TY - JOUR
T1 - Vapor phase transport synthesis of CoAPO-5 molecular sieve and its catalytic performance
AU - Shao, Hui
AU - Ke, Xuebin
AU - Yao, Jianfeng
AU - Zhang, Lixiong
AU - Xu, Nanping
PY - 2008/6
Y1 - 2008/6
N2 - Co-substituted aluminophosphate molecular sieves (CoAPO-5) were synthesized by vapor-phase transport. The influence of the gel composition on the products was investigated. The catalyst physicochemical properties were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), fourier transform infrared (FT-IR) and ultra-voilet absorption spectroscopy (UV-Vis DRS). The results showed that the synthesis conditions affected on the crystalline phase, the acidity, and thereby the catalytic performance of CoAPO-5. CoAPO-5 molecular sieves with AFI topology could be synthesized by crystallizing the gel for 48 h at 200°C, while the molar ratio of Al2O3, P2O5, CoO, (PrO)3N to H2O was 1:1:0.2:1:200 and the volume ratio of triethanolamine to H2Owas 1:0 in the liquid phase. The yield of the ester was 93.2% under the conditions of molar ratio of acetic acid to n-butanol 4:1, reaction temperature 115°C and the mass fraction of catalyst 1% after reaction 5 h.
AB - Co-substituted aluminophosphate molecular sieves (CoAPO-5) were synthesized by vapor-phase transport. The influence of the gel composition on the products was investigated. The catalyst physicochemical properties were characterized by X-ray diffraction (XRD), scanning electron microscopy (SEM), fourier transform infrared (FT-IR) and ultra-voilet absorption spectroscopy (UV-Vis DRS). The results showed that the synthesis conditions affected on the crystalline phase, the acidity, and thereby the catalytic performance of CoAPO-5. CoAPO-5 molecular sieves with AFI topology could be synthesized by crystallizing the gel for 48 h at 200°C, while the molar ratio of Al2O3, P2O5, CoO, (PrO)3N to H2O was 1:1:0.2:1:200 and the volume ratio of triethanolamine to H2Owas 1:0 in the liquid phase. The yield of the ester was 93.2% under the conditions of molar ratio of acetic acid to n-butanol 4:1, reaction temperature 115°C and the mass fraction of catalyst 1% after reaction 5 h.
KW - CoAPO-5 molecular sieve
KW - Esterification
KW - Vapor phase transport
UR - http://www.scopus.com/inward/record.url?scp=54749087921&partnerID=8YFLogxK
M3 - 文章
AN - SCOPUS:54749087921
SN - 1001-7631
VL - 24
SP - 228
EP - 233
JO - Huaxue Fanying Gongcheng Yu Gongyi/Chemical Reaction Engineering and Technology
JF - Huaxue Fanying Gongcheng Yu Gongyi/Chemical Reaction Engineering and Technology
IS - 3
ER -