[article]
Titre : |
Dimethyl ether synthesis from CO2 hydrogenation on a CuO-ZnO-Al2O3-ZrO2/HZSM-5 bifunctional catalyst |
Type de document : |
texte imprimé |
Auteurs : |
Xin An, Auteur ; Yi-Zan Zuo, Auteur ; Qiang Zhang, Auteur |
Année de publication : |
2008 |
Article en page(s) : |
p. 6547–6554 |
Note générale : |
Chemical engineering |
Langues : |
Anglais (eng) |
Mots-clés : |
Dimethy ether synthesis CO2 hydrogenation Bifunctional catalyst |
Résumé : |
A CuO−ZnO−Al2O3−ZrO2 + HZSM-5 physical mixture bifunctional catalyst with a high activity for dimethy ether (DME) synthesis was used for CO2 hydrogenation. Various factors that affect catalyst activity, including the reaction temperature, pressure, and space velocity, were investigated. CO2 conversion reached 0.309, and DME and methanol yields were 0.212 and 0.059 with a stoichiometric ratio of H2 to CO2 of 3 at 523 K, 5 MPa, and a space velocity of 6000 mL/(g cat·h). Well-studied kinetic models for methanol synthesis and methanol dehydration, respectively, were used to fit the experimental data and the kinetic parameters in the rate equations for DME synthesis were obtained by regression. A simulated process for CO2 hydrogenation indicated that a higher DME yield can be obtained with CO recycle that will also give a CO-free product. |
En ligne : |
http://pubs.acs.org/doi/abs/10.1021/ie800777t |
in Industrial & engineering chemistry research > Vol. 47 N°17 (Septembre 2008) . - p. 6547–6554
[article] Dimethyl ether synthesis from CO2 hydrogenation on a CuO-ZnO-Al2O3-ZrO2/HZSM-5 bifunctional catalyst [texte imprimé] / Xin An, Auteur ; Yi-Zan Zuo, Auteur ; Qiang Zhang, Auteur . - 2008 . - p. 6547–6554. Chemical engineering Langues : Anglais ( eng) in Industrial & engineering chemistry research > Vol. 47 N°17 (Septembre 2008) . - p. 6547–6554
Mots-clés : |
Dimethy ether synthesis CO2 hydrogenation Bifunctional catalyst |
Résumé : |
A CuO−ZnO−Al2O3−ZrO2 + HZSM-5 physical mixture bifunctional catalyst with a high activity for dimethy ether (DME) synthesis was used for CO2 hydrogenation. Various factors that affect catalyst activity, including the reaction temperature, pressure, and space velocity, were investigated. CO2 conversion reached 0.309, and DME and methanol yields were 0.212 and 0.059 with a stoichiometric ratio of H2 to CO2 of 3 at 523 K, 5 MPa, and a space velocity of 6000 mL/(g cat·h). Well-studied kinetic models for methanol synthesis and methanol dehydration, respectively, were used to fit the experimental data and the kinetic parameters in the rate equations for DME synthesis were obtained by regression. A simulated process for CO2 hydrogenation indicated that a higher DME yield can be obtained with CO recycle that will also give a CO-free product. |
En ligne : |
http://pubs.acs.org/doi/abs/10.1021/ie800777t |
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