Browse Editions : 2004 / Q3
Title Author Edition
Membrane separation for clean fuels Xinjin Zhao and Gautham Krishnaiah Grace Davison
Todd Cartwright CB&I Process and Technology

 

2004 / Q3

 An illustration of how membrane separation technology can be integrated into a clean fuel strategy at low capital cost relative to hydrotreating. Effective sulphur removal from certain naphtha streams, avoiding the octane penalty, is described

 
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Fundamentals of ULSD Production Salvatore Torrisi, Jr, and P Michael Gunter Criterion Catalysts & Technologies LP

 

2004 / Q3

Determining the best course for producing ULSD depends on four factors – chemistry, composition, reaction conditions and catalysis. Guidelines are offered for effective strategies and for deciding how to optimise future ULSD operations


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The role of hydrogen in clean fuels Visnja Gembicki Cara Roeseler Chris Anderle Neriman Baykal-Agosta Terry Adamopoulos UOP LLC

 

2004 / Q3

A typical refinery configuration is used to show changes in the utilisation of hydrogen from 1990 to the present, with a look into the future. Process strategies to achieve more efficient use of hydrogen under future regulations are presented



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Pretreatment of resid FCC feedstocks Byron G Johnson ConocoPhillips Company
Brian M Moyse Haldor Topsoe Inc

 

2004 / Q3

How a refinery optimised hydrogen consumption to raise API “shift”, enhancing FCC economics. The effect of heavy feedstock reactivity on the operation of refinery units, and its impact on current and future operations, is discussed



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Chemical treatment to solve FCCU problems

Sandra Garcia-Swofford Nalco Energy Services

2004 / Q3

From fouling and catalyst carryover to high feed nickel levels and varying feed qualities, FCCU problems can be solved quickly and cost effectively, says the author, through a well-designed and properly applied chemical programme 



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A range of options for resid conversion Warren S Letzsch and John Lauritzen Stone & Webster Inc

 

2004 / Q3

Resid cracking through the FCC can be cost effective with improvements in hardware, catalyst and operational knowledge. Strategies for processing residual streams with units working in full and partial combustion modes are discussed



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Statistical process control in FCC operations

J W (Bill) Wilson Barnes & Click Inc

2004 / Q3

Statistical process control techniques can be used in analysing and monitoring FCCUs. The author gives examples of the use of XmR charts in evaluating catalyst performance data and coke yield, and reviews other possible applications



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FCC additive demonstrations: Part 1

Guido W Aru Intercat Inc

2004 / Q3

A review of the issues associated with the FCC additive testing, data collection and analysis required by the US Environmental Protection Agency’s consent degrees. There are lessons for refiners in successful testing and demonstration


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Inner workings of the FCC stripper Henrique S Cerqueira Claudia M L A Baptista José M Fusco
Petrobras Research and Development Center (CENPAS)

 

2004 / Q3

Based on large-scale pilot plant and commercial FCC data, the authors consider the influence of operational variables in catalyst stripability, including the use of sampling and radiotracer techniques


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Advantages of profit centred maintenance

Jeffrey Ray Fluor

2004 / Q3

An explanation of how profit centred maintenance can be implemented in an existing facility, and how it can virtually pay for itself using systematic failure elimination and performance-based contracting


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Producing low sulphur gasoline

Adrian Humphries Pieter Imhof Chris Kuehler Terry Reid
Akzo Nobel Catalysts LLC

2004 / Q3

A practical and economic comparison of crude quality, pre-treating, post-treating, FCC additives and sulphur credit options. Solutions to meeting future gasoline specifications could involve a combination of these options 



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Compressor vibration Analysis

A Eijk TNO TPD
Georg Samland Nicole Retz Daniel Sauter Burckhardt Compression AG

2004 / Q3

Compressor manifold vibration analysis can be done economically using a finite element substructuring technique generated from CAD models of compressor parts. Examples are given, demonstrating an accurate analysis according to API 618



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Centrifugal compressor operations

Tony Barletta and Scott W Golden Process Consulting Services Inc

2004 / Q3

The wet gas compressor is used as an example in this article reviewing compressor performance, operating conditions and basic control philosophy – an aid to understanding the interactions influencing compressor performance and control



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Choosing a neutralising amine corrosion inhibitor

Philip R Petersen Petersen Consulting
Samuel A Lordo and Gregg R McAteer Nalco Company

2004 / Q3

A review of physical and chemical properties of commonly used amine-based corrosion inhibitors. The authors highlight the relative strengths and weaknesses of amines, particularly with regard to corrosion caused by hydrochloric acid



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Further advances in light hydrocarbon fractionation

Waldo de Villiers and Jose Bravo, Shell Global Solutions (US) Inc
Peter Wilkinson, Shellglobal Solutions International
Daniel Summers, Sulzer Chemtech

2004 / Q3

Recent developments in high capacity distillation trays focus on increasing capacity in fixed tower sizes in refineries and chemical plants. C2 and C3 splitter revamp case studies illustrate the potential of improved fractionation technology

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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



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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


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