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Heat transfer submodel

The master model consist of five submodels a) Kinetic submodel or crystallization submodel b) Heat transfer submodel c) Pressure model d) Pulling force submodel e) Residual stress submodel. Figure 3 shows the generalized scheme of the pultrusion process. [Pg.130]

Models for simulating the entire pultrusion process are primarily the same as with thermoset polymers (a) Heat Transfer Submodel, (b)Pressure Submodel for consolidation inside the taper, (c) Pulling Force Submodel. In contrast however, there are new difficulties such as non-Newtonian matrix flow, crystallization rate and matrix melting and solidification that must be accounted for. [Pg.145]

Kinetic models determine the minimum time required to cure the resin (i.e., guarantee sufficient physical and mechanical properties). They also determine the heat of reaction of the resin for use by heat transfer models and the degree of crosslinking for use in viscosity submodels. The exothermic cure reaction for the transformation of the epoxy resin to the cured matrix polymer can be expressed as ... [Pg.298]

The simulation program AIOLOS is developed for the numerical calculation of three-dimensional, stationary, turbulent and reacting flows in pulverised coal-fired utility boilers. AIOLOS contains submodels treating fluid flow, turbulence, combustion and heat transfer. In these submodels equations for calculating the conservation of mass, momentum and energy are solved, presupposing high Reynolds-numbers and steady-state flow conditions. It is assumed that the flow field is weakly compressible which means that the density depends only on temperature and fluid composition but not on pressure. [Pg.665]

Similar results are reported from the drying of bark and peat in superheated steam in a pilot-plant pneumatic conveying dryer [22], The results are presented as a convective apparent heat-transfer coefficient, defined with the assumption that the temperature of the particle surface coincides with the saturation temperature of the transport steam. This transfer coefficient shows a clear dependence on the moisture content of the particles and the particle sizes. Fyhr [23] presented a model for a pneumatic conveying steam dryer. The dryer model consists of two submodels, one for the single particle and the other for the hydrodynamics of gas and particles in the dryer. [Pg.737]

The remainder of the chapter focuses on the actual spray modeling. The exposition is primarily done for the RANS method, but with the indicated modifications, the methodology also applies to LES. The liquid phase is described by means of a probability density function (PDF). The various submodels needed to determine this PDF are derived from drop-drop and drop-gas interactions. These submodels include drop collisions, drop deformation, and drop breakup, as well as drop drag, drop evaporation, and chemical reactions. Also, the interaction between gas phase, liquid phase, turbulence, and chemistry is examined in some detail. Further, a discussion of the boundary conditions is given, in particular, a description of the wall functions used for the simulations of the boundary layers and the heat transfer between the gas and its confining walls. [Pg.384]

Within the framework of component development, CFD is used for scientific modeling and model validation in addition to the classical engineering parameter studies and optimization processes. Both approaches are based on the use of HPC calculation capacity. Within the framework of modeling and vahdation, HPC facilitates a complex representation of the physical phenomena with fine space and time discretization. With the aid of such submodels and appropriate laboratory experiments, models for nozzles, heat transfer phenomena, two-phase flow, and so on can be derived and vahdated. CFD models thus selected and validated form the basis for the CFD-based design and optimization of flow systems. The classical engineering problem of parameter variation and optimization requires a large number of simulation calculations and therefore leads to an extremely high cost of computation. HPC allows the parallelization of individual simulations, which in turn makes it possible to calculate several simulations simultaneously and thus enables comprehensive parameter studies and flow optimizations to be completed in an acceptable time frame. In the ATR 10 development process, CFD simulations were conducted on up to 16 cores of the JuRoPA supercomputer simultaneously. This meant that when two simulation... [Pg.729]

Heat Transfer, Pressure and Pulling Force Submodels... [Pg.134]

Moschiar et al. (23) modeled pressure evolution in the die and tiie required pulling force. The heat transfer and pressure submodel were similar to Batch s model (22) however the pulling force submodel was different. It was considered only frictional solid-solid coefficients and it stated a condition for tlie pulling force calculation. The investigators compared their model wifli e qterimental results reported by other autiiors on tile pultrusion of unsaturated polyester matrix-glass fiber composites. [Pg.134]

Fuel thermomechanical models consist of a code for normal operation, which predicts the initial fuel conditions before an accident (strain, fuel-to-sheath heat transfer coefficient, gas release, initial temperatures, etc.), and a transient thermomechanical code for accidents. The latter includes submodels for fuel failure mechanisms due to fuel sheath strain, beryllium braze penetration, sheath embrittlement due to oxidation, athermal strain and excessive fuel energy content. Because of the need to predict the dose for each accident, the models must be able to estimate the percentage of fuel that fails in an accident (if any), and the release of fission products to the channel. [Pg.19]

Like in the thermal-hydraulic stability analyses, the frequency domain analysis method is used here, too. The mathematical model contains six submodels - the neutron kinetics model, the fuel rod heat transfer model, water rod heat transfer model, fuel channel thermal-hydraulic model, water rod thermal-hydraulic model, and the excore circulation system model. The fuel channel thermal-hydraulic model and water rod thermal-hydraulic model are the same as the thermal-hydraulic stability analysis model described in Sect. 5.4.3. [Pg.318]

Thermodynamic models that determine the equilibrium temperature distribution for an atmospheric column and the underlying surface, subject to prescribed solar radiation at the top of the atmosphere and prescribed atmospheric composition and surface albedo. Submodels for the transfer of solar and terrestrial radiation, the heat exchange between the earth s surface and atmosphere, the vertical redistribution of heat within the atmosphere, the atmospheric water vapor content and clouds are included in these one-dimensional models. Abbreviated as RCM. radiatively active gases... [Pg.207]


See other pages where Heat transfer submodel is mentioned: [Pg.130]    [Pg.133]    [Pg.135]    [Pg.130]    [Pg.133]    [Pg.135]    [Pg.314]    [Pg.215]    [Pg.102]    [Pg.419]    [Pg.656]    [Pg.54]    [Pg.99]    [Pg.197]    [Pg.728]    [Pg.135]    [Pg.102]    [Pg.585]    [Pg.348]   
See also in sourсe #XX -- [ Pg.135 ]




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Heat transfer submodels

Heat transfer submodels

Submodel

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