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VI shows the F n.m.r. enhancements for some disubstituted

VI shows the final risk assessment of CGA-72662 to aquatic organisms.

VI shows the following points for the reactivities of asym DAMs

VI shows the GPC results of the polymerization catalyzed by Pd-Gr and palladium acetate. When Pd-Gr was used as a catalyst, the polydispersity indices were lower than those of the polymer prepared by using Radium acetate. Tbe control experiments using an equimolar amount of ethyl acrylate and iodobenzene with Pd-Gr or palladium acetate were carried out in the same condition as the polycondensation. In the case of Pd-Gr, the amount of the product by the second

VI shows the grafting experiments made with 360-A latices. Grafting runs again showed that the initiator system has a significant part in the properties of the grafted polymer. The persulfate system produced a polymer with almost twice the tensile impact as the pentamine peroxide system. Run 33 was scaled-up in the pilot plant.

VI shows the influence of dilution in a Na-4NBr. The smaller precursors are formed in the presence of higher concentrations of TMA ions. Therefore, it seems that TMA ions stabilize not only the precursors of the A-type structure, presumably double 4-rings, but also, at higher concentrations, single 4-rings and 6-rings. The same number of TMA ions may be required for stabilization of either precursor this explains the concentration effect.

VI shows the interaction energies of Ar, 02 and N2 interacting with isolated cations. For Ar, Eqs. . For 02 and N2, the values were calculated from quantum mechanics which represent the sum of L-J and electrostatic interactions Mellot and Lignieres,

VI shows the interaction energies of Ar, O2 and N2 interacting with isolated cations. For Ar, Eqs. . For O2 and N2, the values were calculated from quantum mechanics which represent the sum of L-J and electrostatic interactions Mellot and Lignieres,

VI shows the limiting anion conductances determined from the measurements underlying Fig. 5. Extrapolations were made by taking into account the association of the electrolyte compounds KSCN and Mc4NSCN in methanol via Eqs. . As a result, the theoretical requirement of equal limiting anion conductances is fulfilled within the limits of experimental error.

VI shows the major element composition of the samples as determined by the various laboratories. This table was compiled to emphasize that while there are large discrepancies in the results, most of the laboratories could characterize the samples correctly. Thus, sample 1 is a moderately high tin bronze fail to characterize the samples correctly while the other 17 characterize this sample as a moderately high tin bronze with a little lead.

VI shows the matrix relating the number of amino acids changed per 100 residues between any two dehydrogenases when aligned as shown in Table IV. The uncertainties in correcting for back mutations and superpositions are exceedingly great for proteins that have diverged as far as these dehydrogenases. Thus no attempt has been made to determine the number of accepted point mutations. On the other hand, if the basis

VI shows the range of properties of grades 1, 2, and 4 burner fuel oils marketed in the United States in 1974 . The shale-oil types C-B and T-T diesel fuels would, respectively, fit with the grades 1 and 2 burner fuels. The shale-oil S-M diesel fuel would also fit with the grade 2 burner fuels. The shale-oil fuel oil fraction had a distillation range resembling the grade 2 fuels, but its viscosity was intermediate between those of the grade 2 and grade 4 fuels.

VI shows the rates of S

VI shows the rejection measured for total N2, polyphenols and sugars with DDS 800 and PA 300 membranes. Sugar rejections increased from about 20 with DDS 800 to 100 with PA 300. Table VII shows the rejections of various cations using the PA 300 membrane. The rejection for the majority of cations is higher than 97 . Only Cu and Zn permeate easily through the membrane. The rejections for these two cations is essentially zero. The reason is attributed to a high specific interaction of Cu and Zn with the polymeric materials forming the membranes and to Donnan equilibrium.

VI shows the relative reactivities of various asym DAMs. An equi-molecular mixture of two kinds of asym DAMs was fed as a 5 benzene solution and hydrogenolyzed in order to check the effect of the methyl group on the reactivity. Two kinds of asym DAMs having similar reactivities were selected as a combination. The reaction conditions were temperature, 400 C H2 hydrocarbons molar ratio, 2. The contact time was changed since the reactivities of asym DAMs differed considerably according to their structures this made it possible to evaluate the different reactivities. Side reactions such as demethylation, isomerization, and disproportionation were negligible under these reaction conditions. The relative values for the reactivities of the asym DAMs shown in Table VI are determined when the value of 2,5-DMeDPM as a standard material is fixed at 100.

VI shows the results obtained from the fractionation, according to the non-simplified scheme, of a crude polymerizate containing

VI shows the results of a number of these experiments, using different magnesium sulfate concentrations. The increase of fractionation efficiency with increase of the salt concentration is evident. Independent of the salt concentration, all experiments yield amylose fractions of maximum iodine-absorption capacity, as recrystallization with 1-butanol did not show any increase in the original values.

VI shows the results of polarized light microscopic observations. Sometimes isotropic regions and the middle phase exist simultaneously. The region of the middle phase is marked by heavy lines. The range of the especially viscous middle phase narrows with transition from two to three oxyethylene groups in the surfactant molecule. Up to 27 , the system appears optically isotropic. In this concentration range the viscosity can be increased strongly by addition of NaCl, as shown in table VII.

VI shows the results of predictions similar to those of Tables III and IV for several of the cities for which V concentrations are given in Table V. We have not shown the marine aerosol components since their V contributions are negligible compared with the continental dust components.

VI shows the results of some accuracy comparisons which we have made. The dot product results correspond to a dot product of two vectors of 1000 elements, with random values between 0 and 1. This shows that the AP 190L result gives the first 7 figures of the results from the IBM 370 double precision calculation. The other entries in Table VI show results from the Monte Carlo calculations.

VI shows the results of the three continuous fermentations completed with the r424A organism. The carbon source in the fermentation media was corn fiber hydrolysate produced by the initial hydrolysis method followed by secondary acid hydrolysis. The yeast metabolized over 60 of the total carbohydrates with a g ethanol g carbohydrate yield between 0.50 and 0.55. The lower percentage of total carbohydrates metabolized is likely due to the continuous fermentation method, as shake flask fermentations, albeit at lower dry solids, metabolized up to 91 of the carbohydrates . The carbohydrate utilization will be optimized in future fermentations. The g g yield is near theoretical, therefore the metabolized carbohydrate is converted solely to ethanol. The organic acids, ethanol and dextrose concentrations for a sample fermentation are shown in Figure 1. The ethanol concentration in the fermentor at the end of the run was 55g L. The concentrations of the citric acid, lactic acid and glycerol increase substantially during the fermentation, which are normal byproducts of the ethanol fermentation by Saccharomyces cerevisiae. The volume of the fermentation was doubled with hydrolysate fed into the fermentor. These fermentations show that the organism can ferment the glucose and xylose from the corn fiber hydrolysate to ethanol without detoxification of the hydrolysate. The fermentation conditions were not optimized, so additional improvement in the fermentation is expected.

VI shows the situation. With various concentrations of copper alone, p-nitrophenylglycine ethyl ester is hydrolyzed and the copper catalyzes the hydrolysis. The observed catalysis is rather modest for the hydrolysis of this particular amino acid ester, and the hydrolysis rate is

VI shows the step or cycle

VI shows the water retained in samples Dunk-N-Drain test at zero minute and after oven drying at 100 F at different intervals of time up to 150 minutes. Sample 104 retained 54 g of water vs. 0.15 g in control gauze, after drying for 150 minutes. Since the healthy human body temperature is around 98.6 F, we used a drying temperature of 100 F. The test data have shown that the CM-dressings maintain a moist environment at 100 F.

VI shows values calculated for the ions in Table V for a dielectric constant of 6, which was found to be the dielectric constant of the primary hydration layer. , the permittivity of free space is 8 854 x 10 N m

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