Global Refining Summit 2009

27th - 29th April 2009


Achieve operational and strategic excellence

Articles

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Search by topic : Revamps & Shutdowns

Title Author Edition
Revamping a crude converstion unit to VSS riser technology.

Jorgen Pedersen, Statoil Mongstad

1999 / Q3

An account of the problems encountered - and lessons learned - during a major upgrade of a reduced crude conversion unit, and the efforts of an alliance of specialists that finally brought about a successful revamp.
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Improviing profitability of an FCC

Richard J Higgins, Hans A Dirkse, Ron A van Wijk, Shell International Oil Products BV

1999 / Q3

A review of the hardware modifications that can be applied to FCC units to increase their profitability.  The authors also go through the planning and decision-making process for what to apply at a scheduled turnaround.
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Keeping down the cost of revamp investment.

Gary R Martin, Process Consulting Services Inc
Bryon E Cheatham, Fina Oil & Chemical

1999 / Q3

A comparison of the standard versus practical approach to the revamping of a crude unit.  In this article the focus is on optimising the use of existing equipment, changing the process flow scheme to minimise flash zone pressure and thereby maximising the yield.
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Opportunities for optimising utilities in major refineries.

Ian Dewar, MDC Technology

1999 / Q3

The author deals with the nature of optimisation problems, along with an explanation of applications, such as performance monitoring and equipment selection, which are used to come up with a solution.
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Achieving an accident-free turnaround.

Jim Cripps, AMEC Process and Energy Ltd.

1999 / Q3

The emphasis in the planning of a plant overhaul was that everybody should feel personally responsible for safety on the project: the result has been more than a million manhours without one serious accident.
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Converting VGO HDS units to moderate pressure hydrocracking

David A Pappal, Mobil Technology Co
Michael G Hunter, M W Kellogg Technology Co
Lucas R Groeneveld, Akzo Nobel Chemicals BV

1997 / Q3

An introduction to the technology of MAK Moderate Pressure Hydrocracking (MPHC), together with details of a successful revamp at the Chiba refinery of Kyokuto Petroleum Industries, Japan.
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Revamp process design - optimum crude unit product yields

Scott W Golden, Process Consulting Services Inc

1997 / Q3

Designing a new crude unit is an unconstrained process, limited only by capital investment targets, while revamping an existing unit to optimise product yields is constrained by the existing equipment performance and design.
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Cost effective upgrading of middle distillates

Lee Granniss and Art Suchanek, Criterion Catalyst Co LP

1997 / Q3

SynShift, a process for upgrading poor quality cracked distillate feedstocks, is shown in this article to achieve cost effective deep heteroatom reduction, aromatics removal and cetane/'API gain with substantial liquid yield.
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An alkylation unit refrigeration expansion

Anne Z Jezak, STRATCO Inc

1997 / Q3

Revamp case studies have been made for a North American refinery using Freon-12 to cool the reaction zone of its sulphuric acid alkylation unit.  Supply of Freon-12 is running out now that manufacture of the CFC-based chemical has been banned, and the refinery is having to seek alternative methods.
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Oxygen enhanced Claus operation: a case study

Churl-Hee Lee, Hanwha Energy Co Ltd
Andy Moore, TPA Inc

1997 / Q3

An alternative to building an expensive new sulphur recovery complex under an expansion programme is to increase existing Claus unit capacity by using oxygen.  This article highlights the successful implementation of TPA's Oxygen Injection system at Hanwha Energy's Inchon refinery sulphur recovery unit.
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Revamping crude units to increase capacity

Kirtan Trivedi, Helmy Andrawis, Arif Habibullah, Parsons Energy & Chemicals Group Inc

1998 / Q3

Existing crude/vacuum unit capacity can be increased by revamping heat transfer, distillation columns and other equipment, applying Process Integration concepts.  The authors discuss new approaches to revamping crude columns, incorporating recent innovations in tray technologies.
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Speeding up revamps with modern technology

Richard Elliott, Kvaerner Process

1998 / Q3

Greater emphasis on safety and environmental issues is obliging process plant operators to revamp existing equipment, but new technology can now be used to facilitate the process, save time and costs, and enhance safety of the plant.
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Hydrocracker revamp for Grangemouth refinery

Marco Giannelli, BP Oil Grangemouth Refinery
Nigel Unsworth and Dave North, Foster Wheeler Energy Ltd

1998 / Q3

BP Oil's Grangemouth refinery has completed an extensive revamp of its hydrocracker and FCC, reducing production of fuel oil and upgrading to middle distillates to meet a growing market need. A case history of the project is given.

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Troubleshooting vacuum unit revamps

Scott W Golden, Process Consulting Services Inc

1998 / Q3

While Vaccum unit revamps increase gasoil yield, management is pushing the intervals between turnarounds to four or five years.  To meet the higher operating temperatures, vacuum unit process equipment must be designed for low residence time.
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Maximising asset utilisation for improved profitability

Steven F Eshelman, Michael J Humbach, Michael J Wilcox, UOP

2000 / Q3

The authors describe how the profitability of two plants have been enchanced by programmes for getting the best out of existing facilities, and without the need for heavy investment.

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Cost effective revamps to meet the environmental challenge

Nigel Unsworth and Philip Brown, Foster Wheeler Energy Ltd

2000 / Q3

Expected legislation in Asia for cleaner transportation fuels face refiners there with a challenge to stay profitable, say the authors, and they suggest the new laws can be met in a way that could still generate profitable returns.

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Gas plant revamps for higher capacity and efficiency

Daryl W Hanson and Edward L Hartman, Koch-Glitsch Inc

2000 / Q3

Revamping high pressure distillation columns has become prevalent, with increasing throughput and concerns to keep production costs down.  Two case studies of revamps are presented here: of a C3 splitter and a debutaniser.

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Fixed bed reformer revamps for gasoline improvement

Jean de Bonneville and Jean Luc Nocca, IFP

2000 / Q3

With total or partial bans on MTBE and limitations on olefins and benzene, an octane gap is created in the gasoline pool.  The authors indicate how this can be recovered at minimum cost through some ingenious revamp solutions.

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Increasing hydrocracker capacity at low cost

Gurunath G Bharne and Christine A Groenendaal, Shell Global Solutions International BV

2000 / Q3

Detailed case studies are presented, illustrating the planning and working methods that were followed in revamping the hydrocrackers at two refineries, in Germany and Canada.

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Low-cost methods to improve FCCU energy efficiency

Scott W Golden and Scott Fulton, Process Consulting Services

2000 / Q3

The first step to finding low-cost ways of improving FCC unit efficiency under new enironmental regulations is to determine the true limits of the existing process equipment and flow scheme, say the authors.  They describe ways of influencing heat source temperatures and modifying the flow.   

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The importance of grasping new technology

 Andrew W Sloley, The Distillation Group Inc

2000 / Q3

Part of pushing plant productivity is successful use of technology, says the author, and achieving revamp objectives means moving outside the experieince base - making good use of technology separates the survivors from the failures.

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Maximising performance with new internals

Richard R Rall, Koch-Glitsch Inc

Bernard DeMulder, TotalFinaElf

2001 / Q3

In ther past few years a structured packing alternative to conventional tray design has been developed which, among other effects, maximises stripping performance.  Initial results from the technology's first commercial installation are presented here.

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Vacuum pressure control: impact on profitability

Gary R Martin and Jason M Nigg, Process Consulting Services Inc

2001 / Q3

Optimisation of flash zone pressure and temperature can improve feedstock quality to downstream units.  This article discusses control of column flash zone pressure through the first stage ejector pressure control system.

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Cost efficient rervamps in hydrogen plants

James D Fleshman, Foster Wheeler, USA

2001 / Q3

In the quest for acquiring more hydrogen at lower cost, revamping of existing equipment is often seen as the cheapest and most cost effective solution, but this calls for a thorough knowledge of the plant, its capabilities and its limitations.

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Recovery system to increase ethylene plant capacity

Robert V McDonald and Colin P Bowen, Stone & Webster

2001 / Q3

An examination of the issues facing European producers and the way they are being resolved, particularly with the options available for steam cracker revamps.  Two case studies are presented.

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Organising the plan for turnarounds

Rod Oliver, Meridium Inc

2001 / Q3

In the preparations for any turnaround, a work process must be a part of the company's overall business plan, says the author, so that it takes into account the changing business environment as well as developments in the plan itself.

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Vacuum unit design effect on operating variables.

Gary R Martin, Process Consulting Services Inc

2002 / Q3

To revamp vacuum units, process modelling and equipment design know-how are needed, and the understanding of connected equipment performance can lead to higher gasoil quality and yields, with fewer unscheduled shutdowns.

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Crude unit integrated energy analysis

 Rakesh Mehta, Onward Technologies Ltd

2002 / Q3

Opportunities for process debottlenecking and improving energy efficiency can be identified with the use of pinch analysis.  This article documents a refinery revamp where this method produced a large increase in crude distillation capacity.

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Answering the big turnaround question

James Thompson, Lyondell Chemical Company

Chalres Etter, Equistar Chemicals

2002 / Q3

An account of a risk based model for quantifying the probability and cost of an unplanned outage.  The result is that a defined risk based analysis of turnaround costs and timing is a useful tool for both plant and business management.

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