25 research outputs found
Studying the temperature regime of the heliopyrolysis device reactor
The article presents the principle of the heliopyrolysis device with a solar concentrator and the temperature measurement scheme at the characteristic points of the reactor. Pyrolysis of organic waste was carried out according to the experimental method in laboratory conditions. Experiments were carried out on samples of organic waste (rubber, polyethylene film, plastic bottle) with an initial moisture content of 5Γ·20% and a size of 4Γ·6 mm. Based on the relationship between the amount of solar radiation and the ambient temperature for the city of Karshi (Uzbekistan), the experimental results of studying the temperatures inside the heliopyrolysis reactor when various organic wastes are loaded are presented. 0.25h according to the height of the reactor in the experiment; 0.35h; 0.25h; temperatures on the inner surface at distances of 0.15 h were recorded using the Mobile-CASSY 2 thermometer. It was determined that an average temperature of 350Γ·450 Β°C can be generated in the reactor of the experimental device. Experiments show that in the conditions of the city of Karshi, it is possible to create a mode of 300Γ·500Β°C sufficient for the pyrolysis of organic waste through a parabolic solar concentrator in the daytime mode
Evaluation of heat losses of the solar greenhouse during the heating season
The article presents the results of calculation of heat losses in greenhouses with different coatings, taking into account thermal-physical properties of coatings. In addition, based on the results of changes in external air temperature and solar radiation over time, numerical calculations were made on the heat load of a greenhouse with a useful area of 108 m2 and the thermal power provided by solar energy
Study of the Working Parameters of the Enzyme Protepsin and Its Effect on The Microstructure of Second-Grade Beef
"Protepsin" is an enzyme preparation of animal nature containing a complex of acid proteinases, intended for use in the meat industry for processing meat raw materials. The enzyme composition of the preparation is balanced according to the degree of exposure to various proteins of meat and meat systems used in the technology of obtaining meat products. "Protepsin" works in the meat system similarly to intracellular enzymes (cathepsins). It is their synergist and has additional qualities that allow it to act in a wider range of technological parameters, as well as to influence those protein systems on which intracellular enzymes do not act or have an effect to an insignificant extent [1]. The practical significance of the work lies in the fact that semismoked sausage products are in particular demand among the population. Cost reduction while maintaining their quality in a competitive environment is a time requirement. Therefore, the use of the enzyme is one of the promising directions in the field of meat processing [1]. The aim of the work is to study the working parameters of the enzyme "Protepsin" and its effect on the microstructure of second-grade beef. Histological changes characterize the positive effect of the enzyme on the development of meat quality indicators. In this regard, the processing of meat raw materials with "Protepsin" leads to a significant reduction in the duration of maturation of meat, which makes it possible to achieve the necessary changes in a shorter time compared with the natural way of autolysis
Mathematical Modeling of the Combined Heat Supply System of a Solar House
Today, increasing energy efficiency in residential heating systems, saving fuel and energy resources, and improving the efficiency of using devices based on renewable energy sources is an urgent issue. The purpose of the article is to develop a mathematical model of the heat balance and conduct a theoretical study of one-story rural houses based on the use of solar energy in a non-stationary mode. To achieve this goal, an experimental one-story solar house with autonomous heat supply was built. The heat supply of the experimental solar house mainly uses solar energy, and when the heat supply load exceeds this load, the traditional boiler device is used. The power supply of the experimental solar house is provided by a solar panel (photovoltaic converter). A heat balance scheme for a solar house with autonomous heat supply and an electrothermal scheme of a physical model are proposed. Based on the proposed schemes, a mathematical model of heat balance and a calculation algorithm based on the heat balance equation of the dynamic state of the heat supply system of a one-story experimental solar house in a non-stationary mode have been developed. On the basis of mathematical modeling, the influence of the heat capacity of the wall structure on the temperature regime of the building was studied. On the basis of the MATLAB-Simulink program, the main temperature characteristics were built, on which the change in the temperature of the internal air of the building was analyzed depending on the ambient temperature. On the basis of the program, a modular scheme of the dynamic model was built. Based on the modular scheme, the results of the experiment on changing the air inside the solar house and the outdoor temperature are presented in the form of a graph. The mathematical model of the thermal balance of the building in dynamic mode and the obtained calculation results are recommended for use in the development of energy-efficient solar houses
Heat and Material Balance of Heliopyrolysis Device
The article proposes a technological scheme for the process of obtaining alternative fuels from local biomass by the method of heliopyrolysis. Besides, the temperature regime in the reactor of the pyrolysis device and the thermal energy savings consumed for the specific needs of the device, as well as the thermal performance of the device are analyzed. It is known that reducing energy consumption in pyrolysis technology is a major challenge because energy (heat) must first be supplied to maintain the reactor temperature regime. Typically, the processes carried out in a pyrolysis unit are carried out at the expense of coal, natural gas or electricity consumption. For the operation very large amount of thermal energy is required to decompose biomass waste, and additional heating of biomass requires excessive energy consumption. To prevent these technological problems, the article proposes a solar concentratorβs heliopyrolysis system to heat the pyrolysis reactor. Applying a solar concentrator to this type of pyrolysis device can achieve a temperature of 400β700 Β°C. A schematic diagram of the experimental pyrolysis unit of the solar concentrator was developed, and samples of alternative fuels (pyrogas, liquid, solid fuels) were obtained as a result of thermal processing of biomass. Based on the analysis of the material balance of a heliopyrolysis plant with a parabolic-cylindrical solar concentrator, it was found that about 20 % pyrogas, 60 % liquid fuel, 8β20 % solid alternative fuel were obtained during the pyrolysis of cotton stalks with an initial biomass load of 3.76 kg. In order to determine the consumption of thermal energy in the pyrolysis process, as well as for the replaced solar energy, an analysis of the heat balance of the proposed installation was carried out. It is shown that the use of a solar concentrator makes it possible to reduce the specific energy consumption for the pyrolysis process by up to 30 %. The proposed heliopyrolysis device makes it possible to reduce the consumption of thermal energy for own needs, increase the overall efficiency of the installation and ensure a stable temperature regime for pyrolysis
Π’Π΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ ΠΈ ΠΌΠ°ΡΠ΅ΡΠΈΠ°Π»ΡΠ½ΡΠΉ Π±Π°Π»Π°Π½Ρ Π³Π΅Π»ΠΈΠΎΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½ΠΎΠ³ΠΎ ΡΡΡΡΠΎΠΉΡΡΠ²Π°
The article proposes a technological scheme for the process of obtaining alternative fuels from local biomass by the method of heliopyrolysis. Besides, the temperature regime in the reactor of the pyrolysis device and the thermal energy savings consumed for the specific needs of the device, as well as the thermal performance of the device are analyzed. It is known that reducing energy consumption in pyrolysis technology is a major challenge because energy (heat) must first be supplied to maintain the reactor temperature regime. Typically, the processes carried out in a pyrolysis unit are carried out at the expense of coal, natural gas or electricity consumption. For the operation very large amount of thermal energy is required to decompose biomass waste, and additional heating of biomass requires excessive energy consumption. To prevent these technological problems, the article proposes a solar concentratorβs heliopyrolysis system to heat the pyrolysis reactor. Applying a solar concentrator to this type of pyrolysis device can achieve a temperature of 400β700 Β°C. A schematic diagram of the experimental pyrolysis unit of the solar concentrator was developed, and samples of alternative fuels (pyrogas, liquid, solid fuels) were obtained as a result of thermal processing of biomass. Based on the analysis of the material balance of a heliopyrolysis plant with a parabolic-cylindrical solar concentrator, it was found that about 20 % pyrogas, 60 % liquid fuel, 8β20 % solid alternative fuel were obtained during the pyrolysis of cotton stalks with an initial biomass load of 3.76 kg. In order to determine the consumption of thermal energy in the pyrolysis process, as well as for the replaced solar energy, an analysis of the heat balance of the proposed installation was carried out. It is shown that the use of a solar concentrator makes it possible to reduce the specific energy consumption for the pyrolysis process by up to 30 %. The proposed heliopyrolysis device makes it possible to reduce the consumption of thermal energy for own needs, increase the overall efficiency of the installation and ensure a stable temperature regime for pyrolysis.. ΠΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π° ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΡΠ΅ΡΠΊΠ°Ρ ΡΡ
Π΅ΠΌΠ° ΠΏΡΠΎΡΠ΅ΡΡΠ° ΠΏΠΎΠ»ΡΡΠ΅Π½ΠΈΡ Π°Π»ΡΡΠ΅ΡΠ½Π°ΡΠΈΠ²Π½ΠΎΠ³ΠΎ ΡΠΎΠΏΠ»ΠΈΠ²Π° ΠΈΠ· ΠΌΠ΅ΡΡΠ½ΠΎΠΉ Π±ΠΈΠΎΠΌΠ°ΡΡΡ ΠΌΠ΅ΡΠΎΠ΄ΠΎΠΌ Π³Π΅Π»ΠΈΠΎΠΏΠΈΡΠΎΠ»ΠΈΠ·Π°. ΠΡΠΎΠ°Π½Π°Π»ΠΈΠ·ΠΈΡΠΎΠ²Π°Π½Ρ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΡΠΉ ΡΠ΅ΠΆΠΈΠΌ Π² ΡΠ΅Π°ΠΊΡΠΎΡΠ΅ ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½ΠΎΠΉ ΡΡΡΠ°Π½ΠΎΠ²ΠΊΠΈ, ΡΠΊΠΎΠ½ΠΎΠΌΠΈΡ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ, ΡΠ°ΡΡ
ΠΎΠ΄ΡΠ΅ΠΌΠΎΠΉ Π½Π° ΠΊΠΎΠ½ΠΊΡΠ΅ΡΠ½ΡΠ΅ Π½ΡΠΆΠ΄Ρ ΠΎΠ±ΠΎΡΡΠ΄ΠΎΠ²Π°Π½ΠΈΡ, Π° ΡΠ°ΠΊΠΆΠ΅ ΡΠ΅ΠΏΠ»ΠΎΠ²Π°Ρ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΡ ΡΡΡΠ°Π½ΠΎΠ²ΠΊΠΈ. Π‘Π½ΠΈΠΆΠ΅Π½ΠΈΠ΅ ΡΠ½Π΅ΡΠ³ΠΎΠΏΠΎΡΡΠ΅Π±Π»Π΅Π½ΠΈΡ Π² ΡΠ΅Ρ
Π½ΠΎΠ»ΠΎΠ³ΠΈΠΈ ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π° ΡΠ²Π»ΡΠ΅ΡΡΡ ΡΠ΅ΡΡΠ΅Π·Π½ΠΎΠΉ ΠΏΡΠΎΠ±Π»Π΅ΠΌΠΎΠΉ. ΠΡΠΎ ΡΠ²ΡΠ·Π°Π½ΠΎ Ρ Π½Π΅ΠΎΠ±Ρ
ΠΎΠ΄ΠΈΠΌΠΎΡΡΡΡ ΠΏΠΎΠ΄Π²ΠΎΠ΄Π° ΡΠ½Π΅ΡΠ³ΠΈΠΈ (ΡΠ΅ΠΏΠ»ΠΎΡΡ) Π΄Π»Ρ ΠΏΠΎΠ΄Π΄Π΅ΡΠΆΠ°Π½ΠΈΡ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΠΎΠ³ΠΎ ΡΠ΅ΠΆΠΈΠΌΠ° ΡΠ΅Π°ΠΊΡΠΎΡΠ°, Π΄ΠΎΠΏΠΎΠ»Π½ΠΈΡΠ΅Π»ΡΠ½ΠΎΠ³ΠΎ Π½Π°Π³ΡΠ΅Π²Π° Π±ΠΈΠΎΠΌΠ°ΡΡΡ, Π° ΡΠ°ΠΊΠΆΠ΅ ΠΎΡΠΎΠ±Π΅Π½Π½ΠΎΡΡΡΠΌΠΈ ΠΏΡΠΎΡΠ΅ΡΡΠ° ΡΠ°Π·Π»ΠΎΠΆΠ΅Π½ΠΈΡ ΠΎΡΡ
ΠΎΠ΄ΠΎΠ², Π΄Π»Ρ ΠΊΠΎΡΠΎΡΠΎΠ³ΠΎ ΡΡΠ΅Π±ΡΠ΅ΡΡΡ ΠΎΡΠ΅Π½Ρ Π±ΠΎΠ»ΡΡΠ°Ρ ΡΠ΅ΠΏΠ»ΠΎΠ²Π°Ρ ΡΠ½Π΅ΡΠ³ΠΈΡ. ΠΠ±ΡΡΠ½ΠΎ ΠΏΠΈΡΠΎΠ»ΠΈΠ· ΠΎΡΡΡΠ΅ΡΡΠ²Π»ΡΠ΅ΡΡΡ Π·Π° ΡΡΠ΅Ρ ΠΏΠΎΡΡΠ΅Π±Π»Π΅Π½ΠΈΡ ΡΠ³Π»Ρ, ΠΏΡΠΈΡΠΎΠ΄Π½ΠΎΠ³ΠΎ Π³Π°Π·Π° ΠΈΠ»ΠΈ ΡΠ»Π΅ΠΊΡΡΠΎΡΠ½Π΅ΡΠ³ΠΈΠΈ. Π ΡΡΠ°ΡΡΠ΅ ΠΏΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½ΠΎ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°ΡΡ Π΄Π»Ρ ΠΎΠ±ΠΎΠ³ΡΠ΅Π²Π° ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½ΠΎΠ³ΠΎ ΡΠ΅Π°ΠΊΡΠΎΡΠ° Π³Π΅Π»ΠΈΠΎΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½ΡΡ ΡΠΈΡΡΠ΅ΠΌΡ Ρ ΠΏΠ°ΡΠ°Π±ΠΎΠ»ΠΎ-ΡΠΈΠ»ΠΈΠ½Π΄ΡΠΈΡΠ΅ΡΠΊΠΈΠΌ ΡΠΎΠ»Π½Π΅ΡΠ½ΡΠΌ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΎΡΠΎΠΌ, ΡΡΠΎ ΠΏΠΎΠ·Π²ΠΎΠ»ΡΠ΅Ρ Π΄ΠΎΡΡΠΈΡΡ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ 400β700 Β°C. Π Π°Π·ΡΠ°Π±ΠΎΡΠ°Π½Π° ΠΏΡΠΈΠ½ΡΠΈΠΏΠΈΠ°Π»ΡΠ½Π°Ρ ΡΡ
Π΅ΠΌΠ° ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΎΠΉ ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½ΠΎΠΉ ΡΡΡΠ°Π½ΠΎΠ²ΠΊΠΈ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΎΡΠ° ΠΈ ΠΏΠΎΠ»ΡΡΠ΅Π½Ρ ΠΎΠ±ΡΠ°Π·ΡΡ Π°Π»ΡΡΠ΅ΡΠ½Π°ΡΠΈΠ²Π½ΡΡ
ΡΠΎΠΏΠ»ΠΈΠ². Π’Π°ΠΊ, ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠ° ΡΡΠ΅Π±Π»Π΅ΠΉ Ρ
Π»ΠΎΠΏΡΠ°ΡΠ½ΠΈΠΊΠ° Π΄Π°Π»Π° ΠΎΠΊΠΎΠ»ΠΎ 20 % ΠΏΠΈΡΠΎΠ³Π°Π·Π°, 60 % ΠΆΠΈΠ΄ΠΊΠΎΠ³ΠΎ ΡΠΎΠΏΠ»ΠΈΠ²Π°, 8β20 % ΡΠ²Π΅ΡΠ΄ΠΎΠ³ΠΎ Π°Π»ΡΡΠ΅ΡΠ½Π°ΡΠΈΠ²Π½ΠΎΠ³ΠΎ ΡΠΎΠΏΠ»ΠΈΠ²Π° ΠΏΡΠΈ Π·Π°Π³ΡΡΠ·ΠΊΠ΅ ΠΈΡΡ
ΠΎΠ΄Π½ΠΎΠΉ Π±ΠΈΠΎΠΌΠ°ΡΡΡ 3,76 ΠΊΠ³. Π Π°ΡΡΠΌΠΎΡΡΠ΅Π½ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ ΠΈ ΠΌΠ°ΡΠ΅ΡΠΈΠ°Π»ΡΠ½ΡΠΉ Π±Π°Π»Π°Π½Ρ ΡΡΡΠ°Π½ΠΎΠ²ΠΊΠΈ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ ΠΏΡΠΈΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠ³ΠΎ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΎΡΠ° ΠΏΠΎΠ·Π²ΠΎΠ»ΡΠ΅Ρ ΡΠΌΠ΅Π½ΡΡΠΈΡΡ ΡΠ΄Π΅Π»ΡΠ½ΡΠ΅ ΡΠ½Π΅ΡΠ³ΠΎΠ·Π°ΡΡΠ°ΡΡ Π½Π° ΠΏΡΠΎΡΠ΅ΡΡ ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π° Π΄ΠΎ 30 %. ΠΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Π½Π°Ρ Π³Π΅Π»ΠΈΠΎΠΏΠΈΡΠΎΠ»ΠΈΠ·Π½Π°Ρ ΡΡΡΠ°Π½ΠΎΠ²ΠΊΠ° ΡΠ½ΠΈΠΆΠ°Π΅Ρ ΡΠ°ΡΡ
ΠΎΠ΄ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ Π½Π° ΡΠΎΠ±ΡΡΠ²Π΅Π½Π½ΡΠ΅ Π½ΡΠΆΠ΄Ρ, ΠΏΠΎΠ²ΡΡΠ°Π΅Ρ ΠΎΠ±ΡΠΈΠΉ ΠΊΠΎΡΡΡΠΈΡΠΈΠ΅Π½Ρ ΠΏΠΎΠ»Π΅Π·Π½ΠΎΠ³ΠΎ Π΄Π΅ΠΉΡΡΠ²ΠΈΡ ΠΈ ΠΎΠ±Π΅ΡΠΏΠ΅ΡΠΈΠ²Π°Π΅Ρ ΡΡΠ°Π±ΠΈΠ»ΡΠ½ΡΠΉ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΡΠΉ ΡΠ΅ΠΆΠΈΠΌ ΠΏΠΈΡΠΎΠ»ΠΈΠ·Π°
Study of the physico-chemical properties of goat meat in order to justify the production of children's food products
The issue of rational nutrition of children is still extremely relevant and an effective factor ensuring the preservation of life and health of children. Pathological conditions associated with intolerance to certain components of food are increasingly common. Biologically complete products play an important role in the organization of rational nutrition of children, which can be created only in industrial production conditions. When assessing the chemical composition of experimental samples of goat meat (Zaanenskaya, Alpine, Nubian), no abnormal deviations were detected, and all indicators were in the generally accepted contents of this type of animal muscle tissue. The mineral composition showed that goat meat is rich in such elements as potassium - 1693.22-4125.83mg/kg; sodium - 852.27-1518 mg/kg, magnesium - 125.33-295.8 mg/kg; calcium - 79.27-160.79 mg/kg, iron 11.42-87.52 mg/kg. The vitamin composition of goat meat showed that the content of pantothenic acid (B5) was 0.53-0.62 mg/100g, pyridoxine (B6) 0.52-0.64 mg/100g tocopherol 0.27-0.33 mg/100g. The indicators of the mass fraction of goat meat proteins were 2.1 Β± 0.3- 2.4 Β± 0.4 %. The study of the dynamics of changes in the composition of protein fractions based on the results of comparative studies of the ratio of sarcoplasmic proteins showed the content of water-soluble (1.75-4.06 %), salt-soluble (1.75-2.44 %), alkali-soluble (11.15-15.10 %) proteins. The salt-soluble fraction reflects the total changes in the state of protein fractions, the solubility of which was not the same for the rocks under consideration (the highest concentration was determined in the Nubian rock)
ΠΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠΎΠ΅ ΠΌΠΎΠ΄Π΅Π»ΠΈΡΠΎΠ²Π°Π½ΠΈΠ΅ ΠΊΠΎΠΌΠ±ΠΈΠ½ΠΈΡΠΎΠ²Π°Π½Π½ΠΎΠΉ ΡΠΈΡΡΠ΅ΠΌΡ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΡ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ°)
Today, increasing energy efficiency in residential heating systems, saving fuel and energy resources, and improving the efficiency of using devices based on renewable energy sources is an urgent issue. The purpose of the article is to develop a mathematical model of the heat balance and conduct a theoretical study of one-story rural houses based on the use of solar energy in a non-stationary mode. To achieve this goal, an experimental one-story solar house with autonomous heat supply was built. The heat supply of the experimental solar house mainly uses solar energy, and when the heat supply load exceeds this load, the traditional boiler device is used. The power supply of the experimental solar house is provided by a solar panel (photovoltaic converter). A heat balance scheme for a solar house with autonomous heat supply and an electrothermal scheme of a physical model are proposed. Based on the proposed schemes, a mathematical model of heat balance and a calculation algorithm based on the heat balance equation of the dynamic state of the heat supply system of a one-story experimental solar house in a non-stationary mode have been developed. On the basis of mathematical modeling, the influence of the heat capacity of the wall structure on the temperature regime of the building was studied. On the basis of the MATLAB-Simulink program, the main temperature characteristics were built, on which the change in the temperature of the internal air of the building was analyzed depending on the ambient temperature. On the basis of the program, a modular scheme of the dynamic model was built. Based on the modular scheme, the results of the experiment on changing the air inside the solar house and the outdoor temperature are presented in the form of a graph. The mathematical model of the thermal balance of the building in dynamic mode and the obtained calculation results are recommended for use in the development of energy-efficient solar houses.ΠΠΎΠΏΡΠΎΡΡ ΡΠΊΠΎΠ½ΠΎΠΌΠΈΠΈ ΡΠΎΠΏΠ»ΠΈΠ²Π½ΠΎ-ΡΠ½Π΅ΡΠ³Π΅ΡΠΈΡΠ΅ΡΠΊΠΈΡ
ΡΠ΅ΡΡΡΡΠΎΠ², ΠΏΠΎΠ²ΡΡΠ΅Π½ΠΈΡ ΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΠΎΡΡΠΈ ΡΠΈΡΡΠ΅ΠΌ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΡ ΠΆΠΈΠ»ΡΡ
ΠΏΠΎΠΌΠ΅ΡΠ΅Π½ΠΈΠΉ, Π° ΡΠ°ΠΊΠΆΠ΅ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°Π½ΠΈΡ ΡΡΡΡΠΎΠΉΡΡΠ² Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ Π²ΠΎΠ·ΠΎΠ±Π½ΠΎΠ²Π»ΡΠ΅ΠΌΡΡ
ΠΈΡΡΠΎΡΠ½ΠΈΠΊΠΎΠ² ΡΠ½Π΅ΡΠ³ΠΈΠΈ Π½Π° ΡΠ΅Π³ΠΎΠ΄Π½ΡΡΠ½ΠΈΠΉ Π΄Π΅Π½Ρ ΠΈΠΌΠ΅ΡΡ ΠΎΡΠΎΠ±ΡΡ Π°ΠΊΡΡΠ°Π»ΡΠ½ΠΎΡΡΡ. Π¦Π΅Π»Ρ ΡΡΠ°ΡΡΠΈ β ΡΠ°Π·ΡΠ°Π±ΠΎΡΠ°ΡΡ ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΡΡ ΠΌΠΎΠ΄Π΅Π»Ρ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ Π±Π°Π»Π°Π½ΡΠ° ΠΈ ΠΏΡΠΎΠ²Π΅ΡΡΠΈ ΡΠ΅ΠΎΡΠ΅ΡΠΈΡΠ΅ΡΠΊΠΎΠ΅ ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΈΠ΅ ΠΎΠ΄Π½ΠΎΡΡΠ°ΠΆΠ½ΡΡ
ΡΠ΅Π»ΡΡΠΊΠΈΡ
Π΄ΠΎΠΌΠΎΠ², ΠΈΡΠΏΠΎΠ»ΡΠ·ΡΡΡΠΈΡ
ΡΠΎΠ»Π½Π΅ΡΠ½ΡΡ ΡΠ½Π΅ΡΠ³ΠΈΡ Π² Π½Π΅ΡΡΠ°ΡΠΈΠΎΠ½Π°ΡΠ½ΠΎΠΌ ΡΠ΅ΠΆΠΈΠΌΠ΅. ΠΠ»Ρ Π΅Π΅ ΡΠ΅Π°Π»ΠΈΠ·Π°ΡΠΈΠΈ ΠΏΠΎΡΡΡΠΎΠ΅Π½ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΡΠΉ ΠΎΠ΄Π½ΠΎΡΡΠ°ΠΆΠ½ΡΠΉ ΡΠΎΠ»Π½Π΅ΡΠ½ΡΠΉ Π΄ΠΎΠΌ Ρ Π°Π²ΡΠΎΠ½ΠΎΠΌΠ½ΡΠΌ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΠ΅ΠΌ Π½Π° ΠΎΡΠ½ΠΎΠ²Π΅ ΠΏΡΠ΅ΠΈΠΌΡΡΠ΅ΡΡΠ²Π΅Π½Π½ΠΎ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠΉ ΡΠ½Π΅ΡΠ³ΠΈΠΈ. Π ΡΠ»ΡΡΠ°ΡΡ
, Π΅ΡΠ»ΠΈ Π½Π°Π³ΡΡΠ·ΠΊΠ° Π½Π° ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΠ΅ ΠΏΡΠ΅Π²ΡΡΠ°Π΅Ρ ΡΠΎΠ»Π½Π΅ΡΠ½ΡΡ Π½Π°Π³ΡΡΠ·ΠΊΡ, ΠΏΡΠΈΠΌΠ΅Π½ΡΠ΅ΡΡΡ ΡΡΠ°Π΄ΠΈΡΠΈΠΎΠ½Π½ΠΎΠ΅ ΠΊΠΎΡΠ΅Π»ΡΠ½ΠΎΠ΅ ΡΡΡΡΠΎΠΉΡΡΠ²ΠΎ. ΠΠ»Π΅ΠΊΡΡΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΠ΅ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° ΠΎΠ±Π΅ΡΠΏΠ΅ΡΠΈΠ²Π°Π΅ΡΡΡ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠΉ ΠΏΠ°Π½Π΅Π»ΡΡ (ΡΠΎΡΠΎΡΠ»Π΅ΠΊΡΡΠΈΡΠ΅ΡΠΊΠΈΠΌ ΠΏΡΠ΅ΠΎΠ±ΡΠ°Π·ΠΎΠ²Π°ΡΠ΅Π»Π΅ΠΌ). ΠΡΠ΅Π΄Π»ΠΎΠΆΠ΅Π½Ρ ΡΡ
Π΅ΠΌΠ° ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ Π±Π°Π»Π°Π½ΡΠ° ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° Ρ Π°Π²ΡΠΎΠ½ΠΎΠΌΠ½ΡΠΌ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΠ΅ΠΌ ΠΈ ΡΠ»Π΅ΠΊΡΡΠΎΡΠ΅ΠΏΠ»ΠΎΠ²Π°Ρ ΡΡ
Π΅ΠΌΠ° ΡΠΈΠ·ΠΈΡΠ΅ΡΠΊΠΎΠΉ ΠΌΠΎΠ΄Π΅Π»ΠΈ. ΠΠ° ΠΈΡ
ΠΎΡΠ½ΠΎΠ²Π΅ ΡΠ°Π·ΡΠ°Π±ΠΎΡΠ°Π½Ρ ΠΌΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΌΠΎΠ΄Π΅Π»Ρ ΠΈ Π°Π»Π³ΠΎΡΠΈΡΠΌ ΡΠ°ΡΡΠ΅ΡΠ°, Π±Π°Π·ΠΈΡΡΡΡΠΈΠΉΡΡ Π½Π° ΡΡΠ°Π²Π½Π΅Π½ΠΈΠΈ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ Π±Π°Π»Π°Π½ΡΠ° Π΄ΠΈΠ½Π°ΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΡΠΎΡΡΠΎΡΠ½ΠΈΡ ΡΠΈΡΡΠ΅ΠΌΡ ΡΠ΅ΠΏΠ»ΠΎΡΠ½Π°Π±ΠΆΠ΅Π½ΠΈΡ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ°Π»ΡΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° Π² Π½Π΅ΡΡΠ°ΡΠΈΠΎΠ½Π°ΡΠ½ΠΎΠΌ ΡΠ΅ΠΆΠΈΠΌΠ΅. ΠΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½ΠΎ Π²Π»ΠΈΡΠ½ΠΈΠ΅ ΡΠ΅ΠΏΠ»ΠΎΠ΅ΠΌΠΊΠΎΡΡΠΈ ΡΡΠ΅Π½ΠΎΠ²ΠΎΠΉ ΠΊΠΎΠ½ΡΡΡΡΠΊΡΠΈΠΈ Π½Π° ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΡΠΉ ΡΠ΅ΠΆΠΈΠΌ Π·Π΄Π°Π½ΠΈΡ. Π ΡΡΠ΅Π΄Π΅ ΠΌΠΎΠ΄Π΅Π»ΠΈΡΠΎΠ²Π°Π½ΠΈΡ MATLAB-Simulink ΠΏΠΎΡΡΡΠΎΠ΅Π½Ρ ΠΎΡΠ½ΠΎΠ²Π½ΡΠ΅ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ½ΡΠ΅ Ρ
Π°ΡΠ°ΠΊΡΠ΅ΡΠΈΡΡΠΈΠΊΠΈ, Π½Π° ΠΊΠΎΡΠΎΡΡΡ
ΠΏΡΠΎΠ°Π½Π°Π»ΠΈΠ·ΠΈΡΠΎΠ²Π°Π½ΠΎ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ Π²Π½ΡΡΡΠ΅Π½Π½Π΅Π³ΠΎ Π²ΠΎΠ·Π΄ΡΡ
Π° Π·Π΄Π°Π½ΠΈΡ Π² Π·Π°Π²ΠΈΡΠΈΠΌΠΎΡΡΠΈ ΠΎΡ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ ΠΎΠΊΡΡΠΆΠ°ΡΡΠ΅ΠΉ ΡΡΠ΅Π΄Ρ. ΠΠΎΡΡΡΠΎΠ΅Π½Π° ΠΌΠΎΠ΄ΡΠ»ΡΠ½Π°Ρ ΡΡ
Π΅ΠΌΠ° Π΄ΠΈΠ½Π°ΠΌΠΈΡΠ΅ΡΠΊΠΎΠΉ ΠΌΠΎΠ΄Π΅Π»ΠΈ, ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΡΠΊΡΠΏΠ΅ΡΠΈΠΌΠ΅Π½ΡΠ° ΠΏΠΎ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΡ Π²ΠΎΠ·Π΄ΡΡ
Π° Π²Π½ΡΡΡΠΈ ΡΠΎΠ»Π½Π΅ΡΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° ΠΈ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΡ Π½Π°ΡΡΠΆΠ½ΠΎΠ³ΠΎ Π²ΠΎΠ·Π΄ΡΡ
Π° ΠΏΡΠ΅Π΄ΡΡΠ°Π²Π»Π΅Π½Ρ Π² Π²ΠΈΠ΄Π΅ Π³ΡΠ°ΡΠΈΠΊΠ°. ΠΠ°ΡΠ΅ΠΌΠ°ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΌΠΎΠ΄Π΅Π»Ρ ΡΠ΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ Π±Π°Π»Π°Π½ΡΠ° Π·Π΄Π°Π½ΠΈΡ Π² Π΄ΠΈΠ½Π°ΠΌΠΈΡΠ΅ΡΠΊΠΎΠΌ ΡΠ΅ΠΆΠΈΠΌΠ΅ ΠΈ ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΡ ΡΠ°ΡΡΠ΅ΡΠΎΠ² ΠΌΠΎΠ³ΡΡ ΠΈΡΠΏΠΎΠ»ΡΠ·ΠΎΠ²Π°ΡΡΡΡ ΠΏΡΠΈ ΡΠ°Π·ΡΠ°Π±ΠΎΡΠΊΠ΅ ΡΠ½Π΅ΡΠ³ΠΎΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΡΡ
ΡΠΎΠ»Π½Π΅ΡΠ½ΡΡ
Π΄ΠΎΠΌΠΎΠ²