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Thermal characteristics of the system

The thermal characteristics of the system determine how the output signal (temperature) varies with changes in input (heat). One of the simplest and most common methods to determine the system characteristics is to measure response of temperature to a step change in heating power see Fig. 4.35. [Pg.128]

This temperature/time curve is often referred to as the process reaction curve or simply the response curve. [Pg.128]

From the response curve, several parameters can be established that are important in understanding the behavior of the system. The dead time (b,) is the time to the intersection of the maximum temperature gradient. The constant indicates the ratio of maximum temperature rise to the step change in power. (Ks= AT ax/AZ ax) The time constant (t ) is the maximum change in temperature divided by the maximum temperature gradient. [Pg.129]

The dead time in extruders can range from about 1 to 5 minutes. This constitutes one of the main problems in temperature control, because this means that the effect of a change in power input level is not felt until after at least 1 minute. This thermal lag time is influenced by the depth of the temperature sensor, the thermal conductivity of the barrel, and the design of the barrel heaters. A typical time constant in an extruder can range from 30 to 120 minutes. This value depends on the heating capacity and the specific heat and mass of the extruder barrel. [Pg.129]

Although these parameters do not fully describe the system, they can be used to make approximate predictions of the degree of difHculty in temperature control [41]. [Pg.129]


The quasi-one-dimensional model of flow in a heated micro-channel makes it possible to describe the fundamental features of two-phase capillary flow due to the heating and evaporation of the liquid. The approach developed allows one to estimate the effects of capillary, inertia, frictional and gravity forces on the shape of the interface surface, as well as the on velocity and temperature distributions. The results of the numerical solution of the system of one-dimensional mass, momentum, and energy conservation equations, and a detailed analysis of the hydrodynamic and thermal characteristic of the flow in heated capillary with evaporative interface surface have been carried out. [Pg.374]

The flow and heat transfer in heated micro-channels are accompanied by a number of thermohydrodynamic processes, such as liquid heating and vaporization, boiling, formation of two-phase mixtures with a very complicated inner structure, etc., which affect significantly the hydrodynamic and thermal characteristics of the cooling systems. [Pg.486]

The first measure is to use the evaporative cooling or controlled depressurisation to keep the reaction mass under control. The distillation system must be designed for such a purpose and has to function, even in the case of failure of utilities. A backup cooling system, dumping of the reaction mass, or quenching could also be used. Alternatively, a pressure relief system may be used, but this must be designed for two-phase flow that may occur, and a catch pot must be installed in order to avoid any dispersion of the reaction mass outside the equipment. Of course, all these measures must be designed for such a purpose and must be ready to work immediately after the failure occurs. The use of thermal characteristics of the scenario for the choice of technical measures is presented in detail in Chapter 10. [Pg.70]

The assumed conditions used in evaluating characteristics of the systems are summarized in Table 2. The total areas of the solar collectors and photovoltaic arrays are assumed to be 10 ha. In the solar thermal and hybrid systems, the type of collector is parabolic trough, the condenser outlet pressure 0.1 kg/cm a, and the capacity (maximum net power output) has been determined so as to minimize the unit cost of generated power energy. In the solar photovaltaic system, the conversion efficiency at the array is assumed to be 15 %. The tracking scheme of the solar collector and photovoltaic array is single north-south axis. [Pg.368]

The cooperative mechanism of the spin-crossover phenomenon is well imderstood in some aspects. For instance, theoretical models account for the thermal evolution of the system. However, due to their phenomenologic character, the key parameters accounting for intermolecular interactions do not reflect the relevance of the microscopic details which could orientate us in designing molecules that can recognize each other and combine to produce systems with prescribed characteristics. Consequently, very general principles guide the syntiietic chemistry in the search for suitable spin-crossover compounds often trial and error or serendipity are the sole strategies. [Pg.54]

Some of the characteristics of the large-scale system which are of interest in a thermal runaway hazard evaluation are listed in Table II. First of all, the amount of material which will be handled must be known. The hazards involved are obviously greater when one works with large quantities of material. The heat generated on a laboratory scale is so much less because of the small quantities of material being handled. Often that heat is easily dissipated because of the low sample volume to surface area ratio. Secondly, the heat transfer characteristics of the system must be known. Is special cooling available What is the surface area through which heat can be dissipated ... [Pg.76]

The synthesis of several metallized PTASH films via coordination of the polymer to various transition metal salts followed by a chemical reduction of the resulting chelates films is described. Coordination reaction was carried out either by the mixing or the soaking method. The metallized films showed novel functions due to characteristic properties of metal chelates. The incorporation of metals improved the tensile strength as well as thermal stability of the systems as evidenced by mechanical properties and TGA measurements This improvement could be clearly demonstrated in chelates prepared by the mixing method rather than those prepared by the soaking method. Metallization of the these films has been shown by SHM, X-my diffraction and ESCA measurements which indicated the presence of the metal adhered to the surface of the films Finally, potential advantages of these metallized films lie in their versatility with which their synthesis and processability can be accomplished as well as in their stability towards humid environment. [Pg.42]

It might be helpful to refer to the thermal characteristics of electrochemical systems. Heat generation could he formulated as follows, with two distinct terms ... [Pg.90]

Thus far, the discussion has focused on the various types of temperature controllers. However, the real issue is how the actual temperature of the extruder will change as a result of the action of the temperature controller. In order to determine this, one has to consider the thermal characteristics of the actual system, in this case the extruder. [Pg.128]


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