Journal
MICROPOROUS AND MESOPOROUS MATERIALS
Volume 313, Issue -, Pages -Publisher
ELSEVIER
DOI: 10.1016/j.micromeso.2020.110857
Keywords
Intergrowth zeolite; SAPO-11; SAPO-5; Surface acidity; Hydroisomerization
Categories
Funding
- National Natural Science Foundation of China [21978326, 21991090, 21991091]
- Natural Science Foundation of Shandong Province [ZR2019MB029]
- Fundamental Research Funds for the Central Universities [20CX06059A]
- China Postdoctoral Science Foundation [2020M682259]
- Postdoctoral Applied Research Project of Qingdao [qd20200002]
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Intergrowth zeolites combine advantages of single phases, with the SAPO-11/5 intergrowth zeolite showing intermediate surface acidity and pore volume by controlling the AFI/AEL ratio. The Ni/SAPO-11/5-2 bifunctional catalyst exhibits improved isomers selectivity and yield in n-hexane hydroisomerization, attributed to its unique pore structure and surface acidity.
Intergrowth zeolites are always synthesized to combine advantages of each single phase. Herein, the SAPO-11/5 intergrowth zeolite with controlled AFI/AEL phase ratios was synthesized and used for the n-hexane hydroisomerization. The obtained samples were characterized by XRD, TEM, SEM, N-2 adsorption-desorption, NH3-TPD and Si-29 MAS NMR. The new morphology different from each single phase is obtained over the SAPO-11/5 intergrowth zeolite. It also exhibits intermediate surface acid density and pore volume between the SAPO-11 and SAPO-5. With the increased AFI/AEL ratio, more surface acid sites and larger pore volume are obtained. The SAPO-11/5 intergrowth zeolite was transformed into bifunctional catalysts (Ni/SAPO-11/5-2) by loading with 4.0 wt% Ni via the impregnation method. This novel catalyst shows improved isomers selectivity and yield than each single phase catalyst in the n-hexane hydroisomerization, which is mainly attributed to the intermediate pore structure and surface acidity. Furthermore, the Ni/SAPO-11/5-2 also illustrates higher di-branched isomers selectivity (7.7%) than the Ni/SAPO-11 (2.4%) catalyst, favoring increasing the octane number of gasoline. This work provides an alternative approach to simultaneously regulate surface acidity and pore structure for the hydroisomerization catalyst.
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