scholarly journals Modification of nanocrystalline HZSM-5 zeolite with tetrapropylammonium hydroxide and its catalytic performance in methanol to gasoline reaction

2013 ◽  
Vol 34 (6) ◽  
pp. 1148-1158 ◽  
Author(s):  
Yingping HE ◽  
Min LIU ◽  
Chengyi DAI ◽  
Shutao XU ◽  
Yingxu WEI ◽  
...  
2017 ◽  
Vol 20 (4) ◽  
pp. 385-394 ◽  
Author(s):  
Fanjun Meng ◽  
Yaquan Wang ◽  
Shougui Wang ◽  
Xiao Wang ◽  
Shuhai Wang

2014 ◽  
Vol 953-954 ◽  
pp. 1221-1224
Author(s):  
Ling Jun Zhu ◽  
Jin Feng Guo ◽  
Qian Qian Yin ◽  
Shu Rong Wang

As a diluent, nanocopper was mixed with HZSM-5 for gasoline production from methanol. Diluents have positive effect on the catalyst stability, for diluents help to enhance heat emission. C2-C3 alkenes and DME contents increased obviously while C3H8content decreased with the addition of copper. COx and H2were also observed for the methanol reforming on Cu species. The content of different compositions in the oil products were almost the same as that on HZSM-5 catalyst without diluents.


2014 ◽  
Vol 1008-1009 ◽  
pp. 295-299 ◽  
Author(s):  
Xiao Feng Gao ◽  
Chuan Min Ding ◽  
Wei Li Liu ◽  
Lin Feng Fan ◽  
Gang Song ◽  
...  

Fixed bed reactor was used to explore the catalytic performance of ZSM-5 catalysts with the forms of flake and strip in methanol to gasoline (MTG) reaction. The catalyst samples were characterized by XRD, BET and SEM. The strip ZSM-5 catalyst was modified by 0.4 Molar NaOH solution, which was denoted by TZSM-5/AT. The results show that ZSM-5 molecular sieves could be effectively dispersed to prevent carbon accumulation when extruded with binder. So the coke deposition resistance capacity of strip ZSM-5 has significantly enhancement comparing with flake ZSM-5. Mesoporous structure in strip zeolites formed after NaOH treatment, which could prevent coke formation and further improve catalyst life. The conversion of methanol remains above 80% over 140 hours on alkali-modified strip ZSM-5 operating at atmospheric pressure, 380°C and weight hourly space velocities (WHSV) of 1.5 h-1.


2021 ◽  
Vol 61 (3) ◽  
pp. 394-406
Author(s):  
Yongchao Wang ◽  
O. V. Kikhtyanin ◽  
Cheng Li ◽  
Xiaofang Su ◽  
Xuefeng Bai ◽  
...  

Abstract Three nanosized ZSM-5 zeolites were successfully prepared from reactive gels with the same Si/Al ratios by different synthetic procedures that included the use of tetrapropylammonium hydroxide or n-butylamine as a template and a seeding method that did not use an organic additive. The effect of the synthetic method on the physicochemical properties of the prepared samples was investigated by XRD, XRF, XPS, N2 physisorption, SEM, TEM, 27Al MAS NMR, NH3-TPD, and Py-FTIR. The catalytic performance of the nanosized ZSM-5 zeolites in the alkylation of naphthalene with methanol was compared. The prepared samples were phase-pure, highly crystalline ZSM-5 zeolites, but they had different bulk and surface Si/Al ratios as well as textural and acidic properties. The study of the prepared catalysts in naphthalene methylation revealed that both the acid characteristics of the ZSM-5 nanosized zeolites and their textural properties were responsible for their activity in the reaction. A difference in the composition of monomethylnaphthalenes and dimethylnaphthalenes was attributed to the ability of the catalyst to isomerize the primary reaction products on acid sites located on the external surface of the zeolite crystals. 2,7-DMN was found to be the preferred reaction product over 2,6-DMN when formed at pore entrances to ZSM-5 channels due to the differences in their dimensions. In contrast, 2,6-dimethylnaphthalene could be produced on weaker external Brønsted acid sites, which are hydroxyls attached to octahedral Al atoms. The presented results show that the method used to synthesize nanoscale ZSM-5 zeolites is a critical factor that determines the physicochemical properties and catalytic performance of the resulting crystals.


2018 ◽  
Vol 33 (11) ◽  
pp. 1193 ◽  
Author(s):  
WANG You-He ◽  
WANG Xiao-Dong ◽  
XU Jing-Wei ◽  
SUN Hong-Man ◽  
WU Cheng-Cheng ◽  
...  

2019 ◽  
Vol 9 (3) ◽  
pp. 811-821 ◽  
Author(s):  
Zhao-Meng Wang ◽  
Li-Juan Liu ◽  
Bo Xiang ◽  
Yue Wang ◽  
Ya-Jing Lyu ◽  
...  

The catalytic activity decreases as –(SiO)3Mo(OH)(O) > –(SiO)2Mo(O)2 > –(O)4–MoO.


2020 ◽  
Vol 8 (35) ◽  
pp. 18207-18214
Author(s):  
Dongbo Jia ◽  
Lili Han ◽  
Ying Li ◽  
Wenjun He ◽  
Caichi Liu ◽  
...  

A novel, rational design for porous S-vacancy nickel sulfide catalysts with remarkable catalytic performance for alkaline HER.


2019 ◽  
Author(s):  
M. Alexander Ardagh ◽  
Manish Shetty ◽  
Anatoliy Kuznetsov ◽  
Qi Zhang ◽  
Phillip Christopher ◽  
...  

Catalytic enhancement of chemical reactions via heterogeneous materials occurs through stabilization of transition states at designed active sites, but dramatically greater rate acceleration on that same active site is achieved when the surface intermediates oscillate in binding energy. The applied oscillation amplitude and frequency can accelerate reactions orders of magnitude above the catalytic rates of static systems, provided the active site dynamics are tuned to the natural frequencies of the surface chemistry. In this work, differences in the characteristics of parallel reactions are exploited via selective application of active site dynamics (0 < ΔU < 1.0 eV amplitude, 10<sup>-6</sup> < f < 10<sup>4</sup> Hz frequency) to control the extent of competing reactions occurring on the shared catalytic surface. Simulation of multiple parallel reaction systems with broad range of variation in chemical parameters revealed that parallel chemistries are highly tunable in selectivity between either pure product, even when specific products are not selectively produced under static conditions. Two mechanisms leading to dynamic selectivity control were identified: (i) surface thermodynamic control of one product species under strong binding conditions, or (ii) catalytic resonance of the kinetics of one reaction over the other. These dynamic parallel pathway control strategies applied to a host of chemical conditions indicate significant potential for improving the catalytic performance of many important industrial chemical reactions beyond their existing static performance.


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