تعداد نشریات | 418 |
تعداد شمارهها | 9,983 |
تعداد مقالات | 83,453 |
تعداد مشاهده مقاله | 76,498,432 |
تعداد دریافت فایل اصل مقاله | 53,619,160 |
Optimizing the vacuum gas oil hydrocracking process temperature in the presence of Ni-Mo/γ-Al2O3-SiO2 catalyst | ||
Iranian Journal of Catalysis | ||
مقاله 5، دوره 9، شماره 2، شهریور 2019، صفحه 133-145 اصل مقاله (1.65 M) | ||
نوع مقاله: Articles | ||
نویسندگان | ||
Ehsan Taghizadeh Yusefabad1؛ Ahmad Tavasoli* 1؛ Yahya Zamani2 | ||
1School of Chemistry, College of Science, University of Tehran, Tehran, Iran. | ||
2Research Institute of Petroleum Industry (RIPI), Tehran, Iran. | ||
چکیده | ||
A suitable model for predicting the product quality of vacuum gas oil (VGO) catalytic hydrocracking is developed. Data were obtained using an experimental catalytic hydrocracking reactor loaded with the Ni-Mo/Al2O3-SiO2 catalyst. A set of experimental runs was conducted under various operating temperatures from 380 to 450 ℃. Three distribution models were used to develop the predictive model. By the discrete lumping model, distillation curves of the cracked products (naphtha, kerosene, diesel, and gas) were obtained using the simulated distillation test. Model validation results showed that the proposed models are capable of predicting the distillation curves of the hydrocracked products accurately. Accuracy and simplicity of the developed model make it suitable to estimate the conversion and also the product distribution of hydrocracking units in refineries. | ||
کلیدواژهها | ||
VGO؛ Hydrocracking؛ Discrete lumping model | ||
سایر فایل های مرتبط با مقاله
|
||
مراجع | ||
[1] T.C. Ho, Modeling of Reaction Kinetics for Petroleum Fractions, In C.S. Hsu, P.R. Robinson (Eds.), Practical Advances in Petroleum Processing, Springer, New York, 2006. [2] J. Ancheyta, S. Sánchez, and M.A. Rodríguez, Catal. Today 109 (2005) 76–92. [3] J. Thompson, The Synthesis and Evaluation of Molybdenum-Based Ultra-Dispersed Hydroprocessing Catalysts. M.Sc. Thesis, University of Calgary, Alberta, 2008. [4] M.S. Rana, V. Sámano, J. Ancheyta, and J.A.I. Diaz, Fuel 86 (2007) 1216–1231. [5] P.M. Rahimi, T. Gentzis, The Chemistry of Bitumen and Heavy Oil Processing, In C.S. Hsu, P.R. Robinson (Eds.), Practical Advances in Petroleum Processing, Springer, New York, 2006. [6] B.E. Stangeland, Ind. Eng. Chem. Process Des. Dev. 13 (1974) 71–76. [7] C.S. Laxminarasimhan, R.P. Verma, P.A. Ramachandran, AIChE J. 42 (1996) 2645–2653. [8] A. Barkhordari, S. Fatemi, M. Daneshpayeh, H. Zamani, Int. J. Chem. React. Eng. 8 (2010) A81. [9] G. Astarita, R. Ocone, AIChE J. 34 (1988)1299–1309. [10] G. Astarita, AIChE J. 35 (1989) 529–532. [11] I. Elizalde, J. Ancheyta, Fuel Process. Technol. 123 (2014) 114–121. [12] P.J. Becker, N. Serrand, B. Celse, D. Guillaume, H. Dulot, Fuel 165 (2016) 306–315. [13] S. Sánchez, M.A. Rodríguez, J. Ancheyta, Ind. Eng. Chem. Res. 44 (2005) 9409–9413. [14] H. Hassanzadeh J. Abedi, Fuel 89 (2010) 2822–2828. [15] H. Loria, G. Trujillo-Ferrer, C. Sosa-Stull, P. Pereira-Almao, Energy Fuels 25 (2011) 1364–1372. [16] J. Martínez, J. Ancheyta, Fuel 100 (2012) 193–199. [17] J.R. Restrepo-Garcia, V.G. Baldovino-Medrano, S.A. Giraldo, Appl. Catal. A 510 (2016) 98–109. [18] J.W. Ward, Fuel Process. Technol. 35 (1993) 55–85. [19] P.Y. Looi, A.R. Mohamed, C.T. Tye, Chem. Eng. J. 181 (2012) 717–724. [20] A. Gutiérrez, J.M. Arandes, P. Castaño, M. Olazar, A. Barona, J. Bilbao, Chem. Eng. Technol. 35 (2012) 653–660. [21] N. Panariti, A. Del Bianco, G. Del Piero, M. Marchionna, P. Carniti, Appl. Catal. A 204 (2000) 215–222. [22] J. Mosio-Mosiewski, I. Morawski, Appl. Catal. A 283 (2005) 147–155. | ||
آمار تعداد مشاهده مقاله: 415 تعداد دریافت فایل اصل مقاله: 336 |