Promotion of the performance of La, Ce and Ca impregnated HZSM-5 nanoparticles in the MTO reaction

被引:30
作者
Khezri, Hamed [1 ]
Izadbakhsh, Ali [1 ]
Izadpanah, Amir Abbas [1 ]
机构
[1] Persian Gulf Univ, Fac Petr Gas & Petrochem Engn, Dept Chem Engn, PB 75169-13817, Bushehr, Iran
基金
美国国家科学基金会;
关键词
Catalyst; Methanol to olefin; HZSM-5; Nano; Acidity; Zeolite; SIZED ZSM-5 ZEOLITE; ACID SITES; CATALYTIC PERFORMANCE; COKE FORMATION; LIGHT OLEFINS; METHANOL; CONVERSION; PROPYLENE; CRACKING; FRAMEWORK;
D O I
10.1016/j.fuproc.2019.106253
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Effects of calcium, cerium and lanthanum on the catalytic performance of HZSM-5 nanoparticles in the methanol to olefin, MTO, conversion were investigated. Each samples with the target Si/Al = 400 was synthesized producing nanoparticles about 300 nm. The reactor MTO performance of catalysts at methanol WHSV = 8 g/(g.h) was evaluated at the temperatures of 390, 440, and 490 degrees C. Based on the yield of ethylene and propylene, Ce-Ca-HZSM-5 showed the best catalytic performance. The metal modification of HZSM-5 resulted in the improved yield of ethylene and propylene, which the effect on the yield of ethylene was stronger. Another advantageous feature of metal modified catalyst was the reduction of sensitivity of the yield of propylene to temperature. With decreasing temperature from 490 to 390 degrees C, the yield of propylene decreased from 0.16 to 0.13 over Ce-Ca-HZSM-5 which is significantly more narrow than HZSM-5 (0.15 to 0.10). The main improved characteristic in the performance of the modified catalyst was substantial decrease of coke precipitation as determined by TG analysis. Ce-Ca-HZSM-5 was found to be more stable than parent HZSM-5 over 100 h time on stream, although its initial conversion was lower at the conditions of experiment.
引用
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页数:12
相关论文
共 61 条
[1]   Methanol to gasoline over zeolite H-ZSM-5: Improved catalyst performance by treatment with NaOH [J].
Bjorgen, Morten ;
Joensen, Finn ;
Holm, Martin Spangsberg ;
Olsbye, Unni ;
Lillerud, Karl-Petter ;
Svelle, Stian .
APPLIED CATALYSIS A-GENERAL, 2008, 345 (01) :43-50
[2]   Cracking of pentenes to C2-C4 light olefins over zeolites and zeotypes -: Role of topology and acid site strength and concentration [J].
Bortnovsky, O ;
Sazama, P ;
Wichterlova, B .
APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) :203-213
[3]   Acidity and basicity of zeolites: A fundamental approach [J].
Busca, Guido .
MICROPOROUS AND MESOPOROUS MATERIALS, 2017, 254 :3-16
[4]   Methanol to hydrocarbons: spectroscopic studies and the significance of extra-framework aluminium [J].
Campbell, SM ;
Jiang, XZ ;
Howe, RF .
MICROPOROUS AND MESOPOROUS MATERIALS, 1999, 29 (1-2) :91-108
[5]  
Cejka J, 1995, STUD SURF SCI CATAL, V97, P401
[6]   Aggregates of superfine ZSM-5 crystals: The effect of NaOH on the catalytic performance of methanol to propylene reaction [J].
Chen, Hengbao ;
Wang, Yaquan ;
Meng, Fanjun ;
Sun, Chao ;
Li, Hongyao ;
Wang, Zhao ;
Gao, Fei ;
Wang, Xiao ;
Wang, Shuhai .
MICROPOROUS AND MESOPOROUS MATERIALS, 2017, 244 :301-309
[7]   Recent advancements in ethylene and propylene production using the UOP/Hydro MTO process [J].
Chen, JQ ;
Bozzano, A ;
Glover, B ;
Fuglerud, T ;
Kvisle, S .
CATALYSIS TODAY, 2005, 106 (1-4) :103-107
[8]   Bronsted/Lewis acid sites synergistically promote the initial C-C bond formation in the MTO reaction [J].
Chu, Yueying ;
Yi, Xianfeng ;
Li, Chengbin ;
Sun, Xianyong ;
Zheng, Anmin .
CHEMICAL SCIENCE, 2018, 9 (31) :6470-6479
[9]  
Cobb J., 1995, NZ SYNFUEL STORY WOR
[10]   Synthesis of lower olefins from methanol and subsequent conversion of ethylene to higher olefins via oligomerisation [J].
Dutta, P ;
Roy, SC ;
Nandi, LN ;
Samuel, P ;
Pillai, SM ;
Bhat, BD ;
Ravindranathan, M .
JOURNAL OF MOLECULAR CATALYSIS A-CHEMICAL, 2004, 223 (1-2) :231-235