Global Refining Summit 2009

27th - 29th April 2009


Achieve operational and strategic excellence

Articles

http://www.eptq.com/

Search by topic : Revamps & Turnarounds

Title Author Edition
Maximisingy gas plant capacit

Tony Barletta and Scott Fulton Process Consulting Services Inc

2004 / Q2

Water entrapment and foaming must be avoided to maximise LPG recovery and minimise downstream unit contaminants. Fundamental process and equipment design principles that cause water entrapment and foaming are reviewed

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Fluidised catalytic cracker hydrotreater revamp

Raj Patel Haldor Topsoe Inc
Howard Moore Harrell Duff Brian Hamari Marathon Ashland Petroleum LLC

2004 / Q2

Primary revamp of reactors, exchangers and other FCC pretreater components provided return on investment for a complex refining facility. Improved FCC yields, even from heavier feedstocks, increased the facility’s ULS fuels capacity


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Catalyst addition in ebullated-bed units

Scott Sayles and Jim Bailor KBC Advanced Technologies Inc

2005 / Q2

A simple theoretical approach is available for calculating the catalyst metals content, catalyst physical properties and the effect on catalyst activity. Different catalyst addition rates are reviewed and compared



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Turnaround preparation Don Turner Jacobs Field Services

 

2005 / Q2

Several work processes have been developed for maintenance turnarounds. Incorporating these processes into a master cost-control and scheduling system ensures materials availability as well as correct staffing levels and timely execution




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ULSD production: improved feed stream quality

Daryl Hanson and Steve White, Process Consulting Services Inc

2003 / Q2

Much of hydrotreater revamp investment costs in future will be in dealing with the most difficult-to-remove sulphur species, because of their low reaction rates.  But upstream fractionation improvements could bring significant cost benefits.
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Maximising profitability with FCC revamps

Mark W Schnaith and Larry A Lacijan, UOP

2003 / Q2

Three case studies of the way increased capacity and product flexibility were achieved in the face of equipment limitations and operating constraints.  Optimising feed injectors and riser disengagers was among the strategies employed.
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Hydrogen optimisation at minimal investment

Nick Hallale and Ian Moore, AspenTech Ltd
Dennis Vauk, Air Liquide

2003 / Q2

Refiners making long-term investments to meet clean fuel specifications could at the same time, with already-available technology, improve their existing hydrogen resources to boost profitability in the short term.  The authors review the options.
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C2 splitter retrofit and performance

Sabah Kurukchi and Joseph Gondolfe, Stone and Webster
Antonio Joao Dias Prestes and Sergio Peter, Companhia Petroquimica do Sul (Copesul)
Peter McGuire, UOP

2003 / Q2

High capacity valve trays have been replaced during a tower revamp with a different tray design, providing greater capacity plus ethylene product.  The trays operate at higher turndown in reflux and feed rates and still produce on-spec products.
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