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I Differences between Myeloma Antidextrans W3129 and QUPC 52

I Different characteristics of the catalysts

I Diffraction Energy of d Spacings of RDX for three 2ff Angles

I Diffusion Coefficients of a Number of Steroids, Narcotics and One Prostaglandin in Five Polymers Commonly Used for Drug Delivery

I Diffusion coefficients of ammonia vapor and

I Diffusivities of benzene in H-ZSM-5 or silicalite-1 and comparison with literatme

I Dimensions of Zeolites Commonly Used in Catalysis

I Dipole Moments of isotaotia Poly

I Dipole Moments x of Diatomic Molecules

I Dirac Fock, point nucleus Finite nucleus Breit interaction Transverse correction Self energy Vacuum polarization

I displays the heat resistance, haze, and mechanical properties of blends consisting of PEC and PC-PDMS. When PEC and PC-PDMS were blended and extruded, the plastic pellets were hazy and white . Upon injection-molding of the pellets into plastic articles, the molded disks were pearlescent, showed streaking, and were nearly opaque. However, when the TE catalyst was used in the formulation, the two polymers became more transparent and did not show any pearlescence or flow lines after injection molding. Examples 1-3 each had the TE catalyst in the formulation, which made the blends more miscible and less hazy. The heat resistance of the products was varied by changing the PEC to PC-PDMS ratio in the formulation, and the heat resistance was not significantly affected by the addition of the TE catalyst. The notched-izod impact strength was not decreased by the addition of TE catalyst, and all materials were 100 ductile at 23 C. Chart 1 shows the optical characteristics of Examples 1-6. The chart shows that the percent haze is decreased dramatically by the addition of TE catalyst to the blend.

I displays the mole fraction of the MMA which is in the aqueous phase for the Lj phase and microemulsion systems studied. These fractions were found to be reproducible to within 0.04. As can be seen, MMA favors the micellar phase by at least a four-to-one ratio. The free energy of transfer, calculated for systems less than 0.53 M in MMA was found to be -14.0 kJ mole with an uncertainty of 10 .

I displays the results of rapid, and slow pyrolyses of birch and oak wood at 0.1 MPa. The charcoal yield for rapid heating of birch is 29.5 , and the fixed carbon yield is 21.4 . An increase in the heating time from about 90 min to about 4 h followed by a 4 h soak at 450 C increases the fixed carbon yield to 22.8 . The yields of charcoal from oak wood are somewhat higher than those obtained by American industry with this feed in a Missouri kiln.

I displays the results over several thousand hours of exemplary samples tested at zero length, zero recovery. Brackish water rejection under conditions specified are in excess of 99 at high pressure and greater than 98.5 at lower pressure such as 400 psi. Flux values displayed are those typical of early samples in the development of Quantro II. At low pressure against brackish water such values were 1-2 gfd. Recent values of samples tested under identical conditions have exhibited rejections of 94 at a flux of 5-7 gfd at 400 psi.

I displays values of k for granulated zeolites CaA-I and CaA-II 12 and the pressed powdered zeolite NaX 13 .

I Dissociation Constants of Model Compounds in Aqueous Solution at or Near M C

I Dissociation Energies, D kJ mol- of Homonuclear Diatomic d-Transition Metal Molecules

I Dissociation lifetime of actinomycin D from Poly and temperature.

I Dissolved Organic Carbon and Major Elements in Size-fractionated Samples from Volo Bog.

I Distribution and Putative Functions of Selected High Affinity Calciproteins

I Distribution of Gums According to Industrial Usage33

I Distribution of Heparin in the Body

I Distribution of Maltooligomers at the Hydrolysis of y-cyclo-dextrin by Aspergillus oryzae a-amylase at pjj 5.2 and 31 C

I Distribution of Photolyase and Cryptochromes in the Biological World

I Distribution of the Products of Alkylation of Free Sucrose



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