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| Computational fluid dynamics: understanding unit operations |
Derek A Colman, BP Amoco Chemicals |
1999 / Q4 |
An
account of six cases in which CFD - computational fluid dynamics - was
used not only to aid in understanding and solving existing process
problems but also to assist in the design of new process operations. More
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| Advances in a catalyst cooler technology |
Tiny Y Chan and Dalip S Soni, ABB Lummus Global Inc Zhang Fuyi, Luoyang Petrochemical Engineering Corporation/Sinopec |
1999 / Q4 |
New
concepts have been brought to a well proven catalyst cooler
technology. In this article reliability and flexibility of
operation is assessed, and commercial experience of the technology in
over 20 FCC units is discussed. More
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| Thermal conversion in power integrated refinery schemes |
Frans A M Schrijvers, Peter J W M van den Bosch, Brugt A Douwes, Shell International Oil Products BV |
1999 / Q4 |
New
and economically attractive options for an established technology like
visbreaking are opening up as a result of the growing relationship
between the industrial sectors of refining and electricity generation,
say the authors. More
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| Shell and tube heat exchanger applications |
Cecil C Gentry, Matthew C Gentry, Geoffrey E Scanlon, Phillips Petroleum Company |
1999 / Q4 |
Although
they were originally designed to deal with tube vibration and the
equipment failures that this could cause, the use of Rodbaffles has
spread to a wide range of applications in the petrochemical and other
industries. More
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| Transient analysis of a utility steam system. |
Brian D Bumgarner, Scott Ray, Surajit Dasgupta, John R Cassata, Kellogg Brown & Root |
1999 / Q4 |
Dynamic
simulation in the analysis of complex interactive systems has proved
valuable in determining what effects variations in the dynamic
characteristics of a package boiler would have on overall system
performance. More
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| Effective coke inhibition in pyrolysis furnaces |
S E Babash and T N Mukhina, VNIIOS Institute, Moscow |
1999 / Q4 |
Description
of a technology with the potential for continuous operation of ethylene
pyrolysis furnaces without periodic shutdown for coke removal. In
this article the authors present their work in two parts: 1. Conceptual
aspects of coke formation, and 2. Practical application in a Russian
ethylene plant. More
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1999 / Q4 |
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| Applying advanced process controls to fired heaters |
Lee E Turpin and William J Korchinski, Aspen Technology Inc |
1999 / Q4 |
Some
of the key issues involved in automation of heater firing are
highlighted in this article, which aims to help operators improve
firebox management. Case studies are presented, along with common
mistakes that cost money. More
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| Multiple utilities optimisation to improve process economics. |
H K Shethna, H Singh, Y Makwana, F J L Castillo, Hyprotech Ltd U V Shenoy, Indian Institute of Technology. |
1999 / Q4 |
An
outline of the methodology for computing optimal load targets as an
important factor in arriving at overall optimal cost targets when
external utilities are needed to meet a process plant's heating and
colling requirements. More
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| Combustion science: a contradiction in terms? |
Barrie Jenkins and Mike Boothman, Fuel & Combustion Technology Int. Ltd and Conoco Ltd, Humber Refinery |
1996 / Q4 |
A
coker heater at Conoco's Humber refinery in the UK was limiting
production. Some of its tubes were coking up and there were
frequent shutdowns for decoking, with loss of production. An
assessment of the causes was required. More
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| Heat exchange design to improve profits |
Tim Fox and Vishwas Wadekar, Heat Transfer and Fluid Flow Service (HTFS) |
1996 / Q4 |
Heat
exchange design calculations can have a direct impact on company
profits in today's technically demanding and margin-conscious
downstream industries. The way to increase cost-effectiveness in
thermal equipment sizing, say the authors, is a research-based approach
to method development. More
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| Heat transfer enhancement in solvent extraction plants |
Ian Gibbard and Doug Storey, Cal Gavin Process Intensification Engineering |
1996 / Q4 |
Increasingly,
designers are using heat transfer enhancement at the conceptual design
stages of a project to give themselves more flexibility, substantial
cost savings and the prospect of much longer sustainable performance. More
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| Electric heat tracing optimisation |
Mitch Todd, Dustry Brown, Gerald B Dixon, Nelson Heat Tracing Systems. |
1996 / Q4 |
Electrical
heat tracing system costs range from $50 to over $325/metre of pipe,
depending on pipe size design parameters. Heat tracing cable represents
only about one third of total system cost. Heat tracing system costs
can be minimised by prudent system design and product selection.
More
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| Practical considerations for crude unit revamps |
Tony Barletta, Process Consulting Services Inc |
1998 / Q4 |
Two
examples are used in this article to illustrate how changes in the
process flow scheme can increase preheat train heat recovery.
While each refinery's crude unit design, operation and equipment
constraints differ, a practical approach can be applied to any crude
unit revamp. More
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| Making the right choice in packaged steam generators |
V Ganapathy, ABCO Industries Inc |
1998 / Q4 |
This
article outlines some of the recent developments in design and
construction of packaged steam generators, which have the combined
advantages of lower operating costs and reduced emissions of pollutants
such as NOx and CO. More
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| Direct amine heating - a case study |
Joanne Booth, Foster Wheeler Energy Ltd |
1998 / Q4 |
Indirect
heating of amine has been the traditional method in order to minimise
the risk of overheating. Two amine waste heat reboilers, which
heat amine directly, have been supplied to Tunisia by Foster
Wheeler. They incorporate a number of features to ensure uniform
heating, based on a flow model study. More
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| Revamping vacuum heaters |
Ashutosh Garg, Furnace Improvements |
1998 / Q4 |
With
crudes becoming heavier, a number of refineries are carrying out deep
cut revamps to improve cutpoint. In most cases vacuum heaters can
be revamped to handle increased capacity, with the bonus of improved
efficiency and longer life. More
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| Design guidelines for heat transfer systems. |
LeRoy A Ashman, Petro-Canada Lubricants
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1997 / Q4 |
Proper
design of heat transfer systems should be based on the suitability of
the fluid application needs. This article describes, among other
things, the fluid selection criteria that must be established before
system design can begin.
More
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| Improving plant operations with heat transfer enhancement |
Ian Gibbard, Cal Gavin Process Intensification Engineering
|
1997 / Q4 |
Application
of enhancement techniques gives the process designer a systematic
approach to the control and reduction of fouling, with the benefits of
long onstream performance and improved economics.
More
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| Compact exchanger to reduce refinery fouling |
Doug Storey, Cal Gavin Process Intensification Engineering Rick Van der Ploeg, ABB Lummus Heat Transfer BV
|
1997 / Q4 |
Two
advanced heat transfer technologies have combined to deliver increased
onstream performance in heavy fouling service, using a reduced number
of shell and tube exchangers, in a Germany refinery.
More
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| A new shell-and-tube option for refineries |
H J van der Ploeg and B I Master, ABB Lummus Heat Transfer
|
1997 / Q4 |
The
conventional shell-and-tube is still the standard type of heat
exchanger in the petrochemical and refinery industries. New
Shell-side geometries can offer substantial improvements, and the
advantages of helical baffles are illustrated in case studies of two
successful refinery upgrading projects.
More
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| Trace-heating optimisation for cost effective operation |
Chet Sandberg and Philippe Reinders Folmer, Raychem Corporation
|
1997 / Q4 |
Electrical
trace-heating has become the favoured method for temperature range
processes, while innovations like self-regulating heating cables and
control methods such as proportional ambient sensing control provide a
new range of options for the design engineer.
More
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| Special steel design to prevent H2S related cracking |
V Schwinn and A Streisselberger, Dillinger Huttenwerke AG
|
1997 / Q4 |
Hydrogen-induced
cracking in steel vessels has become a major concern for refiners, and
in this account of a process for producing a steel resistant to attack
the need to be specific when ordering new steel plate is emphasised.
More
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| Cracking furnace design by computer application |
Dieter Kaufmann and Dieter Mihailowitsch, Linde AG
|
2000 / Q4 |
Examples
of how a technique known as Computational Fluid Dynamics (CFD) has been
employed to improve and optimise the design of the cracking
furnace. The authors describe simulation used for the radiant and
heat recovery sections.
More
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| distributed distillation with heat integration. |
John A Reid, Stone & Webster Engineering Corporation
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2000 / Q4 |
Increased
feed capacity and/or reduced energy cost are often possible in the
development or modification of a distillation sequence, using a process
with proven heat integration concepts, such as side reboiler or
pump-around loop.
More
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| Divided-wall columns - a novel distillation concept |
Frank ennenbach, Baerbel Kolbe, Uwe Ranke, Krupp Uhde
|
2000 / Q4 |
The
technology of divided-wall columns using a single distillation tower,
described in this article, is claimed to have investment and operating
advantages over conventional two-column systems for hydrocarbon
fractionation.
More
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| Improved reactor internals for HGO hydrotreaters |
F Emmett Bingham, Haldor Topsoe Inc Edwin Chan, Tony Mankowski, Peter Hubbard, Syncrude Canada Ltd
|
2000 / Q4 |
Reactor
internals of a plant's heavy gasoil hydroprocessing units, which became
inadequate for the operations they were originally designed for, have
been replaced with a system which has significantly improved all-round
performance.
More
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| Optimal cleaning strategies in heat exchanger networks |
Bruce Pretty and Alan Karp, Veritech Inc
|
2000 / Q4 |
Deciding
the best strategy for cleaning a heat exchanger network can be complex
and time-consuming. The authors describe an approach using
spreadsheet-based software tools, found to be quick and practical and
yielding significant benefits.
More
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| Compact heat exchangers: design and service |
Lars Warlin and Tobias Svensson, Alfa Laval Thermal
|
2000 / Q4 |
Heat
exchanger technology has come a long way since the plate heat exchanger
made its first appearance over 60 years ago, and the latest compact
developments, featuring ease of installation, maintenance and cleaning,
are described in detail.
More
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| Explicit equations for pipe sizing |
B B Gulyani and C P Agarwal, Department of Chemical Engineering, University of Roorkee
|
2000 / Q4 |
Fluid
turbulence, viscosity and the degree of roughness or smoothness of the
internal wall of a pipe are all factors influencing the movement of a
fluid to its ultimate destination. The authors describe a method
for estimating these effects.
More
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| An interface to make unit operations interoperable |
Bertrand Braunschweig, Didier Paen, Pascal Roux, Philippe Vacher, Institut Francais du Petrole
|
2001 / Q4 |
A
cooperative effort among a group of major companies within the industry
has resulted in a software program that allows users of simulators to
employ elements from other suppliers directly in their simulations,
without any programming.
More
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| Improved catalyst stripping from cold flow modelling |
Brian W Hedrick, Jeff P Koebel, Ismail B Cetinkaya, UOP LLC
|
2001 / Q4 |
An
account of the application of fluidisation theory and mass transfer
principles to the study of tray design, which has resulted in the
development of stripper internals capable of increasing catalyst
handling capacity by as much as 50 per cent.
More
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| An inferential model for distillation columns |
Y Zak Friedman, Petrocontrol Gwilym T Reedy, Texaco Pembroke
|
2001 / Q4 |
An
account of the setting up of a group of first principle inferential
control models for distillation at a UK refinery, what they were set up
to do and why, and how they performed in a closed loop control
environment.
More
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| Avoiding problems with compressor mechanical seals |
Roger E blanton, Tuthill Pneumatics Group
|
2001 / Q4 |
Positive
displacement, rotary lobe blowers, says the author, are a cost
effective solution to problems that can arise in gas compression
applications. He presents an in-depth review of the functions and
proper handling of this equipment.
More
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| Better furance performance with new alloy radiant coil |
Keizo Hosoya, Nobuo Shiratori, Kenji Satoh, Katsumi Yamamoto, JGC Corporation
|
2001 / Q4 |
By
reducing the amount of coke deposition, a new ethylene furnace tube is
described by the authors as being capable of extending run lengths
under existing operating conditions and doubling the interval times
between decokings.
More
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