Catalysts and shape selective catalysis in the methanol-to-olefin (MTO) reaction

Author(s):  
Jiawei Zhong ◽  
Jingfeng Han ◽  
Yingxu Wei ◽  
Zhongmin Liu
ChemSusChem ◽  
2020 ◽  
Vol 13 (17) ◽  
pp. 4528-4536 ◽  
Author(s):  
Elena Subbotina ◽  
Alexandra Velty ◽  
Joseph S. M. Samec ◽  
Avelino Corma

1991 ◽  
Vol 69 (1) ◽  
pp. 177-186 ◽  
Author(s):  
Shashikala J. Rane ◽  
C.V.V. Satyanarayana ◽  
D.K. Chakrabarty

2019 ◽  
Vol 10 (1) ◽  
Author(s):  
Chuanfu Wang ◽  
Lei Zhang ◽  
Xin Huang ◽  
Yufei Zhu ◽  
Gang (Kevin) Li ◽  
...  

Abstract The shape-selective catalysis enabled by zeolite micropore’s molecular-sized sieving is an efficient way to reduce the cost of chemical separation in the chemical industry. Although well studied since its discovery, HZSM-5′s shape-selective capability has never been fully exploited due to the co-existence of its different-sized straight channels and sinusoidal channels, which makes the shape-selective p-xylene production from toluene alkylation with the least m-xylene and o-xylene continue to be one of the few industrial challenges in the chemical industry. Rather than modifications which promote zeolite shape-selectivity at the cost of stability and reactivity loss, here inverse Al zoned HZSM-5 with sinusoidal channels predominantly opened to their external surfaces is constructed to maximize the shape-selectivity of HZSM-5 sinusoidal channels and reach > 99 % p-xylene selectivity, while keeping a very high activity and good stability ( > 220 h) in toluene methylation reactions. The strategy shows good prospects for shape-selective control of molecules with tiny differences in size.


2019 ◽  
Vol 27 (2) ◽  
pp. 331-338
Author(s):  
Yue Yao ◽  
Miaoguo Zuo ◽  
Peipei Shao ◽  
Xiaoqiao Huang ◽  
Jianxin Li ◽  
...  

2016 ◽  
Vol 14 (5) ◽  
pp. 1047-1057
Author(s):  
Shima Masoumi ◽  
Kobra Rahimi ◽  
Jafar Towfighi

Abstract The effects of templating agent [i. e., tetraethyl ammonium hydroxide (TEAOH), triethylamine (TEA) and morpholine (MOR)] and molar ratio of SiO2/Al2O3 and H2O/Al2O3 over SAPO-34 catalysts in methanol to olefin (MTO) reaction were studied systematically. The exact effect of main factors and their interaction were studied by response surface methodology (RSM) applying central composite design (CCD). Two empirical models for two systems, based on these preparation variables for the yield of ethylene and propylene were constructed in two CCD studies and ultimately these models showed as counter and three-dimensional (3D) diagrams. Analysis of Variance (ANOVA) applied for investigating the significance of the variables indicated that TEA and SiO2/Al2O3 content were the most significant variables in the case (1) and case (2), respectively. The maximum predicted ethylene and propylene yield was 58.57 wt. % and 30.22 wt. %, for catalyst with TEA = 0.2, TEAOH = 0.38 in case (1). For case (2), catalyst with SiO2/Al2O3 = 0.17, H2O/Al2O3 = 101.18 showed the maximum ethylene and propylene yield of 49.87 wt. % and 20.58 wt. %, respectively.


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