(149b) CO2 As a Carbon Source in Direct Synthesis of Dimethyl Ether from Syngas over Silicotungstic Acid Incorporated Bifunctional Catalysts | AIChE

(149b) CO2 As a Carbon Source in Direct Synthesis of Dimethyl Ether from Syngas over Silicotungstic Acid Incorporated Bifunctional Catalysts

Authors 

Dogu, T. - Presenter, Middle East Technical University
Dogu, G., Gazi University
Karaman, B. P., Gazi University
Dimethyl ether (DME) is one of the most promising environmentally friendly diesel fuel alternates with a high cetane number and clean-burning properties. Its synthesis directly from syngas has significant thermodynamic advantages over the conventional two-step process involving methanol synthesis and dehydration reactors [1, 2]. The use of CO2 as the carbon source in the synthesis of DME has added advantages of converting one of the most abundant greenhouse gases to a valuable chemical. Direct synthesis of DME from CO2 requires the development of novel bifunctional catalysts containing both methanol synthesis and dehydration sites within the same proximity. In the present study, core-shell type bi-functional catalysts and an STA incorporated Cu-Zn-Al type methanol synthesis catalyst (25STA@CZA:6/3/1) were synthesized and tested in direct synthesis of DME from syngas containing different CO2/CO mole fractions, ranging between 1/0 and 0/1. In the case of core-shell type catalytic materials (25STA@CZA-EMA), γ-Al2O3 was deposited over the methanol synthesis catalyst, and then STA was impregnated into this layer. Activity test results proved that the overall conversion of CO+CO2 and DME yield values advance with an increase in CO2/CO ratio until a feed composition of H2/CO2/CO = 50/40/10. The highest overall conversion of CO2+CO and the corresponding DME yield values were obtained as 73.4% and 51%, respectively, over the 25STA@CZA catalyst, at 275oC and 50 bar. In the case of using a feed mixture containing only CO2 and H2, lower overall conversion and DME selectivity values were obtained (20% and 55%, respectively). In this case, conversion of CO2 to CO and H2O through reverse-water-gas-shift reaction gains importance, and the increase of H2O in the product stream negatively affects the in-situ dehydration reaction of produced methanol. Results proved that the new STA incorporated methanol synthesis catalysts were highly promising for the conversion of CO2- containing syngas to DME, and the optimum CO2/CO ratio for the highest DME yield was 4/1.

[1] Karaman, BP, Oktar, N., Dogu, G, Dogu, T (2020). Catal. Letters, 150: 2744-2761.

[2] Bayat, A, Dogu T. (2016). Ind. Eng. Chem. Res., 55:11431-39.