| |
| Direct olefin hydration process. |
Dominic W Ching, Equistar Chemicals. |
1999 / Q1 |
A
review of the improvement, operations and economic aspects of direct
olefin hydration, considered to be environmentally and technically a
sound commercial method for obtaining a consistently high-quality
alcohol product. More |
| |
| Reduction of LNG terminal costs |
Arif Habibullah, Parsons Energy & Chemicals Group Inc. |
1999 / Q1 |
The
LNG terminal is an important link in the liquefied natural gas
chain, accounting for 20 per cent or more of the total project
cost. It also has potential for cost reduction. The author
discusses various strategies for cutting cost and their impact on
terminal design. More |
| |
| Plant power failure and its indirect effects: a case study. |
Donald F Schneider, Status Engineering Inc |
1999 / Q1 |
A
total electrical failure at a major olefins plant was restored within
half an hour, but it spawned a succession of health, safety and
environmental problems that were to be felt for months. More |
| |
| New reforming catalyst at Russian gas facility. |
S Z Alekseev, L A Alekseeva, RAO Gasprom V M Berdnikov, Astrakhangasprom A Rouquier, A Pochitaloff, D I Garanin, Procatalyse C Pradel, IFP |
1999 / Q1 |
With
advancing automobile engine design, a major Russian gas processing
complex was faced with the need to produce unleaded, high octane
gasolines, which meant replacing existing monometallic Russian catalyst
with a new breed of catalyst. This is an account of how the
change was accomplished. More |
| |
| Petrochemical building blocks from heavy oils. |
Warren S Letzsch, Stone & Webster Engineering. |
1999 / Q3 |
An
outline of the progress made on some alternative processes for making
propylene and other petrochemical building blocks from heavier
feedstocks. More |
| |
| Catsalysts for cost effective hydrogen production. |
Leif Storgaard and Hans Christian Nielsen, Haldor Topsoe A/S |
1999 / Q3 |
Processes
now used in the new generation of hydrogen plants make a wide choice of
catalysts necessary in order to meet the requirements of particular
systems. This article describes the capabilities of some of these
catalysts. More |
| |
| Performance of specialty amines in gas processing. |
Dieter Plaumann, Erik Stewart, Randy Kuroda, The Dow Chemical Company. |
1999 / Q3 |
A
detailed description of successful gas treating applications carried
out at three plants that had widely differing processing and treating
requirements. More |
| |
| State of the art gas treating |
Mahin Rameshni, Parsons Energy and Chemicals
|
2003 / Q3 |
A
close examination of natural gas preconditioning and final conditioning
processes, including the associated chemical, physical and hybrid
solvents involved. The author also looks at the various Claus
tailgas-treating technologies
More |
| |
| Improvements to tailgas treatment process |
Jean-Pierre Ballaguet and Cécile Barrère-Tricca IFP Christian Streicher Prosernat
|
2003 / Q3 |
A
review of configurations in tailgas treating to achieve 99.9% sulphur
recovery with smaller reactors – the result of advances in gas/liquid
contactor and desalter technologies, enabling longer run lengths and
more effective catalyst performance
More |
| |
| Tackling fouling in vinyl monomer manufacture |
Deborah A Foster Allen R Syrinek J Paul Street Frederic Hisbergues Ondeo Nalco Energy Services
|
2003 / Q3 |
Conventional
and new approaches to the control of fouling in vinyl monomer processes
are discussed in this article, which describes the fouling
characteristics of three vinyl monomer processes: acrylic acid, vinyl
acetate and vinyl chloride
More |
| |
| Catalytic oxidation of nitrogen containing VOC |
Vadim O Strots Grigori A Bunimovich Yuri S Matros, Matros Technologies Inc
|
2003 / Q3 |
An
outline of the treatment of gas streams containing VOCs, focusing on
the kinetics and process design aspects needed to achieve over 98% VOC
destruction efficiency and less than 15% of nitrogen oxidation
converted to nitrogen oxides
More |
| |
| Causes and remedies in caustic tower fouling |
Marilyn W Blaschke, Baker Petrolite
|
2003 / Q3 |
A
review of diagnostic tests that are used for identifying the causes of
caustic system fouling. The author also looks at methods of monitoring
the onset of fouling and some of the ways by which the problem can be
minimised
More |
| |
| Turnaround performance optimisation |
Paul R Hayes Fluor Corporation David K Clark BP Amoco Chemical Company
|
2003 / Q4 |
Complex
problems involving capital and maintenance work at a large olefins
plant were overcome by using a system-based work concept to integrate
these activities. A case study describes how this was accomplished
More |
| |
| Creating value from stranded natural gas |
Waldemar Liebner Martin Rothaemel Jens Wagner, Lurgi Oel-Gas-Chemie GmbH
|
2003 / Q4 |
Recent
developments in methanol-to-propylene conversion are based on a simple
fixed-bed reactor system and common processing elements, providing an
economic route to dedicated propylene independent of petroleum-based
processes
More |
| |
| Microchannel technology for gas-to-liquids conversion |
Terry Mazanec Velocys Inc |
2003 / Q4 |
MPT
technology has the potential to reduce costs in a variety of natural
gas upgrading processes, including steam reforming, FT synthesis and
methanol synthesis, and in chemical processes of many types
More |
| |
| Alternative routes to paraxylene production |
Jacques Rault Christian Dupraz Françoise Montecot Axens
|
2004 / Q2 |
An
integrated refining and petrochemical approach to paraxylene
manufacture from various feedstocks, such as excess aromatics in
reformate or pyrolysis gasoline. A paraxylene production complex is
reviewed and its component units described
More |
| |
| New technology to produce ethyl acetate |
Mike Tuck and Mike Ashley Davy Process Technology
|
2004 / Q2 |
Ethanol
dehydrogenation to ethyl acetate allows a wider choice of feedstocks.
Miniature process units reproduced the conditions for a full-scale
plant with modules to investigate factors of process development and
engineering design
More |
| |
| Engineering gas-to-liquids projects – Part 1 |
Simon C Clarke Foster Wheeler Energy Ltd
|
2004 / Q3 |
An
insight into the R&D, optimisation and engineering activities
needed to take Fischer-Tropsch pilot plant data through all development
stages, from “ballpark” scoping to the more detailed levels of
engineering definition
More |
| |
| Repositioning pygas, octane and toluene |
Mark Fisler Chemical Market Associates Inc
|
2004 / Q3 |
Sulphur
regulations are exerting new pressure to retain aromatics in the
gasoline pool. As a result, new molecules may need to be sourced for
aromatics. The author discusses how current and future configurations
will be used to meet demand
More |
| |
| Asset life extension |
Laza Krstin ABB Engineering Services
|
2005 / Q3 |
A
case study showing how asset life extension helped a leading
manufacturer of ammonia and urea to assess the condition of its plants
and put in place effective asset strategies that support the
achievement of business objectives
More |
| |
| Refinery and petrochemical integration opportunities |
Patrick D Lavergne Lyondell Chemical Company Robert S Bridges Equistar Chemicals
|
2005 / Q3 |
Against
a background of tighter fuel specifications and petrochemical
expansion, various strategies exist for exchanging process streams
between ethylene plants and refineries, bringing about economic
operating benefit and capital reduction
More |
| |
| On-purpose propylene production |
Steve Zinger Chemical Market Associates Inc (CMAI)
|
2005 / Q3 |
Five
types of on-purpose propylene production are available, including
propane dehydrogenation, metathesis, olefins cracking and
interconversion, high severity FCC, and gas-to-olefins. Each one is
discussed in detail
More |
| |
| Process safety through instrumentation |
Roman Maurer Endress+Hauser Messtechnik GmbH+Co KG
|
2005 / Q3 |
Typical
safety loops with pressure transmitters, level monitoring and flow
meters illustrate the application of the international IEC 61511
standard in the petrochemical industry
More |
| |
| Olefin oligomerisation with homogeneous catalysis |
Helene Olivier-Bourbigou, Jean-Alain Chodorge, Philippe Travers, IFP |
1999 / Q4 |
Although
homogeneous catalysis is not as widely used in hydrocarbon processing
as heterogeneous catalysis there are industrial applications where the
former, in liquid phase, has many advantages, including relatively high
selectivity and product purity, low investment and mild operating
conditions. More |
| |
| Simulating coke formation in gas quenchers |
M Sadrameli, H Ebadi, J Towfighi, Tarbiat Modarres University. A Sharifi, Arak Petrochemical Complex |
1999 / Q4 |
A
major requirement in ethylene production is the ability to predect
exchanger parameters, particularly coke thickness inside exchanger
tubes. This article presents the results of a computer simulation
of a naphtha pyrolysis quench cooler, or transfer line exchanger (TLX),
at Arak Petrochemical Complex, Iran. More |
| |
| Troubleshooting against process plant downtime. |
Eike Drewes, Prognost Systems GmbH Uwe Seifert, OMV Deutschland GmbH |
2003 / Q1 |
To
clarify failure mechanisms and determine the measures necessary for
trouble free operation it is essential to combine the available
experiences of all the participants and compare them with the collected
data. More |
| |
| Dynamic simulation of a demethaniser column. |
M Sadrameli, M Sahkeri, J Towfighi, Chemical Engineering Department, Modares University. |
2003 / Q2 |
An
implicity approach-based method for calculating distillation column
dynamics has been used to model time-dependent effects of independent
disturbances with a demethaniser column. Startup and shutdown
sequences can be tested in this way. More |
| |
| Amine filtration in natural gas processing operations. |
John Hampton, Filtration Technolgoy Corporation Guy Weismantel, Weismantel International |
2003 / Q2 |
A
review of improvements in filtration and separation techniques for
reducing processing costs and avoiding corrosion problems in the
removal of H2S, CO2 and other impurities, while also producing high
quality gas. More |
| |
| Removal of chloride compounds |
Peter V Broadhurst, Synetix |
2003 / Q2 |
A
review of the use of chloride guard beds to treat liquid phase and gas
phase streams to prevent operational problems from hard-to-detect
organic chlorides, while at the same time avoiding side reactions and
high partial pressures. More |
| |
| Burning sulphur compounds, with byproduct recovery. |
Olavo C Leite, Thermica Technologies |
2003 / Q2 |
Improved
methods are required to recover elemental sulphur from a gas stream
containing H2S and thereby reduce SO2 emissions. For refining,
natural processing and coal gasification, the sulphur recovery unit is
the primary area of concern. More |
| |
| Modularised technology for GTL applications |
J Richard Hensman and Mike Ashley, Davy Process Technology |
2004 / Q1 |
A
new gas-to-liquid plant designed to convert natural gas to liquid fuel
or syncrude has shown how technical developments, such as smaller
reformers, can bring efficiency, simplicity and reduced plant size and
improve quality of product. More |
| |
| Producing fuels from Fischer-Tropsch Waxes |
Zhong Zhou, Yulong Zhang, John W Tierney, Irving Wender, University of Pittsburgh |
2004 / Q1 |
Hybrid
catalysts made by combining zeolites with platinum-promoted
tungstate-modified zirconia provide a promising way to obtain higher
catalytic activity and higher selectivity for desired fuel products. More |
| |
| Increasing value from steam cracker olefin streams |
Marco Tagliabut, Marco Ferrari, Paolo Pollesel, EniTecnologie SpA |
2004 / Q1 |
The
autors present two different strategies for increasing the value of
C4-C5 streams from steam cracking, by conversion into BTEX aromatics or
propylene: a technology based on two novel catalysts is described. More |
| |
| The vinylchloride monomer process |
Ingolf Mielke, Hoechst AG |
1996 / Q4 |
The
growing demand for polyvinylchloride (PVC) and its raw material
vinychloride monomer (VCM) means expansion of capacity in the coming
years. New plants will need to have low capital and
operating costs and be aware of environmental issues. More |
| |
| Petrochemical industry in the former Soviet Union |
Mikhail G Rudin, Raytheon Engineers and Constructors Inc. |
1996 / Q4 |
The
petrochemical industry in the Soviet Union started in the mid
1930s. Until then, production had been based on coal coke
processing and on feed of alimentary origin. This article reviews
its history and the current situation. More |
| |
| New direct route from butane to 1,4-butanediol |
Andrea Ochs, Lurgi AG |
1997 / Q1 |
A
joint development programme by BP Chemicals and Lurgi has introduced a
new technology, Geminox, for production of 1,4-butanediol (BDO) using
butane as the feedstock. It combines existing technologies of the
two companies and offers a 40 per cent economic saving over other
technologies. More |
| |
| High performance catalyst for liquid phase EB technology |
Frederick Narsolis, Guy Woodle, Gregory Gajda, UOP Dinesh Gandhi, ABB Lummus Global Inc |
1997 / Q3 |
The
EBZ-500 catalyst has raised catalyst performance, achieving not only
greater purity in the ethylbenzene produced and, consequently, in
styrene monomer, but also in extended reactor runs and favourable
investment costs. More |
| |
| Reforming exchanger system in large-scale methanol plants |
Robert V Schneider III and Girish Joshi, The M W Kellogg Co |
1997 / Q3 |
By
eliminating a tubular fired furnace, the Kellogg Reforming Exchanger
System (KRES), used in the production of methanol, is proving to be
profitable and energy efficient against conventional steam reforming. More |
| |
| Contaminant purification with selective alumina adsorbents |
Karl Lin, Alcoa Industrial Chemicals |
1997 / Q3 |
Removal
of trace contaminants in feed and intermediate streams associated with
polyethylene and polypropylene processes is essential for trouble-free
operations. This article reviews these contaminants, together
with the use of molecular sieves and aluminas in purification of
various process streams. More |
| |
| Amine unit cost element |
Mike Zacher, BP Oil Ed Wagner, Chevron Duke Tunnel, Alternate Source Bruce Kennedy, Petro-Canada Lon Stern, Shell Oil Bruce Scott, BSI |
1997 / Q3 |
Two
surveys were organised by the Amine Best Practices Group in order to
build a database to compare the operating efficiency of different amine
units. This article reports the findings of the latest survey,
which focused on the question of operating costs and some of the design
features affecting them. More |
| |
| Converting natural gas into liquid fuels |
Mark A Agee, Syntroleum Corporation |
1997 / Q3 |
A
technology has been developed for converting uneconomically remote,
sub-quality natural gas into synthetic liquid fuels, at plant capital
costs low enough for its recovery to be financially worthwhile, based
on current oil prices. More |
| |
| Ethylene revamps using Advanced Recovery System |
John Reid and Ken Bush, Stone & Webster Engineering Corporation |
1998 / Q1 |
Advanced
Recovery System technology has been widely adapted, with some 4 million
tons a year of new ethylene capacity committed to it and 6 million tons
of revamp capacity operating or being prepared. This article
examines results to date and highlights revamp projects in progress. More |
| |
| Relative economics of mixed C4 processing routes |
Stacia M Edwards, Stephen J Stanley, Margaret M Shreehan, ABB Lummus Global |
1998 / Q1 |
Ethylene
producers are seeking ways to upgrade the mixed C4 stream from ethylene
plants to improve operating economics. Various technologies have
been commercialised, including butadiene extraction, MTBE, and several
others that can be combined to produce or recover various C4 products. More |
| |
| Two-chain characteristics of bimodal polymers |
Jouni Takakarhu, Borealis Polymers Oy |
1998 / Q1 |
The
basis of Borstar polyethylene technology, which offers bimodal PE
grades for many applications requiring combined strength and
processability, is a proprietary catalyst and loop-gas phase reactor
process, described in this article. More |
| |
| Improving para-xylene production economics |
Robert A Lentz, UOP LLC Douglas S Hubbel, Raytheon Engineers & Constructors |
1998 / Q3 |
The
authors describe how an alliance of three companies has brought
together leading technologies from the para-xylene industry for the
design, revamp or reconfiguration of para-xylene production facilities
for increased profitability. More |
| |
| Human factors engineering projects: Part I |
Harrie J T Rensink and Martin E J van Uden, Shell Nederland Raffinaderij/Shell Nederland Chemie BV |
1998 / Q3 |
Integrating
a human factors engineering strategy in the early phases of
preparations for a new project has been shown to produce significant
financial and work-related benefits, not least in reduced capital
expenditure. More |
| |
| Gas phase polyethylene: process developments |
David Newton, Jean-Claude Chinh, Michael Godfrey, John Steedman, BP Chemicals. |
1998 / Q4 |
Since
its discovery in 1933 the history of polyethylene (PE) has been one of
continuous development in areas such as products, process and
catalysis. These developments continue today as new product
applications are sought in an ever-growing marketplace. More |
| |
| Integrating technologies for para-xylene production |
Christian Dupraz, IFP Industrial Division Maria D Farnos, Mobil Technology Company |
1998 / Q4 |
Some
of the new technologies associated with para-xylene production are
discussed in this article, particularly developments that have overcome
previous limitations to productive capacity. More |
| |
| Improved process integration through hydrogen recovery |
Petru Bozga, Emil Olanescu, Dinu Timpoc, SC Fibrex SA Renzo Coletti, Gaetano Iaquaniello, Francesco Vinci, Kinetics Technology Int SpA |
1998 / Q4 |
The
authors describe the upgrading of a purge gas stream from an acetylene
production unit to pure hydrogen and carbon dioxide. Both
products were routed back into the main process in the chemical
complex, achieving a better process integration and reducing the amount
of wastes generated. More |
| |
| Improving profits in olefins complexes |
John Philpot, KBC Advanced Technologies Inc
|
2005 / Q4 |
A
Hungarian ethylene producer has identified more than a $30 per ton
increase in profit. The initial phases of a profitabiltiy
programme show what can be achieved in a collaborative effort with the
right tools and methodologies.
More |
| |
| LNG technology and equipment |
Xiang Dong, Xin Jiang Guagshui Liquefied Natural Gas Develpment Co Ltd Eginhard Berger, Linde AG Albert Meffert, Tractebel Gas Engineering Li Wei Bin, Sinopec Shanghai Engineering Co Ltd
|
2005 / Q4 |
A
review of improvements to the Shan Shan LNG processing facilities,
ranging from gas treatment and liquefaction with a single mixed
refrigerant cycle in spiral-wound heat exchangers through storage to
unloading and distribution in China.
More |
| |
| Ethylene furnace scheduling |
Rob J Vasbinder and Jeff D Kelly, Honeywell Process Solutions
|
2005 / Q4 |
One
solution to the logistical constraints seen in ethylene plant furnace
scheduling is technology that automatically generates multiple
optimised schedules for schedulers to analyse and quickly select the
best one to be executed.
More |
| |
| Effects of feed compositions on acetylene hydrogenation catalyst |
K James Sasaki, Phillips Petroleum Company
|
1997 / Q4 |
The
preferred method of removing acetylene from ethylene and propylene in
olefin polymerisation catalysts is by selective hydrogenation, and
modern methods involve palladium catalysts. An experiment to
learn more about the acetylene removal process under different feed
conditions is described here.
More |
| |
| Selective hydrogenation catalysts for olefin yields |
Frank Mey, Hans-Dieter Neubauer, Rainer Schubert, KataLeuna GmbH Catalysts
|
1997 / Q4 |
Advanced
Leuna-Catalysts for selective hydrogenation of acetylene, MAPD and
C4-cuts have proved an appropriate tool for maximising olefin
yields. A new generation of ring-shaped catalysts for gas phase
selective hydrogenation of acetylene and MAPD can increase converter
capacity up to 140 per cent.
More |
| |
| Novel temperature controlled reactor technology |
Steven T Arakawa, Robert C Mulvaney, Donald E Felch, UOP
|
1997 / Q4 |
Tubular
reactors, used in many processes, have been limited in capacity and
scope by practical and economic constraints. A new technology to
overcome many of these shortcomings has been developed. This
article addresses its advantages for both endothermic and exothermic
reaction systems.
More |
| |
| Solvent recovery enhancers |
Ray Colston, Glitsch Technology Corporation
|
1997 / Q4 |
High
demand for teraphthalic acid (TPA) has raised interest in processes
that improve performance and economics for both new and existing
plants. This article focusses on one section of the TPA plant -
the solvent recovery system - and discusses a configuration applicable
to existing and grassroots plants
More |
| |
| LNG plant operator training |
Alex K C Tang and Grant Stephenson, Honeywell Hi-Spec Solutions
|
1997 / Q4 |
Advances
in computer technology have made it possible for dynamic process
simulation to be used in a wide range of applications. This
article describes the Trainer system and its use as a training
simulator for LNG plant operators.
More |
| |
| Upgrading kerosene to normal paraffins |
Anne McPhee, UOP
|
2000 / Q1 |
A global shortage of n-paraffins,
and the consequent rise in prices, presents an opportunity to refiners
and petrochemical producers to add value to their kerosene by
diversifying into normal paraffins, says the author. The
technology for doing so is illustrated by operating data.
More |
| |
| Monomer recovery in polyolefin plants |
Marc L Jacobs, Douglas E Gottschlich, Richard W Baker, Membrane Technology & Research Inc (MTR)
|
2000 / Q1 |
This
article outlines the application in polyolefin plants of a membrane
based process, VaporSep, for separating and recovering hydrocarbons
from nitrogen - in particular, the treatment of resin degassing vent
streams.
More |
| |
| For low cost chemicals and flexible power |
John Griffiths and Nathan East, Jacobs Engineering UK Ltd
Gijs van Lammeren, UOP NV
|
2000 / Q3 |
Description
of a means of using low-grade feedstock to supply both a competitively
priced synthetic chemical and low cost and reliable peaking
electricity, without the need to develop any new processes or
equipment.
More |
| |
| The gas/ethylene plant: concept and integration |
Greg E Ameringer, GECONCEPT Technology
|
2000 / Q3 |
A
process has been developed to combine the cryogenic natural gas liquid
plant, NGL fractionation plant and the ethylene plant into a single
plant, with substantial savings in energy and an improved ethylene
profit margin.
More |
| |
| Post reactor technology in phthalic anhydride plants |
Hans-Jurgen Eberle Consortium fur Elektrochemische Industrie GmbH Josef Breimair, Wacker Chemie GmbH
Helmuth Domes and Thomas Gutermuth, Lurgi Oel Gas Chemie GmbH
|
2000 / Q3 |
The
authors describe a post reactor process, downstream from the main
reactor, for eliminating detrimental byproducts from the catalytic PA
reactor.
More |
| |
| Fluidised bed propanne dehydrogenation |
Roberto Trotta and Domenico Sanfilippo, Snamprogetti SpA
|
2001 / Q1 |
The
authors foresee propane dehydrogenation playing a major part in meeting
a shortage in the supply of propylene. Fluidised bed
dehydrogenation (FDB) offers an opportunity to make propylene supply
independent of that of ethylene.
More |
| |
| Expanding the properties of polypropylene |
Anton de Vries, Montell Technology - Europe
|
2001 / Q1 |
The
author sees the future for polypropylene expanding as new materials,
some of which are described here, rejuvenate existing applications and
create new opportunities based on competition between materials and
product differentiation.
More |
| |
| Working with an extractive distillation process |
Gerd Emmrich, Helmut Gehrke, Uwe Ranke, Krupp Uhde GmbH
|
2001 / Q3 |
A
cost comparison between progressive extractive distillation of
aromatics versus a more conventional technology has shown there can be
considerable savings in operating costs during the production of high
purity benezene.
More |
| |
| Cost eeffective hydrogen from refinery offgases |
Sanjiv Ratan and Paul Wentink, Technip Benelux
|
2001 / Q3 |
Efficient
utilisation of refinery offgases can prove to be attractive for
hydrogen production by employing hybrid or integrated systems.
But attention must be given to specific operational requirements to
achieve flexibility and reliability.
More |
| |
| Metathesis: refinery and ethylene plant applications |
Ronald M Venner and Stephen I Kantorowicz, ABB Lummus Global
|
2001 / Q3 |
With
the demand for propylene now exceeding that for C4S, the authors see
the integration of the metathesis process in FCC units and steam
crackers as a low capital cost way of increasing propylene production
and reducing the C4s product.
More |
| |
| Technology for redcucing para-xylene costs |
Scott Ramsey, ExxonMobil Chemical
|
2001 / Q3 |
Recently
introduced technologies are offering para-xylene producers the option
of lowering production costs by reducing feedstock requirements and,
says the author, enabling para-xylene production increases without
hardware modifications.
More |
| |
| Catalysed revamp of older ethylbenzene plants |
Sam E Knipling, Partec Resources Inc
|
2001 / Q4 |
There
are options that operators of older plants should consider for
maintaining high yields and quality while still avoiding byproduct
generation and the capital cost of a new unit.
More |
| |
| A cost effective methanol to propylene route |
Hans-dieter Holtmann and Martin Rothaemel, Lurgi Oel Gas Chemie GmbH
|
2001 / Q4 |
A
detailed review of a proprietary technology that reduces methanol
production costs wherever low cost natural gas is available. With
rising oil prices, low cost methanol is seen as a profitable feedstock
for conventional petrochemical processes.
More |
| |
| Simulation of furnace run length |
J Towfighi, M Sadramel, A Niaei, Chemical Engineering Department, Tarbiat Modares University, Tehran
|
2001 / Q4 |
Decoking
means a loss in production capacity, so assessment of coke formation is
vital, along with the need to predict a furnace's run time. This
article describes a simulation network for the prediction of radical
reactions and firebox calculations.
More |
| |
| Improved operating margins with ethylene recovery |
T R Tomlinson, Costain Oil, Gas & Process Ltd
|
2002 / Q2 |
An
overview of ethylene recovery and processing, outlining low
temperature/cryogenic processes for recovery of ethylene from refinery
offgases and from polyethylene plants offgas streams, and the
purification of recovered ethylene.
More |
| |
| Implenting non-linear model predictive control |
Tim Wilmarth, Chevron Phillips Chemical Co Rik Wuyts, John Crosby, Randy Wagler, Honeywell Hi-Spec Solutions Jeff Renfro, John Goodman, Dot Products
|
2002 / Q2 |
An
account of the thinking that went into a project for optimising the
controls on a polyethylene production line and the benefits that
resulted, including higher plant capacity, reduced transition times and
improved product quality control.
More |
| |
| Column design using mass transfer rate simulation |
Ralph H Weiland and John C Dingman, Optimized Gas Treating Inc
|
2002 / Q2 |
This
article looks at examples of commercial columns used in CO2 removal and
selective H2S treating, comparing performance test data to demonstrate
benefits of modelling actual column internals using mass transfer rate
process simulation.
More |
| |
| Improved steam cracker furnace efficiency |
Joel Magnan, Kubota Metal Corporation Kaoru Hamada and Kenji Otsubo, Kubota Corporation
Elizabeth Sohn, Technip USA Corporation
|
2002 / Q3 |
A
description of the use of high heat transfer mixing element radiant
tubes for reducing coking rates and increasing run lengths, and for
improving thermal efficiency. Such tubes are proving to be more
beneficial than finned tubes.
More |
| |
| Improving hydrogen plant performance: Part I |
P V Broadhurst and P E J Abbott, Synetix
|
2002 / Q3 |
A
reliable and cost effective asset management strategy can increase
hydrogen plant throughout as well as optimise operating conditions and
energy efficiency. This article looks at the way current
operations may be optimised.
More |
| |
| Submerged quench incineration |
Olavo C Leite, Thermica Technologies
|
2002 / Q3 |
Severe
regulatory pressures in the processing industry require more effective
measures to destroy pollutants beyond ordinary water treatment methods.
More |
| |
| Improving hydrogen plant performance: Part II |
P V Broadhurst and P E J Abbott, Synetix
|
2002 / Q4 |
Optimisation
of operating conditions requires an in-depth study of the hydrogen
plant, say the authors. They consider the optimisation of
catalyst and absorbent to maximise hydrogen output beyond the
capabilities of operations strategies.
More |
| |
| Choosing a selectiv hydrogenation system |
Ronald G McClung and Steve Novalany, Engelhard Corporation
|
2002 / Q4 |
Data
has shown the effectiveness of palladium catalyst for the removal of
diolefins and acetylenes in steam cracking as well as catalytic
cracking operations. In the interpretation of pilot plant test
results, however, caution should be used.
More |
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| Recovering energy and acid from hydrocarbons |
Olavo C Leite, Thermica Technologies
|
2002 / Q4 |
How
fully automated thermal oxidiser units containing energy and byproduct
recovery systems are able to resolve operational concerns over organic
wastes, and can be the most economic way to dispose of chlorinated
hydrocarbon residues.
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| Advances in naphtha steam cracking |
Tony Pavone, SRI Consulting
|
2006 / Q1 |
A
review of technology developments being incorporated in
state-of-the-art naphtha steam crackers. Incremental upgrades to
improve safety, environmental performance, manufacturing excellence and
profitability to existing steam crackers are discussed.
More |
| |
| Measuring volumetric flow |
Keven Conrad, Endress & Hauser Inc Joel Clancy, CEESI Iowa High Flow Test Facility
|
2006 / Q1 |
The
extended application of Coriolis meters for measuring natural gas
minimises the uncertainties associated with volumetric flow
measurement. Installation requirements and overall cost can also
be simplified and reduced.
More |
| |
| Refinery CO2 challenges: part II |
Joris Mertens, KBC Process Technology Ltd
|
2006 / Q2 |
CO2
emissions and hydrogen production costs in hydrogen plants.
Understanding how the impact of unit configuration, operation
conditions, feed type, fuel costs and other cost factors set the cost
of hydrogen production.
More |
| |
| Applying ultra-low-NOx burners |
Simon Barendregt, Iek Risseeuw and Frank Waterreus, Technip Benelux
|
2006 / Q2 |
Application
of computational fluid dynamics in the design of a high-flux ethylene
furnace equipped with ultra-low NOx vortex burners. The
fundamental kinetics mechanisms that are important in NOx formation
under combustion are described.
More |
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