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Zr改性Y分子筛中油型加氢裂化催化剂设计制备
引用本文:崔勍焱,张浩彬,魏强,岳源源,王廷海,朱海波,周亚松,鲍晓军. Zr改性Y分子筛中油型加氢裂化催化剂设计制备[J]. 化工学报, 2019, 70(10): 3949-3955. DOI: 10.11949/0438-1157.20190651
作者姓名:崔勍焱  张浩彬  魏强  岳源源  王廷海  朱海波  周亚松  鲍晓军
作者单位:1. 福州大学石油化工学院,福建 福州 3501082. 中国石油大学(北京)化学工程学院,北京 102249)
摘    要:采用等体积浸渍法对Y分子筛进行了Zr修饰改性,系统考察了不同用量Zr对改性Y分子筛的结构、催化剂的理化性质和加氢裂化反应性能的影响规律。通过XRD、NH3-TPD、H2-TPR和TEM等方法对改性分子筛和催化剂进行表征分析。结果表明:Zr改性降低了Y分子筛的酸量,随着改性Zr用量的增加,这种变化趋势不断增大。同时,Zr改性有效地削弱了分子筛催化剂中金属活性组分与载体间的作用,提高了W物种在催化剂表面的分散程度。加氢裂化反应结果表明:与Y分子筛催化剂相比,Zr改性Y分子筛催化剂的减压馏分油(VGO)转化率降低,中间馏分油选择性提高约20%,随着改性Zr用量的增加,VGO的转化率不断降低,中间馏分油选择性略有增加。

关 键 词:催化剂  分子筛  载体  加氢裂化  Zr改性  中间馏分油  
收稿时间:2019-06-11
修稿时间:2019-07-22

Development of hydrocracking catalyst supported on Y zeolite modified with Zr
Qingyan CUI,Haobin ZHANG,Qiang WEI,Yuanyuan YUE,Tinghai WANG,Haibo ZHU,Yasong ZHOU,Xianjun BAO. Development of hydrocracking catalyst supported on Y zeolite modified with Zr[J]. Journal of Chemical Industry and Engineering(China), 2019, 70(10): 3949-3955. DOI: 10.11949/0438-1157.20190651
Authors:Qingyan CUI  Haobin ZHANG  Qiang WEI  Yuanyuan YUE  Tinghai WANG  Haibo ZHU  Yasong ZHOU  Xianjun BAO
Affiliation:1. College of Chemical Engineering, Fuzhou University, Fuzhou 350108, Fujian, China2. State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, China
Abstract:Y zeolite was modified with Zr by equal volume impregnation method. The effects of different amounts of Zr on the structure of modified Y zeolite, the physicochemical properties of the catalyst and the performance of hydrocracking reaction were investigated systematically. The modified Y zeolite and catalyst were characterized by X-ray diffraction (XRD), NH3 temperature programmed desorption (NH3-TPD), H2 temperature programmed reduction (H2-TPR) and transmission electron microscopy (TEM). The results show that Zr modification decreased the amount of acid sites of Y zeolite, and the trend became larger with an increase of Zr content. Moreover, Zr modification availably weakened the relation of metal species and support in the catalyst with Y zeolite, and improved the dispersion of W species on the catalyst surface. The hydrocracking reaction results suggested that VGO conversion over the catalyst with Y zeolite modified with Zr decreased compared with that with Y zeolite, and middle distillates increased about 20%(mass), as well as VGO conversion gradually decreased and the middle distillates slightly increased as the Zr content increased.
Keywords:catalyst  zeolite  support  hydrocracking  Zr modification  middle distillates  
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