Global Refining Summit 2009

27th - 29th April 2009


Achieve operational and strategic excellence

Articles

http://www.eptq.com/

Search by topic : Revamps & Operations

Title Author Edition
FCC vapour line coking

Christopher F Dean, Saudi Aramco, Dhahran, Saudi Arabia
Scott W Golden, Process Consulting Services Inc, Houston, Texas, USA

2003 / Revamps

Identifying the causes, penalties and possible solutions to coking in the FCC reactor vapour line, particularly with regard to inlet nozzle coking affecting unit capacity, conversion, reliability, pressure and heat balance.
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Accurate FCC yield for unit optimisation and revamp

Robert Campagna and Dennis Kowalczyk, Refining Process Services, Cheswick Pennsylvania, USA
Jeffrey Sexton, Marathon Ashland Petroleum LLC, Findlay, Ohio, USA

2003 / Revamps

Measurement of yields and defining key process parameters from reaction mix sampling can be used to tune process models, update LP vectors, audit revamp or catalyst changes and determine optimum process conditions.
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Crude column revamp using radial temperature profiles.

Glaucia Alves Da Silva Torres and Silvia Waintraub, Petrobras, Rio de Janeiro, Brazil.
Edward L Hartman, Process Consulting Services Inc, Houston, TX, USA

2003 / Revamps

Designers need to be aware of all the factors influencing packed bed performance such as feed zone mixing problems.  Accurate assessment of temperature variations above and below fractionation zones can pinpoint efficiency problems.
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Hydrotreater revamps for ULSD fuel.

R E (Ed) Palmer, Mustang Engineers and Constructors Inc, Houston, Texas, USA
Salvatore P Torrisi, Criterion Catalysts & Technologies

2003 / Revamps

Scope and capital investment for revamping an existing diesel hydrotreater to meet the 15wppm sulphur standard.  The base design is typical of hydrotreaters commissioned in the early 1990s to meet on-road specifications of 500 wppm sulphur.
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FCCU gas plant revamp boosts C3 recovery.

Keith Whitt and Charlie Herron, Shell Global Solutions, Houston, Texas, USA
Jenifer Suffridge, Shell Deer Park Refining Company, Houston, Texas, USA

2003 / Revamps

The plant of a large refinery has been revamped using high-capacity trays and other hardware revisions to significantly increase the recovery of C3s and to reduce the C4s content of the FCCU gasoline.
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Vacuum unit troubleshooting.

Norman P Lieberman, Process Improvement Engineering, Metairie, Louisiana, USA.
Daryl W Hanson, Process Consulting Services Inc, Houston, Texas, USA

2003 / Revamps

Case studies show how accurate field-measured differential pressure can be interpreted incorrectly when troubleshooting refinery vacuum columns.
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Turnarounds and process control.

Lyman Gilbert, Lyman Gilbert Consulting Inc, Alta Loma, California, USA
Guy Weismantel, Weismantel International, Kingwood, Texas, USA

2003 / Revamps

Smart sensors with self-diagnostic capabilities, advances in closed-loop process controllers, and instruments that monitor online conditions and anticipate problems can be integrated into a plant's monitoring and control netowrk during a turnaround.
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Managing vanadium from high metals crude oils.

Scott W Golden, Process Consulting Services Inc, Houston, Texas, USA

2003 / Revamps

Improvements in process and equipment design with regard to crude unit and delayed coker distillation column performance can reduce metals content.  Vacuum units with a stirpping section and upgraded coker main fractionator wash zones should be considered.
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Better feed entry ups debutaniser capacity.

Henry Z Kister, Fluor, Alison Viejo, CA, USA
David E Grich and Ryan Yeley, BP America Inc, Texas City, USA

2003 / Revamps

Points of transition, where streams enter or leave the tower, are some of the most common and sever tower bottlenecks. Combining hydraulic evaluation with field data and gamma scan analysis is key to identifying and eliminating such bottlenecks.
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Catalyst circulation in a pressure-balanced FCCU

David Spires, Farmland Industries Inc, Coffeyville, Kansas, USA
David Hunt, Davison Catalysts, Houston, Texas, USA

2003 / Revamps

Significant improvements have been made in FCC reactor temperature control at Farmland's Coffeyville refinery.  Data interpretation is presented along with points to consider when troubleshooting a pressure-balanced FCCU operation.
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Crude unit start-ups: the results of a high liquid level.

N M "Tinus" Erasmus, Sasol, South Africa
Tony Barletta, Process Consulting Services Inc, Houston, Texas, USA

2003 / Revamps

Pressure-measurement techniques can avoid the dangers of rapidly changing flow rates and levels during start-up.  Also, column internals directly above and below flash zones need to be designed for higher uplift forces.
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FCC gas plant stripper capacity

Dave Langdon, Total Lindsey Oil Refinery (LOR) Ltd
Tony Barletta and Scott Fulton, Process Consulting Services Inc

2004 / Revamps

Deethaniser operating difficulties can be caused by water phase formation, water entrapment, foaming and other factors.  "Short-term" capacity improvements implemented at one refinery were able to eliminate these difficulties.
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Revamping automation systems

Terry Gebert, Ronnie Villarreal and Frank R Whitsura, Honeywell

2004 / Revamps

To achieve a safe and profitable upgrade, the many factors affecting revamp project scope must be taken into account.  The authors focus on the automation components that maximise performance of process equipment.
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Process Equipment specification and selection

Christopher F Dean, Saudi Aramco
Scott W Golden and Richard E Pulley, Process Consulting Services

2004 / Revamps

Process design as well as equipment specifications and selection can cause unintended problems following unit revamps.  Identification of the true constraints may result in significant capital savings.
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Conditions influencing coke formation

Tony Barletta, Process Consulting Services Inc

2004 / Revamps

Hotspots in fired heaters can lead to accelerated rates of coking and tube failure.  Two examples show how integrating fireside and oil-side calculations can help identify and correct conditions leading to high localised peak flux rates.
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Steam reboiler system operations

Ken Weston, CITGO Petroleum Corporation
Steve White, Process Consulting Services Inc

2004 / Revamps

Basic heat exchange principles are used to explain gas plant thermosiphon reboiler hydraulic constraints.  Field measurements help clarify "off-design" operations that were not apparent and were causing high condensate levels.
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Producing sulphur-free diesel

Gordon Low Haldor Topsoe Inc
Jamie Townsend and Tim Shooter BP

2004 / Revamps

A systematic approach to revamping a low-pressure HDT. 10 ppm diesel production at the BP Coryton refinery was possible without the expense of building a new high-pressure unit.
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Vacuum ejector performance break

Norm Lieberman, Process Improvement Engineering
Edward Hartman and Daryl Hanson, Process Consulting Services Inc

2004 / Revamps

Understanding vacuum ejector performance is the key to maintaining reliability and distillate yields.  A low VGO yield may result from a breaking ejector system, but bypassing a fouled inter-condenser can restore lost yield.
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Targeting overhead exchanger failures

Richard Mathers, Nalco Energy Services LP

2004 / Revamps

A complete risk assessment of severe crude unit overhead corrosion reduced corrosion-related failures.  Costly equipment upgrades were avoided and significant savings generated without any increase in operating expenditure.
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Diesel and VGO recovery

Tony Barletta, Process Consulting Services Inc

2005 / Revamps

Fundamental design considerations influencing diesel and vacuum gas oil (VGO) recovery when revamping existing or designing grassroots crude units.  By increasing vacuum column diesel recovery, crude throughputs via major conversion units may also be increased.

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Corrosion monitoring improvements

Richard E Mathers, Nalco Ltd

2005 / Revamps

Case study examines prediction, monitoring and mitigation of corrosion-related effects at a West European refinery operating in a high temperature, naphthenic acid environment, and shows how metal loss was prevented when processing heavy acidic crudes.
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Crude unit preflash drums and columns

Scott W Golden, Process Consulting Services Inc

2005 / Revamps

Preflash drums and preflash columns have a significant effect on crude charge hydraulics.  The reasons for using preflash equipment are discussed, including general design considerations and problems that are created if they are designed incorrectly.
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The role of maintenance in start-ups

Brian Pritchard, Shell Canada Ltd

2005 / Revamps

A multi-billion dollar heavy oil upgrader project emphasised the importance of maintenance management considerations during project development.  The author reviews the critical role that maintenance played in this successful start-up.  Key phase considerations are outlined.
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Maximise VGO yield

Greg Cantley, Kevin Basham and Steve Barnett, Marathon Petroleum Company LLC
Edward Hartman, Process Consulting Services Inc.

2005 / Revamps

Fundamental operating principles of vacuum ejectros are discussed, including incidents leading to sudden increases in ejector suction pressure, known as breaking.  Proper ejector component selection and design can significantly prevent breaking and increase VGO yield, while reducing resid production
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Dynamic corrosion appraisal

Russell D Kane, Dawn C Eden and David A Eden, InterCorr International Inc

2005 / Revamps

Monitoring time-varying corrosion with technology that inputs corrosion as a real-time process variable lets operators correlate corrosion excursions with operating and process parameters and helps manage chemical and other corrosion prevention treatments.
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Improving sulphur recovery

Lorenzo Micucci, Siirtec Nigi SpA

2005 / Revamps

Use of high Claus ratio technology permits operating Claus plants off-ratio, regardless of tail gas technology employed.  Sulphur recovery at 99.8% is possible regardless of flow rates and/or composition changes to sulphur recovery units.
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Maximising plant productivity

George DeBakey, AP Netowrks LLC
Bassam Samman, CMCS
Sulaiman Sultan Mohammad, Kuwait National Petroleum Company
Kirk Blanchard, Valero Energy, St Charles Refinery
Dean Edmundson, Primavera Systems Inc

2005 / Revamps

Combined project management, risk assessment and asset management tools and methodologies can achieve the optimum systems integration capable of addressing every aspect of a project.
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Reducing refinery heater revamp costs

Tony Tindall, Foster Wheeler Energy Ltd

2005 / Revamps

The current condition of thousands of fired heaters built since the second half of the 20th century requires urgent attention.  This article discusses the importance of being able to deliver a safe, cost-effective heater revamp, in the shortest possible shutdown.
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Optimising plant steam systems

Kerrigan Mendicino, Pipe Line Development Co.

2005 / Revamps

How one process facility avoided excessive boiler feed water leaks and steam venting between major turnarounds.  A shear plug system helped maintain steam system temperatures at the desired letdown rates, eliminating significant imbalances.
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