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Heat Capacity Effects

By diluting a reactive sample powder with an inert powder (e.g. AI2O3), the heat capacity of the sample can be made to match more closely that of the reference, hence baseline float can be dampened. This is a useful technique for reactions of significant thermal effect, e.g. combustion, since sample dilution diminishes the intensity of the differential temperature signal. Since the diluent adds a thermal resistance between the reaction zones and the temperature measuring device, the onset of reactions will shift to higher temperatures. [Pg.75]

For reactions of minute thermal effect, e.g. second order transitions, it is advantageous to use as much sample mass as feasible in the heat-flux DSC sample pan. It is advisable to use an adequate thermal mass of reference powder to match that of the sample. This has the advantage of not only minimizing baseline float, but also smooths out what may appear to be signal noise When the reference lacks thermal mass, its temperature will vary responsively to random thermal fluctuations in its surroundings. On a sensitive scale, the changing reference temperature will be manifested as noise on the amplified differential thermocouple signal. [Pg.75]


Course B. To correct the heats of dissociation to correspond to dissociation (or association) at room temperature. This has the disadvantages that heat capacity effect corrections (at present unknown and unmeasured) would have to be made to embrace a considerable temperature range, heats of transition of the soaps and acid-soaps to the phases stable at room temperature would have to be measured, and the heats of interaction would in certain cases involve soaps in different forms [form A for C8, Ci0 B for Ci2 to Ci8 (14)]. It would, on the other hand, allow heats to be compared at one standard temperature. [Pg.83]

For the problem to be tractable, the enthalpies of the two phases must be known as functions of the respective phase compositions. When heats of mixing and heat capacity effects are small, the enthalpies of mixtures may be compounded of those of the pure components thus... [Pg.380]

This represents the key aspect of polymer fire retardancy using hydrated fillers, and involves energy changes that occur on the decomposition of the filler, related heat capacity effects, which influence the degradation profile of the polymer and thermal barrier formation resulting from the residue remaining from degraded filler. [Pg.169]

Paschek D. Heat capacity effects associated with the hydrophobic... [Pg.1922]

The level at 15.254 cm" has a large effect on the heat capacity and entropy below 100 K. The heat capacity effect decreases to zero above 600 K where the 15.254 cm" level Is fully populated. The higher excited states affect the heat capacity values above 3000 K. The Gibbs energy function values up to 6000 K are essentially Independent of the cut-off procedure, the inclusion of levels for n>2, and the estimated missing levels (for n<39). [Pg.179]

J. H., Nollmann, M., Heat does not come in different colours entropy-enthalpy compensation, free energy windows, quantum confinement, pressure perturbationcalorimetry, solvation and the multiple causes of heat capacity effects in biomolecular interactions Biophys. Chem. 2001, 93, 215-230. [Pg.77]

Although the glass transition resembles characteristics of a second-order thermodynamic transition such as changes in the coefficient of expansion and heat capacity, the temperature of the transition is a function of the heating or cooling rate and of the rate of deformation. The methods used to determine Tg are based either on static or dynamic mechanical processes. The former uses volume effects (dilatometry) and heat capacity effects in differential scanning calorimetry (DSC), entailing conditions of very low deformation. The latter utilizes the response to imposed deformation of the system. [Pg.97]

The oxygen produces exothermic reactions, whereas the steam decreases the temperature of the reaction using a heat capacity effect and by endothermic reactions. On the whole, the reaction occurs in a quasi-adiabatic manner at temperatures between 1300 and 1500 °C. The reaction is carried out at pressures from 2 to 6 MPa. [Pg.60]

Adding heat to a sample can also have an effect that does not increase the temperature. This heat is called a latent heat. It has its origin in a change of the structure of the sample as in a chemical reaction (heat of reaction) or a phase transition (heat of transition). The measurement of a latent heat is done by direct calorimetry as described in Chap. 4. Note that the latent heat is only the heat of reaction or transition if temperature, T, is constant if not, heat capacity effects must be considered separately. [Pg.84]

The application of the ATHAS has produced a large volume of critically reviewed and interpreted heat capacity data on solid and liquid homopolymers. This knowledge is helpful in the determination of the integral thermodynamic functions which are also part of the data bank. Even of greater importance is the help these basic data give in the separation of nonequilibrium enthalpy and heat capacity effects as will be illustrated in a number of examples. [Pg.134]

Extrapolations from the MHTGR (considering heat capacity, effective silo surface area, and available temperature to drive heat from the silo wall to the environment) indicate that a 2400 MW(t) AHTR with beyond-design-basis-accident capabilities could be built. However, major uncertainties remain because such systems imply high temperatures near the silo and reactor facilities. There are many design choices and tradeoffs, including options that may not require a secondary salt. [Pg.80]

For the second set of conditions, the temperature given in 2 (400 K) is different from the temperature that was used to calculate AG in Example 2.1 (298 K). Thus, we must first determine AG at this new temperature. This would best be done by consulting a thermodynamic database to get values for A//° and 5 for HI(g), 12(g), and H2(g) at P = 400 K and then using those values to calculate AG at 400 K in a manner analogous to what was done in Example 2.1 at 298 K. Alternatively, values for AH and 5 at 400 K could be estimated from the values at 298 K if we knew the heat capacities of HI(g), 12(g), and H2(g). However, we can also make the assumption (reasonable for modest changes in temperature) that these heat capacity effects are negligible. In this case, we can approximate AG at 400 K with Equation 2.1using the previously calculated values for AH and A5J at P = 298 K ... [Pg.24]

It is important to note that the AH and AS determined by van t HoflF analysis are determined at the T. If large temperature extrapolation is required (greater than 20 C away from Tm), then heat capacity effects should be accoimted for. Previous data have indicated that ACJ is usually small for nucleic adds (14,15). Based on these data, an approximate estimate of AC is in the range of 0-120 entropy units (cal K mol) per base pair and AC is assumed to be temperature independent. Given AC, the AHj-, AS -, and AGt can be calculated more accurately than equation 2 with the equations 5 (14). [Pg.332]

While clearly demonstrating the importance of the endotherm in the heat balance, it is interesting to note that the heat capacity effects, especially of the evolved gases, are also significant contributors. [Pg.279]

Much of the essential physical chemistry of the hydrophobic effect has emphasized the transfer of small organics from the gas phase to water. As we have said, hydrocarbons have very low solubilities in water. While this is the characteristic feature of the hydrophobic effect, other thermodynamic effects are seen, including unusual entropy effects and often large heat capacity effects. To a very good approximation, AG° of transfer scales with surface area of the hydrocarbon that is exposed to water on dissolution. The exact scaling factor is debated and appears to depend on context. Values as low as 15 cal/ mol in AG° for every A of exposed aliphatic or aromatic hydrocarbon and as high as 75 cal / mol "A are reported, but a more typical range is 30-50 cal/mol A. If we settle on 40 cal/mol A, and assume a surface area of 29 A for a CH2 in an alkane, then every additional CH2 adds 1.2 kcal/mol of destabilization in a hydrophobic effect. [Pg.189]

Ignoring the small terms for translation and heat capacity effect, this is rearranged and the In function performed to yield... [Pg.97]


See other pages where Heat Capacity Effects is mentioned: [Pg.258]    [Pg.259]    [Pg.262]    [Pg.44]    [Pg.173]    [Pg.70]    [Pg.71]    [Pg.75]    [Pg.77]    [Pg.120]    [Pg.30]    [Pg.44]    [Pg.272]    [Pg.253]    [Pg.13]    [Pg.229]    [Pg.346]    [Pg.294]    [Pg.883]    [Pg.202]    [Pg.236]    [Pg.239]    [Pg.371]    [Pg.48]    [Pg.97]   


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