Browse Editions : 2011 / Q2
Title Author Edition
Optimising safety relief and flare systems

 Alban Sirven, Julien Grosclaude and Guillaume Fenol, Technip France

Jeremy Saada, Invensys Operations Management

2011 / Q2

Understanding the behaviour of refinery units by dynamic modelling of emergencies enables the prediction of realistic relief loads

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Energy performance monitoring

Robert Chares, Herve Closon and Hugues Stefanski, Belsim

Jean-Claude Noisier, SIR

2011 / Q2

A integrated energy management system supports improvements to a refinery's performance in energy consumption and emissions control

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SO2 emission control for resid combustion

 Rick Birnbaum, Cansolv Technologies

2011 / Q2

Regenerable and non-regenerable SO2 scrubbing systems for high-sulphur residuum combustion are compared.

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Bulk separation of gas-liquid mixtures

Giuseppe Mosca, Pierre Schaeffer and Bart Griepsma, Sulzer Chemtech

Harry Kooijman, Shell Global Solutions International

2011 / Q2

Effective gas-liquid separation is increasingly important to produce high-quality products from feedstocks of decreasing quality.

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Diverting low-sulphur heavy stocks for fuel oil production

 Rajeev Kumar, Chithra V, Peddy V C Rao and N V Choudary, Bharat Petroleum Corporation Ltd, India

2011 / Q2

Studies enabled a refinery to divert low-value product stocks into higher-value products and preserve crude throughput levels.

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Reducing carbon footprint

Tanmay Taraphdar, Technip KT India

2011 / Q2

An integrated programme of process integration techniques lowers CO2 emissions levels in refineries through energy savings.

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A promoter for selective H2S removal: part II

 Gerald Vorberg, Ralf Notz and Torsten Katz, BASF SE

Wieland Wache and Claus Schunk, Bayernoil Raffineriegesellschaft

2011 / Q2

Refinery trials of an MDEA promoter demonstrate low H2S lean loadings and the option for enhanced process stability during high-sulphur operation.

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Main fracionator revamp

John Payne and Dan Darby, Foster Wheeler

2011 / Q2

Space restrictions on site called for an innovative solution to replace a refinery's main fractionator mid-section

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Small-scale gas to liquids

 Andrew Holwell, Oxford Catalysts Group

2011 / Q2

Microchannel reactor technology is on trial for the small-scale production of liquids from stranded gas.

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Simulation of a visbreaking unit

S Reza Seif Mohaddecy, Sepehr Sadighi, Omid Ghabuli and Mahdi Rashidzadeh, Research Institute of Petroleum Industry

2011 / Q2

Simulation of a commercial visbreaking unit supports optimisation of the unit's performance

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Modelling for ULSD optimisation

Klas Dahlgren, Apex Optimisation/Dynaproc 

An Rigden, Chevron

Henrik Terndrup, Apex Optimisation

2011 / Q2

On-line coordination and optimisation of refinery process units led to a 10% increase in middle distillate production.

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