Catalysts for CCR Process Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 248
Catalyst Suppliers . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . . .. . 249
Deactivation and Regeneration . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 249
Regeneration Steps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 250
SR Regeneration . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 250
Reforming Process Conditions . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . .. . . . . . . 251
Pressure . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 251
Temperature and Space Velocity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 252
Hydrogen-to-Hydrocarbon Ratio . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Process Flow Schemes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Fixed-Bed SR Reforming Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Cyclic Reforming Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 254
Continuous Catalyst Regeneration Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 255
Secondary Recovery . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 256
Unit Improvements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 256
Process Comparison and Economics . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 258
References . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 259
Abstract
Catalytic naphtha reforming is a major process in the petroleum refinery that
converts low value naphthas into high-octane reformate product for gasoline
blending and into high-value aromatics for petrochemical processing. Catalytic
reforming also provides valuable hydrogen for hydroprocessing units to produce
clean fuels. In the reforming process, naphthas rich in paraffins and naphthenes
are converted mainly to aromatic hydrocarbons by contacting with a platinumcontaining acidic catalyst at elevated temperatures and pressures. This chapter
will briefly review the history of catalytic reforming and then describe the
naphtha feed properties, market trends, reforming reactions, catalysts, deactivation mechanisms, catalyst regeneration, unit diagrams, process conditions and
economics.
Keywords
Catalytic reforming • Platforming • Semiregenerative • Continuous • Cyclic •
Platinum • Chlorided alumina • Fixed-bed • Naphtha • Octane • Aromatics •
Paraffins • Naphthenes • Motor fuels • Reformate • CCR • Redispersion •
Deactivation • BTX • Rhenium • Pt-Re • Pt-Sn • Hydrotreating
Introduction
Catalytic reforming is a process in which petroleum naphthas, rich in paraffins and
naphthenes, are contacted with a platinum-containing acidic catalyst at elevated
temperatures and pressures for converting to a product that is rich in aromatic
hydrocarbons. When the objective is to create motor fuels, low octane naphtha feed
is converted, or “reformed,” to a high-octane liquid gasoline blending component
called reformate. When the objective is to create aromatics as a feedstock for the
230
M.P. Lapinski et al.
Catalyst Suppliers . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . .. . . . . . . . . . . . . .. . 249
Deactivation and Regeneration . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 249
Regeneration Steps . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 250
SR Regeneration . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 250
Reforming Process Conditions . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . .. . . . . . . . . . . . . . . . . . . .. . . . . . . 251
Pressure . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 251
Temperature and Space Velocity . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 252
Hydrogen-to-Hydrocarbon Ratio . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Process Flow Schemes . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Fixed-Bed SR Reforming Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 253
Cyclic Reforming Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 254
Continuous Catalyst Regeneration Units . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 255
Secondary Recovery . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 256
Unit Improvements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 256
Process Comparison and Economics . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 258
References . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 259
Abstract
Catalytic naphtha reforming is a major process in the petroleum refinery that
converts low value naphthas into high-octane reformate product for gasoline
blending and into high-value aromatics for petrochemical processing. Catalytic
reforming also provides valuable hydrogen for hydroprocessing units to produce
clean fuels. In the reforming process, naphthas rich in paraffins and naphthenes
are converted mainly to aromatic hydrocarbons by contacting with a platinumcontaining acidic catalyst at elevated temperatures and pressures. This chapter
will briefly review the history of catalytic reforming and then describe the
naphtha feed properties, market trends, reforming reactions, catalysts, deactivation mechanisms, catalyst regeneration, unit diagrams, process conditions and
economics.
Keywords
Catalytic reforming • Platforming • Semiregenerative • Continuous • Cyclic •
Platinum • Chlorided alumina • Fixed-bed • Naphtha • Octane • Aromatics •
Paraffins • Naphthenes • Motor fuels • Reformate • CCR • Redispersion •
Deactivation • BTX • Rhenium • Pt-Re • Pt-Sn • Hydrotreating
Introduction
Catalytic reforming is a process in which petroleum naphthas, rich in paraffins and
naphthenes, are contacted with a platinum-containing acidic catalyst at elevated
temperatures and pressures for converting to a product that is rich in aromatic
hydrocarbons. When the objective is to create motor fuels, low octane naphtha feed
is converted, or “reformed,” to a high-octane liquid gasoline blending component
called reformate. When the objective is to create aromatics as a feedstock for the
230
M.P. Lapinski et al.