Catalyst utilization increased

This arrangement ensures more efficient overall catalyst utilization and a significant increase in the yield of octenes. As an example, dimer selectivity in the 90-92 % range with butene conversion in the 80-85 % range can be obtained with a C4 feed containing 60 % butenes. Thanks to the biphasic technique, the dimerization... 

Catalyst layer architecture As a consequence of the diminishing remrns from ever higher dispersion, the effort to increase the active catalyst surface area per unit mass of Pt has centered in recent years primarily on optimization of catalyst layer properties, aiming to maximize catalyst utilization in fuel cell electrodes based on Pt catalyst particle sizes of 2-5 nm. High catalyst utilization is conditioned on access to the largest possible percentage of the total catalyst surface area embedded in a catalyst... 

Antoine et al. [28] inveshgated the gradient across the CL and found that the Pt utilization was dependent on the CL porosity. In a nonporous CL, catalyst utilization was increased through the preferential locahon of Pt close to the gas diffusion layer in a porous CL, catalyst utilization efficiency was increased through the preferential location of Pt close to the polymer electrolyte membrane. In PEM fuel cells, fhe CL has a porous structure, and better performance is expected if higher Pf loading is used af preferential locahons close to the membrane/catalyst layer interface. 

As mentioned, the reaction distribution is the main effect on the catalyst-layer scale. Because of the facile kinetics (i.e., low charge-transfer resistance) compared to the ionic resistance of proton movement for the HOR, the reaction distribution in the anode is a relatively sharp front next to the membrane. This can be seen in analyzing Figure 10, and it means that the catalyst layer should be relatively thin in order to utilize the most catalyst and increase the efficiency of the electrode. It also means that treating the anode catalyst layer as an interface is valid. On the other hand, the charge-transfer resistance for the ORR is relatively high, and thus, the reaction distribution is basically uniform across the cathode. This means... 

Intramolecular rhodium-catalyzed carbamate C-H insertion has broad utility for substrates fashioned from most 1° and 3° alcohols. As is typically observed, 3° and benzylic C-H bonds are favored over other C-H centers for amination of this type. Stereospecific oxidation of optically pure 3° units greatly facilitates the preparation of enantiomeric tetrasubstituted carbinolamines, and should find future applications in synthesis vide infra). Importantly, use of PhI(OAc)2 as a terminal oxidant for this process has enabled reactions with a class of starting materials (that is, 1° carbamates) for which iminoiodi-nane synthesis has not proven possible. Thus, by obviating the need for such reagents, substrate scope for this process and related aziridination reactions is significantly expanded vide infra). Looking forward, the versatility of this method for C-N bond formation will be advanced further with the advent of chiral catalysts for diastero- and enantio-controlled C-H insertion. In addition, new catalysts may increase the range of 2° alkanol-based carbamates that perform as viable substrates for this process. 

In this article we approach the topic of coherent control from the perspective of a chemist who wishes to maximize the yield of a particular product of a chemical reaction. The traditional approach to this problem is to utilize the principles of thermodynamics and kinetics to shift the equilibrium and increase the speed of a reaction, perhaps using a catalyst to increase the yield. Powerful as these methods are, however, they have inherent limitations. They are not useful, for example, if one wishes to produce molecules in a single quantum state or aligned along some spatial axis. Even for bulk samples averaged over many quantum states, conventional methods may be ineffective in maximizing the yield of a minor side product. 

Zinc fluoride can often be used in a polar solvent to effect fluorinations that are difficult with other reagents (equation 18). The addition of CI2 or SbCls to SbFs as a catalyst greatly increases the utility of SbFs in flnorinations (equations 19-22). 

Figure 24 describes schematically the three recent modes of preparation of membrane/electrode assemblies based on commercially available dispersed platinum catalysts. Comparison of catalyst utilization obtained with the different PEFC catalyzation techniques is given in Fig. 25. The advantage in catalyst utilization of the thin-layer approach is clearly seen, increasing at the higher cell currents (lower cell voltage) thanks to minimized mass-transport limitations in the thin catalyst layer.

Fig. 25. Air cathode catalyst utilization for different types of catalyst layers in contact with ionomeric membranes. , Platinum black/PTFE (4 mg/cm ) ionomer-impregnated gas-diffusion electrodes (0.45 mg Pt/cm ) A, thin film of Pt/C//ionomer composite (0.13 mg Pt/cm ). The advantage of thin-film catalyst layers increases particularly at high current density (lower cell voltage) because transport limitations within the catalyst layer are minimized.

Equation (22) shows that the total surface area of the catalyst at given level of dispersion (given r) increases linearly with overall catalyst mass loading, m. The same is not true, however, for the effective or utilizable catalyst surface area. It has been the experience of developers of PEFC and DM FC M EAs that, catalyst utilization,... 

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