TY - JOUR
T1 - Structure and evolution of confined carbon species during methane Dehydroaromatization over Mo/ZSM-5
AU - Kosinov, Nikolay
AU - Uslamin, Evgeny A.
AU - Coumans, Ferdy J.A.G.
AU - Wijpkema, Alexandra S.G.
AU - Rohling, Roderigh Y.
AU - Hensen, Emiel J.M.
PY - 2018/9/7
Y1 - 2018/9/7
N2 - Surface carbon (coke, carbonaceous deposits) is an integral aspect of methane dehydroaromatization catalyzed by Mo/zeolites. We investigated the evolution of surface carbon species from the beginning of the induction period until the complete catalyst deactivation by the pulse reaction technique, TGA, 13C NMR, TEM, and XPS. Isotope labeling was performed to confirm the catalytic role of confined carbon species during MDA. It was found that "hard" and "soft" coke distinction is mainly related to the location of coke species inside the pores and on the external surface, respectively. In addition, MoO3 species act as an active oxidation catalyst, reducing the combustion temperature of a certain fraction of coke. Furthermore, after dissolving the zeolite framework by HF, we found that coke formed during the MDA reaction inside the zeolite pores is essentially a zeolite-templated carbon material. The possibility of preparing zeolite-templated carbons from the most available hydrocarbon feedstock is important for the development of these interesting materials.
AB - Surface carbon (coke, carbonaceous deposits) is an integral aspect of methane dehydroaromatization catalyzed by Mo/zeolites. We investigated the evolution of surface carbon species from the beginning of the induction period until the complete catalyst deactivation by the pulse reaction technique, TGA, 13C NMR, TEM, and XPS. Isotope labeling was performed to confirm the catalytic role of confined carbon species during MDA. It was found that "hard" and "soft" coke distinction is mainly related to the location of coke species inside the pores and on the external surface, respectively. In addition, MoO3 species act as an active oxidation catalyst, reducing the combustion temperature of a certain fraction of coke. Furthermore, after dissolving the zeolite framework by HF, we found that coke formed during the MDA reaction inside the zeolite pores is essentially a zeolite-templated carbon material. The possibility of preparing zeolite-templated carbons from the most available hydrocarbon feedstock is important for the development of these interesting materials.
KW - methane dehydroaromatization
KW - Mo/ZSM-5
KW - hydrocarbon pool
KW - coke
KW - zeolite-templated carbon
UR - http://www.scopus.com/inward/record.url?scp=85053247830&partnerID=8YFLogxK
U2 - 10.1021/acscatal.8b02491
DO - 10.1021/acscatal.8b02491
M3 - Article
C2 - 30271670
AN - SCOPUS:85053247830
SN - 2155-5435
VL - 8
SP - 8459
EP - 8467
JO - ACS Catalysis
JF - ACS Catalysis
IS - 9
ER -