A ZSM-5-based catalyst was prepared by spray-dry method for fluidized-bed naphtha catalytic cracking. Multi-techniques, such as X-ray diffraction, scanning electron microscope, (27)Al MAS NMR, and NH(3)-TPD, were employed for the investigation of ZSM-5 framework stability, framework dealumination, and catalyst acidity variation in hydrothermal treatment. Catalytic performances of fluidized-bed naphtha catalytic cracking at 630-680 C indicated that light olefins and other value-added products could be more efficiently produced compared with the commercial process of thermal steam cracking. Long-term catalytic evaluation implied that naphtha catalytic cracking over the catalyst prepared with spray-dry method and hydrothermal treatment can be ...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...
Naphtha catalytic cracking were carried out at 650 degrees C over modified ZSM-5. Light olefins and ...
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...
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...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
ZSM-5 (HZ) was prepared by hydrothermal synthesis and, zinc and gallium incorporated ZSM-5 catalysts...
Catalytic cracking of light naphtha was carried out in a fixed bed reactor over ZSM-48 and EU-1 zeol...
The aromatic oil, which is a byproduct of the processes of naphtha steam cracking (NSC), was hydrocr...
A novel concept of cracking-based oligomerization of naphtha (C5-C8) to produce higher range hydroca...
Symposium on Advances in the Chemistry of Asphaltene and Related Substances at the 5th North America...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...
Naphtha catalytic cracking were carried out at 650 degrees C over modified ZSM-5. Light olefins and ...
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...
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...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
Steam catalytic cracking of naphtha in smaller FCC units can be considered an option to produce more...
ZSM-5 (HZ) was prepared by hydrothermal synthesis and, zinc and gallium incorporated ZSM-5 catalysts...
Catalytic cracking of light naphtha was carried out in a fixed bed reactor over ZSM-48 and EU-1 zeol...
The aromatic oil, which is a byproduct of the processes of naphtha steam cracking (NSC), was hydrocr...
A novel concept of cracking-based oligomerization of naphtha (C5-C8) to produce higher range hydroca...
Symposium on Advances in the Chemistry of Asphaltene and Related Substances at the 5th North America...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
A comprehensive naphtha cracking kinetic model was developed and regressed to predict the cracking o...
One option to produce more ethene and propene can be to crack naphtha type fractions in dedicated sm...