Abstract
As discussed in other chapters, catalytic hydrotreating upgrades petroleum fractions by saturating olefins and aromatics with hydrogen, and by converting contaminants such as sulfur, nitrogen and sometimes oxygen into H2S, NH3, and H2O respectively. Hydrotreating also remove trace elements such as Ni, V, Fe, Si, As and Hg. Catalytic hydrocracking converts heavy hydrocarbons into lighter material by breaking carbon-carbon bonds.
The hydroprocessing process is exothermic, and thus produces heat as the process stream and treat gas are reacted in the catalyst bed. Controlling temperature rise is a major concern during design and operation. Flow distribution is also important. Inside reactors during normal operation, fluid flow is the only significant way to remove process heat. Uneven fluid flow can impair performance. It can lead to hot spot formation, which can jeopardize process safety and catalyst life.
While proper catalyst loading and grading is very important, reactor design, specifically the internals, is the key to controlling both the exotherm and fluid flow.
This chapter provides an overview of essential components of reactor internals, with emphasis on the relative performance of different designs.
Access this chapter
Tax calculation will be finalised at checkout
Purchases are for personal use only
References
T. Petrich, P. Martinenghi: Method of and apparatus for liquid distribution, US Patent (Application) 5192465A (1993), Glitch, Inc.
F.A. Aly, R.G. Graven, D.W. Lewis: Distribution system for downflow reactors, US Patent (Application) 4836989A (1989), Mobil Oil Co.
R. Smith, J. Strickland, J. Sanwald: Vertical reactor, US Patent (Application) 3824080A (1974), Texaco, Inc.
M.P. Grosboll, R.R. Edison, T. Dresser: Apparatus and process for distributing a mixed phase through solids, US Patent (Application) 4126540A (1978), Atlantic Richfield Co.
J.E. Riopelle: Bed reactor with quench deck, US Patent (Application) 3353924A (1967), Shell Oil Co.
C.-C.J. Shih, B.A. Christolini: Vapor-liquid distributionmethod and apparatus, US Patent (Application) 5158714A (1992), Union Oil Co. of California
J.H. Ballard, J.E. Hines, Jr.: Vapor-liquid distribution method and apparatus for the conversion of hydrocarbons, US Patent (Application) 3218249A (1965), Union Oil Co. of California
J.H. Ballard, J.E. Hines, Jr.: Apparatus for mixing fluids in concurrent downflow relationship, US Patent (Application) 3502445A (1970), Union Oil Co. of California
Author information
Authors and Affiliations
Editor information
Editors and Affiliations
Rights and permissions
Copyright information
© 2017 Springer-Verlag Berlin Heidelberg
About this chapter
Cite this chapter
Bingham, F.E., Nelson, D.E., Morton, D. (2017). Hydroprocessing Reactor Internals. In: Hsu, C.S., Robinson, P.R. (eds) Springer Handbook of Petroleum Technology. Springer Handbooks. Springer, Cham. https://doi.org/10.1007/978-3-319-49347-3_23
Download citation
DOI: https://doi.org/10.1007/978-3-319-49347-3_23
Publisher Name: Springer, Cham
Print ISBN: 978-3-319-49345-9
Online ISBN: 978-3-319-49347-3
eBook Packages: Chemistry and Materials ScienceChemistry and Material Science (R0)