The Penex process is a continuous catalytic process used in the refining of crude oil. It isomerizes light naphtha (C5/C6) into higher-octane, branched C5/C6 molecules. It also reduces the concentration of benzene in the gasoline pool.[1] It was first used commercially in 1958.[2] Ideally, the isomerization catalyst converts normal pentane (nC5) to isopentane (iC5) and normal hexane (nC6) to 2,2- and 2,3-dimethylbutane. The thermodynamic equilibrium is more favorable at low temperature.[3]
Background edit
In the petroleum industry, much research has been done on the upgrading of light hydrocarbons. The realisation that normal pentane is one of the most important remaining components of naphtha that can be easily upgraded prompted Phillips Petroleum to investigate the various processes for converting normal (linear) pentane into (branched) isopentane. The decisive factor in the isomerisation of normal pentane is an increase in the total octane number. This improvement in quality makes the result more valuable for blending with today's high-octane fuels. In addition, like other isoparaffins, isopentane has a low sensitivity (research octane minus engine octane) which means improved performance at street octane. Increasing the octane number also allows larger quantities of pentanes to be blended into premium petrol.[4]
In a refinery, light naphtha can come from the distillation column ("straight-run naphtha") or from other processes, for example the cracking units.
Process edit
During isomerisation, the low-octane normal hydrocarbons are converted into their higher-octane isomers. For this purpose, the feed material is passed over a fixed bed catalyst in the presence of hydrogen. The hydrogen is continuously circulated in the reactor circuit.[5] The Penex process uses fixed-bed catalysts containing chlorides.[6]
As this is an equilibrium reaction, 100% conversion of the normal isomers is not achieved. The maximum octane number of the product is achieved by separating the unconverted normals using a molecular sieve (Molex technology) and returning them to the reactor.[5]
Results edit
A single pass of feedstock with an octane rating of 50-60 through such a bed typically produces an end product rated at 82-86. If the feedstock is subsequently passed through a DIH (deisohexanizer) column, the end product typically has an octane rating of 87-90.5. If the feedstock is subsequently passed through a Molex-technology column, the end product typically has an octane rating of 88-91. If the feedstock is first passed through a DIP (deisopentanizer) column to remove iso-pentanes, then through the Penex bed, and subsequently through the DIH column, the end product typically has an octane rating of 91-93.
Field use edit
The Penex Process is licensed by the UOP corporation and currently utilized at more than 120 units at petroleum refineries and natural gas liquids plants throughout the world.[7]
References edit
- ^ "Isomerization HOT Penex Process by UOP - Oil & Gas Process Engineering". Retrieved 2023-03-05.
- ^ "UOP Penex Process website" (PDF). Archived from the original (PDF) on 2010-12-01. Retrieved 2009-04-09.
- ^ a b "Isomerization Process". Hassan ElBanhawi. Retrieved 2023-03-05.
- ^ Dean, L. E. (1959). "The Penex Process for Pentane Isomerisation". Platinum Metals Rev. 3 (1) (9).
- ^ a b "18,000 BPD C5/C6 Isomerization for Sale at Phoenix Equipment | Isomerization Units for Sale". www.phxequip.com. Retrieved 2023-11-23.
- ^ Takao, Kimura (2003). "Development of Pt/SO 4 2−/ZrO 2 catalyst for isomerization of light naphtha". Catalysis Today. 81 (1): 57–63. doi:10.1016/s0920-5861(03)00102-0.
- ^ Maples, Robert E. (2000). Petroleum refinery process economics. Penwell Books. p. 455. ISBN 9780878147793. Retrieved 13 April 2015.
External links edit
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