Abstract
The basis for the creation of new designs dryers laid the mathematical description of the test process, taking into account the method of loading and handling of the product in the machine, how to supply coolant or other type of energy supply, the theoretical performance, and structural (geometric) component of the apparatus. To simulate the process of our work was considered of cylindrical dryers with active hydrodynamic regime and microwave energy supply, one feature of which is the loading of the product in a stream tangential coolant flow. The object of the study was chosen millet grain, because of the high biological value and high prevalence in the southern regions of the Russian Federation. On the basis of theoretical analysis, it was decided to divide the mathematical model into two conditional components: the study of heat and mass transfer study of aerodynamic component of the drying process. In this paper, we have been disclosed in detail is the second part of the process. The basis of this model were the equations of motion of millet grains by Newton's second law. The coolant in the framework of the proposed model is considered to be a continuous medium, highly compressible and has an internal viscosity, described by the Navier-Stokes equations. The initial conditions of the mathematical model were the following assumptions: the speed of the mechanical motion elements are equal to zero, the initial density of the air environment in all nodes is the equilibrium density of the air, the initial velocity of the air quality in all nodes is zero. The boundary conditions can be described as the constancy of the flow temperature and humidity, and its displacement is directly design constraints of the drying chamber. This model will be useful for professionals engaged in the problems of calculation and design of drying equipment.
Highlights
The basis for the creation of new designs dryers laid the mathematical description of the test process
simulate the process of our work was considered of cylindrical dryers with active hydrodynamic regime and microwave energy supply
one feature of which is the loading of the product in a stream tangential coolant flow
Summary
В основу модели данного процесса закладываются две составляющие: движение двух различных сред (газообразная среда – теплоноситель и сыпучая среда – зерно проса), взаимодействующих друг с другом и с рабочими поверхностями сушильной камеры, и тепло- и массообменные процессы в зернах проса. В настоящей работе поставлена задача определения основных уравнений, начальных и граничных условий математической модели процесса движения зерна проса во взвешенно-закрученном слое, обладающую высокой детализацией и высокой адекватностью, базирующейся на общепринятых методах моделирования и физико-математического описания, но использующей в полной мере вычислительные возможности современных компьютеров. Для начала моделирования определяем количество одновременно находящихся в сушильной камере зерен проса, количество которых составляет порядка 104.
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