Higher Alcohols Synthesis over Carbon Nanohorn-Supported KCoRhMo Catalyst: Pelletization and Kinetic Modeling

Abstract

In this study, two catalyst grain sizes (fine powders and pellets) have been investigated to elucidate the effects of both external and internal mass transfer diffusion as well as particle size during the CO hydrogenation reaction to produce higher alcohols. Catalyst grain sizes of 88 and 254 μm were advisedly chosen based on our previous investigations with a similar catalyst matrix for the higher alcohol synthesis (HAS) reaction. The focus in this work was to explore the attractive textural properties of CNH support for CO hydrogenation reaction to produce higher alcohols under specified reaction conditions. Also, to ascertain the possibilities of commercialization of the developed carbon nanohorn (CNH)-supported KCoRhMo catalyst, bentonite clay was added to the pristine support as a binder to enhance its mechanical/crushing strength and kinetic analyses of such catalyst assessed. The influence of bentonite clay was investigated by incorporating 5 wt % of this binder into the formulation of the KCoRhMo/CNH catalyst. For mass transfer considerations, the finely ground KCoRhMo/CNH catalyst powder of 88 μm particle size was used so as to eradicate mass transfer resistance. CO hydrogenation experiments were carried out using a twophase fixed-bed reactor system to ascertain the intrinsic kinetics of the liquid alcohol products (methanol, ethanol, higher alcohols) as well as the gaseous products generated by the reaction. Syngas of H 2 /CO ratio of 1.25 was used as feedstock at temperatures, pressures, and gas hourly space velocity ranges of 290−350 °C, 800−1400 psig, and 2.4−4.8 m 3 STP/kg cat /h, respectively. The power law model was used to fit experimental data to evaluate kinetic parameters for the HAS reaction on the catalyst surface. Fitting of the experimental data with the developed power law models showed good fits with high R 2 values in the range of 0.88−0.96 for the components evaluated. The activation energies computed for ethanol and propanol in the HAS reaction over CNH-supported KCoRhMo catalyst were 54.4 and 92.2 kJ/mol, which are low compared to values obtained by other researchers in similar studies.

CO hydrogenation over K‐Co‐MoSxcatalyst to mixed alcohols: A kinetic analysis

“…It should be mentioned that the water concentration was about 10% of the overall liquid products, which is negligible. For kinetic model development, a power‐law approach was applied 19,27,30–32 . Reaction rates of the individual compounds are expressed as follows: …”

“…For kinetic model development, a power-law approach was applied. 19,27,[30][31][32] Reaction rates of the individual compounds are expressed as follows:…”

Sustainable Aviation Fuel from Syngas through Higher Alcohols

“…It was proposed that graphene oxide can act as an electron donor enhancing carbides formation, which in turn enhances higher alcohol synthesis. In that case the cobalt particle size was only 8.6 nm (Table 2, entry 13) [25] . Interestingly it was also confirmed that the alcohol selectivity at the same CO conversion level was directly comparative to the ratio of Co 2 C/Co determined by XRD when using catalysts with different amounts of graphene oxide (GO) in Co/GO‐OMS catalysts [29] .…”

Selective Conversion of Syngas into Higher Alcohols via a Reaction-Coupling Strategy on Multifunctional Relay Catalysts

“…The results suggest that the effects of GHSV on external mass-transfer diffusion are negligible in our work. The effects of internal diffusion were also estimated according to the Weisz–Prater criterion ( C WP ), − which was summarized in Table S7. When C WP ≪ 1, internal diffusion limitation is negligible, and if C WP ≫ 1, there are internal diffusion effects on the reaction.…”