Journal of Northeastern University ›› 2009, Vol. 30 ›› Issue (1): 113-116+124.DOI: -

• OriginalPaper • Previous Articles     Next Articles

A new low-temperature synthesizing process of methanol from CO/CO2/H2 and catalysts used

Li, Wen-Ze (1); Zhang, Bao-Yan (1); Xiao, Lin-Jiu (2); Yang, Rui-Qin (2)   

  1. (1) School of Sciences, Northeastern University, Shenyang 110004, China; (2) School of Applied Chemistry, Shenyang Institute of Chemical Technology, Shenyang 110142, China
  • Received:2013-06-22 Revised:2013-06-22 Online:2009-01-15 Published:2013-06-22
  • Contact: Li, W.-Z.
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Abstract: Methanol was synthesized with syngas (CO/CO2/H2) as starting material and Cu-Zn based catalysts at low temperature/pressure (443 K/3.0 MPa), where the 2-butanol was used as solvent. In such a reaction process the alcohol solvent was not consumed but played a catalytic role. The effects of the carriers and rare-earth additives on the activity of catalyst were investigated, and the results showed that the Cu/ZnO catalyst exhibits the highest activity in all catalysts prepared using ZnO, MgO, Al2O3, La2O3, Y2O3 as carriers in low-temperature synthesis reaction process of methanol. The activity of the Cu-Zn based catalysts increases if using rare-earth elements as additives, and the highest activity belongs to the Cu/ZnO/Y2O3 catalyst in which the Y content is 7.5 wt% or the Cu/ZnO/La2O3 catalyst in which the La content is 10 wt%, i.e., the total carbon conversion rate is 10 % or 17.5% higher than using Cu/ZnO only, respectively. The methanol output increases by 17.5% if using Cu/ZnO/Y2O3 or Cu/ZnO/La2O3 catalyst in comparison with using Cu/ZnO catalyst.

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