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The performance of the high activity DN 110 V2O5/Al2O3 catalyst is given for many design operating parameters along with information on catalyst activity under commercial conditions for various units.
HDS activity of each MoS2 catalyst was tested, and the %DBT conversion of each catalyst is given in Table 2.
A summary of the different reactions involved upon the reducing treatment in 10%% H2 in Ar of the citric acid-synthesized CoMo catalyst is given in Fig. 9.
A schematic representation of the evolution of Co and Mo citrate species with the thermal treatment to produce Co and Mo oxo species dispersed on alumina and the panoramic image of the sulfided catalyst is given in Fig. 10a.
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When the surface heat flux as well as the total mass of porous catalyst are given, solving the newly deduced governing equations directly gives the optimal porosity distribution of catalyst under different working conditions.
The results for carburised support and supported catalyst are given in Fig. 6b and c, respectively.
The FTIR spectra of both Pomacea sp. shell and catalyst are given in Figure4.
The estimated values of kinetic constants both in presence and absence of the Pd(0) catalyst are given in Table 1 for each combustion temperature.
The structure, p Ka values, and specific disulfide-reductase activities for these peptide substrates (I IV) using mTR3Δ8 as the enzyme catalyst are given in Table 1.
A detailed description of the materials and instrumentation used in this study, as well as the procedure for preparing the reference Pt Sn/Al2O3 catalyst, are given in the Supporting Information.
The application of such studies to vanadia-titania DeNOx catalysts is given.
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