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Historically, skeletal nickel is the catalyst of choice in the production of sorbitol on industrial scale.
Currently, for the industrial ethylene epoxidation α-alumina supported silver catalysts are the only catalyst of choice.
This development is prompted by the observation that supported gold catalysts can be a catalyst of choice for some reactions.
The chloroperoxidase from Caldariomyces fumago (CPO) is the catalyst of choice in sulfoxidation, hydroxylation and epoxidation on account of its high activity and enantioselectivity.
A catalyst of choice is one that is inert and can liquefy, if not as a pure element, at least by eutectic reaction with another element, below the growth temperature.
Despite current debates in relation to the order of activity of group VIII elements in DRM reactions, Rh was always elected as the catalyst of choice by most chemists.
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Since extremozymes also exhibit high resistances to solvents, detergents, and high pressure (Alcaide et al. 2014), they became the catalysts of choice in different industrial bio-processes (Egorova and Antranikian 2005).
In this paper we stress the critical role of future load serving entities (LSEs) as aggregators and catalysts of customer choice at the value as one possible way forward.
Finally, the implications of catalyst choice for application in different reactors are discussed, paying specific attention to the maximum production capacity of a single reactor.
The preparation of Pt-zeolite catalysts, including choice of the noble metal precursor and loading (1.0 1.8 wt.%), was optimized for maximizing the catalytic activity in thiophene hydrodesulphurization (HDS) and benzene hydrogenation (HYD).
For this reason here we present a methodology based on computer-aided and mathematical tools to solve the problem of choice of catalysts for a hydrotreating industrial process.
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