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I compares the experimentally obtained data and the theoretically computed heat transfer values through typical samples. The edge losses due to radiation from warm walls of the apparatus to the specimen s side area were estimated on the basis of results obtained with - and ys-in.-thick samples.

I compares the important physical properties of the currently used acrylic resin denture bases - the heat cured and self cured bases. These are typically powder liquid mixtures containing benzoyl peroxide redox systems activated by a tertiary aromatic amine. Among these are the vinyl chloride - vinyl acetate - methyl methacrylate mixtures and the newer pour type denture bases - the latter designed for laboratory convenience and model fit by control of polymerization shrinkage. On this half of the table the important comparative properties are transverse deflection, failure and water sorption.

I compares the measured values of extinction coefficients with the values calculated from theory at wavelengths of 25U, 280 and 350 nm. The lower values of extinction coefficients for the larger particles measured, using the online detector compared to the Beckman instrument, are due to the optical effects discussed above. The disagreement between the extinction coefficients calculated from Mie theory for non-absorbing spheres and the measured values from the Beckman instrument is very significant, particularly at 2 k and 280 nm.

I compares the pore properties for the starting metakaolln and the LSX pellets, and Figure 6 plots differential pore volume distributions for both materials. The pore distribution data show that the macroporosity of the LSX pellets 1s approximately half that of the starting metakaolln. The difference between pore volumes measured with helium and mercury 1s used as an Indicator for the microporosity of the sample.

I compares the predicted and measured decay constants.. Calculated values of K f are shown for reference. The uncertainty indicated for the decay constants is only the standard deviation due to counting statistics based on the least squares analyses of the various runs. Measured and calculated values agree within 47. The differences increase steadily with decreasing core size.

I compares the reactivity of 1 with that of other catalysts for eq 1 . All

I compares the relative field plot aphid ratings with the composition and levels of the trichome-produced cuticular components. The aphid susceptible cultivars NC 2326 . The TI 1112 and breeding

I compares the results for the hydrogenation of 1-hexene in methanol with the intercalated and homogeneous catalyst systems. Under the reaction conditions employed, the hydrogen uptake rate is lower for the intercalated catalyst than for the homogeneous catalyst. However, the intercalated catalyst greatly reduces the extent of 1-hexene to 2-hexene isomerization, relative to homogeneous solution. The ability of the intercalated catalyst to inhibit substrate isomerization has been attributed to the existence of a surface equilibrium between a monohydride

I compares the saddle point characteristics of the Raff surface to those calculated by the ab initio polarization-configuration-interaction method.The Raff surface has a lower and earlier, but also thinner barrier. Since, all other things being equal, one expects higher barriers to have higher imaginary frequencies, it

I compares the specifications for the 40-55 grades. Glyceryl monostearate PhEur and mono- and di-glycerides USPNF. PhEur divides glyceryl monostearate 40-55 into three types according to the proportion of stearic acid ester in the mixture, and those specifications are presented in Table II. Table III presents the specifications for glyceryl monostearate USPNF . Since the JP specifications are broad enough to encompass both grades, JP is included in both Table I and Table III.

I compares the two methods in regard to many factors.

I compares the work input and rate of entropy production in the practical process with corresponding quantities in the ideal process. This brings out the fact that the single place where the greatest reduction in power can be effected is in the main exchanger, and also shows the relative importance of the individual pieces of equipment as contributors of the total work input. It also shows that the total work input is the sum of the work equivalent of irreversible entropy production, given by the product of AS rr and ambient temperature To.

I Comparism of Collagen and Procollagen

I Comparison of Activities from Labeled D-Ghicose Calculated for Tetrose Phosphate, and Found in Carbon Atoms S,4,S, and 8 of Shikimate

I Comparison of averages for different flows and drag reduction methods.

I Comparison of Bitumen Upgrading Processes

I Comparison of Brisance Values Calculated by Kast s Formula, Relative Brisance Values Obtained by Various Experimental Procedures

I Comparison of Catalytic Properties of Ferrierite Like Materials.

I COMPARISON OF COMPUTER-CONTROLLED YEAST FERMENTATIONS WITH DIFFERENT

I Comparison of Crystallinity Values Obtained by Infrared and by X-ray Measurements

I Comparison of DDT Distribution in Hood River and Medford Orchard Soils, 1965

I Comparison of EcQC, 2 for in Eq. with EcAPP, as where n is the ground-state density of Hj30

I Comparison of Endgroup Determinations

I Comparison of energy correlations in UHV adsorption experiments

I Comparison of Estimated and Experimental Vibrational Frequencies for Trifluoromethyl.



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