Characterization of Equilibrium Catalysts from the Fluid Catalytic Cracking Process of Atmospheric Residue
Abstract
:1. Introduction
2. Results and Discussion
2.1. N2 Isotherm and Pore Size Distribution Analysis
2.2. Crystallography Analysis
2.3. UV-Visible Near-Infrared Spectra and Raman Spectra Analysis
2.4. Solid-State LECO Carbon Analyzer and NMR 13C Studies
2.5. Catalyst Morphology Changes during the FCC Process
2.6. Catalyst Acidity Evolution during the FCC Process
2.7. Thermal Analysis
2.8. Kinetics and Thermodynamics Parameters Calculation Using TGA
3. Material and Methods
3.1. Sampling of Catalyst
3.2. Cracking Reaction and Regeneration Conditions
3.3. Catalyst Characterization
4. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Samples | SBET (m2g−1) | Sext (m2g−1) | Smicro (m2g−1) | Vtotal (cm3g−1) | Vmicro (cm3g−1) | Microporosity (%) |
---|---|---|---|---|---|---|
Fresh | 158.13 | 94.24 | 63.8825 | 0.147 | 0.028 | 40.39 |
Regenerated | 76.78 | 38.55 | 38.2327 | 0.098 | 0.017 | 49.79 |
Spent | 57.45 | 28.87 | 28.5726 | 0.077 | 0.012 | 49.73 |
property | Fresh | Regenerated | Spent |
---|---|---|---|
Composition (wt.%) | |||
CO2 | 9.64 | 3.56 | 9.58 |
N | 0.27 | ||
Na2O | 0.10 | 0.12 | 0.11 |
MgO | 0.35 | 0.14 | 0.11 |
Al2O3 | 50.71 | 50.28 | 47.04 |
SiO2 | 34.65 | 39.04 | 37.35 |
P2O5 | 0.51 | 0.54 | 0.35 |
SO3 | 0.33 | 0.2 | 0.26 |
K2O | 0.47 | 0.54 | 0.56 |
CaO | 0.07 | 0.12 | 0.10 |
TiO2 | 0.22 | 0.19 | 0.20 |
V2O5 | 0.06 | 0.05 | |
Fe2O3 | 0.44 | 0.55 | 0.50 |
Co2O3 | 0.12 | 0.08 | |
NiO | 2.05 | 1.52 | |
CuO | 0.004 | ||
ZnO | 0.003 | 0.013 | 0.008 |
Ga2O3 | 0.012 | 0.012 | 0.010 |
GeO2 | 0.004 | ||
Rb2O | 0.002 | 0.003 | |
Y2O3 | 0.66 | 0.14 | 0.08 |
ZrO2 | 0.003 | 0.004 | |
Sb2O3 | 0.05 | 0.02 | |
La2O3 | 1.18 | 1.66 | 1.61 |
CeO2 | 0.48 | 0.32 |
Samples | Pyridine, μmol g−1 | |||
---|---|---|---|---|
Brönsted Acid | Lewis Acid | |||
150 °C | 500 °C | 150 °C | 500 °C | |
Fresh | 89 | 138 | 121 | 71 |
Regenerated | 25 | 5 | 44 | 6 |
Spent | 14 | 0 | 37 | 2 |
Fresh Catalyst | Regenerated Catalyst | Spent Catalyst | |||||||||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Zone | T °C | Ea Jmol−1 (×102) | Jmol−1 (×10−2) | Jmol−1K−1 (×105) | Jmol−1 (×106) | Fitting Equation | R2 | Ea Jmol−1 (×102) | Jmol−1 (×10−2) | Jmol−1K−1 (×105) | Jmol−1 (×106) | Fitting Equation | R2 | Ea Jmol−1 (×102) | Jmol−1 (×10−2) | Jmol−1K−1 (×105) | Jmol−1 (×106) | Fitting Equation | R2 |
1 | 100–300 | 10.85 | −3.03 | 51.73 | 5.34 | Y = −0.13065x − 0.0994 | 0.99 | 12.37 | −3.02 | 58.93 | 6.06 | Y = −0.1488x −0.0984 | 0.99 | 42.45 | −2.86 | 202.24 | 20.38 | Y = −0.5106x + 0.5913 | 0.98 |
2 | 300–450 | 21.44 | −3.00 | 128.89 | 13.10 | Y = −0.2579x + 0.318 | 0.98 | 31.01 | −2.94 | 186.42 | 18.85 | Y = −0.373x + 0.6749 | 0.99 | 66.63 | −2.84 | 400.58 | 40.26 | Y = −0.8015x + 1.0601 | 0.97 |
3 | 450–550 | 133.44 | −2.63 | 913.11 | 91.52 | Y = −1.605x + 3.2677 | 0.98 | 52.08 | −2.88 | 356.37 | 35.87 | Y = −0.6264x + 1.252 | 0.99 | 201.00 | −2.59 | 1380 | 138 | Y = −2.4176x + 3.296 | 0.98 |
4 | 550–700 | 77.43 | −2.82 | 626.40 | 62.91 | Y = −0.9313x + 2.0443 | 0.99 | 79.01 | −2.84 | 639.18 | 64.19 | Y = −0.9503x + 1.8307 | 0.99 | 190.16 | −2.65 | 1540 | 154 | Y = −2.2872x + 3.2081 | 0.97 |
5 | 700–850 | 137.75 | −2.72 | 1290 | 129 | Y = −1.6568x + 3.0534 | 0.98 | 164.49 | −2.69 | 1540 | 154 | Y = −1.9784x + 3.275 | 0.98 | 134.56 | −2.77 | 1260 | 126 | Y = −1.6185x + 2.4638 | 0.98 |
Item | Value |
---|---|
Density (g/cm3) | 0.9215 |
API | 22.05 |
Aniline point (°C) | 52.9 |
Residual carbon (wt.%) | 5.5 |
Nickel (ppm) | 22.9 |
Vanadium (ppm) | 0.3 |
Iron (ppm) | 3.2 |
Sulfur (wt.%) | 0.24 |
Nitrogen (wt.%) | 0.17 |
Average molecular weight (g/mol) | 462 |
Distillation TBP (°C) | |
50% | 343.0 |
90% | 378.0 |
95% | 385.0 |
SARA fractions (wt.%) a | |
Aromatics | 18.34 |
Asphaltenes | 7.10 |
Saturates | 33.44 |
NS0 b | 41.12 |
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Zakariyaou, S.Y.; Ye, H.; Oumarou, A.D.M.; Abdoul Aziz, M.S.; Ke, S. Characterization of Equilibrium Catalysts from the Fluid Catalytic Cracking Process of Atmospheric Residue. Catalysts 2023, 13, 1483. https://doi.org/10.3390/catal13121483
Zakariyaou SY, Ye H, Oumarou ADM, Abdoul Aziz MS, Ke S. Characterization of Equilibrium Catalysts from the Fluid Catalytic Cracking Process of Atmospheric Residue. Catalysts. 2023; 13(12):1483. https://doi.org/10.3390/catal13121483
Chicago/Turabian StyleZakariyaou, Seybou Yacouba, Hua Ye, Abdoulaye Dan Makaou Oumarou, Mamane Souley Abdoul Aziz, and Shixian Ke. 2023. "Characterization of Equilibrium Catalysts from the Fluid Catalytic Cracking Process of Atmospheric Residue" Catalysts 13, no. 12: 1483. https://doi.org/10.3390/catal13121483
APA StyleZakariyaou, S. Y., Ye, H., Oumarou, A. D. M., Abdoul Aziz, M. S., & Ke, S. (2023). Characterization of Equilibrium Catalysts from the Fluid Catalytic Cracking Process of Atmospheric Residue. Catalysts, 13(12), 1483. https://doi.org/10.3390/catal13121483