Abstract
The lumping kinetic approach was used to model the hydrotreatment of full-range middle temperature coal tar at various operating conditions. A seven-lump model, which contains 20 constants, was proposed according to the reaction mechanism and a series of assumptions. The kinetic parameters were estimated by means of applying a variable metric method (BFGS). The results were validated by a series of further experiments. The effects of hydrogen partial pressure, LHSV (liquid hourly space velocity, h−1) and bed temperature on the performance of hydrotreatment were also investigated. Comparisons between experimental and calculated data showed good agreement.
Similar content being viewed by others
Abbreviations
- Mi :
-
Mass fraction, wt%
- t :
-
Residence time, h
- k ij :
-
Rate constant, h−1
- \(p_{{{\text{H}}_{2} }}^{{}}\) :
-
Initial hydrogen pressure, MPa
- LHSV:
-
Liquid hourly space velocity, h−1
- a :
-
Hydrogen pressure index
- b :
-
LHSV index
- k 0 :
-
M, pre-exponential factor, (hb+1·MPa−a)
- E a :
-
Apparent activation energy, J/mol
- T :
-
Reaction temperature, K
- R :
-
Gas constant, 8.314 J/(mol·K);
- VGO:
-
Lump corresponding to a boiling point range of 350–510 °C
References
Wang QY (2011) Chinese energy situation and prospects. China Coal 31:23–28
Schobert HH, Song C (2002) Chemical and materials from coal tar in 21st century. Fuel 81:15–32
Li CS, Suzuki K (2010) Resources, properties and utilization of tar. Resour Conserv Recycl 54:905–915
Kan T, Wang HY, He HX, Li CS, Zhang SJ (2011) Experimental study on two-stage catalytic hydroprocessing of middle-temperature coal tar to clean liquid fuels. Fuel 90:3404–3409
Kusy J, Andel L, Safarova M, Vales J, Ciahotny K (2012) Hydrogenation process of the tar obtained from the pyrolisis of brown coal. Fuel 101:38–44
Zhang XJ (2011) Hydrogenating process for coal tar from mid-low-temperature coal carbonization. J China Coal Soc 36:840–844
Li D, Li WH, Gao X, Yang XY, Teng JH, Cui LW et al (2009) Hydro-grading process of medium and low temperature coal tar. Coal Convers 32:81–84
Atsushi I, Wang XS, Hiroaki S, Toshiaki K (1993) Hydrogenation of coal tar pitch with tritiated hydrogen catalyzed by metal carbonyl complexes. Estimation of hydrogen mobility of coal tar pitch in catalytic systems. Energ Fuel 7:334–336
Tang W, Fang MX, Wang HY, Yu PL, Wang QH, Luo ZY (2014) Mild hydrotreatment of low temperature coal tar distillate: product composition. Chem Eng J 236:529–537
Mosby JF, Buttke RD, Cox JA, Nikolaides C (1986) Process characterization of expanded-bed reactors in series. Chem Eng Sci 41:989–995
Nguyen TS, Tayakout-Fayolle M, Ropars M, Geantet C (2013) Hydroconversion of an atmospheric residue with a dispersed catalyst in a batch reactor: kinetic modeling including vapor–liquid equilibrium. Chem Eng Sci 94:214–223
Chen C, Yang BL, Yuan J, Wang ZW, Wang LY (2007) Establishment and solution of eight-lump kinetic model for FCC gasoline secondary reaction using particle swarm optimization. Fuel 86:2325–2332
Jacob SM, Gross B, Voltz SE, Weekman VW (1976) A lumping and reaction scheme for catalytic cracking. AIChE J 22:701–713
Meng XH, Xu CM, Gao JS, Li L (2006) Catalytic pyrolysis of heavy oils: 8-lump kinetic model. Appl Catala Gen 301:32–38
Lababidi HMS, AlHumaidan FS (2011) Modeling the hydrocracking kinetics of atmospheric residue in hydrotreating processes by the continuous lumping approach. Energ Fuel 25:1939–1949
Klein SCKMT (1995) Polynuclear aromatic hydrocarbons hydrogenation. 1. Experimental reaction pathways and kinetics. Ind Eng Chem Res 34:101–117
Elizalde I, Ancheyta J (2014) Modeling catalyst deactivation during hydrocracking of atmospheric residue by using the continuous kinetic lumping model. Fuel Process Technol 123:114–121
Elizalde I, Ancheyta J (2011) On the detailed solution and application of the continuous kinetic lumping modeling to hydrocracking of heavy oils. Fuel 90:3542–3550
Balasubramanian P (2009) Analytical solution for discrete lumped kinetic equations in hydrocracking of heavier petroleum fractions. Ind Eng Chem Res 48:6608–6617
Ancheyta-Juárez J, López-Isunza F, Aguilar-Rodríguez E (1999) 5-Lump kinetic model for gas oil catalytic cracking. Appl Catala Gen 177:227–235
Bollas GM, Lappas AA, Iatridis DK, Vasalos IA (2007) Five-lump kinetic model with selective catalyst deactivation for the prediction of the product selectivity in the fluid catalytic cracking process. Catal Today 127:31–43
Froment GF (1987) The kinetics of complex catalytic reactions. Chem Eng Sci 42:1073–1087
Deng XL, Sha YX, Wang LY, Wang GL, Meng FD (1994) Studies on a kinetic model of resid catalytic crack. Pet Process petrochem 25:35–39
Fang XC, Tan HS, Zhao YZ, Zhao CQ (1996) Study on hydrocracking lumping kinetic model. Acta Petrolei Sinica (Petroleum Processing Section) 12:33–38
Weekman VW (1968) Model of catalytic cracking conversion in fixed, moving, and fluid-bed reactors. Ind Eng Chem Process Design Dev 7:90–95
Weekman VW, Nace DM (1970) Kinetics of catalytic cracking selectivity in fixed, moving, and fluid bed reactors. AIChE J 16:397–404
Yu SF, Luo WS (2007) Four lumping kinetic model of heavy oil hydrocracking[J]. Petrochem Design 24:15–17
Dai F, Gao MJ, Li CS, Xiang SG, Zhang SJ (2011) Detailed description of coal tar hydrogenation process using the kinetic lumping approach. Energ Fuel 25:4878–4885
Li D, Li Z, Li WH, Liu QC, Feng ZL, Fan Z (2013) Hydrotreating of low temperature coal tar to produce clean liquid fuels. J Ana Appl Pyrol 100:245–252
Luenberger DG, Ye Y (2008) Linear and nonlinear programming. Springer, New York
Avriel M (2012) Nonlinear programming: analysis and methods. Courier Dover Publications, New York
Shi Q, Pan N, Long HY, Cui DC, Guo XF, Long YH et al (2013) Characterization of middle-temperature gasification coal tar. part 3: molecular composition of acidic compounds. Energ Fuel 27:108–117
Sanchez-Minero F, Ancheyta J, Silva-Oliver G, Flores-Valle S (2013) Predicting SARA composition of crude oil by means of NMR. Fuel 110:318–321
Pitault I, Forissier M, Bernard J-R (1995) Détermination de constantes cinétiques du craquage catalytique par la modélisation du test de microactivité (MAT). Can J Chem Eng 73:498–504
Li D, Li WH, Cui LW, Yang XY, Zhang MX, Yan SH (2011) Optimization of processing parameters and macrokinetics for hydrodenitrogenation of coal tar. Adv Sci Lett 4:1514–1518
Lei YC, Li D, Li WH, Ma W, Teng JH (2012) Study on grading of coal tar hydrotreatment catalysts. Acta Pet Sin (Petroleum Processing Section) 28:83–87
Absi-Halabi M, Stanislaus A, Qamra A, Chopra S (1996) Effect of presulfiding on the activity and deactivation of hydrotreating catalysts in processing Kuwait vacuum residue. In: Absi-Halabi M, Stanislaus A (eds) Studies in Surface Science and Catalysis, vol 100. Elsevier, Amsterdam, pp 243–251
Acknowledgments
We gratefully acknowledge the financial support of the National Natural Science Foundation of China (21206136), Overall Science and Technology Innovation Project of Shaanxi province (2011KTCL01-15) and Research Fund for the Doctoral Program of Higher Education of China (20126101120013).
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Sun, J., Li, D., Yao, R. et al. Modeling the hydrotreatment of full range medium temperature coal tar by using a lumping kinetic approach. Reac Kinet Mech Cat 114, 451–471 (2015). https://doi.org/10.1007/s11144-014-0791-2
Received:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s11144-014-0791-2