Coke Forming Reactions During Methanol Conversion on Zeolite Catalysts

Author(s):  
H. Schulz ◽  
Zhao Siwei ◽  
W. Baumgartner
Catalysts ◽  
2020 ◽  
Vol 10 (6) ◽  
pp. 671
Author(s):  
Massimo Migliori ◽  
Antonio Condello ◽  
Francesco Dalena ◽  
Enrico Catizzone ◽  
Girolamo Giordano

The assessment of the catalytic performance of “hybrid” metal/zeolite catalysts (based on FER or MFI structure and CuZnZr metal complexes) in the methanol dehydration step to DME has been studied in this work. The results clearly show that there is an important effect of the interaction between metal and acid sites affecting the acid catalyst performances. Additionally, deactivation, studied by means of a Timo-on-Stream (TOS) test, was affected by the type of zeolite structure used for hybrid catalyst preparation. The decrease in DME selectivity can be attributed to the cooperation of metal and acid sites in the production of different compounds (mainly methyl formate and dimethoxy methane) converting methanol and DME. The presence of these compounds (indicating different reaction pathways active) was found to be dependent on the zeolite structure and on the type of co-precipitation medium (water or ethanol) used to prepare the hybrid catalyst.


2020 ◽  
Vol 22 (9) ◽  
pp. 5293-5300 ◽  
Author(s):  
Huan Li ◽  
Chenxi Guo ◽  
Liqiong Huang ◽  
Jun Long ◽  
Xiaoyan Fu ◽  
...  

A general description for zeolites and transition metal catalysts has been established for methanol conversion.


2017 ◽  
Vol 751 ◽  
pp. 512-517 ◽  
Author(s):  
Supranee Lao-Ubol ◽  
Phunthinee Somwongsa ◽  
Pracha Laoauyporn ◽  
Pasinee Panith ◽  
Siriporn Larpkiattaworn ◽  
...  

Five different types of silica catalyst (SBA-15, SBA-15-PO3H2, and three different Si/Al ratio of commercial zeolites (30, 80 and 280) were used to study the transformation of methanol to hydrocarbon (MTH). The aim of this study was to investigate the effect of pore diameter and acidity in the structure of silica catalysts on the process performances in terms of methanol conversion and hydrocarbon selectivity. The mesoporous silica catalysts were prepared by co-condensation method. The catalysts samples were characterized by GC-MS, XRD, BET, and NH3-TPD techniques. The catalytic performance of synthesized and commercial catalysts for MTH process was evaluated using a homemade fixed bed reactor at temperature (300°C). It was found that the liquid hydrocarbon product provided by zeolite catalysts is aromatic hydrocarbons-rich. High Si/Al zeolites with larger pore size lead to higher selectivity and yield to paraffins (C1-C7). In contrast to commercial zeolite catalyst, SBA-15 and its modification with phosphorus species showed no conversion under studied condition. These results indicate that both pore diameter and acidity influence the product distribution in methanol to hydrocarbon process.


1987 ◽  
Vol 33 (2) ◽  
pp. 305-310 ◽  
Author(s):  
G. V. Echevskii ◽  
N. G. Kalinina ◽  
V. F. Anufrienko ◽  
V. A. Poluboyarov

2021 ◽  
Vol 12 (1) ◽  
Author(s):  
Boyuan Shen ◽  
Xiao Chen ◽  
Xiaoyu Fan ◽  
Hao Xiong ◽  
Huiqiu Wang ◽  
...  

AbstractThe micro-structures of catalyst materials basically affect their macro-architectures and catalytic performances. Atomically resolving the micro-structures of zeolite catalysts, which have been widely used in the methanol conversion, will bring us a deeper insight into their structure-property correlations. However, it is still challenging for the atomic imaging of silicoaluminophosphate zeolites by electron microscopy due to the limits of their electron beam sensitivity. Here, we achieve the real-space imaging of the atomic lattices in SAPO-34 and SAPO-18 zeolites, including the Al–O–P atoms and bonds, by the integrated differential phase contrast scanning transmission electron microscopy (iDPC-STEM). The spatial distribution of SAPO-34 and SAPO-18 domains in SAPO-34/18 intergrowths can be clearly resolved. By changing the Si contents and templates in feed, we obtain two SAPO-34/18 catalysts, hierarchical and sandwich catalysts, with highly-mixed and separated SAPO-34 and SAPO-18 lattices respectively. The reduced diffusion distances of inside products greatly improve the catalytic performances of two catalysts in methanol conversion. Based on the observed distributions of lattices and elements in these catalysts, we can have a preliminary understanding on the correlation between the synthesis conditions and structures of SAPO-34/18 intergrowth catalysts to further modify their performances based on unique architectures.


2021 ◽  
Author(s):  
Huiqiu Wang ◽  
Boyuan Shen ◽  
Xiao Chen ◽  
Hao Xiong ◽  
Hongmei Wang ◽  
...  

Abstract The tunability of local structures determines various catalytic performances of zeolite catalysts. The acid sites in zeolite catalysts are important local structures to control the products in methanol conversion. However, it remained still a great challenge to precisely design the acid sites, since there is a lack of controllable methods to generate and identify the acid sites with a high resolution. Here, we use the lattice mismatch of zeolite intergrowth to enrich the inherent Lewis acid sites (LASs) at the interface of a mortise-tenon ZSM-5 catalyst (ZSM-5-MT) showing a 90° intergrowth structure. ZSM-5-MT is formed by two perpendicular blocks that can be atomically resolved by the integrated differential phase contrast scanning transmission electron microscope (iDPC-STEM). It can be revealed by various methods that more framework-associated Al (AlFR) LASs are generated in ZSM-5-MT than single-crystal ZSM-5 catalyst. Combining with the iDPC-STEM results, we demonstrate that the partial missing of O atoms at interfaces results in the formation of inherent LASs in ZSM-5-MT. According to the catalytic performances, LAS-enriched ZSM-5-MT shows a higher selectivity of light olefins than the single-crystal ZSM-5 catalyst in methanol conversion. These results provide an efficient strategy to design the Lewis acidity in zeolites for tailored catalytic functions via interface engineering.


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