horns and feathers.  61. The method according to p. 60, characterized in that the outer diameter of the products is 2 30 mm, the products are made short with a length of 1.5 to 30.0 cm and longer than 30 cm.  62. The method according to p, characterized in that the product is made with a cross-sectional shape of round, or square, or grooved, or elliptical, or combined.  63. The method according to item 62, wherein the product is made with unequal cross-section.  64. The method according to item 62, wherein in the manufacture of products with a corrugated sectional shape, the corrugation is carried out external and / or internal.  65. The method according to p. 61 or 62, characterized in that the product is released curved or straight.  66. The method according to one of paragraphs 61, 62 and 65, characterized in that the products give a spiral axial twist.  67. The method according to claim 1, characterized in that the pasta is made curly of any shape and size, while the maximum thickness of any part of the product on the fracture should not exceed 1.5 3.0 mm  68. The method according to one of paragraphs.47, 50, 57 and 61, characterized in that the pasta is subjected to drying on bastuns. 69. The method according to claim 1, characterized in that the pasta is made with a moisture content of 12 13% protein content 11.1 11.8% fat 1.5 1.8% carbohydrates 64.4 66.5% potassium 0.189 0.253% calcium 0.025 0.033% phosphorus 0.136 0.186% vitamins B ₁ , B ₁ and PP the rest, while the energy value of 100 g of the finished product is 327 333 kcal.  70. The method according to claim 1 or 69, characterized in that in the manufacture of pasta type "Table" for kneading use wheat flour of the 1st or 2nd grade from durum durum wheat.  71. The method according to claim 1 or 69, characterized in that in the manufacture of pasta type "New" for kneading, a mixture of wheat flour of the 1st or 2nd grade from durum durum wheat and premium wheat flour from soft wheat is used when the mass ratio in the mixture, respectively, 0.7 0.1 0.9 1.0.  72. The method according to p. 48 or 68, characterized in that the arches are separated from the edges obtained by cutting long pasta dried on bastuns and sent to the packaging as commercial products.  73. The method according to one of claims 1 to 72, characterized in that the pasta is packaged on a filling machine, including a proximity sensor mounted on the scales of the filling machine and having a generator, signal amplifier and a key made on a transistor and a resistor, while parallel to the last a diode is on, and a resistance is connected in series to the transistor base.  74. The method according to claim 1, characterized in that the packaging is carried out on an automated packaging line "Zamboni".  75. The method according to claim 1 or 2, characterized in that the pasta is packaged on an automated packaging line having a metering device with an adjustment element and a dispensing device, which includes a bucket elevator, while the number of buckets of the latter is increased by at least eight and bring the total number of buckets to at least forty, which lengthens the upper horizontal section of the elevator, having a broken configuration with at least one horizontal and at least one vertical section, and for more its precise dosing increase the limit value of power dissipation adjusting member via a parallel connection of two transistors.  76. The method according to p. 68 or 72, characterized in that the packaging of the arms is carried out on an automated packaging machine, which is installed under the upper horizontal section of the bucket elevator.  77. The method according to claim 1, characterized in that the automated packaging machine "Pavan" is used as an automated packaging machine.  78. The method according to one of paragraphs.74 to 77, characterized in that the packaging is carried out in hard or soft containers.  79. The method according to p. 78, characterized in that as a soft container using a film of polyethylene, or polyethylene terephthalate, or prolipropylene, or in the form of an adjacent composition of these materials, taken in any combination.  80. The method according to p. 79, characterized in that the packaging is carried out in a layered composition, the surface of which is metallized by spraying or applications with aluminum.  81. The method according to p, characterized in that the packaging is carried out in a layered composition that does not transmit ultraviolet rays and the visible part of the solar spectrum and has at least one liner made of aluminum foil or aluminized materials.  82. The method according to p, characterized in that the packaging in hard or soft containers is carried out with the filling of the internal volume of the latter with nitrogen.  83. The method according to p. 81, characterized in that at least one layer of the layered composition is impermeable to ultraviolet rays and other rays of the solar spectrum.  84. The method according to claim 1, characterized in that the automated packaging machine "Pavan" is used as an automated packaging machine.  85. The method according to claim 1, characterized in that the flour carriers contain at least two containers that are installed on an automobile platform.  86. The method according to p, characterized in that the tank is installed on a railway platform.  87. The method according to p. 85 or 86, characterized in that the containers are fixed permanently, or with the possibility of changing the spatial orientation, or with the possibility of vibration of the housing.  88. The method according to claim 1, characterized in that the flour truck is fed to the unloading zone using a cable and a winch.

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