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CLC number: TE624.42
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
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A study on naphtha catalytic reforming reactor simulation and analysis
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Liang Ke-min, GUO Hai-yan, PAN Shi-wei. A study on naphtha catalytic reforming reactor simulation and analysis[J]. Journal of Zhejiang University Science B, 2005, 6(6): 590-596.
@article{title="A study on naphtha catalytic reforming reactor simulation and analysis",
author="Liang Ke-min, GUO Hai-yan, PAN Shi-wei",
journal="Journal of Zhejiang University Science B",
volume="6",
number="6",
pages="590-596",
year="2005",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.2005.B0590"
}
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A1 - PAN Shi-wei
J0 - Journal of Zhejiang University Science B
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PB - Zhejiang University Press & Springer
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DOI - 10.1631/jzus.2005.B0590
Abstract: A naphtha catalytic reforming unit with four reactors in series is analyzed. A physical model is proposed to describe the catalytic reforming radial flow reactor. kinetics and thermodynamics equations are selected to describe the naphtha catalytic reforming reactions characteristics based on idealizing the complex naphtha mixture by representing the paraffin, naphthene, and aromatic groups by single compounds. The simulation results based above models agree very well with actual operation unit data.
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[2] Jerzy, S., 1999. On the kinetics of catalytic reforming with the use of various raw materials. Energy Fuels, 13(1):29-39.
[3] Jorge, A.J., Eduardo, V.M., 2000. Kinetic modeling of naphtha catalytic reforming reactions. Energy Fuels, 14(5):1032-1037.
[4] Lu, H., 1982. Manual of Petrochemical Industry Fundamental Data. Chemical Industy Press, Beijing (in Chinese).
[5] Melnikov, V.B., Makarova, N.P., 1998. Modification of reforming: Without hydrogen circulation. Khim. Tekhnol. Topl. Masel., 23(1):9-13.
[6] Pontes, L.A.M., Rangel, M.D.C., Mario, D.J.M., 1999. Catalytic reforming of naphtha. An Assoc. Bras. Quim., 48(3):169-179.
[7] Rase, H.F., 1977. Chemical Reactor Design for Process Plants. Vol. 2, John Wiley & Sons, Inc.
[8] Reid, R.C., Prausnitz, J.M., Sherwood, T.K., 1977. The Properties of Gases and Liquids. 3rd Ed., McGraw-Hill Co., p.108-109.
[9] Smith, R.B., 1959. Kinetic analysis of naphtha reforming with platinum catalyst. Chem. Eng. Progr., 55(6):76-80.
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Open peer comments: Debate/Discuss/Question/Opinion
<1>
蔡奥飞<1030379023@qq.com>
2014-12-27 19:59:30
I need this document. Thanks
hu@uni<a>
2012-08-11 11:17:56
Thanks
NAJIB@ALYOUSEFI<ALYOUSEFIES@HOTMAIL.COM>
2010-12-10 19:29:21
DEAR SIR
WE HAVE THREE REACTORS IN THE REFORMER UNIT I WOULD ASK ABOUT THE DELTA P IF ITS INCREASE IN REACTOR 1 TO 13-14
HOW CAN I DECREASE IT TO THE RANGE AND WHAT IS THE RESONS THATS MAKE IT INCREASE?
WITH MY THANKS
NAJIB