1992
DOI: 10.1007/bf00770902
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Characterization of silica supported Ni and Mg basic carbonate catalyst precursors

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Cited by 4 publications
(6 citation statements)
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“…Therefore the presence of Mg 2+ minimizes the reducibility difference between the two Ni species, resulting in a symmetric TPR peak. 31 In the metalcatalyzed CVD process, the morphologies of the as-synthesized nanostructures are normally closely related to the shape and size of the metal clusters. The shape and size distribution of the metal clusters are determined by the reaction conditions, which are chosen primarily based on the reduction stability of the metal catalysts.…”
Section: Characterization Of Metal Incorporated Mcm-41mentioning
confidence: 99%
“…Therefore the presence of Mg 2+ minimizes the reducibility difference between the two Ni species, resulting in a symmetric TPR peak. 31 In the metalcatalyzed CVD process, the morphologies of the as-synthesized nanostructures are normally closely related to the shape and size of the metal clusters. The shape and size distribution of the metal clusters are determined by the reaction conditions, which are chosen primarily based on the reduction stability of the metal catalysts.…”
Section: Characterization Of Metal Incorporated Mcm-41mentioning
confidence: 99%
“…In general, such nanoparticles of metals such as nickel, palladium, ruthenium, or platinum are used for hydrogenation, since the dissociatively adsorbed hydrogen is easily accessible on these group VIII metals. Supported metal catalysts containing both a group VIII and a group II metal [32,35,36], or a case where the catalysts containing both a group VIII and a group IB metal [22,29,[37][38][39][40] although insufficiently studied, can be found in the literature. In these catalysts, the metal of group II or group IB is added as the modifier with the purpose of promoting the cis-isomer selectivity.…”
Section: Introductionmentioning
confidence: 99%
“…In the partial hydrogenation process of edible oils, a catalyst with the high activity and selectivity is required [50][51][52]. To meet these requirements, the catalyst support should provide sufficient surface area for the metal to disperse and there must be adequate metalsupport interaction [35,43,46,48,49,[53][54][55][56][57]. The nickel phase on different support surfaces exhibits different extents of metal-support effects.…”
Section: Introductionmentioning
confidence: 99%
“…21,22 To investigate the correlation between o-Ps lifetimes and pore size/pore size distribution, a series of compounds having a varying SiO 2 /Ni ratio and doped with Mg and Li separately were synthesized in a controlled manner with different pore sizes. 20 An attempt has been made to correlate the results of PAL investigations with BET data.…”
Section: Introductionmentioning
confidence: 99%
“…They are reduced at (400−450 °C) to convert them into supported nickel catalysts used in the hydrogenation of oils. In these amorphous systems, reduced nickel crystallite is attached/bonded to the porous network structure of Si−O−Ni linkages. , Evidence of such bonding comes from higher reduction temperature (400−500 °C) for nickel in these compounds compared to unsupported systems (300−320 °C) as well as incomplete reduction of nickel in supported systems even at 450 °C. , To investigate the correlation between o-Ps lifetimes and pore size/pore size distribution, a series of compounds having a varying SiO 2 /Ni ratio and doped with Mg and Li separately were synthesized in a controlled manner with different pore sizes . An attempt has been made to correlate the results of PAL investigations with BET data.…”
Section: Introductionmentioning
confidence: 99%