Catalyst Deactivation during Upgrade of Light Catalytic Cracking Gas Oil to Ultralow-Sulfur and Low-Aromatic Diesel

2008 ◽  
Vol 22 (3) ◽  
pp. 1509-1518 ◽  
Author(s):  
Roberto R. Galiasso Tailleur
2019 ◽  
Vol 62 (4) ◽  
pp. 164-168
Author(s):  
A. S. Lavrova ◽  
V. V. Vasilyev ◽  
V. M. Strakhov

1966 ◽  
Vol 2 (4) ◽  
pp. 223-227
Author(s):  
K. M. Vaisberg ◽  
I. I. Shabalin ◽  
�. A. Kruglov ◽  
M. A. Shmeleva

1971 ◽  
Vol 7 (3) ◽  
pp. 181-183
Author(s):  
M. S. Tsekhanovich ◽  
V. F. Surovikin ◽  
Yu. I. Popugaev ◽  
A. K. Charin

2017 ◽  
Vol 68 (4) ◽  
pp. 732-736
Author(s):  
Constantin Sorin Ion ◽  
Mihaela Bombos ◽  
Gabriel Vasilievici ◽  
Casen Panaitescu ◽  
Raluca Dragomir

Desulphurization by reactive adsorption was studied on sand abrasive blasting grit/ bentonite. The adsorbent was characterized by determining the composition, adsorption isotherms, specific surface area, pore volume and average pore diameter. Adsorption experiments were performed in continuous system at 260�300oC, 25 atm and volume hourly space velocities of 1-2 h-1. The efficiency of adsorption was evaluated at desulphurization of a synthetic reaction mixture and a catalytic cracking gas oil.


Author(s):  
Clifford S. Rainey

The spatial distribution of V and Ni deposited within fluidized catalytic cracking (FCC) catalyst is studied because these metals contribute to catalyst deactivation. Y zeolite in FCC microspheres are high SiO2 aluminosilicates with molecular-sized channels that contain a mixture of lanthanoids. They must withstand high regeneration temperatures and retain acid sites needed for cracking of hydrocarbons, a process essential for efficient gasoline production. Zeolite in combination with V to form vanadates, or less diffusion in the channels due to coke formation, may deactivate catalyst. Other factors such as metal "skins", microsphere sintering, and attrition may also be involved. SEM of FCC fracture surfaces, AEM of Y zeolite, and electron microscopy of this work are developed to better understand and minimize catalyst deactivation.


1971 ◽  
Vol 7 (3) ◽  
pp. 187-191
Author(s):  
T. P. Vishnyakova ◽  
V. V. Zamanov ◽  
G. S. Kaganer ◽  
A. A. Drichko ◽  
A. I. Mezhlumova ◽  
...  

1992 ◽  
Vol 13 (4) ◽  
pp. 383-387 ◽  
Author(s):  
Nelson P. Mart�nez ◽  
Andr�s M. Quesada P.

2013 ◽  
Vol 27 (2) ◽  
pp. 654-665 ◽  
Author(s):  
Jinhong Zhang ◽  
Honghong Shan ◽  
Wenjing Liu ◽  
Xiaobo Chen ◽  
Chunyi Li ◽  
...  

Paliva ◽  
2020 ◽  
pp. 98-106
Author(s):  
Tomáš Macek ◽  
Miloš Auersvald ◽  
Petr Straka

The article summarized the possible transformations of pyrolysis bio-oil from lignocellulose into 2nd generation biofuels. Although a lot has been published about this topic, so far, none of the published catalytic pro-cesses has found commercial application due to the rapid deactivation of the catalyst. Most researches deal with bio-oil hydrotreatment at severe conditions or its pro-cessing by catalytic cracking to prepare 2nd generation biofuels directly. However, this approach is not commercially applicable due to high consumptions of hydrogen and fast catalyst deactivation. Another way, crude bio-oil co-processing with petroleum fractions in hydrotreatment or FCC units seems to be more promising. The last approach, bio-oil mild hydrotreatment followed by final co-processing with petroleum feedstock using common refining processes (FCC and hydrotreatment) seems to be the most promising way to produce 2nd generation biofuels from pyrolysis bio-oil. Co-processing of bio-oil with petroleum fraction in FCC increases conversion to gasoline and, thus, it could be a preferable process in the USA. Otherwise, co-hydrotreatment of hydrotreated bio-oil with LCO leads not only to the reduction of hydrogen consumption but also to the conversion preferably to diesel. This process seems to be more suitable for Europe. Further research on bio-oils upgrading is still necessary before the commercialization of the bio-oil conversion into biofuels suitable for cars. However, the first commercial bio-refinery that will convert bio-oil into biofuel for marine transport is planned to be built in the Netherlands.


2021 ◽  
Vol 625 (3) ◽  
pp. 28-31
Author(s):  
P. V. Kugatov ◽  
◽  
B. S. Zhirnov ◽  
A. E. Eremenko ◽  
◽  
...  

Samples of petroleum pitches were obtained from heavy pyrolysis resin and decantoil (heavy gas-oil of catalytic cracking) by thermal polycondensation at atmospheric pressure, temperatures of 380–400 and 410–440°С (for resin and decantoil, respectively) and isothermal holding time of 30–480 min. Analysis of the dependence of the softening point on the mesophase content for the obtained samples showed that at the same mesophase content, decantoil pitches exhibit a lower softening point compared to pyrolysis resin pitches, for which, even at 30 % mesophase, the softening point approaches 300°C. This suggests that it is impossible to obtain pitch from pyrolysis resin with high mesophase content without preliminary preparation (for example, by hydrogenation). On the other hand, it has been shown that for pitches from decantoil, it is possible to isolate the mesophase up to 65% or more with a softening point not higher than 250°C.


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