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    Yu-ping Li, Jun-ling Tu, Tie-jun Wang, Long-long Ma, Xing-hua Zhang, Qing Zhang, Chi-liu Cai. Production of Light Olefins from Biosyngas by Two-stage Catalytic Conversion Process via Dimethyl Ether[J]. Chinese Journal of Chemical Physics , 2014, 27(2): 227-232. DOI: 10.1063/1674-0068/27/02/227-232
    Citation: Yu-ping Li, Jun-ling Tu, Tie-jun Wang, Long-long Ma, Xing-hua Zhang, Qing Zhang, Chi-liu Cai. Production of Light Olefins from Biosyngas by Two-stage Catalytic Conversion Process via Dimethyl Ether[J]. Chinese Journal of Chemical Physics , 2014, 27(2): 227-232. DOI: 10.1063/1674-0068/27/02/227-232

    Production of Light Olefins from Biosyngas by Two-stage Catalytic Conversion Process via Dimethyl Ether

    • NiSAPO-34 and NiSAPO-34/HZSM-5 were prepared and evaluated for the performance of dimethyl ether (DME) conversion to light olefins (DTO). The processes of two-stage light olefin production, DME synthesis and the following DTO, were also investigated using biosyngas as feed gas over Cu/Zn/Al/HZSM-5 and the optimized 2%NiSAPO-34/HZSM-5. The results indicated that adding 2%Ni to SAPO-34 did not change its topology structure, but resulted in the forming of the moderately strong acidity with decreasing acid amounts, which slightly enhanced DME conversion activity and C2=-C3= selectiv-ity. Mechanically mixing 2%NiSAPO-34 with HZSM-5 at the weight ratio of 3.0 further prolonged DME conversion activity to be more than 3 h, which was due to the stable acid sites from HZSM-5. The highest selectivity to light olefins of 90.8% was achieved at 2 h time on stream. The application of the optimized 2%NiSAPO-34/HZSM-5 in the second-stage reactor for DTO reaction showed that the catalytic activity was steady for more than 5 h and light olefin yield was as high as 84.6 g/m3syngas when the biosyngas (H2/CO/CO2/N2/CH4=41.5/26.9/14.2/14.6/2.89, vol%) with low H/C ratio of 1.0 was used as feed gas.
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