HYDROISOMERIZATION OF n-ALKANE OVER ZEOILTE SUPPORTED CATALYST

محتوى المقالة الرئيسي

Abdul-Halim A.K. Mohamed
Mohamed Kamel

الملخص

The conversion of nC5-nC7 over 0.32wt%Pt/HY-Zeolite catalyst was studied with temperature range 240-270ºC, liquid hourly space velocity range 1-3h-1, hydrogen to n-alkane mole ratio 8-24 and atmospheric total pressure. The effect of the PH2, PnC5, PnC6, and PnC7 orders on the overall reaction rate was studied. For nC7, the reaction order with respect to hydrogen varied between -0.998 and -0.948 while with respect to nC7 varied between 0.154 and 0.156. For nC6, the reaction order varied between -0.811 and -0.808 while with respect to nC6 varied between 0.332 and 0.337. For nC5, the reaction order with respect to hydrogen varied between -0.652 and -0.620 while the reaction order with respect to nC5 was varied between 0.336 and 0.339. The values of apparent activation energy were obtained and found to be varied between 110 and 111 kJ/mol for nC7, 120 to 122 kJ/mol for nC6, and 145 to 148 kJ/mol for nC5.

تفاصيل المقالة

القسم

Articles

كيفية الاقتباس

"HYDROISOMERIZATION OF n-ALKANE OVER ZEOILTE SUPPORTED CATALYST" (2009) مجلة الهندسة, 15(03), ص 3919–3940. doi:10.31026/j.eng.2009.03.08.

المراجع

 Jafar Sadeghzadeh Ahari, Kayvan Khorsand, Azita A Hosseini, Amir Farshi ," EXPERIMENTAL STUDY OF C5/C6 ISOMERIZATION IN LIGHT STRAIGHT RUN GASOLINE (LSRG) OVER PLATINUM MORDENITE ZEOLITE", Pet. & Co. 48 (3), 42-50, 2006.

 Allain J. F., P. Magnoux, Ph. Schulz and M. Guisnet," Hydroisomerization of n-hexane over platinum mazzite and platinum mordenite catalysts kinetics and mechanism", App. Cat. Vol.152, (2) , 221-235,1997

 Alvarez, F., Ribeiro, F.R., Perot, G., Thomazeau, C., Guisnet, M., Jour.of Cat., Vol. 162,(2, 179-189), 1996.

 Asuquo R.A.,G.Eder-Mirth, K. Seshan, J. A. Z. Piterse, and J. A. Lercher " Improving the stability of H-mordenite for n-butane isomerization" , Jour.of Cat.,168,292-300(1997).

 Cañizares P., A. Durán, F. Dorado and M. Carmona, App.Clay Sci.Vol.16, 273-287,2000

 Exner H., E. Nagy, F. Fetting, and L. Gubicza, conf. of app. Chem. Vol 2 420-425( 1989).

 Giuseppe E. Glannetto, Guy R. Perot, and Michel I., Ind. Eng. Chem. Prod. Res. D8V. 1986, 25, 481-490

 Kouwenhoven H.W. and W.C. Van Zijll Langhout, ,.Chem .Eng. Prog., v.67, p.65, 1971

 Kuchar P. J., J. C. Bricker, M. E. Reno, R. S. Haizmann, Fuel Pro. Tech., Vol.35, . 1-2, 183-200,1993

 Lanewala M. A., P. E. Pickert and A. P. Botton, Journal of CatalysisVolume 9, Issue 1, September 1967, Pages 95-97.

 Meyers, A. Robert, “Handbook of Petroleum Refining Process.” McGraw Hill, New York (1996).

 Martens G.G., G.B.Marin, J.A.Martens, P.A. Jacobs, and G.V. Baron" A fundemental kinetic model for hydrocracking of C8 to C12 alkanes on Pt/US-Yzeolites", jor.of cat.195,253-267 (2000).

 Narbesshuber Thomas F., Axel Brait, Kulathuyiedr Seshan, and Johannes A. Lercher "Dehydrogenation of light alkanes over zeolite" , jor. of cat. 172,127-136(1997).

 OKUHARA Toshio, Skeletal Isomerization of n-Heptane to Clean Gasoline,jour. Of jap.petr.inst. 47,(1),1-10, 2004

 Pine L. A., P. J. Maher, W. A. Wachter," Prediction of cracking catalyst behavior by a zeolite unit cell size model" Jour. of Cat., Vol. 85, .2, 466-476,1984.

 Ribeiro F., C. Marcilly, M. Guisnet, Jour. of Cat., Vol. 78, 2, , Pages 267-274,1982.

 Runstraat A. van de, J. A. Kamp, P. J. Stobbelaar, J. van Grondelle, S. Krijnen, and R. A. van Santen, Jour. of Cat. 171, 77–84 (1997a)

 Runstraat A. van de, Joop van Grondelle, and Rutger A. van santen, Ind. Eng. Chem. Res.,36,3116-3125. (1997b)

 Santen R. A. van, Runstraat A. van de, J. van Grondelle, , Jour.of Cat., Volume 167, .2, Pages 460-463 ,1997.

 Serge Raseev, "Catalytic processes in petroleum refining", New York 2003.

المؤلفات المشابهة

يمكنك أيضاً إبدأ بحثاً متقدماً عن المشابهات لهذا المؤلَّف.