1993CHEMTECH; (United States)Requires access

Meeting the challenge of reformulated gasoline

Robin Schmidt, N.L. Gilsdorf, P.L. Bogdan

Open publisher page 2 citations

Abstract

The need to include oxygenates in motor fuel in certain areas of the United States and the effect of government-mandated aromatics and endpoint reduction will dramatically change gasoline composition and processing technology. The refinery product that boils in the range of 350-450 F will be particularly difficult for a refiner to blend into gasoline if the gasoline endpoint or 90% point (T90) specifications are reduced. The UOP I-Forming process selectively cracks naphtha, kerosene, or both to generate high yields of isobutane. It can offer a cost-effective solution to some of the requirements of reformulated gasoline (RFG). Isobutane is used for the manufacture of methyl tert-butyl ether (MTBE) (after dehydrogenation to isobutene) or the production of gasoline alkylate. This article describes reformulated gasoline; the I-Forming process; and process variables.

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What this paper is about

The need to include oxygenates in motor fuel in certain areas of the United States and the effect of government-mandated aromatics and endpoint reduction will dramatically change gasoline composition and processing technology. The refinery product that boils in the range of 350-450 F will be particularly difficult for a refiner to blend into gasoline if the gasoline endpoint or 90% point (T90) specifications are reduced. The UOP I-Forming process selectively cracks naphtha, kerosene, or both to generate high yields of isobutane. It can offer a cost-effective solution to some of the requirements of reformulated gasoline (RFG). Isobutane is used for the manufacture of methyl tert-butyl ether (MTBE) (after dehydrogenation to isobutene) or the production of gasoline alkylate. This article describes reformulated gasoline; the I-Forming process; and process variables.

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Available abstract

The need to include oxygenates in motor fuel in certain areas of the United States and the effect of government-mandated aromatics and endpoint reduction will dramatically change gasoline composition and processing technology. The refinery product that boils in the range of 350-450 F will be particularly difficult for a refiner to blend into gasoline if the gasoline endpoint or 90% point (T90) specifications are reduced. The UOP I-Forming process selectively cracks naphtha, kerosene, or both to generate high yields of isobutane. It can offer a cost-effective solution to some of the requirements of reformulated gasoline (RFG). Isobutane is used for the manufacture of methyl tert-butyl ether (MTBE) (after dehydrogenation to isobutene) or the production of gasoline alkylate. This article describes reformulated gasoline; the I-Forming process; and process variables.

Key concepts: Gasoline, Naphtha, Oxygenate, Isobutane, Refinery, Kerosene, Waste management, Petroleum product

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