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The effect of temperature variations

If we regard the reciprocal of the effectiveness factor as a resistance we see that this is the sum of two resistances, the first for internal diffusion and the second for external mass transfer (see Exercise 6.4.2). Written in the form [Pg.141]

Exercise 6.5,1. A first order reaction A — B is taking place in a packed bed, through which the reacting fluid flows with velocity Vq, (This velocity is the volume flow rate of the reaction mixture divided by the total cross-sectional area. The fluid is assumed to be incompressible.) Set up an equation for a z), the concentration of 4 at a point distant z from the inlet, and show that it can be written as [Pg.141]

H has the dimensions of a length and has been called the height of a reactor unit, by analogy with heights of transfer units and equivalent theoretical plates. Interpret Eq. (6.5.4) to show that H is the sum of a height for external mass transfer HTU) and a term dependent on the reaction, the so-called height of a catalytic unit (HCU). Examine the contribution of these terms when the mass transfer, diffusion, and kinetic regimes are dominant. [Pg.141]

Up to this point, we have overlooked entirely the important effects of temperature variations, both between the pellet and stream and within the [Pg.141]

The transport of heat to the external surface of a catalyst particle can be described in the same way as the mass transport, by a transfer coefficient. Thus if the stream temperature is T and the surface temperature of the particle r the rate of heat transport is [Pg.142]


Equation (6.32) allows us to conveniently assess the effect of temperature variation on the rate of polymerization. This effect is considered in the following example. [Pg.367]

The proviso all other things being equal in discussing the last point clearly applies to temperature as well, since the kinetic constants are highly sensitive to temperature. To evaluate the effect of temperature variation on the molecular weight of an addition polymer, we follow the same sort of logic as was used in Example 6.3 ... [Pg.370]

Air flows at 12 m/s through a pipe of inside diameter 25 mm. The rate of heat transfer by convection between the pipe and the air is 60 W/m2K. Neglecting the effects of temperature variation, estimate the pressure drop per me Ire length of pipe. [Pg.863]

Fig. 12.1 Illustration of the temperature sensitivity of 15N relaxation parameters, Rlf R2t and NOE, as indicated. Shown are the relative deviations in these relaxation parameters from their values at 25 °C as a function of temperature in the range of + 3 °C. The expected variations in / ] and R2 due to temperature deviations of as little as +1 °C are already greater than the typical level of experimental precision ( % ) of these measurements (indicated by the dashed horizontal lines). For simplicity, only temperature variation of the overall tumbling time of the molecule (due to temperature dependence of the viscosity of water) is taken into account the effect of temperature variations on local dynamics is not considered here. Fig. 12.1 Illustration of the temperature sensitivity of 15N relaxation parameters, Rlf R2t and NOE, as indicated. Shown are the relative deviations in these relaxation parameters from their values at 25 °C as a function of temperature in the range of + 3 °C. The expected variations in / ] and R2 due to temperature deviations of as little as +1 °C are already greater than the typical level of experimental precision ( % ) of these measurements (indicated by the dashed horizontal lines). For simplicity, only temperature variation of the overall tumbling time of the molecule (due to temperature dependence of the viscosity of water) is taken into account the effect of temperature variations on local dynamics is not considered here.
Two parameters that are accessible to the experimentalist have been the effect of the interchange of a deuteron for a proton upon the dynamics of transfer and the effect of temperature variation upon the kinetics of proton-deuteron transfer [49]. As previously mentioned, the semiclassical model has been employed in the rationalization of kinetic deuteron isotope effects that exceed the factor of 7.0, the maximum predicted by the classical model [5]. However, the full quantum model also allows for the wide range in the kinetic deuteron isotope effect, the range of which overlaps that predicted by the semiclassical model [53]. Thus, the kinetic deuteron isotope effect in and of itself cannot be used to distinguish between the two models. [Pg.79]

One such study details the effects of temperature variation on substrate and metabolite concentration predictions, and used an artificial neural network creating a nonlinear multivariate model to improve concentration predictions. Another study notes the effects of temperature on the mid-infrared spectral data as well, but also noted that the sensor was not affected by reactor operating conditions such as agitation, airflow and backpressure. ... [Pg.453]

Assuming the material density or the intrinsic averaged density of phase k to be constant (as is true for the solids and almost true for the fluid when the effect of temperature variation on the material density can be neglected), we have... [Pg.194]

The conditions for both API and drug products registration stability studies are summarized in Table 4. In addition, cycling studies to determine the effect of temperature variations on certain drug products should be considered. [Pg.201]

Ambient temperature variations will affect the accuracy and reliability of temperature detection instrumentation. Variations in ambient temperature can directly affect the resistance of components in a bridge circuit and the resistance of the reference junction for a thermocouple. In addition, ambient temperature variations can affect the calibration of electric/electronic equipment. The effects of temperature variations are reduced by the design of the circuitry and by maintaining the temperature detection instrumentation in the proper environment. [Pg.27]

Boyle s measurements were made on a fixed sample of gas over a short time, so that his laboratory temperature could be considered constant. Soon after, Charles explicitly investigated the effect of temperature variation.1 He found that if pressure was held constant, the volume varied linearly with temperature ... [Pg.17]

Also Senkan et al. (6) and Schehl et al. (3) have shown that for methanation, the material balance equation can be solved independently of the energy balance equation in diffusion-limited cases, because the effects of temperature variation on gas properties essentially cancel each other. It is therefore justified to consider the isothermal model for the purpose of yield optimization. [Pg.459]

Most of the alcohol radicals have hyperfine coupling constants slightly dependent on both temperatures and solvents. Ayscough and McClung (220) have also studied in detail the effect of temperature variation on proton hyperfine splitting of the biacetyl semidione radical in the range 250-400 K. Livingston and Zeldes (156) observed... [Pg.67]

Although the dependence of reaction rates on temperature has been well known for over a century (Moore and Pearson, 1981), the temperatures at which transformation half-lives are measured are often not reported, either by the original publications or in data compilations (e.g., Nash, 1988 USDA/ARS, 1995 Pehkonen and Zhang, 2002). Similarly, as noted by Barbash and Resek (1996), the effects of temperature variations on transformation rates are rarely incorporated... [Pg.5099]

Below, we describe tbe design formulation of isothermal batch reactors with multiple reactions for various types of chemical reactions (reversible, series, parallel, etc.). In most cases, we solve the equations numerically by applying a numerical technique such as the Runge-Kutta method, but, in some simple cases, analytical solutions are obtained. Note that, for isothermal operations, we do not have to consider the effect of temperature variation, and we use the energy balance equation to determine tbe dimensionless heat-transfer number, HTN, required to maintain the reactor isothermal. [Pg.199]

In the work presented here, these processes have been studied primarily by calorimetry. Planned measurements of partial specific heat and partial molal volume will give additional thermodynamic data on the structure of micellar systems. Heat capacity measurements will allow "simple" extrapolation of measured enthalpy terms to higher temperatures. In addition, a direct measure of the effect of temperature variation is of interest for solution structure studies. Partial molal volume measurements give information on the packing of surfactant monomers and micelles within the water structure. The effect of cosurfactants on the partial molal volume will be of particular interest. [Pg.94]

For asphalt sands, compressive strength at about 40°C is only one third of its value at 18 °C and tensile strength falls to one tenth of its 18 °C level. It must be shown whether products incorporating S/A binders are less sensitive or not to the effects of temperature variations. [Pg.154]

Abstract We review recent progress in wide bandgap thin-film and nanorod sensors made from GaN or ZnO and related materials for applications in the detection of gases such as oxygen, carbon dioxide and hydrogen. Practical aspects are covered, such as the use of differential sensor pairs to eliminate the effects of temperature variations and of the effect of humidity on the detection sensitivity. [Pg.159]

The effect of temperature variation on the strength of adhesive-repaired structures can be divided in two categories. One category considers the effect of temperature changes due to natural environmental causes. In this category, the temperature varies from —18 to 65°C, a reasonable expected variation. The second major effect to be considered is fire, where extreme temperatures are reached [23]. [Pg.286]

The rigoroiis analysis of the effect of temperature variations on interfacial properties is a key tool to provide new and valuable information on the structure and reactivity of the metal solution interphase. The entropy of the components that form the interphase is a unique probe of their stmctural properties. Therefore, this experimental data is particularly useful for the validation of molecular models of electrified interphases. In addition, the use of fast temperature perturbations is especially suitable for the selective characterization of different inter-facial components, based on their different response time towards the temperature change. In this way, the entropic properties of doublelayer phenomena and charge-transfer adsorption processes can be evaluated separately. It will be shown in this chapter that the combina-... [Pg.1]

As pointed out in Sect. 1.7, the viscoelastic functions of many materials depend strongly on temperature. The simplest realistic way of incorporating this dependence is to assume that the material is thermorheologically simple (TRS) in the sense defined in Sect. 1.7. This implies a non-linear dependence on the temperature field which renders the solution of most problem categories very difficult, in particular those where the temperature field is not given a priori but must be determined as part of the solution. A way out of this is to adopt a fully linear theory, as developed for example by Christensen (1982), Chap. 3. The assumption behind such a theory is that the effects of temperature variation on the viscoelastic functions is sufficiently small that its product with the field variables can be neglected. In many cases, this is very restrictive on the allowed range of temperature variation. A fully linear theory will not be considered here. We remark however that such a theory is susceptible to treatment by the Correspondence Principle-based methods, discussed in Chap. 2. [Pg.199]

Similarly, the effects of temperature variations in the cooling water supply on operation of the condenser can be mitigated by use of a temperature control loop. If disturbances are particularly large in a utility supply, a cascade secondary controller can be employed to control the temperature or pressure of the utility stream at the point it leaves the process, with a primary controller used to maintain the process temperature (Chapter 16). Cascade control, which is applied in Step III.B, is not used here for reasons of simplicity. [Pg.562]


See other pages where The effect of temperature variations is mentioned: [Pg.157]    [Pg.1113]    [Pg.176]    [Pg.294]    [Pg.113]    [Pg.377]    [Pg.29]    [Pg.205]    [Pg.141]    [Pg.141]    [Pg.145]    [Pg.499]    [Pg.338]    [Pg.113]    [Pg.54]    [Pg.64]    [Pg.194]    [Pg.114]    [Pg.452]   


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