A model for the hydrogenation of aromatic compounds during gasoil hydroprocessing

Chemical Engineering Science

Volumn 59, Issue 22-23, 2004, Pages 5671-5677

  Melis, Stefano ^a   Erby, Lara ^b   Sassu, Lorenzo ^a   Baratti, Roberto ^b  

^a Saras Ricerche Sr1 ^*  (Italy)

^b UNIVERSITY OF CAGLIARI   (Italy)

Author keywords

Catalysis; Gasoil; Hydroprocessing; Kinetics; Mathematical modeling

Indexed keywords

GAS ADSORPTION; HYDROGENATION; MATHEMATICAL MODELS; MIXTURES; RATE CONSTANTS;

GASOIL HYDROPROCESSING; HYDROPROCESSING CATALYSTS;

AROMATIC COMPOUNDS;

HYDROGENATION;

EID: 10044273093     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2004.09.010     Document Type: Conference Paper

References (18)

1. Al-Dahnan, M.H., Larachi, F., Dudukovic, M.P., Laurent, A., 1997. High-pressure trickle-bed reactors: a review. Industrial and Engineering Chemistry Research 36, 3292-3314.
2. Chowdhury, R., Pedemera, E., Reimert, R., 2002. Trickle-bed reactor model for desulfurization and dearomatization of diesel. A.I.Ch.E Journal 48, 126-135.
3. De Wind, M., Plantenga, F.L., Heinerman, J.J.L., Homan Free, H.W., 1988. Upflow versus downflow testing of hydrotreating catalysts. Applied Catalysis 43, 29-42.
4. Girgis, M.J., Gates, B.C., 1991. Reactivities, reaction networks, and kinetics in high-pressure catalytic hydroprocessing. Industrial and Engineering Chemistry Research 30, 2021-2058.
5. Glueckauf, E., 1955. Theory of cromatography, Part 10. Formulæ for diffusion into spheres and their application to chromatography. Transactions of the Faraday Society 51, 1540-1551.
6. Goto, S., Smith, J.M., 1975. Trickle-bed reactor performance. Part I. Holdup and mass transfer effects. A.I.Ch.E Journal 21, 715-719.
7. Koltai, T., Macaud, M., Guevara, A., Schulz, E., Lemaire, M., Bacaud, R., Vrinat, M., 2002. Comparative inhibiting effect of polycondensed aromatics and nitrogen compounds on the hydrodesulfurization of alkyldibenzothiophenes. Applied Catalysis A 231, 253-261.
8. Korre, S.C., Neurock, M., Klein, M.T., Quann, R.J., 1994. Hydrogenation of polynuclear aromatic hydrocarbons. Part 2. Quantitative structure/reactivity correlations. Chemical Engineering Science 49, 4191-4210.
9. Korsten, H., Hoffmann, U., 1996. Three-phase reactor model for hydrotreating in pilot trickle-bed reactors. A.I.Ch.E Journal 42, 1350-1360.
10. Marchal, N., Mignard, S., Kasztelan, S., 1996. Aromatics saturation by sulfided nickel-molibdenum hydrotreating catalysts. Catalysis Today 29, 203-207.
11. Quann, R.J., Jaffe, S.B., 1992. Structure-oriented lumping: describing the chemistry of complex hydrocarbon mixtures. Industrial and Engineering Chemistry Research 31, 2483-2497.
12. Quann, R.J., Jaffe, S.B., 1996. Building useful models of complex reaction systems in petroleum refining. Chemical Engineering Science 51, 1615-1635.
13. 3. Chemical Engineering Science 56, 1247-1254.
14. 3. Reactivities and reaction networks. Industrial and Engineering Chemistry Proc Development 20, 68-73.
15. Sassu, L., Delitala, C., Leoni, L., Baratti, R., Melis, S., 2003 Class separation of aromatic compounds in diesel fuels. Chemical Engineering Transactions 3, 491-496.
16. Stanislaus, A., Cooper, B.H., 1994. Aromatic hydrogenation catalyis: a review. Catalysis Review - Science and Engineering 36, 75-123.
17. Toppinen, S., Rantakylä, T.K., Salmi, T., Aittamaa, J., 1996. Kinetics of the liquid-phase hydrogenation of benzene and some monosubstituted alkylbenzenes over a nickel catalyst. Industrial and Engineering Chemistry Research 35, 1824-1833.
18. Toppinen, S., Salmi, T., Rantakylä, T.K., Aittamaa, J., 1997. Liquid-phase hydrogenation kinetics of aromatic hydrocarbons mixtures. Industrial and Engineering Chemistry Research 36, 2101-2109.