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External heat reservoir

Another model which includes interaction and for which partial results are available on the decay of initial correlations is that of the one dimensional time-dependent Ising model. This model was first suggested by Glauber,18 and analyzed by him for one-dimensional Ising lattices. Let us consider a one-dimensional lattice, each of whose sites contain a spin. The spin on site,/ will be denoted by s/t) where Sj(t) can take on values + 1, and transitions are made randomly between the two states due to interactions with an external heat reservoir. The state of the system is specified by the spin vector s(t) = (..., s- f), s0(t), Ji(0>---)- A- full description of the system is provided by the probability P(s t), but of more immediate interest are the reduced probabilities... [Pg.212]

The physical system and the scaled system are related by Eq. (6). The scaling of velocities permits the exchange of heat between the simulated and the external heat reservoir. The equations of motion for the N atoms and the scaling factor g are solved numerically and averages calculated from the trajectory. The special choice (/+ I) kTo In g for the potential energy associated with g guarantees that the averages of equilibrium quantities calculated from the MD trajectory are the same as those in the canonical ensemble. [Pg.144]

Z3 A rigid vessel 10(ft)3 in volume contains saturated-vapor steam at 75(psia). Heat exchange with a single external heat reservoir at 60(°F) reduces the temperature of the contents of the vessel to 60(°F). Determine. What is the irreversible feature of this process ... [Pg.423]

A new evaluation standard for the dehydrogenation catalysts in the superheated liquid-film states is introduced here. This standard is called as the "ratio of heat recuperation" [39], being defined as the ratio of endothermic reaction heat to the denominator of heat supplied from the external thermo-reservoir to the catalyst layer shown as follows (Equations 13.10 and 13.11) ... [Pg.463]

One-pass conversion obtained in the continuous dehydrogenation reactor equipped with an external condenser (Figures 13.18 and 13.22) gives the extent of energy recuperation from the ICE waste heat through hydrogen generation, because induction of heat from the external thermo-reservoir to the catalyst layer must be consumed stationarily to allot the supplied heat to the endothermic reaction heat as well as the evaporation heat. [Pg.464]

The power versus efficiency characteristics of the endoreversible Carnot heat engine is a parabolic curve. The endoreversible heat engine is a simple model, which considers the external heat-transfer irreversibility between the heat engine and its surrounding heat reservoirs only. [Pg.363]

We return to the piston-and-cylinder arrangement discussed in Section 2.3. In that discussion we did not completely describe the process because we were interested only in developing the concept of work. Here, to complete the description, we choose an isothermal process and a gas to be the fluid. We then have a gas confined in the piston-and-cylinder arrangement. A work reservoir is used to exert the external force, Fe, on the piston this reservoir can have work done on it by the expansion of the gas or it can do work by compressing the gas. A heat reservoir is used to make the process isothermal. The piston is considered as part of the surroundings, so the lower surface of the piston constitutes part of the boundary between the system and its surroundings. Thus, the piston, the cylinder, and the two reservoirs constitute the surroundings. [Pg.25]

Fig. 17. Schematic design of a heat flux calorimeter. Both the temperature in the reactor and in the circuit (or jacket) are measured as sensitively and reproducibly as possible. A well-tuned temperature controller keeps the reactor temperature constant by feeding the circuit with warmer or colder water or oil. The circulating water or oil can be taken from either a chilled and a heated reservoir or, as shown, be heated or cooled via external heat exchangers. Calibration is made possible via an electric heater of known power... Fig. 17. Schematic design of a heat flux calorimeter. Both the temperature in the reactor and in the circuit (or jacket) are measured as sensitively and reproducibly as possible. A well-tuned temperature controller keeps the reactor temperature constant by feeding the circuit with warmer or colder water or oil. The circulating water or oil can be taken from either a chilled and a heated reservoir or, as shown, be heated or cooled via external heat exchangers. Calibration is made possible via an electric heater of known power...
Let the walls of the cylinder be thermally insulating and its base be thermally conducting which is kept in contact with a heat reservoir at temperature Tj. Let the weight of the piston and the external pressure and load on it be such that it just balances the pressure of the gas. In such a situation, there will not be any net heat flow between gas and the heat source. [Pg.42]

Now if the weight on the piston is very slowly reduced so that the gas expands reversibly, the temperature of gas will tend to fall as it is performing work against the external pressure. The gas will therefore pick up heat from the heat reservoir to maintain its temperature. Suppose the gas expands to a volume of V2 so that the pressure is 2-... [Pg.42]

I. The cjdinder containing the mole of ideal gas, occupying a volume Fa, is placed in the/heat reservoir at the higher temperature. The external pressure is adjusted so that it is always infinitesimally less than the gas pressure, and the temperature of the gas is infinitesimally less than that of the reservoir. In this manner, the gas is expanded isothermally and reversibly until its volume has increased to Vb- The path of the process is represented by the isothermal curve AB in Fig. 11. Since the gas is ideal, the work done Wi is given by equation (8.4) thus, for 1 mole of gas,... [Pg.135]

If the above law did not hold we could suppose that there was a cyclic process in which the lower isotherm DC (cf. the diagram below, which is drawn in the usual manner) is at the absolute zero. We might, for instance, suppose that a solid or liquid body expanded at the low but finite absolute temperature AT, while it was maintained in constant communication with a heat reservoir—isotherm AB that it was then disconnected front the reservoir and further expanded adiabatically until it became cooled to the absolute zero— adiabatic BC. It is then compressed at the absolute zero —isothermal CD—and finally warmed an infinitely small amount by an infinitely small addition of external work, such that it is brought again by the adiabatic compression to the temperature AT and the original volume—adiabatic DA. [Pg.87]

Now in such a reversible cyclic process a certain finite amount of external work will be supplied, which is given by the area contained between the four curves. Since no heat is taken up on the curves BC and DA, and since, by equation (1), no heat can be taken up over the curve CD because the latent heat disappears at the absolute zero, it follows that the external work must have been supplied at the cost of the heat removed from the heat reservoir at the temperature AT, which is very low perhaps, but still finite. But as this contradicts the Second Law, we arrive at the conclusion which was to be demonstrated. [Pg.88]

One of the laws of physics is termed the Second Law of Thermodynamics. Physicist Lord Kelvin, the man who first defined this law, stated it in technical terms as follows "There is no natural process the only result of which is to cool a heat reservoir and do external work."... [Pg.7]

The objective here is to show that the reaction equilibrium criteria (7.6.3) are a consequence of the more general equilibrium criterion (7.1.40) that applies to any NPT system, including reacting systems. Consider a system of C species confined to a closed vessel and maintained at constant T and P by contact with an external heat and work reservoir. The species may undergo 51 independent chemical reactions. Since T and P are fixed for the entire system, the NPT criterion for equilibrium (7.1.40) applies that is, when all reactions are complete and equilibrium is reached, the system s total Gibbs energy will be a minimum,... [Pg.304]

Heat may be removed fi om the primary coolant system by means of a heat exchanger positioned in the primary vessel and which operates by natural convection to an external heat exchanger in the atmosphere or in a large tank of water within the primary containment. In some cases the system requires valve operation to bring it into service while in others it operates continuously. A valved system may operate in a water solid mode or in a boiling and condensing mode and will need some form of reservoir to prime it. Wffiere the system operates continuously, so that there is no problem of start up in an accident situation, there is a steady loss of around 6% of... [Pg.21]

A heat reservoir can be a body that is so large that its temperature changes only imperceptibly during heat transfer a thermostat bath whose temperature can be controlled or an external system of coexisting phases of a pure substance (e.g., ice and water) at constant pressure. [Pg.50]


See other pages where External heat reservoir is mentioned: [Pg.349]    [Pg.444]    [Pg.449]    [Pg.449]    [Pg.470]    [Pg.475]    [Pg.144]    [Pg.617]    [Pg.305]    [Pg.266]    [Pg.349]    [Pg.444]    [Pg.449]    [Pg.449]    [Pg.470]    [Pg.475]    [Pg.144]    [Pg.617]    [Pg.305]    [Pg.266]    [Pg.195]    [Pg.478]    [Pg.151]    [Pg.27]    [Pg.29]    [Pg.44]    [Pg.232]    [Pg.287]    [Pg.121]    [Pg.28]    [Pg.356]    [Pg.343]    [Pg.79]    [Pg.127]    [Pg.34]    [Pg.263]    [Pg.260]    [Pg.366]    [Pg.797]    [Pg.50]   
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