Synergy in the Cracking of a Blend of Bio-oil and Vacuum Gasoil under Fluid Catalytic Cracking Conditions

2016 ◽  
Vol 55 (7) ◽  
pp. 1872-1880 ◽  
Author(s):  
Álvaro Ibarra ◽  
Elena Rodríguez ◽  
Ulises Sedran ◽  
José M. Arandes ◽  
Javier Bilbao
2019 ◽  
Vol 188 ◽  
pp. 164-171 ◽  
Author(s):  
Eduardo Santillan-Jimenez ◽  
Robert Pace ◽  
Tonya Morgan ◽  
Craig Behnke ◽  
Daniel J. Sajkowski ◽  
...  

2014 ◽  
Vol 86 (5) ◽  
pp. 859-865 ◽  
Author(s):  
Andrea de Rezende Pinho ◽  
Marlon Brando Bezerra de Almeida ◽  
Fabio Leal Mendes ◽  
Vitor Loureiro Ximenes

AbstractThis paper shows how some existing refining technologies such as fluid catalytic cracking (FCC) can be modified to process bio-oil, derived from agricultural lignocellulosic wastes such as the sugar cane straw. Tests carried out in demonstration scale (150 kg/h) show the potential of these alternative materials to produce lignocellulosic gasoline or aromatic compounds, suitable to the petrochemical industry.


Author(s):  
José Ignacio Alvira ◽  
Idoia Hita ◽  
Elena Rodriguez ◽  
Jose M Arandes ◽  
Pedro Castaño

Associating the most influential parameters with the product distribution is of uttermost importance in complex catalytic processes such as fluid catalytic cracking (FCC). These correlations can lead to the information-driven catalyst screening, kinetic modeling and reactor design. In this work, a dataset of 104 uncorrelated experiments, with 64 variables, has been obtained in an FCC simulator using 6 types of feedstock (vacuum gasoil, polyethylene pyrolysis waxes, scrap tire pyrolysis oil, dissolved polyethylene and blends of the previous), 36 possible sets of conditions (varying contact time, temperature and catalyst/oil ratio) and 3 industrial catalysts. Principal component analysis (PCA) has been applied over the dataset, showing that the main components are associated with feed composition (27.41% variance); operational conditions (19.09%) and catalyst properties (12.72%). The variables of each component have been correlated with the indexes and yields of the products: conversion, octane number, aromatics, olefins (propylene) or coke, among others.


Processes ◽  
2018 ◽  
Vol 6 (12) ◽  
pp. 243 ◽  
Author(s):  
José Alvira ◽  
Idoia Hita ◽  
Elena Rodríguez ◽  
José Arandes ◽  
Pedro Castaño

Establishing a reaction network is of uttermost importance in complex catalytic processes such as fluid catalytic cracking (FCC). This step is the seed for a faithful reactor modeling and the subsequent catalyst re-design, process optimization or prediction. In this work, a dataset of 104 uncorrelated experiments, with 64 variables, was obtained in an FCC simulator using six types of feedstock (vacuum gasoil, polyethylene pyrolysis waxes, scrap tire pyrolysis oil, dissolved polyethylene and blends of the previous), 36 possible sets of conditions (varying contact time, temperature and catalyst/oil ratio) and three industrial catalysts. Principal component analysis (PCA) was applied over the dataset, showing that the main components are associated with feed composition (27.41% variance), operational conditions (19.09%) and catalyst properties (12.72%). The variables of each component were correlated with the indexes and yields of the products: conversion, octane number, aromatics, olefins (propylene) or coke, among others. Then, a data-driven reaction network was proposed for the cracking of waste feeds based on the previously obtained correlations.


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

2020 ◽  
Vol 105 ◽  
pp. 18-26 ◽  
Author(s):  
Elena Rodríguez ◽  
Roberto Palos ◽  
Alazne Gutiérrez ◽  
José M. Arandes ◽  
Javier Bilbao

Author(s):  
Idoia Hita ◽  
Jose Maria Arandes ◽  
Javier Bilbao

2016 ◽  
Vol 182 ◽  
pp. 336-346 ◽  
Author(s):  
Álvaro Ibarra ◽  
Antonio Veloso ◽  
Javier Bilbao ◽  
José Mª Arandes ◽  
Pedro Castaño

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