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Setting of temperature

Two conditions that are often important in chemical experiments are temperature and pressure. Consequently, chemists usually control and measure these conditions during experiments. In addition, it is useful to refer many experimental results to a standard and generally accepted set of temperature and pressure conditions. This facilitates comparison of results of different types and from different laboratories. [Pg.53]

This system of i + 2 equations is nonlinear, and for this reason probably has not received attention in the least-squares method (207). We are able to give an explicit solution (163) for the particular case when Xy = xj and m,- = m for all values of i that is, when all reactions of the series are studied at a set of temperatures, not necessarily equidistant, but the same for all reactions. Let us introduce... [Pg.440]

The usual derivation of an activation energy from a set of temperature dependent rates as the slope of an Arrhenius plot gives ... [Pg.278]

MICROMEHT R can observe the ehange of length as a function of several settings of temperature. aLis obtained as described before. [Pg.397]

What is the best set of temperature and pressure conditions for the Haber process—the industrial process to convert hydrogen and nitrogen to ammonia ... [Pg.297]

The direct determination of cadmium in seawater is particularly difficult because the alkali and alkaline earth salts cannot be fully charred away at temperatures that will not also volatilise cadmium. Most workers in the past [125,132-135] who have attempted a direct method have volatilised the cadmium at temperatures which would leave sea salts in the furnace. This required careful setting of temperatures, and was disturbed by situations that caused temperature settings to change with the life of the furnace tubes. [Pg.147]

Propane - Water System. The interaction parameters for the propane - water system were obtained over a temperature range from 42°F to 310°F using exclusively the data of Kobayashi and Katz (24). This is because among the available literature on the phase behavior of this binary system, their data appear to give the most extensive information. A constant interaction parameter was obtained for the propane-rich phases at all temperatures. The magnitude of the temperature - dependent interaction parameter for this binary was less than that for the ethane - water binary at the same temperature. Azarnoosh and McKetta (25) also presented experimental data for the solubility of propane in water over about the same temperature range as that of Kobayashi and Katz but at pressures up to 500 psia only. However, a different set of temperature - dependent parameters... [Pg.403]

Figure 9. AFM profiles of 1 - and 2-D gratings following annealing at sets of temperatures between 900C and 1200C. The 1 -D profiles shown in a) have a small flat at the maxima and minima except at 1200C and are nearly symmetrical. The 2-D profiles in b) also show flats at the lower temperatures and at 11OOC they are very asymmetrical[30]. Figure 9. AFM profiles of 1 - and 2-D gratings following annealing at sets of temperatures between 900C and 1200C. The 1 -D profiles shown in a) have a small flat at the maxima and minima except at 1200C and are nearly symmetrical. The 2-D profiles in b) also show flats at the lower temperatures and at 11OOC they are very asymmetrical[30].
The terms in the models may be classified by degree of complexity. First order terms cause linear effects, second order terms cause curvature, third order terms more complex curvature etc. When d, m, c, e, t, and h are used for, respectively, the concentrations of DBA, MeOH, CHCI3, EtAc and the setting of temperature and relative humidity, then examples of second order terms are d m, d e, e t and t h. The complete first order model is ... [Pg.250]

The results can be divided in several parts. The first part concerns the determination of suitable models which describe the R as function of the solvent composition, temperature and relative humidity. This part can be subdivided in the selection of a suitable Box-Cox transformation, determination of the suitable models and a discussion of the performance of the models found versus the more chromatographic models such as models (5) and (6). The second part of the results concerns the search for an optimum separation. This can be subdivided in a part concerning an optimum at a fixed setting of temperature and relative humidity and a part concerning the search for an optimum separation which is robust against changes in temperature and relative humidity. [Pg.254]

Accidental or uninstructed setting of temperature control above safe operating limits... [Pg.355]

Ash fusion temperatures set of temperatures that characterize the behavior of ash as it is heated. These temperatures are determined by heating cones of ground, pressed ash in both oxidizing and reducing atmospheres. [Pg.196]

Due to the irreversible heat exchange between the four heat reservoirs (for T0 = 300 K and T, = 600 K), the real maximum power is found to be close to a value of 0.3 rather than the ideal value of 0.5. The maximum power is found at an optimal flow rate (32 corresponding to an optimal set of temperatures T2 and T3/ satisfying the Carnot relation... [Pg.207]

Figure 5. Cell temperature as a function of gas flow rate with a different set of temperatures [4]... Figure 5. Cell temperature as a function of gas flow rate with a different set of temperatures [4]...
Based on the most recent set of temperatures and total flow rates, calculate the component vapor rates using the tridiagonal matrix method. Find the component liquid rates by l j = Ay i>y,... [Pg.156]

Calculate all of the independent functions and their norm. Get a new set of temperatures T/b by solving the independent equations during one pass through the Newton-Raphson procedure. [Pg.162]

Initialize the outside-loop variables the reference base K-value, KfyRet, the relative volatilities, a, and parameters Aj and Bj of the K-value model, parameters oy- and bi of the activity coefficient model and parameters Cj, Dt, E, and Fj of the enthalpy models, using the actual J -value and enthalpy correlations and the estimated set of temperatures and compositions. [Pg.175]

Data should be reported with a description of their quality. For example, the temperature of a spring measured by one person five times in succession was 16.5, 17.2, 14.0, 15.7, and 16.9° C. The same spring measured by a second person five times in succession yielded 16.0, 16.1, 15.8, 16.1, and 16.4° C. A quick glance reveals that the second person s measurements are closer to each other, or to use a more technical expression, the second set of data reveals a higher degree of reproducibility. This degree of reproducibility may be expressed quantitatively by calculating the mean deviation for the sets of data. The mean value in the first set of temperature measurements is 16.1° C and the mean deviation is + 1.0°C. Hence, the mean value of the first set of measurements is 16.1° C + 1.0° C. The mean value of the second set of measurements is 16.1° C + 0.2° C. Hence, the reproducibility in the... [Pg.102]


See other pages where Setting of temperature is mentioned: [Pg.945]    [Pg.493]    [Pg.158]    [Pg.660]    [Pg.953]    [Pg.204]    [Pg.6]    [Pg.510]    [Pg.56]    [Pg.44]    [Pg.126]    [Pg.504]    [Pg.67]    [Pg.13]    [Pg.63]    [Pg.66]    [Pg.186]    [Pg.55]    [Pg.236]    [Pg.140]    [Pg.447]    [Pg.204]    [Pg.148]    [Pg.258]    [Pg.27]    [Pg.399]   
See also in sourсe #XX -- [ Pg.238 , Pg.248 , Pg.492 ]




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Temperature set

Temperature settings

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