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WO2009005485A1 - Procédé de fabrication d'une poudre alimentaire à partir d'une matière première biologique et installation correspondante - Google Patents

Procédé de fabrication d'une poudre alimentaire à partir d'une matière première biologique et installation correspondante Download PDF

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Publication number
WO2009005485A1
WO2009005485A1 PCT/UA2008/000036 UA2008000036W WO2009005485A1 WO 2009005485 A1 WO2009005485 A1 WO 2009005485A1 UA 2008000036 W UA2008000036 W UA 2008000036W WO 2009005485 A1 WO2009005485 A1 WO 2009005485A1
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WIPO (PCT)
Prior art keywords
cyclone
drying chamber
raw materials
food powder
activator
Prior art date
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Ceased
Application number
PCT/UA2008/000036
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English (en)
Russian (ru)
Inventor
Aleksandr Illarionovich Judin
Svetlana Dmitrievna Judina
Sergey Aleksandrovych Judin
Yevgeniy Aleksandrovych Judin
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Individual
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Individual
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Publication of WO2009005485A1 publication Critical patent/WO2009005485A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
    • A23B7/00—Preservation of fruit or vegetables; Chemical ripening of fruit or vegetables
    • A23B7/02—Dehydrating; Subsequent reconstitution
    • A23B7/026—Spray-drying
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
    • A23B7/00—Preservation of fruit or vegetables; Chemical ripening of fruit or vegetables
    • A23B7/02—Dehydrating; Subsequent reconstitution
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/10—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
    • F26B17/101—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers the drying enclosure having the shape of one or a plurality of shafts or ducts, e.g. with substantially straight and vertical axis
    • F26B17/103—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers the drying enclosure having the shape of one or a plurality of shafts or ducts, e.g. with substantially straight and vertical axis with specific material feeding arrangements, e.g. combined with disintegrating means
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/005—Treatment of dryer exhaust gases

Definitions

  • the claimed group of inventions relates to the food industry, and in particular to technologies for producing powder from biological raw materials, and can be used in food, confectionery, food concentrate and other industries.
  • the main problem in the production of powders from biological raw materials is to obtain the final product of the required dispersion, not subject to clumping during storage, while maximally preserving all the properties of the original product in it, namely biologically active substances, vitamins, flavoring, aromatic, and other components.
  • a known method of producing food powder from biological 15 raw materials according to which pre-prepared biological raw materials are ground until a homogeneous mixture is formed, dried and ground
  • Drying is carried out by microwave currents while simultaneously grinding during spraying by ultrasonic vibrations with a frequency of 18-80 kHz.
  • the disadvantage of this method is the uneven degree of grinding of the prepared biological raw materials, due to its different initial viscosity, humidity and other rheological parameters, which leads to the production of food powder with a different 5 degree of dispersion.
  • the resulting food powder due to the high speed of movement of the particles during spraying, is electrified, which leads to its clumping during storage.
  • the known method requires the use of expensive equipment, complex and not sufficiently reliable in operation, which limits the scope of application of the known method.
  • the disadvantage of this method is the relatively low quality of the obtained product due to the low organoleptic properties of the food powder due to the uneven heating of the biological raw materials in the drying chamber, which leads to local overheating of the biological raw materials in the drying chamber and coagulation of proteins in the biological raw materials, which causes the appearance of extraneous odor not characteristic of processed raw materials.
  • the objective of the proposed method is to obtain food powder from biological raw materials with uniform dispersion and high biological value while maintaining the vitamin composition and organoleptic properties of the original biological raw materials.
  • Another objective of the claimed group of inventions is the development of technology and the creation of an installation for biologically active 5 moisture, in the form of a liquid concentrate extracted from biological raw materials.
  • the problem in part of the method, is solved by the fact that in the known method for producing food powder from biological raw materials, according to which a previously prepared crushed biological raw material is mixed until a homogeneous mixture is formed, it is fed into a drying chamber, where it is further crushed to obtain particles of a given dispersion by crushing on the activator and dried in a stream of gaseous coolant with a temperature of 80-165 0 C, moving in the upward direction with a speed of 1, 0-1, 5 free speed falling particles, which are then carried out of the drying chamber in
  • a gaseous heat carrier stream is introduced into the drying chamber along its axis in the direction of the activator, and moisture is taken from the moistened coolant in the water separator after removal a humidified coolant stream from said cyclone and irrigated with condensate previously isolated from a moistened coolant.
  • the installation contains a preliminary preparation unit of the initial biological raw material, where it is crushed to a puree state and mixed with dry vegetable components to a dry matter content of 20-30% in the mixture. Then the resulting mixture is sprayed in a stream of gaseous carbon dioxide with a temperature of 150-180 0 C and a pressure of 150-250 kPa. The mixture is dried in a drying chamber in the spray mode under vacuum with a residual pressure of not more than 50 kPa.
  • the disadvantages of the known installation is the low quality of the obtained powder due to the high drying temperature, which leads to coagulation of proteins and destruction of the molecules of biological raw materials and, consequently, to a deterioration of the biological properties of the obtained product, as well as an uneven degree of grinding of the prepared biological raw materials, due to its different initial viscosity and humidity.
  • the resulting product is not subject to long-term storage, since the resulting food powder is electrified due to the high atomization rate, which leads to its clumping during storage.
  • a known installation for producing food powder from biological raw materials containing a mixer, a drying chamber adjacent to the mixer, and a grinder (see patent of the Russian Federation N ° 2060670, IPC A23B 7/026, publ. 05.27.96).
  • the drying chamber is equipped with an ultrasonic atomizer and microwave emitters, and the grinder is made in the form of a rod-type ultrasonic atomizer installed in the drying chamber. Drying is carried out by microwave currents while grinding during spraying by ultrasonic vibrations with a frequency of 18-80 kHz.
  • a disadvantage of the known installation is to obtain the final product with different dispersion, due to uneven grinding
  • a known installation for producing food powder from biological raw materials adopted as a prototype, containing a preliminary preparation of biological raw materials, equipped with a mixer, a heat generator with an outlet pipe, a drying chamber, which is made in the form of a cylindrical body, in the lower part of which there is a chopper made in the form activator, and a cyclone for collecting food powder, equipped with inlet and outlet nozzles, while the upper part of the drying chamber is connected to the inlet of said cyclone and, in accordance with the patent of Ukraine Ns 46435, IPC A23B 7/026, publ. 05/15/2005
  • the heat generator is located in the pipe, which tangentially adjoins the cylindrical body of the drying chamber.
  • a disadvantage of the known installation is the relatively low quality of the obtained product, due to the low organoleptic properties of the food powder due to the uneven heating of biological raw materials located in the drying chamber, due to its sticking in the lower part of the drying chamber, in the area where the activator and heat generator pipes are located. This is due, first of all, to the tangential placement of the gaseous coolant inlet nozzles having a temperature of 80-165 0 C into the drying chamber, which leads to partial overheating of the biological feedstock in separate zones of the drying chamber and to coagulation of proteins in the biological feedstock located in these zones, which causes the burning of biological raw materials and the appearance of a foreign smell that worsens the organoleptic characteristics of the resulting food powder.
  • Another disadvantage of the known installation is the inability to isolate a biologically active liquid concentrate from biological raw materials.
  • the objective of the claimed group of inventions is also the creation of an installation designed to produce food powder from biological raw materials and providing a yield of finely divided final product with a high degree of purity, with high biological value while maintaining the vitamin composition and organoleptic properties of the original biological raw material.
  • Another objective of the claimed group of inventions is the creation of an installation for biologically active liquid concentrate extracted from biological raw materials.
  • the problem regarding the claimed installation, is solved by the fact that in the known installation for producing food powder from biological raw materials containing a preliminary preparation of biological raw materials, equipped with a mixer, a heat generator with an outlet pipe, a drying chamber, which is made in the form of a cylindrical body, in the lower part which has a chopper, made in the form of an activator, and a cyclone for collecting food powder, equipped with inlet and outlet nozzles, while the upper part of the soy drying chamber dinene with the inlet of the cyclone, according to the invention, the outlet of the heat generator is located along the axis of the drying chamber, while its nozzle is facing the activator, and the installation contains a moisture separator attached to the outlet of the cyclone for collecting food powder and equipped with a condensation unit with a condensate collection container, whose output equipped with a condensate atomization unit located in the outlet of said cyclone.
  • the inventive installation is equipped with at least one additional cyclone located in the technological scheme of the installation between the drying chamber and the cyclone for collecting food powder, while the inlet pipe of the additional cyclone is attached to the upper part of the drying chamber, and the outlet pipe to the inlet pipe of the cyclone for collecting food powder.
  • the technical result of the claimed group of inventions is to ensure the release of fine food powder with a high degree of purity, with high biological value while maintaining the vitamin composition and organoleptic properties of the original biological raw materials, as well as obtaining a biologically active liquid concentrate extracted from biological raw materials.
  • FIG. 1 shows a General view of the installation for obtaining food powder from biological raw materials
  • FIG. 2 is a private embodiment of the inventive installation.
  • the apparatus for producing food powder from biological raw materials contains a preliminary preparation of biological raw materials, equipped with a mixer 1, a heat generator 2 with an outlet pipe 3 and a drying chamber 4.
  • the drying chamber 4 is made in the form of a cylindrical body, in the lower part of which there is a chopper made in the form of an activator 5.
  • the installation also includes a cyclone 6 for collecting food powder, which is equipped with an inlet pipe 7 and an outlet pipe 8, while the upper part of the drying chamber 4 is connected to the inlet pipe 7 6.
  • the outlet pipe 3 of the heat generator 2 is located along the axis of the drying chamber 4, while its nozzle 9 is facing the activator 5.
  • the installation further comprises a moisture separator 10 connected to the outlet pipe 8 of the cyclone 6 and equipped with a condensing unit 11 with a capacity 12 for collecting condensate, the outlet of which is equipped with a condensate atomization unit 13 located in the outlet pipe 8 of the cyclone 6.
  • the installation contains a dispenser 14 and a container 15 for collecting food powder, which are adjacent to the drying chamber 4.
  • the cyclone 6 is also equipped with a hopper 16 for collecting schevogo powder.
  • the installation is equipped with an additional cyclone 17 located in the technological scheme of the installation between the drying chamber 4 and cyclone 6, while the inlet pipe 18 of the additional cyclone 17 is connected to the upper part of the drying chamber 4, and the outlet pipe 19 is connected to the inlet pipe of the cyclone 6.
  • Additional cyclone 17 is also provided with a hopper 20 for collecting food powder. Equipping the installation with an additional cyclone 17 provides an increase in the degree of purification of biologically active liquid concentrate extracted from biological raw materials.
  • the method of obtaining food powder from biological raw materials and biologically active liquid concentrate is as follows.
  • the pre-prepared crushed biological raw material which is a biological mass, in the form of pieces of chips or pulp, is fed into the mixer 1, where it is mixed until a homogeneous mixture is formed, which then passes through the batcher 14 into the cylindrical body of the drying chamber 4. Simultaneously with the biological raw material the drying chamber 4 is supplied with a gaseous coolant, which is heated with a heat generator 2 to a temperature of 80-165 0 C, in the drying chamber 4, the mixture of biological raw materials is further crushed until particles of a given dispersion are obtained by crushing on the activator 5.
  • the flow of gaseous coolant is introduced into the drying chamber 4 through the nozzle 9 along its axis in the direction of the activator 5, blowing it and preventing the formation of bedding zones and burning of particles of biological raw materials in the drying chamber 4.
  • the gaseous coolant moves in the upward direction in the form of a swirling flow using activator 5, picking up particles of biological raw materials, crushed on activator 5.
  • Particles of biological raw materials, moving s in a flow of coolant give moisture to the heat carrier, moving in an upward direction at a rate of 1, 0-1, 5 of particles free falling velocity. This ensures the active removal of moisture, both from the surface of the particles, and partial removal of free capillary moisture contained in biological raw materials, resulting in the formation of a stream of moistened heat carrier enriched with a gas-vapor mixture extracted from biological raw materials.
  • the effect of the high temperature of the gaseous coolant (80-165 0 C) on the biological feedstock during the drying process does not pose a risk of overheating of the biological feedstock, since the coolant temperature does not correspond to the temperature on the surface of the wet particles of the biological feedstock, on which the vapor-gas shell forms, protecting the feed particles from excessive heat.
  • the temperature on the surface of the particles of raw materials does not exceed 25-38 0 C.
  • the speed of the coolant chosen equal to 1, 0-1, 5, the free fall speed of the particles, allows them to circulate in the cylindrical body of the drying chamber 4, at which further crushing of the particles of raw materials until they reach the required degree of dispersion, and sufficient to remove surface and part of capillary moisture from the surface of the particles of raw materials.
  • a decrease in the velocity of the coolant below 1, 0 of the speed of free fall of particles prevents the removal of particles of a given dispersion from the working zone of the drying chamber 4 and leads to their further grinding, and an excess of the speed of the coolant above 1, 5 of the speed of free fall of particles leads to the removal of particles with a larger , in comparison with the set dispersion.
  • the formation of raw material particles of a given dispersion is accompanied by a corresponding release of additional capillary moisture until the final moisture content of the resulting food powder is 6-8%.
  • the selected temperature equal to 80-165 0 C, contributes to the rapid transition of capillary moisture into the vapor-gas mixture.
  • An increase in the temperature of the coolant is irrational, since it leads to an increase in energy consumption, and a decrease in temperature leads to a decrease in the efficiency of moisture extraction. Active collection of moisture from the particles of raw materials occurs in the drying chamber 4 for 10-50 s.
  • the released vapor-gas mixture moisturizes the gaseous the coolant in the cylindrical body of the drying chamber 4 and, together with the particles obtained, the moistened coolant is discharged from the drying chamber 4 through the inlet pipe 7 to the cyclone 6 to collect food powder.
  • the particles of biological raw materials separated from the heat carrier flow in cyclone 6 have preset dispersion and are food powder of the required humidity with maximum preservation of the vitamin composition and organoleptic properties of the initial biological raw material in the final product.
  • moisture is taken from the humidified coolant stream, condensed in the condensation unit i5 11 and collected in a container 12 for collecting condensate.
  • the condensate from the tank 12 is re-sent to irrigate the humidified coolant leaving the cyclone to collect food powder, for which it is introduced into the outlet pipe 8 of the cyclone 6 through the condensate atomization unit 13. This allows to improve the quality of the obtained liquid condensate extracted from biological raw materials, with maximum preservation in it of the organoleptic properties of the original biological raw materials.
  • the spent gaseous 5 coolant After passing the dehumidifier 10, the spent gaseous 5 coolant is discharged into the atmosphere.
  • the stream of moistened coolant, together with the obtained particles of biological raw materials is removed from the drying chamber 4 through the inlet pipe 18 to an additional cyclone 17.
  • an additional cyclone 17 the initial particles of biological raw materials are extracted from the coolant stream and the food powder is collected in the hopper 20. Then, the outlet of the gaseous coolant stream, together with the remaining particles of biological raw materials, is removed to the cyclone 6, where it is carried out final separation of the food powder from the coolant stream.
  • Example 1 As a pre-prepared biological raw material, 20 kg of crushed apples were taken, which were loaded into mixer 1. As a result of their processing in mixer 1, we obtained a homogeneous homogeneous mixture with a moisture content of 88%, which was introduced into drying chamber 4, where it was subjected to preliminary crushing on activator 5. At the same time, a gas-like coolant stream with a temperature of 125 ° C was introduced into drying chamber 4, which was fed axially to the zone of activator 5. The resulting particles of biological raw materials 40 ⁇ m in size worked in the flow of the coolant moving in the upward direction with a speed of 8 m / s, which was 1, 5 the speed of free fall of particles in the drying chamber 4.
  • the stream of moistened coolant enriched in a gas-vapor mixture obtained from biological raw materials, together with particles of food powder was carried out from the drying chamber 4 through the inlet pipe 7 to the cyclone 6 (see Fig. 1), where the food powder was captured.
  • the total drying time of 20 kg of feedstock was 1.5 hours, and the yield of the obtained powder with a moisture content of 6% was 3.480 kg.
  • the moistened coolant flow entered the moisture separator 10, where moisture was taken from the moistened flow coolant, its condensation in the condensing unit 11 and accumulation in the tank 12 for collecting condensate.
  • the amount of condensate was 4.96 liters.
  • Example 2 As a pre-prepared biological material was taken 20 kg of boiled chicken meat, which was loaded into the mixer 1. As a result of its processing in the mixer 1, a milled homogeneous mixture with a moisture content of 82% was obtained, which was introduced into the drying chamber 2. At the same time, in the drying chamber 4 gas-injected coolant flow with a temperature 9O 0 C, which was fed axially into the activator location zone 5. The resulting particle size of 75 microns biological raw material treated in a stream of coolant, peremeschayuschegos in the ascending direction at a speed of 8 m / s, which was 1.5 the speed of free fall of particles in the drying chamber 4.
  • the total drying time of 20 kg of feedstock was 0.3 h, and the yield of the obtained powder with a moisture content of 10% was 4 kg.
  • Example 3 As a pre-prepared biological material was taken 10 kg of garlic with a moisture content of 78%.
  • a grated homogeneous mixture was obtained, which was introduced into the drying chamber 4 at a coolant temperature of 100 0 C, where it was subjected to preliminary crushing on the activator 5.
  • the obtained particles of biological raw materials of 30 ⁇ m in size were processed in a flow of a coolant moving in the upward direction at a speed of 7.5 m / s, which was 1, 1 of the speed of free fall of particles in the drying chamber 4.
  • the processing of the initial biological raw material lasted 0.8 hours, and the yield of the obtained powder was 7.5% amounted to 1, 876 kg.
  • the collected amount of condensate was 2.76 liters.
  • the processing of the source of biological raw materials lasted 12.1 hours, and the yield of the obtained powder with a moisture content of 6.1% was 5.1 kg.
  • the humidified coolant flow entered the dehumidifier 10, where moisture was taken from the carrier fluid, its condensation in the condensation unit 11 and filling in the tank 12 for condensate collection.
  • the amount of condensate collected was 14.9 liters.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Zoology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Wood Science & Technology (AREA)
  • General Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Freezing, Cooling And Drying Of Foods (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Beans For Foods Or Fodder (AREA)

Abstract

L'invention concerne l'industrie alimentaire. Dans cette invention, un procédé de fabrication d'une poudre alimentaire à partir d'une matière première biologique consiste à mélanger la matière première broyée, à l'acheminer dans une chambre de séchage où elle subit un broyage supplémentaire sur activateur, et à la sécher dans un flux de caloporteur gazeux qui est injecté dans la chambre de séchage le long de son axe dans la direction de l'activateur. Les particules séchées avec le flux d'air humidifié sont introduites dans un cyclone. L'évacuation d'humidité à partir du caloporteur humidifié est effectué dans un séparateur d'humidité après la sortie du cyclone du flux de caloporteur humidifié et après son aspersion avec du condensat préalablement obtenu à partir du caloporteur humidifié. L'installation pour fabriquer de la poudre alimentaire comprend une unité de séchage préalable de la matière première avec un mélangeur, un générateur de chaleur avec une tubulure de sortie, une chambre de séchage se présentant comme un corps cylindrique et dans la partie inférieure de laquelle on a monté une broyeuse se présentant comme un activateur ainsi qu'un cyclone de collecte de poudre. La partie supérieure de la chambre de séchage est reliée à la tubulure d'entrée du cyclone. La tubulure de sortie du générateur de chaleur est disposée le long de l'axe de la chambre de séchage, et sa buse est orientée vers l'actionneur. L'installation comprend un séparateur d'humidité, raccordé à la tubulure du cyclone à des fins de collecte de poudre et doté d'un appareil de condensation avec un récipient de collecte de condensat dont la sortie est équipée avec une unité de pulvérisation de condensat disposée dans la tubulure de sortie du cyclone.
PCT/UA2008/000036 2007-07-02 2008-06-18 Procédé de fabrication d'une poudre alimentaire à partir d'une matière première biologique et installation correspondante Ceased WO2009005485A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UAA200707444A UA85769C2 (ru) 2007-07-02 2007-07-02 Способ получения пищевого порошка и установка для его осуществления
UAA200707444 2007-07-02

Publications (1)

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WO2009005485A1 true WO2009005485A1 (fr) 2009-01-08

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PCT/UA2008/000036 Ceased WO2009005485A1 (fr) 2007-07-02 2008-06-18 Procédé de fabrication d'une poudre alimentaire à partir d'une matière première biologique et installation correspondante

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Country Link
RU (1) RU2381657C1 (fr)
UA (1) UA85769C2 (fr)
WO (1) WO2009005485A1 (fr)

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RU2637528C2 (ru) * 2016-03-09 2017-12-05 Василий Григорьевич Густинович Дезинтеграционно-конвективно-кондуктивный сушильный агрегат - устройство получения порошков из различных видов сельскохозяйственного сырья и дикоросов
RU2630315C1 (ru) * 2016-06-20 2017-09-07 Василий Григорьевич Густинович Состав для получения десертного блюда быстрого приготовления
RU2635572C1 (ru) * 2016-10-27 2017-11-14 Василий Григорьевич Густинович Пищевая добавка
RU2635574C1 (ru) * 2016-10-31 2017-11-14 Василий Григорьевич Густинович Пищевая добавка
RU2635573C1 (ru) * 2016-10-31 2017-11-14 Василий Григорьевич Густинович Пищевая добавка
RU2635576C1 (ru) * 2016-11-14 2017-11-14 Василий Григорьевич Густинович Пищевая добавка
RU2643717C1 (ru) * 2016-11-14 2018-02-05 Василий Григорьевич Густинович Пищевая добавка
RU2643716C1 (ru) * 2016-11-14 2018-02-05 Василий Григорьевич Густинович Пищевая добавка
RU2635575C1 (ru) * 2016-11-14 2017-11-14 Василий Григорьевич Густинович Пищевая добавка
RU2643720C1 (ru) * 2016-11-14 2018-02-05 Василий Григорьевич Густинович Пищевая добавка
RU2635446C1 (ru) * 2016-11-14 2017-11-13 Василий Григорьевич Густинович Пищевая добавка
RU2650901C1 (ru) * 2017-04-20 2018-04-18 Василий Григорьевич Густинович Состав теста для макаронных изделий
RU2650902C1 (ru) * 2017-05-03 2018-04-18 Василий Григорьевич Густинович Состав для приготовления хлебобулочных изделий
RU2650903C1 (ru) * 2017-05-10 2018-04-18 Василий Григорьевич Густинович Состав для производства мучных кондитерских изделий
RU2726441C1 (ru) * 2019-11-13 2020-07-14 Анатолий Тимофеевич Лариков Измельчитель пищевого продукта

Citations (3)

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Publication number Priority date Publication date Assignee Title
US2911036A (en) * 1955-01-03 1959-11-03 Melvin E Lazar Spray-drying apparatus
RU2060670C1 (ru) * 1993-11-11 1996-05-27 Всероссийский научно-исследовательский институт консервной и овощесушильной промышленности Способ получения фруктовых порошков для детского питания и установка для его осуществления
RU2246839C2 (ru) * 2001-07-16 2005-02-27 Александр Илларионович Юдин Способ получения порошка из растительного сырья и устройство для его осуществления

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2911036A (en) * 1955-01-03 1959-11-03 Melvin E Lazar Spray-drying apparatus
RU2060670C1 (ru) * 1993-11-11 1996-05-27 Всероссийский научно-исследовательский институт консервной и овощесушильной промышленности Способ получения фруктовых порошков для детского питания и установка для его осуществления
RU2246839C2 (ru) * 2001-07-16 2005-02-27 Александр Илларионович Юдин Способ получения порошка из растительного сырья и устройство для его осуществления

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RU2381657C1 (ru) 2010-02-20
UA85769C2 (ru) 2009-02-25
RU2008125733A (ru) 2009-12-27

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