Nanotechnological characterization of allofanite and faujasite (Y-faujasite) catalysts and comparing with a commercial FCC catalyst (X-zeolite)

We studied the synthesis variables of the faujasite using natural clinker of the Cotopaxi volcano, and allophane (allofanite) from the province of Santo Domingo de los Tsachilas as raw materials, as well as their physicochemical properties and their influence on the catalytic efficiency for Ecuadorian oil and asphalt. The synthesized materials were subjected to laboratory tests, like thermogravimetric characterization, BET area, FTIR, chemisorption and AFM. Tests of catalytic activity in crude oil and asphalt with different °API and percentage of Sulfur showed ranges of optimal efficiency. These ranges contributed to obtain a logistic regression model with min. 90% accuracy, which was entered into a confusion matrix. This function can be optimized in the intervals of each of the variables of any refinery. It is concluded that the logistic regression model for catalytic efficiency is sensitive to changes in the amount of faujasite and allophane (allofanite) in the catalytic cracking process. In the same way, a fundamental dependence of the surface area (BET) was found, which for the case of allophane is formed in contribution of each of the nanopores whose size is in the order of 3 to 5 nm, while the faujasite has nanopore sizes from 17 to 35 nm.

[1]  S. Bhatia Shape Selective Catalysis , 2020 .

[2]  Q. Crowley,et al.  Logistic regression model for detecting radon prone areas in Ireland. , 2017, The Science of the total environment.

[3]  P. Herrera,et al.  Study of the catalytic activity of the faujasite from natural clinker and pumice , 2017 .

[4]  Bilge Yilmaz,et al.  Zeolites in Fluid Catalytic Cracking (FCC) , 2016 .

[5]  Z. Abidin,et al.  Structure and distribution of allophanes, imogolite and proto-imogolite in volcanic soils , 2012 .

[6]  S. Gíslason,et al.  Silicon isotopes in allophane as a proxy for mineral formation in volcanic soils , 2011 .

[7]  R. Jahn,et al.  Quantification of Allophane from Ecuador , 2010 .

[8]  L. Eichinger,et al.  Allophane compared with other sorbent minerals for the removal of fluoride from water with particular focus on a mineable Ecuadorian allophane , 2010 .

[9]  J. M. Arandes,et al.  HZSM-5 Zeolite As Catalyst Additive for Residue Cracking under FCC Conditions , 2009 .

[10]  M. Frechen,et al.  A new massive deposit of allophane raw material in Ecuador , 2009 .

[11]  D. Ruthven DIFFUSION IN ZEOLITE MOLECULAR SIEVES , 2007 .

[12]  A. Razafitianamaharavo,et al.  Synthetic allophane-like particles: textural properties , 2005 .

[13]  P. Russo,et al.  Environmental catalysis: trends and outlook , 2002 .

[14]  T. Degnan,et al.  Applications of zeolites in petroleum refining , 2000 .

[15]  M. Dry,et al.  New catalytic applications of zeolites for petrochemicals , 1996 .

[16]  M. Stöcker Review on recent NMR Results , 1994 .

[17]  M. M. Mitchell,et al.  Fluid catalytic cracking : science and technology , 1993 .

[18]  L. Rees Introduction to Zeolite Science and Practice , 1992 .

[19]  R. Madon Role of ZSM-5 and ultrastable Y zeolites for increasing gasoline octane number , 1991 .

[20]  N. Chen,et al.  Shape Selective Catalysis in Industrial Applications , 1989 .

[21]  Thomas F. Degnan,et al.  Industrial catalytic applications of zeolites , 1988 .

[22]  P. Maher,et al.  Prediction of cracking catalyst behavior by a zeolite unit cell size model , 1984 .