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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

Postal Subscription Code 80-969

2018 Impact Factor: 2.809

Front Chem Sci Eng    2011, Vol. 5 Issue (1) : 60-66    https://doi.org/10.1007/s11705-010-0540-7
RESEARCH ARTICLE
Effects of the SAPO-11 synthetic process on dehydration of ethanol to ethylene
Lina WU1, Xiaoxing SHI1, Qun CUI1(), Haiyan WANG1, He HUANG2
1. College of Chemistry and Chemical Engineering, Nanjing University of Technology, Nanjing 210009, China; 2. Biotechnology and Pharmaceutical Engineering, Nanjing University of Technology, Nanjing 210009, China
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Abstract

The effects of the synthetic condition of SAPO-11 molecular sieves on ethanol dehydration to ethylene were studied. Product-compositions, ethanol conversion, and selectivity to ethylene of synthesized and commercial SAPO-11 molecular sieves were compared. Results are as follows: the optimal synthetic conditions for SAPO-11 molecular sieves are adding pseudoboehmite before orthophoshporic, using di-n- propylamine as the template, having a mass fraction of 40% colloidal silica as the silica source and the starting gel obtained, and running at 200°C for 48 h. From the patterns of NH3-TPD, the amount of acid synthesized by SAPO-11 molecular sieves is less than that by commercial SAPO-11 molecular sieves, and has a stronger weak acid. Also, ethanol conversion and selectivity to ethylene reached 99% at 280°C on synthesized SAPO-11, lower by 20°C compared to commercial SAPO-11. For two SAPO-11 molecular sieves, the by-products in the gas phase are mainly ethane, propane, propene, isobutane, n-butane, propadiene, butylene and some higher hydrocarbons. The by-products in the liquid phase are ethyl ether and acetaldehyde.

Keywords SAPO-11 molecular sieves      synthesis      ethanol      ethylene      dehydration     
Corresponding Author(s): CUI Qun,Email:cuiqun@njut.edu.cn   
Issue Date: 05 March 2011
 Cite this article:   
Lina WU,Xiaoxing SHI,Qun CUI, et al. Effects of the SAPO-11 synthetic process on dehydration of ethanol to ethylene[J]. Front Chem Sci Eng, 2011, 5(1): 60-66.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-010-0540-7
https://academic.hep.com.cn/fcse/EN/Y2011/V5/I1/60
sampleadding sequencecrystal time /hcolloidal silica /wt-%template
SAPO-11-150H2O, 1.2P2O5, Al2O3, 1.2Ra), 0.5SiO22440DPA
SAPO-11-250H2O, 1.2P2O5, Al2O3, 1.2R, 0.5SiO23640DPA
SAPO-11-350H2O, 1.2P2O5, Al2O3, 1.2R, 0.5SiO24840DPA
SAPO-11-450H2O, Al2O3, 1.2P2O5, 1.2R, 0.5SiO24840DPA
SAPO-11-550H2O, 1.2P2O5, Al2O3, 1.2R, 0.5SiO24840DIPA
SAPO-11-650H2O, Al2O3, 1.2P2O5, 1.2R, 0.5SiO24825DPA
Tab.1  Different chemical component of SAPO-11 molecular sieves
Fig.1  Influence of crystal time on ethanol conversion of SAPO-11 molecular sieves
Fig.2  Influence of crystal time on selectivity to ethylene of SAPO-11 molecular sieves
Fig.3  Influence of adding orders on ethanol conversion of SAPO-11 molecular sieves
Fig.4  Influence of adding orders of SAPO-11 molecular sieves on selectivity to ethylene
Fig.5  Influence of different templates on ethanol conversion of SAPO-11 molecular sieves
Fig.6  Influence of different templates on selectivity to ethylene of SAPO-11 molecular sieves
Fig.7  Influence of different silicasols on ethanol conversion of SAPO-11 molecular sieves
Fig.8  Influence of different silicasols on selectivity to ethylene of SAPO-11 molecular sieves
Fig.9  XRD patterns of synthesized SAPO-11 molecular sieves (a) and commercial SAPO-11 molecular sieves (b)
Fig.10  NH-TPD patterns of synthesized SAPO-11 molecular sieves (a) and commercial SAPO-11 molecular sieves (b)
Fig.11  SEM patterns of synthesized SAPO-11 molecular sieves (× 2000) (a) and commercial SAPO-11 molecular sieves (× 10000) (b)
Fig.12  Ethanol conversion of two SAPO-11 molecular sieves
Fig.13  Selectivity to ethylene on two SAPO-11 molecular sieves
catalystTemp /°Cgas production compositions /%liquid production compositions /%
C2H4C2H6C3C4≥C5C2H5OHC4H10OC2H4OH2O
synthesized SAPO-11-425098.240.030.830.550.350.033.710.0096.26
28097.450.480.081.030.950.080.310.0099.60
30093.890.850.103.721.440.020.130.0399.83
32092.080.900.124.842.070.010.000.0199.99
commercial SAPO-1125097.890.300.200.501.2430.0134.250.0235.72
28099.120.170.050.400.2634.2911.180.1654.36
30098.040.140.341.000.481.550.750.1397.57
32093.630.151.022.13.100.850.410.0498.70
Tab.2  Product-compositions of two SAPO-11 molecular sieves at different temperatures
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