Fundamental study of hierarchical millisecond gas-phase catalytic cracking process for enhancing the production of light olefins from vacuum residue

Fuel ◽  
2019 ◽  
Vol 237 ◽  
pp. 1-9 ◽  
Author(s):  
Yuanjun Che ◽  
Meng Yuan ◽  
Yingyun Qiao ◽  
Qin Liu ◽  
Jinhong Zhang ◽  
...  
2012 ◽  
Vol 26 (3) ◽  
pp. 1870-1879 ◽  
Author(s):  
Haohua Gao ◽  
Gang Wang ◽  
Hao Wang ◽  
Jianliang Chen ◽  
Chunming Xu ◽  
...  

2010 ◽  
Vol 46 (2) ◽  
pp. 99-107 ◽  
Author(s):  
B. Z. Solyar ◽  
E. Z. Aladysheva ◽  
M. V. Mnev ◽  
V. N. Popov ◽  
L. Sh. Glazov ◽  
...  

2010 ◽  
Vol 46 (3) ◽  
pp. 164-169 ◽  
Author(s):  
B. Z. Solyar ◽  
L. Sh. Glazov ◽  
E. A. Klimtseva ◽  
I. M. Liberzon ◽  
M. V. Mnev ◽  
...  

2020 ◽  
Vol 5 (1) ◽  
pp. 9-14
Author(s):  
Metta Wijayanti ◽  
Sri Haryati ◽  
Muhammad Djoni Bustan

2020 ◽  
Vol 5 (2) ◽  
pp. 69-75
Author(s):  
Aditya Retno Utami ◽  
◽  
Deby Ansyory ◽  
Sri Haryati ◽  
M. Djoni Bustan

2018 ◽  
Vol 69 (10) ◽  
pp. 2633-2637
Author(s):  
Raluca Dragomir ◽  
Paul Rosca ◽  
Cristina Popa

The main objectives of the present paper are to adaptation the five-kinetic model of the catalytic cracking process and simulation the riser to predicts the FCC products yields when one of the major input variable of the process is change. The simulation and adaptation are based on the industrial data from Romanian refinery. The adaptation is realize using a computational method from Optimization Toolbox from Matlab programming language. The new model can be used for optimization and control of FCC riser.


Fuel ◽  
2021 ◽  
Vol 292 ◽  
pp. 120364
Author(s):  
Peipei Miao ◽  
Xiaolin Zhu ◽  
Yangling Guo ◽  
Jie Miao ◽  
Mengyun Yu ◽  
...  

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