25 research outputs found

    Studying the temperature regime of the heliopyrolysis device reactor

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    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

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    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

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    "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

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    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

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    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 concentrator’s heliopyrolysis system to heat the pyrolysis reactor. Applying a solar concentrator to this type of pyrolysis device can achieve a temperature of 400–700 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, 8–20 % 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°Ρ‚Π΅Ρ€ΠΈΠ°Π»ΡŒΠ½Ρ‹ΠΉ баланс Π³Π΅Π»ΠΈΠΎΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π½ΠΎΠ³ΠΎ устройства

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    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 concentrator’s heliopyrolysis system to heat the pyrolysis reactor. Applying a solar concentrator to this type of pyrolysis device can achieve a temperature of 400–700 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, 8–20 % 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.. ΠŸΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Π° тСхнологичСская схСма процСсса получСния Π°Π»ΡŒΡ‚Π΅Ρ€Π½Π°Ρ‚ΠΈΠ²Π½ΠΎΠ³ΠΎ Ρ‚ΠΎΠΏΠ»ΠΈΠ²Π° ΠΈΠ· мСстной биомассы ΠΌΠ΅Ρ‚ΠΎΠ΄ΠΎΠΌ Π³Π΅Π»ΠΈΠΎΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π°. ΠŸΡ€ΠΎΠ°Π½Π°Π»ΠΈΠ·ΠΈΡ€ΠΎΠ²Π°Π½Ρ‹ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½Ρ‹ΠΉ Ρ€Π΅ΠΆΠΈΠΌ Π² Ρ€Π΅Π°ΠΊΡ‚ΠΎΡ€Π΅ ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π½ΠΎΠΉ установки, экономия Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ энСргии, расходуСмой Π½Π° ΠΊΠΎΠ½ΠΊΡ€Π΅Ρ‚Π½Ρ‹Π΅ Π½ΡƒΠΆΠ΄Ρ‹ оборудования, Π° Ρ‚Π°ΠΊΠΆΠ΅ тСпловая ΠΏΡ€ΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΡΡ‚ΡŒ установки. Π‘Π½ΠΈΠΆΠ΅Π½ΠΈΠ΅ энСргопотрСблСния Π² Ρ‚Π΅Ρ…Π½ΠΎΠ»ΠΎΠ³ΠΈΠΈ ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π° являСтся ΡΠ΅Ρ€ΡŒΠ΅Π·Π½ΠΎΠΉ ΠΏΡ€ΠΎΠ±Π»Π΅ΠΌΠΎΠΉ. Π­Ρ‚ΠΎ связано с Π½Π΅ΠΎΠ±Ρ…ΠΎΠ΄ΠΈΠΌΠΎΡΡ‚ΡŒΡŽ ΠΏΠΎΠ΄Π²ΠΎΠ΄Π° энСргии (Ρ‚Π΅ΠΏΠ»ΠΎΡ‚Ρ‹) для поддСрТания Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½ΠΎΠ³ΠΎ Ρ€Π΅ΠΆΠΈΠΌΠ° Ρ€Π΅Π°ΠΊΡ‚ΠΎΡ€Π°, Π΄ΠΎΠΏΠΎΠ»Π½ΠΈΡ‚Π΅Π»ΡŒΠ½ΠΎΠ³ΠΎ Π½Π°Π³Ρ€Π΅Π²Π° биомассы, Π° Ρ‚Π°ΠΊΠΆΠ΅ особСнностями процСсса разлоТСния ΠΎΡ‚Ρ…ΠΎΠ΄ΠΎΠ², для ΠΊΠΎΡ‚ΠΎΡ€ΠΎΠ³ΠΎ трСбуСтся ΠΎΡ‡Π΅Π½ΡŒ большая тСпловая энСргия. ΠžΠ±Ρ‹Ρ‡Π½ΠΎ ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ· осущСствляСтся Π·Π° счСт потрСблСния угля, ΠΏΡ€ΠΈΡ€ΠΎΠ΄Π½ΠΎΠ³ΠΎ Π³Π°Π·Π° ΠΈΠ»ΠΈ элСктроэнСргии. Π’ ΡΡ‚Π°Ρ‚ΡŒΠ΅ ΠΏΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½ΠΎ ΠΈΡΠΏΠΎΠ»ΡŒΠ·ΠΎΠ²Π°Ρ‚ΡŒ для ΠΎΠ±ΠΎΠ³Ρ€Π΅Π²Π° ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π½ΠΎΠ³ΠΎ Ρ€Π΅Π°ΠΊΡ‚ΠΎΡ€Π° Π³Π΅Π»ΠΈΠΎΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π½ΡƒΡŽ систСму с ΠΏΠ°Ρ€Π°Π±ΠΎΠ»ΠΎ-цилиндричСским солнСчным ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ‚ΠΎΡ€ΠΎΠΌ, Ρ‡Ρ‚ΠΎ позволяСт Π΄ΠΎΡΡ‚ΠΈΡ‡ΡŒ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Ρ‹ 400–700 Β°C. Π Π°Π·Ρ€Π°Π±ΠΎΡ‚Π°Π½Π° ΠΏΡ€ΠΈΠ½Ρ†ΠΈΠΏΠΈΠ°Π»ΡŒΠ½Π°Ρ схСма ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½ΠΎΠΉ ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π½ΠΎΠΉ установки солнСчного ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ‚ΠΎΡ€Π° ΠΈ ΠΏΠΎΠ»ΡƒΡ‡Π΅Π½Ρ‹ ΠΎΠ±Ρ€Π°Π·Ρ†Ρ‹ Π°Π»ΡŒΡ‚Π΅Ρ€Π½Π°Ρ‚ΠΈΠ²Π½Ρ‹Ρ… Ρ‚ΠΎΠΏΠ»ΠΈΠ². Π’Π°ΠΊ, тСрмичСская ΠΏΠ΅Ρ€Π΅Ρ€Π°Π±ΠΎΡ‚ΠΊΠ° стСблСй Ρ…Π»ΠΎΠΏΡ‡Π°Ρ‚Π½ΠΈΠΊΠ° Π΄Π°Π»Π° ΠΎΠΊΠΎΠ»ΠΎ 20 % ΠΏΠΈΡ€ΠΎΠ³Π°Π·Π°, 60 % ΠΆΠΈΠ΄ΠΊΠΎΠ³ΠΎ Ρ‚ΠΎΠΏΠ»ΠΈΠ²Π°, 8–20 % Ρ‚Π²Π΅Ρ€Π΄ΠΎΠ³ΠΎ Π°Π»ΡŒΡ‚Π΅Ρ€Π½Π°Ρ‚ΠΈΠ²Π½ΠΎΠ³ΠΎ Ρ‚ΠΎΠΏΠ»ΠΈΠ²Π° ΠΏΡ€ΠΈ Π·Π°Π³Ρ€ΡƒΠ·ΠΊΠ΅ исходной биомассы 3,76 ΠΊΠ³. РассмотрСн Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ ΠΈ ΠΌΠ°Ρ‚Π΅Ρ€ΠΈΠ°Π»ΡŒΠ½Ρ‹ΠΉ баланс установки. Показано, Ρ‡Ρ‚ΠΎ ΠΏΡ€ΠΈΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ солнСчного ΠΊΠΎΠ½Ρ†Π΅Π½Ρ‚Ρ€Π°Ρ‚ΠΎΡ€Π° позволяСт ΡƒΠΌΠ΅Π½ΡŒΡˆΠΈΡ‚ΡŒ ΡƒΠ΄Π΅Π»ΡŒΠ½Ρ‹Π΅ энСргозатраты Π½Π° процСсс ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π° Π΄ΠΎ 30 %. ΠŸΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Π½Π°Ρ гСлиопиролизная установка сниТаСт расход Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠΉ энСргии Π½Π° собствСнныС Π½ΡƒΠΆΠ΄Ρ‹, ΠΏΠΎΠ²Ρ‹ΡˆΠ°Π΅Ρ‚ ΠΎΠ±Ρ‰ΠΈΠΉ коэффициСнт ΠΏΠΎΠ»Π΅Π·Π½ΠΎΠ³ΠΎ дСйствия ΠΈ обСспСчиваСт ΡΡ‚Π°Π±ΠΈΠ»ΡŒΠ½Ρ‹ΠΉ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½Ρ‹ΠΉ Ρ€Π΅ΠΆΠΈΠΌ ΠΏΠΈΡ€ΠΎΠ»ΠΈΠ·Π°

    Study of the physico-chemical properties of goat meat in order to justify the production of children's food products

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    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)

    ΠœΠ°Ρ‚Π΅ΠΌΠ°Ρ‚ΠΈΡ‡Π΅ΡΠΊΠΎΠ΅ ΠΌΠΎΠ΄Π΅Π»ΠΈΡ€ΠΎΠ²Π°Π½ΠΈΠ΅ ΠΊΠΎΠΌΠ±ΠΈΠ½ΠΈΡ€ΠΎΠ²Π°Π½Π½ΠΎΠΉ систСмы тСплоснабТСния солнСчного Π΄ΠΎΠΌΠ°)

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    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.Вопросы экономии Ρ‚ΠΎΠΏΠ»ΠΈΠ²Π½ΠΎ-энСргСтичСских рСсурсов, ΠΏΠΎΠ²Ρ‹ΡˆΠ΅Π½ΠΈΡ эффСктивности систСм тСплоснабТСния ΠΆΠΈΠ»Ρ‹Ρ… ΠΏΠΎΠΌΠ΅Ρ‰Π΅Π½ΠΈΠΉ, Π° Ρ‚Π°ΠΊΠΆΠ΅ использования устройств Π½Π° основС возобновляСмых источников энСргии Π½Π° сСгодняшний дСнь ΠΈΠΌΠ΅ΡŽΡ‚ ΠΎΡΠΎΠ±ΡƒΡŽ Π°ΠΊΡ‚ΡƒΠ°Π»ΡŒΠ½ΠΎΡΡ‚ΡŒ. ЦСль ΡΡ‚Π°Ρ‚ΡŒΠΈ – Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚Π°Ρ‚ΡŒ ΠΌΠ°Ρ‚Π΅ΠΌΠ°Ρ‚ΠΈΡ‡Π΅ΡΠΊΡƒΡŽ модСль Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ баланса ΠΈ провСсти тСорСтичСскоС исслСдованиС одноэтаТных ΡΠ΅Π»ΡŒΡΠΊΠΈΡ… Π΄ΠΎΠΌΠΎΠ², ΠΈΡΠΏΠΎΠ»ΡŒΠ·ΡƒΡŽΡ‰ΠΈΡ… ΡΠΎΠ»Π½Π΅Ρ‡Π½ΡƒΡŽ ΡΠ½Π΅Ρ€Π³ΠΈΡŽ Π² нСстационарном Ρ€Π΅ΠΆΠΈΠΌΠ΅. Для Π΅Π΅ Ρ€Π΅Π°Π»ΠΈΠ·Π°Ρ†ΠΈΠΈ построСн ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½Ρ‹ΠΉ одноэтаТный солнСчный Π΄ΠΎΠΌ с Π°Π²Ρ‚ΠΎΠ½ΠΎΠΌΠ½Ρ‹ΠΌ тСплоснабТСниСм Π½Π° основС прСимущСствСнно солнСчной энСргии. Π’ случаях, Ссли Π½Π°Π³Ρ€ΡƒΠ·ΠΊΠ° Π½Π° тСплоснабТСниС ΠΏΡ€Π΅Π²Ρ‹ΡˆΠ°Π΅Ρ‚ ΡΠΎΠ»Π½Π΅Ρ‡Π½ΡƒΡŽ Π½Π°Π³Ρ€ΡƒΠ·ΠΊΡƒ, примСняСтся Ρ‚Ρ€Π°Π΄ΠΈΡ†ΠΈΠΎΠ½Π½ΠΎΠ΅ ΠΊΠΎΡ‚Π΅Π»ΡŒΠ½ΠΎΠ΅ устройство. ЭлСктроснабТСниС ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° обСспСчиваСтся солнСчной панСлью (фотоэлСктричСским ΠΏΡ€Π΅ΠΎΠ±Ρ€Π°Π·ΠΎΠ²Π°Ρ‚Π΅Π»Π΅ΠΌ). ΠŸΡ€Π΅Π΄Π»ΠΎΠΆΠ΅Π½Ρ‹ схСма Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ баланса солнСчного Π΄ΠΎΠΌΠ° с Π°Π²Ρ‚ΠΎΠ½ΠΎΠΌΠ½Ρ‹ΠΌ тСплоснабТСниСм ΠΈ элСктротСпловая схСма физичСской ΠΌΠΎΠ΄Π΅Π»ΠΈ. На ΠΈΡ… основС Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚Π°Π½Ρ‹ матСматичСская модСль ΠΈ Π°Π»Π³ΠΎΡ€ΠΈΡ‚ΠΌ расчСта, Π±Π°Π·ΠΈΡ€ΡƒΡŽΡ‰ΠΈΠΉΡΡ Π½Π° ΡƒΡ€Π°Π²Π½Π΅Π½ΠΈΠΈ Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ баланса динамичСского состояния систСмы тСплоснабТСния ΡΠΊΡΠΏΠ΅Ρ€ΠΈΠΌΠ΅Π½Ρ‚Π°Π»ΡŒΠ½ΠΎΠ³ΠΎ Π΄ΠΎΠΌΠ° Π² нСстационарном Ρ€Π΅ΠΆΠΈΠΌΠ΅. ИсслСдовано влияниС тСплоСмкости стСновой конструкции Π½Π° Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½Ρ‹ΠΉ Ρ€Π΅ΠΆΠΈΠΌ здания. Π’ срСдС модСлирования MATLAB-Simulink построСны основныС Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Π½Ρ‹Π΅ характСристики, Π½Π° ΠΊΠΎΡ‚ΠΎΡ€Ρ‹Ρ… ΠΏΡ€ΠΎΠ°Π½Π°Π»ΠΈΠ·ΠΈΡ€ΠΎΠ²Π°Π½ΠΎ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Ρ‹ Π²Π½ΡƒΡ‚Ρ€Π΅Π½Π½Π΅Π³ΠΎ Π²ΠΎΠ·Π΄ΡƒΡ…Π° здания Π² зависимости ΠΎΡ‚ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Ρ‹ ΠΎΠΊΡ€ΡƒΠΆΠ°ΡŽΡ‰Π΅ΠΉ срСды. ΠŸΠΎΡΡ‚Ρ€ΠΎΠ΅Π½Π° ΠΌΠΎΠ΄ΡƒΠ»ΡŒΠ½Π°Ρ схСма динамичСской ΠΌΠΎΠ΄Π΅Π»ΠΈ, Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Ρ‹ экспСримСнта ΠΏΠΎ измСнСнию Π²ΠΎΠ·Π΄ΡƒΡ…Π° Π²Π½ΡƒΡ‚Ρ€ΠΈ солнСчного Π΄ΠΎΠΌΠ° ΠΈ Ρ‚Π΅ΠΌΠΏΠ΅Ρ€Π°Ρ‚ΡƒΡ€Ρ‹ Π½Π°Ρ€ΡƒΠΆΠ½ΠΎΠ³ΠΎ Π²ΠΎΠ·Π΄ΡƒΡ…Π° прСдставлСны Π² Π²ΠΈΠ΄Π΅ Π³Ρ€Π°Ρ„ΠΈΠΊΠ°. ΠœΠ°Ρ‚Π΅ΠΌΠ°Ρ‚ΠΈΡ‡Π΅ΡΠΊΠ°Ρ модСль Ρ‚Π΅ΠΏΠ»ΠΎΠ²ΠΎΠ³ΠΎ баланса здания Π² динамичСском Ρ€Π΅ΠΆΠΈΠΌΠ΅ ΠΈ Ρ€Π΅Π·ΡƒΠ»ΡŒΡ‚Π°Ρ‚Ρ‹ расчСтов ΠΌΠΎΠ³ΡƒΡ‚ ΠΈΡΠΏΠΎΠ»ΡŒΠ·ΠΎΠ²Π°Ρ‚ΡŒΡΡ ΠΏΡ€ΠΈ Ρ€Π°Π·Ρ€Π°Π±ΠΎΡ‚ΠΊΠ΅ энСргоэффСктивных солнСчных Π΄ΠΎΠΌΠΎΠ²
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