Oxygen-containing coke species in zeolite-catalyzed conversion of methanol to hydrocarbons

2016 ◽  
Vol 6 (22) ◽  
pp. 8157-8165 ◽  
Author(s):  
Zhaohui Liu ◽  
Xinglong Dong ◽  
Xin Liu ◽  
Yu Han

Oxygen-containing coke species are identified during methanol-to-hydrocarbons reactions, and their influence on the deactivation of catalyst is investigated.

1987 ◽  
Vol 52 (7) ◽  
pp. 1701-1707 ◽  
Author(s):  
Miloslav Křivánek ◽  
Nguyen Thiet Dung ◽  
Pavel Jírů

The catalytic activity of Na, H-Y zeolite samples with a varying Si/Al ratio (2·5 to 20) in the transformation of methanol was determined. The amounts of formed individual aliphatic hydrocarbons as function of reaction time were correlated with the amount of Bronsted and Lewis centres on the catalysts. The effect of coke formation on the over-all course of the reaction has been demonstrated.


2021 ◽  
Vol 11 (1) ◽  
Author(s):  
Yoottapong Klinthongchai ◽  
Seeroong Prichanont ◽  
Piyasan Praserthdam ◽  
Bunjerd Jongsomjit

AbstractMesocellular foam carbon (MCF-C) is one the captivating materials for using in gas phase dehydrogenation of ethanol. Extraordinary, enlarge pore size, high surface area, high acidity, and spherical shape with interconnected pore for high diffusion. In contrary, the occurrence of the coke is a majority causes for inhibiting the active sites on catalyst surface. Thus, this study aims to investigate the occurrence of the coke to optimize the higher catalytic activity, and also to avoid the coke formation. The MCF-C was synthesized and investigated using various techniques. MCF-C was spent in gas-phase dehydrogenation of ethanol under mild conditions. The deactivation of catalyst was investigated toward different conditions. Effects of reaction condition including different reaction temperatures of 300, 350, and 400 °C on the deactivation behaviors were determined. The results indicated that the operating temperature at 400 °C significantly retained the lowest change of ethanol conversion, which favored in the higher temperature. After running reaction, the physical properties as pore size, surface area, and pore volume of spent catalysts were decreased owing to the coke formation, which possibly blocked the pore that directly affected to the difficult diffusion of reactant and caused to be lower in catalytic activity. Furthermore, a slight decrease in either acidity or basicity was observed owing to consumption of reactant at surface of catalyst or chemical change on surface caused by coke formation. Therefore, it can remarkably choose the suitable operating temperature to avoid deactivation of catalyst, and then optimize the ethanol conversion or yield of acetaldehyde.


1986 ◽  
Vol 27 (2) ◽  
pp. 393-396
Author(s):  
W.G.B. Mandersloot ◽  
C.P. Nicolaides ◽  
M.S. Scurrell

2017 ◽  
Vol 129 (31) ◽  
pp. 9167-9171 ◽  
Author(s):  
Xinqiang Wu ◽  
Shutao Xu ◽  
Wenna Zhang ◽  
Jindou Huang ◽  
Jinzhe Li ◽  
...  

2011 ◽  
Vol 402 (1-2) ◽  
pp. 208-217 ◽  
Author(s):  
Antoine Lacarriere ◽  
Francis Luck ◽  
Dariusz Świerczyński ◽  
François Fajula ◽  
Vasile Hulea

ACS Catalysis ◽  
2011 ◽  
Vol 2 (1) ◽  
pp. 26-37 ◽  
Author(s):  
Shewangizaw Teketel ◽  
Wegard Skistad ◽  
Sandrine Benard ◽  
Unni Olsbye ◽  
Karl Petter Lillerud ◽  
...  

2018 ◽  
Vol 368 ◽  
pp. 248-260 ◽  
Author(s):  
Jie Zhang ◽  
Lanjian Xu ◽  
Yanfei Zhang ◽  
Zhihua Huang ◽  
Xiaomin Zhang ◽  
...  

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