Overview
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Read the articleAUTHORS
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Gilles FOURNIER: Marketing Manager, AromaticsAXENS-IFP Group Technologies
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Jean-François JOLY: PhD-engineer Catalytic reforming project manager IFP (Solaize)
INTRODUCTION
Update of the article by A. Chauvel and G. Lefebvre (IFP) published in 1988
Catalytic reforming has been a gasoline refining process since its origins in the USA in 1939, but it also plays a significant role in the supply of aromatic hydrocarbons to the petrochemical industry, since the steam cracking of petroleum cuts is the second main route for the production of benzene, toluene and xylenes.
Originally, the aim of catalytic reforming was essentially to transform low-octane petroleum cuts (40-60), commonly known as naphtha, into high-octane fuel bases. As this improvement in index was essentially due to a sharp increase in aromatics content, the process was also considered for the production of aromatics. In this case, a selected gasoline cut was processed under specific conditions, with a view to producing hydrocarbons specifically for the chemical industry.
However, for both economic and technical reasons, this distinction has become blurred. The need for high-performance fuels has grown faster than the need for benzene, toluene and xylenes. The quest for a high octane number (90 to 100), linked to the aromatic content of reformates and the severity of processing, has led to operating conditions and results that are more or less the same for both types of production.
Two more recent events have further accentuated this trend towards higher yields of aromatic compounds. These are the introduction of anti-pollution regulations, in particular to reduce the lead content of gasolines, and the obligation to save energy by making better use of oil cuts. As a result, manufacturers have developed processes that are more specific and better adapted to their constraints:
for refining, reforming processes operating under severe conditions, with greater operating stability and higher gasoline yields;
for petrochemicals, techniques that operate at higher temperatures and optimize aromatics production.
This second aspect of catalytic reforming is the only one dealt with here, and the reader is referred to the article Treatment of aromatic gasolines for petrochemical applications. for aromatic hydrocarbon separation techniques.
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Catalytic reforming
Bibliography
Economic data
In 2000, worldwide catalytic reforming capacity stood at 530 Mt/year, corresponding to 660 plants in operation worldwide.
In 2000, worldwide production capacity for aromatic hydrocarbons was 40 Mt/year for benzene, 21 Mt/year for toluene and 34 Mt/year for xylenes, with catalytic reforming and steam cracking of petroleum cuts being the two main production routes. At that date, reforming accounted...
Catalyst manufacturers
The global market for catalytic reforming catalysts in 2000 is estimated at around 5,000 t.
As a result of mergers and acquisitions and withdrawals, there are now around 5 catalyst manufacturers, marketing some 40 different products.
The main ones are :
UOP (Union Oil Products)
Procatalysis
...
User industries
There are around 660 catalytic reforming plants in 770 refineries worldwide. In short, all major refineries have a reforming unit, and the industrialists are therefore all types of refiner, and in particular :
the major groups: Exxon-Mobil, Shell, BP, Chevron-Texaco and TotalFinaElf;
national companies: Pemex, Saudi Aramco, Sonatrach... ;...
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