2014
DOI: 10.1002/er.3219
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Direct conversion of syngas to DME over CuO-ZnO-Al2O3/HZSM-5 nanocatalyst synthesized via ultrasound-assisted co-precipitation method: New insights into the role of gas injection

Abstract: SUMMARYIn this study, direct synthesis of dimethyl ether (DME) is conducted over a bifunctional CuO-ZnO-Al 2 O 3 /H Zeolite Socony Mobil-5 (HZSM-5) nanocatalyst. A hybrid method of ultrasound-assisted co-precipitation is used for the synthesis of catalysts, and the effect of gas injection during sonication is investigated. The physicochemical characteristics of the catalysts are analysed by X-ray diffraction (XRD), field emission scanning electron microscopy (FESEM), particle size distribution (PSD), energy di… Show more

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Cited by 14 publications
(10 citation statements)
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“…One is that the improvement of hydrophobicity of solid acid catalyst promotes the conversion of methylal and formaldehyde to PODE 2 and further polymerization reaction. PODE [2][3][4][5] selectivity was enhanced with the increase of dichlorodiphenylsilane content. Thus, the consumption of methylal leads to breaking the reaction equilibrium of methanol and formaldehyde to methylal and improvement of methanol conversion.…”
Section: Catalyst Activitymentioning
confidence: 97%
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“…One is that the improvement of hydrophobicity of solid acid catalyst promotes the conversion of methylal and formaldehyde to PODE 2 and further polymerization reaction. PODE [2][3][4][5] selectivity was enhanced with the increase of dichlorodiphenylsilane content. Thus, the consumption of methylal leads to breaking the reaction equilibrium of methanol and formaldehyde to methylal and improvement of methanol conversion.…”
Section: Catalyst Activitymentioning
confidence: 97%
“…Thus, the modified catalysts with dichlorodiphenylsilane exhibited higher performance in the target product selectivity. PODE [2][3][4][5] selectivity was enhanced with the increase of dichlorodiphenylsilane content. We can also conclude that the hydrophobic treatment can change the product distribution of methanol and formaldehyde aqueous solution to PODE.…”
Section: Catalyst Activitymentioning
confidence: 97%
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“…Gasoline range hydrocarbons (i.e., light hydrocarbon components) are normally produced using Iron (Fe)‐based catalysts at temperatures ≥300 ° C. Catalysts based on Cobalt (Co) are commonly employed at low reaction temperatures for the production of longer chain/heavier hydrocarbons (i.e., in the diesel and wax range). According to Allahyari et al and Bin et al , bifunctional catalysts like CuO–ZnO–Al 2 O 3 /H‐ZSM‐5 can produce high yields (>70%) of dimethyl ether from syngas at temperatures lower than 300 ° C. Modification of the reaction parameters such as catalyst compositions, temperature, syngas ratio, and pressure is therefore very critical in deriving specific liquid fuel components. Distillation process is usually accomplished to separate the various fuel components derived from the reaction.…”
Section: Syngas Upgrading Via Fischer–tropschmentioning
confidence: 99%
“…In recent decades, considerable efforts have been devoted to enhancing catalytic performance of SMNCs by modulating and optimizing their size, shape, composition and structure, among other parameters [15][16][17][18][19][20]. Accordingly, various SMNCs have been developed via numerous traditional methods, such as precipitation [21][22][23][24][25][26][27], sol-gel [28][29][30][31][32], solvothermal [33][34][35][36][37][38], and high temperature pyrolysis [39][40][41][42][43][44] (Fig. 1(b)).…”
Section: Introductionmentioning
confidence: 99%