Naphtha catalytic cracking were carried out at 650 degrees C over modified ZSM-5. Light olefins and BTX could be obtained over the catalysts. The products showed variable distribution with different catalyst modification. Some modification, such as Fe, Cu and La favored the BTX generation and P and Mg modification favored the light olefins production. In N-2 stream cracking catalyzed by LaZSM-5, more than 50% naphtha feed were converted to BTX, while in steam cracking, with an improved modified catalyst, P, La/ZSM-5, naphtha can be converted to light olefins with high activity and long-term stability
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
A novel concept of cracking-based oligomerization of naphtha (C5-C8) to produce higher range hydroca...
A ZSM-5-based catalyst was prepared by spray-dry method for fluidized-bed naphtha catalytic cracking...
Steam cracking, the major, current existing route for light olefin production, is the most energy co...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
A series of fluorinated HZSM-5 zeolites (F/HZSM-5) were prepared by immersing the zeolites with diff...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
This study focuses on the modification of ZSM-5 in order to enhance the catalytic cracking of refine...
Catalytic cracking of light naphtha was carried out in a fixed bed reactor over ZSM-48 and EU-1 zeol...
BACKGROUND: The conversions of bicyclic compounds, both a naphthenic-aromatic compound (tetralin) an...
A conceptual design of the catalytic oxidative cracking (COC) of hexane as a model compound of napht...
process that increases light olefin yield under high severity reaction conditions. The process has b...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
A novel concept of cracking-based oligomerization of naphtha (C5-C8) to produce higher range hydroca...
A ZSM-5-based catalyst was prepared by spray-dry method for fluidized-bed naphtha catalytic cracking...
Steam cracking, the major, current existing route for light olefin production, is the most energy co...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
A series of fluorinated HZSM-5 zeolites (F/HZSM-5) were prepared by immersing the zeolites with diff...
In order to increase ethene and propene, naphtha steam catalytic cracking has been considered. The c...
This study focuses on the modification of ZSM-5 in order to enhance the catalytic cracking of refine...
Catalytic cracking of light naphtha was carried out in a fixed bed reactor over ZSM-48 and EU-1 zeol...
BACKGROUND: The conversions of bicyclic compounds, both a naphthenic-aromatic compound (tetralin) an...
A conceptual design of the catalytic oxidative cracking (COC) of hexane as a model compound of napht...
process that increases light olefin yield under high severity reaction conditions. The process has b...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
A novel concept of cracking-based oligomerization of naphtha (C5-C8) to produce higher range hydroca...