On the synthesis and catalytic cracking properties of Al-ITQ-13 zeolites

被引:5
作者
Zeng, Penghui [1 ]
Guo, Xiaozhong [1 ]
Zhu, Xiaochun [1 ]
Guo, Qiaoxia [1 ]
Wang, Yandan [1 ]
Ren, Shenyong [1 ]
Shen, Baojian [1 ]
机构
[1] China Univ Petr, Coll Sci, Coll Chem Engn, State Key Lab Heavy Oil Proc, 18 Fuxue Rd, Beijing 102249, Peoples R China
基金
中国国家自然科学基金;
关键词
Zeolite; Al-ITQ-13; Si/Al ratio; Synthesis; 1-Butene catalytic cracking; HYDROTHERMAL SYNTHESIS; SELECTIVE CATALYST; CRYSTAL-STRUCTURE; PORE ZEOLITE; SI/AL RATIOS; RING PORES; SILICA; ITQ-13; CHANNELS;
D O I
10.1016/j.micromeso.2017.03.033
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Al-ITQ-13 zeolites with different Si/A1 atom ratios above 25 were successfully synthesized in short crystallization time by using seeds in the gel. A variety of synthesis conditions were investigated in-depth and the resultant zeolite samples were characterized by XRD, SEM, N-2 physisorption and FTIR spectra. Al-TQ-13 zeolite samples synthesized with different Si/AI ratios exhibit similar textural properties. The amount and strength of acid sites decrease with increasing Si/Al ratio of Al-ITQ-13 zeolites. It was found that H-Al-ITQ-13 samples with low Si/A1 ratios show a very high B/L ratio (such as 2.40) at a desorption temperature of 573 K. 1-Butene cracking reaction over proton form Al-ITQ-13 zeolites (Si/Al atom ratio from 47 to 179) was carried out in a continuous flow stainless steel reactor. It was found that the higher of the aluminium content in Al-ITQ-13 (i.e. lower Si/Al ratio), the better selectivity for ethylene and propylene yield. While the hydrogen transfer reaction and alkylation reaction were suppressed with increasing Si/A1 ratio. (C) 2017 Elsevier Inc. All rights reserved.
引用
收藏
页码:186 / 192
页数:7
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