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