Handbook of Petroleum Refining Processes, Third Edition

Part 10: SEPARATION PROCESSES

Chapter 10.1: CHEVRON LUMMUS GLOBAL ON-STREAM CATALYST REPLACEMENT TECHNOLOGY FOR PROCESSING HIGH-METAL FEEDS
Chapter 10.2: THE ROSE PROCESS
Chapter 10.3: UOP SORBEX FAMILY OF TECHNOLOGIES
Chapter 10.4: UOP/FW USA SOLVENT DEASPHALTING PROCESS
Chapter 10.5: UOP ISOSIV PROCESS
Chapter 10.6: KEROSENE ISOSIV PROCESS FOR PRODUCTION OF NORMAL PARAFFINS
Chapter 10.7: UOP MOLEX PROCESS FOR PRODUCTION OF NORMAL PARAFFINS
Chapter 10.8: UOP OLEX PROCESS FOR OLEFIN RECOVERY

David E. Earls

Chevron Lummus Global
Richmond, California

INTRODUCTION

In processing less expensive, high-metal feeds, the need for frequent catalyst change-outs can make conventional fixed-bed residuum hydrotreating technology uneconomical. Chevron Lummus Global (CLG) developed on-stream catalyst replacement (OCR) to remove metals from feed before it is hydrotreated in fixed-bed residuum desulfurization (RDS) units. The ability to add and withdraw catalyst from the high-pressure, moving-bed OCR reactor while it is onstream gives refiners the opportunity to process heavier, high-metal feeds or to achieve deeper desulfurization while maintaining fixed-bed run lengths and improving product properties.

DEVELOPMENT HISTORY

Development of the OCR process started in 1979 as part of the research on new reactor concepts which might be applied to synthetic fuels and heavy oil upgrading. Most of these alternative fuels are difficult to upgrade to transportation fuels. Typically high in nitrogen, sulfur, and metals, they tend to deactivate catalyst very rapidly. Consequently, conventional fixed-bed hydrotreating processes can not upgrade these feedstocks economically. CLG determined that if fresh catalyst could be continually moved through a reactor, then catalytic activity could be maintained without shutting down the unit. Theoretically,...

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