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Heat flow linear systems

The basic principle of heat-flow calorimetry is certainly to be found in the linear equations of Onsager which relate the temperature or potential gradients across the thermoelements to the resulting flux of heat or electricity (16). Experimental verifications have been made (89-41) and they have shown that the Calvet microcalorimeter, for instance, behaves, within 0.2%, as a linear system at 25°C (41)-A. heat-flow calorimeter may be therefore considered as a transducer which produces the linear transformation of any function of time f(t), the input, i.e., the thermal phenomenon under investigation]] into another function of time ig(t), the response, i.e., the thermogram]. The problem is evidently to define the corresponding linear operator. [Pg.211]

The combination of Eqs. (28) and (22) gives the Laplace transform of the impulse response H(p) which allows us to solve Eq. (21). By the inverse transformation, the relation which gives the output of the linear system g(t) (the thermogram) to any input/(0 (the thermal phenomenon under investigation) is obtained. This general equation for the heat transfer in a heat-flow calorimeter may be written (40, 46) ... [Pg.213]

The heat removal depends linearly on the difference between the reactor temperature and the coolant temperature since qm = UAS(T - Tm), where the subscript "m" refers to the cooling medium. The heat removal is represented by straight lines on the figure. The heat flow is zero if no heat is removed, which is the case if the coolant temperature is equal to the temperature of the system. Thus, the intersection of a heat removal line with the Y-axis (e.g., Tm,i)... [Pg.104]

The third section of the memoir, Reflections on the theory of heat, summarized lucidly what Lavoisier and Laplace sought to accomplish with their machine exact quantitative control of the distribution and the flow of heat in a system of bodies. In order to frame a complete theory of heat, four different kinds of measurement were necessary a linear thermometer, the specific heats of bodies as a function of temperature, the absolute quantities of heat contained in bodies at a given temperature, and the quantities of heat evolved or absorbed in chemical combinations or decompositions. This is in fact an excellent summary of the directions in which the thermometric investigation of heat had proceeded until then, except for the last item, which Lavoisier and Laplace added. They could not measure all these quantities directly, however, as they readily admitted. Particularly problematic was the relationship between the thermometer readings and the absolute quantities of heat. The assumption that the ratio of absolute heats was proportional to the ratio of specific heats was very uncertain and would require many experiments for confirmation. Specific heats only indicated the difference... [Pg.347]

The shape factor has a value of Sb = 12.85. The corners increase the heat flow by 28.5% compared with Q(, the heat flow calculated with the internal wall area. These are inaccurate approximations due to the coarseness of the grid. A refined grid would deliver more accurate temperatures, but increase the number of difference equations. Halving the mesh size (Ax = (5/4) already leads to a system of 24 linear equations. [Pg.217]

The energy balance equations for all the zones need to be established to solve this radiative exchange problem. This is done using the net-radiation method introduced by G. Poljak [5.49], This yields a system of linear equations that, when solved, deliver the unknown temperatures and heat flows. With simple... [Pg.579]

The zones 1,2,... m shall have given temperatures and the zones m + 1, m + 2,... n shall have stipulated heat flows. The linear equation system for the radiosities becomes... [Pg.588]

The temperature dependence of the internal energy and enthalpy of all substances (not merely ideal gases) can be found by measuring the temperature rise that accompanies a heat flow into a closed stationary system. If a sufficiently small quantity of heat is added to such a system, it is observed that the temperature rise produced, AT, is linearly related to the heat added and inversely proportional to /V, the number of moles in the system ... [Pg.60]

The difference of the measured electron and phonon temperatures in the b power, i.e. T -Tph) was plotted against applied power density (see inset in Fig. 2) and from the slope of the graph we obtain the electron-phonon coupling constant 27. The dependence is linear in this scale and it indicates that the heat flow between the electron and phonon systems has a 7 -dependence. This corresponds to Te.ph °c 1 for the electron-phonon interaction relaxation time. [Pg.229]

Figure2 Ohnishi et al. (1985) and Chijimatsu et al. (2000)) and reactive-mass transport model (inside the box named Chemical in Figure 2). This is a system of governing equations composed of Equations (l)-(9), which couple heat flow, fluid flow, deformation, mass transport and geochemical reaction in terms of following primary variables temperature T, pressure head y/, displacement u total dissolved concentration of the n master species C< > and total dissolved and precipitated concentration of the n" master species T,. Here we set master species as the linear independent basis for geochemical reactions, and speciation in solution and dissolution/precipitation of minerals are calculated by a series of governing equations for geochemical reaction. Now we adopt equilibrium model for geochemical reaction (Parkhurst et al. (1980)), mainly because of reliability and abundance of thermodynamic data for geochemical reaction. Figure2 Ohnishi et al. (1985) and Chijimatsu et al. (2000)) and reactive-mass transport model (inside the box named Chemical in Figure 2). This is a system of governing equations composed of Equations (l)-(9), which couple heat flow, fluid flow, deformation, mass transport and geochemical reaction in terms of following primary variables temperature T, pressure head y/, displacement u total dissolved concentration of the n master species C< > and total dissolved and precipitated concentration of the n" master species T,. Here we set master species as the linear independent basis for geochemical reactions, and speciation in solution and dissolution/precipitation of minerals are calculated by a series of governing equations for geochemical reaction. Now we adopt equilibrium model for geochemical reaction (Parkhurst et al. (1980)), mainly because of reliability and abundance of thermodynamic data for geochemical reaction.
Beyond linear response theory, molecular dynamics has the capability in principle of simulating processes which are well away from equilibrium. This capability has been exploited in the development of nonequilibrium molecular dynamics, as described by Hoover and Ashurst, and recently reviewed by Hoover.The technique is to modify the equations of motion, which in effect couples the system to momentum and energy reservoirs, so that the computer can simulate a nonequilibrium steady state. Applications Include viscous flows, heat flows, and chemical reactions. [Pg.559]

In a paper machine heat recovery system (HRS) the exhaust air streams of the paper machine dryer section are utilised for heating different cold streams. Condensation of the air moisture causes strong non-linearities in the system, notably the heat flow rates per °C and the heat transfer coefficients in the exchangers. A mixed integer non-linear programming (MINLP) model has been developed that takes into account these non-linearities (Soderman et al., 1999). Additionally the heat transfer area prices can be given as concave price curves in the model and the climate of the mill location can be taken into account with a multiple period formulation. [Pg.1062]

Figure 6.15 Schematic representation of the measuring system of a scanning calorimeter in a linear simplification with the corresponding temperature field in the presence of a steady-state heat flow. Figure 6.15 Schematic representation of the measuring system of a scanning calorimeter in a linear simplification with the corresponding temperature field in the presence of a steady-state heat flow.
Figure 6.20 shows the measured heat flow rate function of a power-compensated DSC containing a substance in the sample cmcible and another one with an empty crucible. The difference between the two measurements directly yields the heat flow rate into the sample because possible influences of asymmetries of the two systems are eliminated. In reality, the heat flow rate is measured as a function of time f. Because the heating electronic circuit always keeps the measured temperature T equal to the desired program temperature, the output signal can also be the heat flow rate as a function of temperature as there is a linear relationship... [Pg.112]

The three formulas (2.22)-(2.24) are examples of linear transport equations they relate the response of a system (the flux) to a small perturbing force (the gradient). The transport coefficients Z), rj, and x are the parameters of proportionality, to be determined experimentally. A familiar transport equation is Ohm s law. Here voltage is the force, current the response, and conductivity (the reciprocal of resistance) the transport coefficient. In general, equations of transport are not as simple as these. In a two-component system with a temperature gradient, Fourier s law states that there is only heat flow. However, if the masses of the components... [Pg.26]


See other pages where Heat flow linear systems is mentioned: [Pg.214]    [Pg.233]    [Pg.53]    [Pg.6]    [Pg.470]    [Pg.573]    [Pg.578]    [Pg.120]    [Pg.71]    [Pg.70]    [Pg.112]    [Pg.118]    [Pg.108]    [Pg.753]    [Pg.242]    [Pg.50]    [Pg.337]    [Pg.10]    [Pg.430]    [Pg.75]    [Pg.123]    [Pg.721]    [Pg.228]    [Pg.168]    [Pg.28]    [Pg.422]    [Pg.170]    [Pg.243]    [Pg.200]    [Pg.253]    [Pg.217]    [Pg.135]    [Pg.6]    [Pg.470]    [Pg.33]   
See also in sourсe #XX -- [ Pg.63 , Pg.64 , Pg.65 , Pg.66 , Pg.67 , Pg.68 , Pg.69 , Pg.70 ]




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