Diesel-like fuel production from catalytic cracking and esterification of waste oil

2013 ◽  
Vol 5 (5) ◽  
pp. 052004 ◽  
Author(s):  
J. Chen ◽  
J. C. Jiang ◽  
X. A. Nie ◽  
J. M. Xu ◽  
X. Chang ◽  
...  
2019 ◽  
Vol 93 ◽  
pp. 162-172 ◽  
Author(s):  
Elena Rodríguez ◽  
Alazne Gutiérrez ◽  
Roberto Palos ◽  
Francisco J. Vela ◽  
José M. Arandes ◽  
...  

2018 ◽  
Vol 51 (9) ◽  
pp. 778-785 ◽  
Author(s):  
Iori Shimada ◽  
Yoshitaka Nakamura ◽  
Haruhisa Ohta ◽  
Kengo Suzuki ◽  
Toru Takatsuka

2018 ◽  
Vol 112 ◽  
pp. 138-143 ◽  
Author(s):  
Iori Shimada ◽  
Yoshitaka Nakamura ◽  
Shin Kato ◽  
Ryohei Mori ◽  
Haruhisa Ohta ◽  
...  

Author(s):  
Xia Jiang ◽  
Feng Long ◽  
Jiaping Zhao ◽  
Peng Liu ◽  
Jianchun Jiang ◽  
...  

Abstract: Molecular structural modification was a critical step for the production of high-quality biofuel. In this study, it was found that catalytic cracking followed by products isomerization is an effective...


2018 ◽  
Vol 217 ◽  
pp. 233-240 ◽  
Author(s):  
Wenchao Ma ◽  
Bin Liu ◽  
Ruixue Zhang ◽  
Tianbao Gu ◽  
Xiang Ji ◽  
...  

2020 ◽  
Vol 63 (1) ◽  
pp. 10-19
Author(s):  
Iori SHIMADA ◽  
Takuya MATSUMOTO ◽  
Haruhisa OHTA ◽  
Toru TAKATSUKA

2018 ◽  
Vol 61 (5) ◽  
pp. 302-310 ◽  
Author(s):  
Iori Shimada ◽  
Yutaka Kobayashi ◽  
Haruhisa Ohta ◽  
Kengo Suzuki ◽  
Toru Takatsuka

2020 ◽  
Vol 3 (1) ◽  

Currently, refiners are experiencing a big challenge due to the slow economic growth, over diesel production and decreased demand of it. Refineries are searching for technologies that could reduce diesel output, particularly the inferior light cycle oil (LCO) fraction. Here in, this article mainly we will describes the industrialized technologies for LCO processing such as LCO upgrading, LCO blending into available plants such as fluid catalytic cracking (FCC), and hydro-refining/treating unit, LCO moderate hydrocracking, and LCO to some aromatic rich stream and also with gasoline with the integration of selective hydro-refining and resulting optimized FCC unit. It is analyzed that the LCO moderate hydrocracking can provide more gasoline at the expense of high H2 consumption, while LCO to aromatics and gasoline (LTAG) technology needs more steps for clean fuel production and retrofitting of FCC plant. Based on the analyses of current technologies, it is suggested that implementation of such technologies should consider the configuration of refineries, as well as the benefit of end users.


Author(s):  
J.K. Lampert ◽  
G.S. Koermer ◽  
J.M. Macaoy ◽  
J.M. Chabala ◽  
R. Levi-Setti

We have used high spatial resolution imaging secondary ion mass spectrometry (SIMS) to differentiate mineralogical phases and to investigate chemical segregations in fluidized catalytic cracking (FCC) catalyst particles. The oil industry relies on heterogeneous catalysis using these catalysts to convert heavy hydrocarbon fractions into high quality gasoline and fuel oil components. Catalyst performance is strongly influenced by catalyst microstructure and composition, with different chemical reactions occurring at specific types of sites within the particle. The zeolitic portions of the particle, where the majority of the oil conversion occurs, can be clearly distinguished from the surrounding silica-alumina matrix in analytical SIMS images.The University of Chicago scanning ion microprobe (SIM) employed in this study has been described previously. For these analyses, the instrument was operated with a 40 keV, 10 pA Ga+ primary ion probe focused to a 30 nm FWHM spot. Elemental SIMS maps were obtained from 10×10 μm2 areas in times not exceeding 524s.


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