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| 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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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. More
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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.
More
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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. More
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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. More
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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. More
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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 More
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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. More
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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. More
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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. More
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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. More
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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. More
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