Handbook of Petroleum Refining Processes, Third Edition

Part 1: ALKYLATION AND POLYMERIZATION

Chapter 1.1: NExOCTANE TECHNOLOGY FOR ISOOCTANE PRODUCTION
Chapter 1.2: STRATCO EFFLUENT REFRIGERATED H 2SO 4 ALKYLATION PROCESS
Chapter 3: UOP ALKYLENE PROCESS FOR MOTOR FUEL ALKYLATION
Chapter 1.4: UOP HF ALKYLATION TECHNOLOGY
Chapter 1.5: LINEAR ALKYLBENZENE (LAB) MANUFACTURE
Chapter 1.6: Q-MAX PROCESS FOR CUMENE PRODUCTION
Chapter 1.7: CONOCOPHILLIPS REDUCED VOLATILITY ALKYLATION PROCESS (ReVAP)

Ronald Birkhoff

Kellogg Brown & Root, Inc. (KBR)

Matti Nurminen

Fortum Oil and Gas Oy

INTRODUCTION

Environmental issues are threatening the future use of MTBE (methyl-tert-butyl ether) in gasoline in the United States. Since the late 1990s, concerns have arisen over ground and drinking water contamination with MTBE due to leaking of gasoline from underground storage tanks and the exhaust from two-cycle engines. In California a number of cases of drinking water pollution with MTBE have occurred. As a result, the elimination of MTBE in gasoline in California was mandated, and legislation is now set to go in effect by the end of 2003. The U.S. Senate has similar law under preparation, which would eliminate MTBE in the 2006 to 2010 time frame.

With an MTBE phase-out imminent, U.S. refiners are faced with the challenge of replacing the lost volume and octane value of MTBE in the gasoline pool. In addition, utilization of idled MTBE facilities and the isobutylene feedstock result in pressing problems of unrecovered and/or underutilized capital for the MTBE producers. Isooctane has been identified as a cost-effective alternative to MTBE. It utilizes the same isobutylene feeds...

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