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Enthalpy heats calculated from

This process is shown as a horizontal line on the chart, since there is no change in the moisture content. The loss of sensible heat can be read off the chart in terms of enthalpy, or calculated from the dry bulb reduction, considering the drop in the sensible heat of both the dry air and the water vapour in it. [Pg.243]

The vapour enthalpies are calculated from the molar heat capacity functions for the vapour components and the latent heats of vaporisation at standard temperature. The vapour overflow, V, is then obtained from the energy balance as... [Pg.217]

Make sure the heat input Q matches the temperature-enthalpy difference calculated from the inlet process temperature/enthalpy minus the outlet process temperature/enthalpy. The program calculates the outlet process temperature therefore, Q must be adjusted accordingly. This may result in several runs being necessary to get a match of Q input vs. Q allowable per the tube area input. [Pg.208]

Figure 4 Examples of the differential sorption heat calculated from the sorption data using the Clausius-Clapeyron equation. The arrows depict the most negative enthalpy value in the region of strongly (SP) and weakly (WP) bound water, the limit of the strongly bound water region (SBC), the moisture content where bound water first appeared (BWiso), and the tissue moisture range corresponding to weakly bound water (WBC) [56]. Figure 4 Examples of the differential sorption heat calculated from the sorption data using the Clausius-Clapeyron equation. The arrows depict the most negative enthalpy value in the region of strongly (SP) and weakly (WP) bound water, the limit of the strongly bound water region (SBC), the moisture content where bound water first appeared (BWiso), and the tissue moisture range corresponding to weakly bound water (WBC) [56].
The reaction enthalpies were calculated from the the heat of formation for the species in the hydrogenation of CO2 and water gas shift reactions. The overall process is strongly exothermic. [Pg.966]

In other words, at its boiling point water requires the further addition of 970 Btu of energy to convert one pound of water to steam, which is 5.39 times as much energy as required to raise the water temperature from 0 °C (32 °F) to 100 °C. The temperature of the hot water remains constant until it has been entirely vaporized, at which point the steam is fully saturated with heat and the enthalpy of the steam (heat content as calculated from a starting point ofO °C) is 1,150 Btu/lb. [Pg.4]

In a procedure similar to that described earlier for N , the entropy at T = 49.44 K point (a) can be calculated from the heat capacities and the enthalpies of transition, by following two different paths. Sm 49 44 was found to be 34.06 J-K-1 mol-1 following the solid III— solid II path and Sm.49.44 = 34.02 JK 1 mol l following the (solid V— solid IV—>solid II) path. The two results agree well within experimental error, which requires that the entropy of solid III and solid V be the same at 0 K, an occurrence that is unlikely unless Sm 0 = 0 for both forms. [Pg.166]

Statistical thermodynamics provides the relationships that we need in order to bridge this gap between the macro and the micro. Our most important application will involve the calculation of the thermodynamic properties of the ideal gas, but we will also apply the techniques to solids. The procedure will involve calculating U — Uo, the internal energy above zero Kelvin, from the energy of the individual molecules. Enthalpy differences and heat capacities are then easily calculated from the internal energy. Boltzmann s equation... [Pg.497]

STRATEGY The heat released by the reaction at constant pressure is calculated from the temperature change multiplied by the heat capacity of the calorimeter. Use the molar mass of one species to convert the heat released into the reaction enthalpy corresponding to the thermochemical equation as written. If the temperature rises, the... [Pg.361]

Using standard enthalpies from Ref. 132) a reaction enthalpy of 92 kJ mol-1 is the result for reaction (24). This value lies near the above estimated limit and not far from the values which have been calculated from experimental heats of formation for the second and third propagation step (102 kJ mol-1). [Pg.218]

The enthalpy changes are calculated from molar heat capaeities given by the usual functions of temperature, according to... [Pg.216]

Enthalpy can be calculated from specific and latent heat data see Section 3.5. [Pg.63]

Mean specific heat values are tabulated in various handbooks. If the values are for unit mass, calculated from some standard reference temperature, tr, then the change in enthalpy between temperatures i and t2 is given by ... [Pg.68]

The standard enthalpy of formation AH°f of a compound is defined as the enthalpy change when one mol of the compound is formed from its constituent elements in the standard state. The enthalpy of formation of the elements is taken as zero. The standard heat of any reaction can be calculated from the heats of formation —AH of the products and reactants if these are available or can be estimated. [Pg.79]

This program can be used to calculate the heat input or cooling required for a process unit, where the stream enthalpies relative to the datum temperature can be calculated from the specific heat capacities of the components (equation 3.11). [Pg.94]

Calculate the specific enthalpy of water at a pressure of 1 bar and temperature of 200 °C. Check your value using steam tables. The specific heat capacity of water can be calculated from the equation ... [Pg.130]

The heat of dilution was calculated from an enthalpy — concentration diagram given in Perry s Chemical Engineers Handbook, 5th edn, p. 3.205, Figure 3.42. [Pg.165]

Before equation 12.1 can be used to determine the heat transfer area required for a given duty, an estimate of the mean temperature difference A Tm must be made. This will normally be calculated from the terminal temperature differences the difference in the fluid temperatures at the inlet and outlet of the exchanger. The well-known logarithmic mean temperature difference (see Volume 1, Chapter 9) is only applicable to sensible heat transfer in true co-current or counter-current flow (linear temperature-enthalpy curves). For counter-current flow, Figure 12.18a, the logarithmic mean temperature is given by ... [Pg.655]

One problem remains. The reference enthalpy must be defined at temperature T and pressure P0. The reference state for enthalpy can be taken as an ideal gas. At zero pressure, fluids are in their ideal gaseous state and the enthalpy is independent of pressure. The ideal gas enthalpy can be calculated from ideal gas heat capacity data3 ... [Pg.73]

The enthalpy of reaction that is most needed is the not the enthalpy of any specific reaction, desired or undesired, but rather the global or macro enthalpy of reaction at various conditions, including different temperatures. This term is defined as the heat evolved by the reaction system in which reactants are converted into products and by-products by one or more reactions. The global enthalpy of reaction is difficult to calculate, but relatively easy to measure by experiment. Any such experiment must simulate the conditions which exist in the process under study (i.e., concentrations, temperatures, and pressures). The experimental values will, of course, include the heat evolved from the desired reaction(s) and from all of the undesired reactions that happen to occur under the selected conditions. [Pg.93]

Fig. 9. Effect of the chain length of hydrocarbons on the adsorption enthalpy and rates of desorption. (A) Hydrocarbon in interaction with zeolite framework. Methyl groups interact with the framework oxygen protons exhibit an additional attractive force. (B) Heat of adsorption as a function of carbon number for zeolites MFI and FAU in the acidic and non-acidic form. (C) Relative desorption rates of a C12, Ci6, and C20 alkane compared to octane at 348 K. Values calculated from the linear extrapolation of the heat of adsorption values shown in (B). Fig. 9. Effect of the chain length of hydrocarbons on the adsorption enthalpy and rates of desorption. (A) Hydrocarbon in interaction with zeolite framework. Methyl groups interact with the framework oxygen protons exhibit an additional attractive force. (B) Heat of adsorption as a function of carbon number for zeolites MFI and FAU in the acidic and non-acidic form. (C) Relative desorption rates of a C12, Ci6, and C20 alkane compared to octane at 348 K. Values calculated from the linear extrapolation of the heat of adsorption values shown in (B).

See other pages where Enthalpy heats calculated from is mentioned: [Pg.197]    [Pg.361]    [Pg.26]    [Pg.332]    [Pg.336]    [Pg.42]    [Pg.300]    [Pg.576]    [Pg.1910]    [Pg.66]    [Pg.245]    [Pg.341]    [Pg.1042]    [Pg.161]    [Pg.96]    [Pg.557]    [Pg.186]    [Pg.460]    [Pg.536]    [Pg.387]    [Pg.87]    [Pg.307]    [Pg.399]    [Pg.467]    [Pg.32]    [Pg.346]   


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