Methanol 2018
DOI: 10.1016/b978-0-444-63903-5.00002-9
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State of the Art of Conventional Reactors for Methanol Production

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Cited by 22 publications
(21 citation statements)
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“…They might be caused either by pore diffusion inside the catalyst particle, by film diffusion through the boundary layer around the catalyst particle or by limited transport of the gaseous reactants into the carrier liquid [11,12]. Slurry reactors have the potential advantage that catalysts in powder shape can be applied without inducing a high pressure drop in the reactor [28]. For finding the upper size limit of the catalyst pellet, three pellet sizes of the same catalyst batch (see Tab.…”
Section: Excluding Mass Transport Effects In the Applied Slurry Methamentioning
confidence: 99%
“…They might be caused either by pore diffusion inside the catalyst particle, by film diffusion through the boundary layer around the catalyst particle or by limited transport of the gaseous reactants into the carrier liquid [11,12]. Slurry reactors have the potential advantage that catalysts in powder shape can be applied without inducing a high pressure drop in the reactor [28]. For finding the upper size limit of the catalyst pellet, three pellet sizes of the same catalyst batch (see Tab.…”
Section: Excluding Mass Transport Effects In the Applied Slurry Methamentioning
confidence: 99%
“…The commercial catalysts based on CuO/ZnO/Al 2 O 3 are widely used in methanol production [38], since they provide both high activity and selectivity of typically above 99.5% [29]. Nonetheless, there is still room for improvement of the catalyst performance in terms of activity, selectivity, stability, and durability [41]. Catalyst deactivation usually occurs due to the poisoning by the impurities in the system and due to thermal effects, such as sintering of the copper particles.…”
Section: Traditional Methodsmentioning
confidence: 99%
“…Catalyst deactivation usually occurs due to the poisoning by the impurities in the system and due to thermal effects, such as sintering of the copper particles. The representative converter designs and catalysts for methanol synthesis are thoroughly reviewed in the literature [29,30,35,38,41].…”
Section: Traditional Methodsmentioning
confidence: 99%
“…Ela inibe a sobreposição de locais ativos de cobre e isto influencia na adsorção e atividade do catalisador [56,58]. A presença de íons Al 3+ aumenta a área de superfície do catalisador e sua presença diminui a suscetibilidade da sinterização do cobre [46,61]. A alumina também protege o local ativo de envenenamento e sinterização.…”
Section: Catalisadores De Cu E Znunclassified
“…O cobre pode se apresentar na interface do óxido de zinco, como nanopartículas, como cobre metálico, ou como óxido [56,61]. Quanto maior a interface do cobre sobre o ZnO maior é a adsorção dos elementos do reagente [61].…”
Section: Catalisadores De Cu E Znunclassified