Article Title,Year,Volume,Issue,Page Range,Author
The Extent of Regulatory Consensus on Health and Safety Expenditure Part 1: Development of the J-Value Technique and Evaluation of Regulators' Recommendations,2006,84,5 B,329-336,Thomas
The Extent of Regulatory Consensus on Health and Safety Expenditure Part 2: Applying the J-Value Technique to Case Studies Across Industries,2006,84,5 B,337-343,Thomas
Analytical modelling of hydrocarbon pool fires: Conservative evaluation of flame temperature and thermal power,2012,90,2,121-128,Palazzi
Challenges and needs for process safety in the new millennium,2012,90,2,91-100,Mannan
Comparative consequence analysis of the BLEVE phenomena in the context on Land Use Planning; Case study: The Feyzin accident,2011,89,1,1-7,Török
SHIPP methodology: Predictive accident modeling approach. Part I: Methodology and model description,2011,89,3,151-164,Khan
SHIPP methodology: Predictive accident modeling approach. Part II. Validation with case study,2011,89,2,75-88,Khan
The safety of the future hydrogen economy,2011,89,6,452-462,Royle
Modelling complex pipeline network leak detection systems,2007,85,6,579-598,Abhulimen
The Expertise and the Practice of Loss Prevention in the Indian Process Industry: Some Pointers for the Third World,2005,83,5,413-420,Abbasi
Impact of Human Behaviour on Process Safety Management in Developing Countries,2004,82,6,431-437,Abu-Khader
Comparison of methods for assessing environmental health and safety (EHS) hazards in early phases of chemical process design,2008,86,2,77-93,Hungerbühler
A New Safety Risk Index for Use in Petrochemical Planning,2007,85,6,533-540,Al-Sharrah
Theoretical and Experimental Methods for the Evaluation of Reactive Chemical Hazards,2002,80,3,141-149,Aldeeb
A comparison between end-vented and side-vented gas explosions in large l/d vessels,1997,75,1,9-13,Alexiou
Reduction of Dust Explosion Hazard by Fuel Substitution in Power Plants,2003,81,6,457-462,Amyotte
Application of a Loss Causation Model to the Westray Mine Explosion,2002,80,1,55-59,Amyotte
Application of inherent safety principles to dust explosion prevention and mitigation,2009,87,1,35-39,Khan
Behavioural Safety and Major Accident Hazards: Magic Bullet or Shot in the Dark?,2005,83,2,109-116,Anderson
Quantitative evaluation of precautions on chemical tanker operations,2009,87,2,113-120,Arslan
Venting of Low Pressure Hydrogen Gas: A Critique of the Literature,2007,85,4,289-304,Astbury
A review of the properties and hazards of some alternative fuels,2008,86,6,397-414,Astbury
Buncefield: A violent episodic vapour cloud explosion,2011,89,6,360-370,Atkinson
Blast damage to storage tanks and steel clad buildings,2011,89,6,382-390,Atkinson
Can We Predict Occupational Accident Frequency?,2006,84,3,208-221,Attwood
Indicators of Sustainable Development for Industry: A General Framework,2000,78,4,243-261,Azapagic
Accidents Causes of Accidents and Learning from SEVESO II Implementation,2005,83,5,437-442,Babinec
A phenomenological model for predicting the thermal loading to a cylindrical vessel impacted by high pressure natural gas jet fires,1998,76,1,3-13,Baillie
Terror-Proofing Chemical Process Industries,2007,85,6,559-565,Bajpai
Oscillatory thermal instability and the Bhopal disaster,2011,89,5,317-322,Ball
Evaluation of EHS hazard and sustainability metrics during early process design stages using principal component analysis,2012,90,1,8-26,Hungerbühler
Study on Main Factors Influencing Acetylene Formation During Coal Pyrolysis in Arc Plasma,2006,84,3,222-226,Bao
Modeling the fate and transport of non-volatile organic chemicals in the agro-ecosystem: A case study of Cameron Highlands Malaysia,2009,87,2,121-134,Batiha
Recent Railway Industry Accidents: Learning Points for the Process Industries,2002,80,1,25-32,Beale
Modelling accidental releases of dangerous gases into the lower troposphere from mobile sources,2008,86,3,198-207,Bernatik
A Janus Approach to Safety,2002,80,1,9-15,Bond
Professional ethics and corporate social responsibility,2009,87,3,184-190,Bond
Experimental Analysis of Hydrodynamics in a Jar-test,2005,83,1,22-30,Bouyer
Hydrocarbon aerosol explosion hazards: a review,1999,77,1,22-30,Bowen
Criteria for autoignition of combustible fluids in insulation materials,1999,77,2,61-68,Zhang
Risk Management One Man's Risk is Another Man's Industry (editorial),2003,81,1,1,Brown
The case for safety,1999,77,3,107-108,Brown
Never Ever? What's the Measure?,2001,79,4,195,Brown
Risk Analysis on a Fuel Cell in Electric Vehicle Using the MADS/MOSAR Methodology,2007,85,3,241-250,Bultel
Novel Cloud Chamber Design for 'Transition Range' Aerosol Combustion Studies,2001,79,4,197-205,Bowen
Experimental analysis of gas explosions at non-atmospheric initial conditions in cylindrical vessel,2010,88,5,341-349,Cammarota
Appropriate Risk Assessment Methods for Major Accident Establishments,2003,81,1,12-18,Carter
Route risk evaluation on class-2 hazmat transportation,2011,89,4,248-260,Chakrabarti
A risk-based approach to design warning system for processing facilities,2011,89,5,310-316,Khan
An experimental study of worst case scenarios of nitric acid decomposition in a toluene nitration process,1998,76,3,211-216,Chen
Pilot-Scale Study of Multi-Phase Venting from a Vessel at Elevated Pressure and Temperature,2000,78,6,434-444,Lee
Several important issues related to the crossing-point temperature (cpt) method for measuring self-ignition kinetics of combustible solids,1998,76,2,90-93,Chen
Improved Coward explosive triangle for determining explosibility of mixture gas,2011,89,2,89-94,Yang
Research on 3D dynamic visualization simulation system of toxic gas diffusion based on virtual reality technology,2009,87,3,175-183,Chen
An Experimental Study of Vented Explosions in a 3:1 Aspect Ratio Cylindrical Vessel,2000,78,6,425-433,Chow
Calculation and Consideration of the Lewis Number for Explosion Studies,2002,80,3,135-140,Clarke
Is Environmental Protection in Danger of Banning Useful Chemicals Too Soon?,2000,78,5,337-338,Clayton
A model to predict the characteristics of fires following the rupture of natural gas transmission pipelines,2001,79,1,3-12,Cumber
Cup and Grip Seal Failures on Low Pressure Gasholders: Part 2. Gas Dispersion,2004,82,4,274-282,Cleaver
Cup and Grip Seal Failures on Low Pressure Gasholders: Part 1. The Release Rate,2004,82,4,269-273,Cleaver
Probability Bow-Ties: A Transparent Risk Management Tool,2005,83,4,307-316,Cockshott
Factors affecting vapour production in large scale evaporating liquid cascades,2011,89,6,371-381,Atkinson
Electrokinetic Behaviour of Chlorinated Phenols in Soil and their Electrochemical Degradation,2005,83,2,178-183,Cong
Exploring the Role and Content of the Safety Case,2004,82,4,283-290,Conlin
Assessing Longford Gas Plant 1 Staffing Arrangements,2006,84,1,10-20,Conlin
The major accident risk (MAR) process - developing the profile of major accident risk for a large multi national oil company,2009,87,1,59-63,Considine
Assessment of the thermal and toxic effects of chemical and pesticide pool fires based on experimental data obtained using the tewarson apparatus,1999,77,3,154-164,Costa
Behavioural Safety and Accident Prevention: Short-Term 'Fad' or Sustainable 'Fix'?,2006,84,3,164-170,Jones
The change in safety management for offshore oil and gas production systems,1999,77,3,143-148,Crawley
Optimizing the Life Cycle Safety Health and Environment Impact of New Projects,2004,82,6,438-445,Crawley
Concept risk assessment of offshore hydrocarbon production installations,1997,75,3,157-163,Crawley
Oil and gas pipeline failure modelling,2003,81,1,3-11,Crawley
Modelling spills of water-reactive chemicals,2011,89,6,415-423,Cruse
Lumped kinetics for supercritical water oxidation of oily sludge,2011,89,3,198-203,Cui
The integration of HAZOP expert system and piping and instrumentation diagrams,2010,88,5,327-334,Cui
Human Factors Integration for a New Top Tier COMAH Site: Optimizing Safety and Meeting Legislative Requirements,2005,83,2,101-108,Anderson
Predicting Outflow from High Pressure Vessels,2001,79,1,13-22,Cumber
Reducing Human Error by Improvement of Design and Organization,2006,84,3,191-199,Dalijono
Development and Verification of a New Approach for Operator Action Analysis,2005,83,4,331-337,Dalijono
Is Operating Cost a Direct Measure of Inherent Safety?,2003,81,6,414-417,Dalzell
Nothing is safety critical,1997,75,3,152-156,Dalzell
Preliminary risk assessment of ecotoxic substances accidental releases in major risk installations through fuzzy logic,2008,86,2,103-111,Darbra
Determination of Minimum Inerting Concentrations for Combustible Dusts in a Laboratory-Scale Chamber,2002,80,6,287-297,Dastidar
Using Calculated Adiabatic Flame Temperatures to Determine Dust Explosion Inerting Requirements,2004,82,2,142-155,Amyotte
Analysis of an LPG Accidental Release,2004,82,2,128-131,Demichela
Explosions Near the Surface of Organic Liquids,2005,83,5,452-458,Dengel
Propagation of laminar flames in wet premixed natural gas-air mixtures,1998,76,2,81-89,Dlugogorski
Runaway hazard assessment of cumene hydroperoxide from the cumene oxidation process,1997,75,2,73-80,Lee
Thermal decomposition kinetics of cumene hydroperoxide,1998,76,4,271-276,Kao
Conducting HAZOPs in continuous chemical processes: Part II. A new model for estimating HAZOP time and a standardized approach for examining nodes,2011,89,4,224-233,Arnaldos
Conducting HAZOPs in continuous chemical processes: Part I. Criteria tools and guidelines for selecting nodes,2011,89,4,214-223,Arnaldos
Are we too Risk-Averse for Inherent Safety?: An Examination of Current Status and Barriers to Adoption,2005,83,2,90-100,Edwards
Ignition characteristics conditions of criticality and disappearance of criticality of cumene hydroperoxide reaction by modeling approach,2009,87,5,293-299,El-Sayed
Organic dust ignition in the high temperature flow behind a shock wave,1997,75,1,14-18,El-Sayed
Process Intensification: Safety Pros and Cons,2005,83,2,85-89,Etchells
Implosion of a Large Crystallizer Vessel,2006,84,1,21-26,Ettouney
Explosion of ammonium nitrate solutions two case studies,2012,90,1,1-7,Ettouney
Who Learns When Workers are Trained? A Case of Safety Training of Maintenance Contractors' Workers For A Major Petrochemical Plant Shutdown,2003,81,1,44-51,Aini
Value at Risk Perspective on Layers of Protection Analysis,2007,85,1,81-87,Mannan
Can the Energy Market Protect the Environment?,2000,78,4,328-331,Fells
Handling data uncertainties in event tree analysis,2009,87,5,283-292,Sadiq
Methodology for computer aided fuzzy fault tree analysis,2009,87,4,217-226,Amyotte
Water Reactive Materials: Incorporation into Safety and Environmental Risk Assessments,2007,85,2,162-168,Fernie
Consequence analysis by means of characteristic curves to determine the damage to humans from bursting spherical vessels,2008,86,2,121-129,Gimeno
Consequence analysis by means of characteristic curves to determine the damage to buildings from bursting spherical vessels,2008,86,3,175-181,Gimeno
Safety Performance Improvement Through Culture Change,2005,83,4,324-330,Fitzgerald
Can Technology Eliminate Human Error?,2006,84,3,171-173,Foord
A Simplified Method for the Estimation of Individual Risk,2006,84,2,101-108,Franks
Design of Intelligent Fault Diagnostic System (FDS),2007,85,6,566-578,Gabbar
Dispersion of the vapour cloud in the Buncefield Incident,2011,89,6,391-403,Atkinson
Flammability of hydrocarbon and carbon dioxide mixtures,2011,89,6,472-481,Gant
Development of a Fuzzy Logic-Based Inherent Safety Index,2003,81,6,444-456,Rogers
Process safety-a subject for scientific research,1999,77,3,149-153,Gibson
Increasing Human Reliability in the Chemical Process Industry Using Human Factors Techniques,2006,84,3,200-207,Löwe
Measurement of charge transfer during filling and emptying FIBC,2009,87,1,64-69,Glor
An international comparison of four quantitative risk assessment approaches--A benchmark study based on a fictitious LPG plant,2012,90,2,101-107,Gooijer
Calorimetric studies on the thermal stability of methyl ethyl ketone peroxide (MEKP) formulations,2011,89,6,424-433,Graham
Process industry accidents in Sri Lanka: Analysis and basic lessons learnt,2008,86,6,421-426,Gunasekera
Estimating the Environmental Impact of Catastrophic Chemical Releases to the Atmosphere: An Index Method for Ranking Alternative Chemical Process Routes,2003,81,6,463-474,Edwards
Bhopal: … Eighteen going on Nineteen and Fading?,2003,81,4,227-228,Gupta
Inherently Safer Design--Present and Future,2002,80,3,115-125,Gupta
The Real Cost of Process Safety--A Clear Case for Inherent Safety,2003,81,6,406-413,Mannan
How the Study of Accident Case Histories Can Prevent Runaway Reaction Accidents from Recurring,2002,80,1,16-24,Gustin
The Hydrogen Economy,2000,78,4,324-327,Guy
Jet Fires Involving Releases of Crude Oil Gas and Water,2007,85,3,221-229,Hankinson
Promoting inherent safety,2010,88,3,168-172,Hansson
On System Condition Auditing,2002,80,4,197-203,Harris
Occupational chemical exposure and risk estimation in process development and design,2010,88,4,225-235,Hassim
Computer-aided valuation of safety management,1998,76,4,286-290,Hauptmanns
Worst Case Dispersion Scenarios--Obstacles or Roughness?,2001,79,2,63-64,Havens
The evolution of probabilistic risk assessment in the nuclear industry,1999,77,3,117-142,Hayns
Lessons from Human Error Incidents in Process Plants,2006,84,3,174-178,Hendershot
Assessment of Conventional and Radiological Risks for the Handling of Hazardous Substances in a Research Centre,2002,80,6,298-304,Hille
Building an Executive Information System for Maintenance Efficiency in Petrochemical Plants--An Evaluation,2007,85,2,139-146,Hwang
More effective permit-to-work systems,1999,77,2,69-76,Iliffe
Potential risks at an industrial site: A wind tunnel study,2010,88,3,185-190,Janour
Taking Credit for Loss Control Measures in the Plant with the Likely Loss Fire and Explosion Index (LL-F&EI),2007,85,1,51-58,Jensen
An Analysis of the Cumulative Uncertainty Associated with a Quantitative Consequence Assessment of a Major Accident,2007,85,3,256-259,Jirsa
Can Chemical Plants be Protected Against Terrorist Attacks?,2005,83,5,459-462,Jochum
Large-scale free and impinging turbulent jet flames: numerical modelling and experiments,1997,75,3,145-151,Johnson
The equation for critical flow of gas through an orifice,2012,90,1,76,Jones
Calculating the life extension achieved by reducing nuclear accident frequency,2009,87,2,81-86,Jones
Numerical Techniques for Speeding up the Calculation of the Life Extension Brought About by Removing a Prolonged Radiation Exposure,2007,85,4,269-276,Jones
Numerical Techniques for Speeding up the Calculation of the Life Extension Brought about by Removing a Prolonged Radiation Exposure,2007,85,6,599,Jones
Modelling of BP Texas City refinery accident using dynamic risk assessment approach,2010,88,3,191-199,Khan
Risk Management: An Australasian View,2003,81,1,31-35,Keey
Sensitivity Studies of Offshore Gas Detector Networks Based on Experimental Simulations of High Pressure Gas Releases,2005,83,3,262-269,Connolly
Accident hazard index: a multi-attribute method for process industry hazard rating,1997,75,4,217-224,Abbasi
Safety Weighted Hazard Index (SWeHI): A New User-friendly Tool for Swift yet Comprehensive Hazard Identification and Safety Evaluation in Chemical Process Industrie,2001,79,2,65-80,Abbasi
Risk-Based Inspection and Maintenance (RBIM): Multi-Attribute Decision-Making with Aggregative Risk Analysis,2004,82,6,398-411,Khan
Hazard Assessment for Fires in Agrochemical Warehouses: The Role of Combustion Products,2001,79,3,145-156,Maddison
Availability of Community Level Information on Industrial Risks in the EU,2000,78,2,81-90,Kirchsteiger
How Frequent are Major Industrial Accidents in Europe?,2001,79,4,206-210,Kirchsteiger
Review of International Industrial Safety Management Frameworks,2002,80,5,235-244,Kirchsteiger
The origins and history of loss prevention,1999,77,3,109-116,Kletz
Accident Investigation--Missed Opportunities,2002,80,1,3-8,Kletz
Inherently Safer Design--Its Scope and Future,2003,81,6,401-405,Kletz
Comparison of Methods Suitable for Assessing the Hazard Potential of Chemical Processes During Early Design Phases,2001,79,3,157-166,Koller
Evaluating Thermal Explosion Hazard by Using Kinetics-Based Simulation Approach,2004,82,6,421-430,Kossoy
A comparison between superfine magnesium hydroxide powders and commercial dry powders on fire suppression effectiveness,2008,86,3,182-188,Huang
CFD simulations of ammonia dispersion using "dynamic" boundary conditions,2010,88,4,243-252,Labovský
Helping Engineers to Analyse and Influence the Human Factors in Accidents at Work,2006,84,3,179-183,Lardner
Fire Detection: A New Approach Based on a Low Cost CCD Camera in the Near Infrared,2007,85,3,193-206,Le Maoult
The successes and challenges of implementing high reliability principles: A case study of a UK oil refinery,2011,89,6,443-451,Lekka
Inherent safety index module (ISIM) to assess inherent safety level during preliminary design stage,2008,86,2,113-119,Shariff
Research on OREMS-based large-scale emergency evacuation using vehicles,2011,89,5,300-309,Zhang
Are micro reactors inherently safe? An investigation of gas phase explosion propagation limits on ethene mixtures,2012,90,2,77-82,Hieronymus
Emergency response study for chemical releases in the high-tech industry in Taiwan--A semiconductor plant example,2009,87,6,353-360,Shu
Societal risk assessment of major hazard installations using QuickRisk,2011,89,6,404-414,Lisbona
A review of hazards associated with primary lithium and lithium-ion batteries,2011,89,6,434-442,Lisbona
The Effect of Baffle Design on Longitudinal Liquid Movement in Road Tankers: An Experimental Investigation,2002,80,4,181-185,Lloyd
The Precautionary Principle: Risk Regulation and Politics,2003,81,1,36-43,Lofstedt
Self-Ignition of Combustible Bulk Materials Under Various Ambient Conditions,2005,83,2,145-150,Steinbach
Process Security Assessment: Operational Space Classification and Process Security Index,2003,81,6,418-429,Lou
An Overview of the Nature of Hydrocarbon Jet Fire Hazards in the Oil and Gas Industry and a Simplified Approach to Assessing the Hazards,2007,85,3,207-220,Hankinson
Vapour cloud explosions in a long congested region involving methane/hydrogen mixtures,2011,89,4,234-247,Johnson
Large scale high pressure jet fires involving natural gas and natural gas/hydrogen mixtures,2012,90,2,108-120,Lowesmith
The Acid-Catalyzed Phenol-Formaldehyde Reaction: Critical Runaway Conditions and Stability Criterion,2004,82,1,37-47,Lu
Investigation of the decomposition reaction and dust explosion characteristics of crystalline dicumyl peroxide,2010,88,5,356-365,Lu
Study on the stability of nitroglycerine spent acid,2009,87,2,87-93,Lu
The kinetic parameters and safe operating conditions of nitroglycerine manufacture in the CSTR of Biazzi process,2008,86,1,37-47,Lu
A study of the dynamic response of emergency shutdown valves following full bore rupture of gas pipelines,1997,75,4,201-209,Mahgerefteh
Modelling of Formation and Combustion of Accidentally Released Fuel Clouds,2005,83,2,171-177,Makhviladze
Achieving Risk Reduction Effectively,2006,84,3,184-190,Manuele
Post-accident analysis of vapour cloud explosions in fuel storage areas,1999,77,6,360-365,Salzano
"Bow-tie" model in layer of protection analysis,2011,89,4,205-213,Markowski
Modelling Aspects of Sprinkler Spray Dynamics in Fires,2004,82,2,97-104,Marshall
An anatomy of hazard systems and its application to acute process hazards,1997,75,2,65-72,Marshall
Implementation of Transaction Processing Technology in Permit-to-Work Systems,2002,80,4,204-210,Matsuoka
Use of Advanced Techniques to Model the Dispersion of Chlorine in Complex Terrain,2001,79,2,89-102,Lea
HAZID A Computer Aid for Hazard Identification: 2. Unit Model System,1999,77,6,328-334,Chung
HAZID a Computer Aid for Hazard Identification: 5. Future Development Topics and Conclusions,2000,78,2,120-142,Chung
HAZID A Computer Aid for Hazard Identification: 4. Learning Set Main Study System Output Quality and Validation Trials,2000,78,2,91-119,Chung
HAZID A Computer Aid for Hazard Identification: 3. The Fluid Model and Consequence Evaluation Systems,1999,77,6,335-353,Chung
HAZID A Computer Aid for Hazard Identification: 1. The Stophaz Package and the Hazid Code: An Overview the Issues and the Structure,1999,77,6,317-327,Chung
Pressure Relief of Liquids Containing Suspended Solids,2004,82,1,26-36,Mcintosh
The Application of Risk Control Concepts and Experience to Sustainable Development,2000,78,4,262-269,Mcquaid
Stabilization-Solidification Process: Comparison of Synthetic Sludge and Volcanogenic Massive Sulphide Tailings,2007,85,3,260-264,Mijno
Fuzzy risk assessment of oil and gas offshore wells,2011,89,5,277-294,Wang
Integrating Sustainability in Chemical Engineering Practice and Education: Concentricity and its Consequences,2000,78,4,237-242,Mitchell
Effects of Wind Flow on Self-Heating Characteristics of Coal Stockpiles,2000,78,6,445-453,Dlugogorski
Rethinking the Physics of a Large-Scale Vented Explosion and its Mitigation,2006,84,1,33-39,Molkov
Semi-quantitative risk assessment of commercial scale supply chain of hydrogen fuel and implications for industry and society,2010,88,2,97-108,Moonis
Design of explosion isolation barriers,2005,83,2,161-170,Moore
Real-time fault diagnosis using knowledge-based expert system,2008,86,1,55-71,Khan
Risk analysis and risk perception: the social limits of technological change,1997,75,3,133-137,Newby
Check Cards for Runaway (CCR): An Operative Tool for the Risk Assessment of Highly Reactive Systems Performed in Small-and Medium-sized Enterprises,2004,82,1,5-11,Nomen
Vent Sizing Criteria for Partial Volume Deflagration,2007,85,6,549-558,Salzano
A Study on Road Tunnel Fires Using Hazmat with Emphasis on Critical Ventilation Velocity,2005,83,5,443-451,Currò
From laboratory simulation to scale-up and design of spray barriers mitigating toxic gaseous releases,2009,87,1,26-34,Fabiano
Towards Improved Reaction Runaway Studies: Kinetics of the N-Oxidation of 2-Methylpyridine Using Heat-flow Calorimetry,2002,80,4,186-196,Papadaki
A Multi-Criteria and Fuzzy Logic Based Methodology for the Relative Ranking of the Fire Hazard of Chemical Substances and Installations,2005,83,2,122-134,Paralikas
An approach to risk management of city gas pipeline,2004,82,6,446-452,Park
Runaway Reaction During Production of an Azo Dye Intermediate,2002,80,1,33-39,Partington
Playing with Fire: Safety and Reaction Efficiency Research on Gas Phase Hydrocarbon Oxidation Processes: Project SAFEKINEX,2005,83,4,317-323,Griffiths
EFCE Working Party on Loss Prevention and Safety Promotion in the Process Industries,2005,83,1,18-21,Pasman
Modelling of dispersion of two-phase releases: part 2--numerical solution scheme and validation,1998,76,1,41-49,Pattison
Modelling of dispersion of two-phase releases: part 1--conservation equations and closure relationships,1998,76,1,31-40,Pattison
Electrostatic Hazards in the Process Industries,2004,82,2,132-141,Pavey
Distinction between the upper explosion limit and the lower cool flame limit in determination of flammability limit at elevated conditions,2009,87,1,47-52,Pasman
Determination of the Explosion Behaviour of Methane and Propene in Air or Oxygen at Standard and Elevated Conditions,2005,83,5,421-429,Pasman
A Review of Explosion Prevention and Protection Systems Suitable as Ultimate Layer of Protection in Chemical Process Installations,2005,83,1,1-17,Pasman
New Probit equations for the calculation of thermal effects on humans,2010,88,2,109-113,Alonso
Sustainable Communication: Implications for Industry,2000,78,4,270-278,Petts
Main differences on European regulations in the frame of the Seveso Directive,2009,87,1,53-58,Pey
Large N.G. explosion and fire involving several buried utility networks,2009,87,2,73-80,Piccinini
High Speed Measurement of the Lower Flammable Limits in a Rapidly Changing Vapour Stream,2005,83,5,430-436,Pilkington
Assessment of the Consequences of Accident Scenarios Involving Dangerous Substances,2007,85,1,23-38,Pintarič
A survey of the origin type and consequences of fire accidents in process plants and in the transportation of hazardous materials,1997,75,1,3-8,Planas-Cuchi
A Grid Based Approach for Fire and Explosion Consequence Analysis,2006,84,2,79-91,Amyotte
Rigorous Calculation of Critical Flow Conditions for Pressure Safety Devices,2007,85,4,277-288,Raimondi
Minimizing Uncertainty in Vapour Cloud Explosion Modelling,2005,83,4,298-306,Raman
Modelling of thermal radiation from external hydrocarbon pool fires,1997,75,2,81-89,Rew
Blowdown of LPG Pipelines,1996,74,4,235-244,Richardson
Major Hazards Analysis for Populations Adjacent to Chemical Storage Facilities,2004,82,5,341-351,Rigas
Thermal Radiation from Fireballs on Failure of Liquefied Petroleum Gas Storage Vessels,2000,78,3,184-192,Roberts
Design and Protection of Pressure Systems to Withstand Severe Fires,2004,82,2,89-96,Lowesmith
Fire resistance of passive fire protection coatings after long-term weathering,2010,88,1,1-19,Shirvill
Reliable Qualitative Data for Safety and Risk Management,2005,83,2,117-121,Ross
Study of the Ratio of Injuries to Deaths for Single Incidents in the Process Industries,2005,83,4,338-342,Rushton
"Total risk of death"--Towards a common and usable basis for consequence assessment,2009,87,1,21-25,Rushton
Effects of a Duct on the Venting of Explosions--Critical Review,2007,85,1,9-22,Di Benedetto
On the design of thermal breathing devices for liquid storage tanks,1999,77,6,354-359,Salatino
Study of Major Accidents Involving Chemical Reactive Substances: Analysis and Lessons Learned,2007,85,2,117-124,Nomen
Application of the HarsMeth methodology as a tool for analysing the chemical accidents reported to the MARS database,2008,86,2,95-102,Sales
Enhancing the Accuracy of Forecasting Impact of Accidents in Chemical Process Industry by the Application of Cellular Automata Technique,2006,84,5,355-370,Abbasi
Leakage in ethylene pipelines,2004,82,1,61-68,Richardson
Learning organisations for major hazards and the role of the regulator,2010,88,4,236-242,Saw
The Ignition of Low-Exothermicity Solids by Local Heating,2004,82,2,156-169,Brindley
A Hierarchical Approach for the Evaluation of Chemical Process Aspects from the Perspective of Inherent Safety,2003,81,6,430-443,Fischer
Inherent risk assessment--A new concept to evaluate risk in preliminary design stage,2009,87,6,371-376,Shariff
Challenges in building resilience engineering (RE) and adaptive capacity: A field study in a chemical plant,2012,90,2,83-90,Shirali
Should and can safety be taught?,1999,77,4,185-186,Skelton
Flixborough Revisited,2001,79,2,64,Skelton
Simulating Dust Explosions with the First Version of DESC,2005,83,2,151-160,Skjold
Advanced multi-perspective computer simulation as a tool for reliable consequence analysis,2012,90,2,129-140,Sklavounos
The Lockerbie Investigation: Understanding of the Effects of the Detonation of 'Improvised Explosive Devices' on Aircraft Pressure Cabins,1997,75,3,138-144,Smart
Fatigue in transport: problems solutions and future threats,1998,76,3,217-223,Smith
Interaction Between Water and Hot Cyclohexane in Closed Vessels,2001,79,2,81-88,Snee
Pilot-Scale Evaluation of the Inhibition of Exothermic Runaway,2005,83,2,135-144,Cusco
The New Version of ARIPAR and the Benefits Given in Assessing and Managing Major Risks in Industrialised Areas,2003,81,1,19-30,Spadoni
A statistical approach for evaluating inherent benign-ness of chemical process routes in early design stages,2008,86,3,163-174,Srinivasan
New methodologies for security risk assessment of oil and gas industry,2010,88,6,407-412,Gupta
Planning protection measures against runaway reactions using criticality classes,2009,87,2,105-112,Stoessel
Fire and explosion assessment on oil and gas floating production storage offloading (FPSO): An effective screening and comparison tool,2009,87,3,147-160,Mannan
How do different process options and evaluation settings affect economic and environmental assessments? A case study on methyl methacrylate (MMA) production processes,2009,87,6,361-370,Hungerbühler
On the Conditions Required for Explosion Mitigation by Water Sprays,2000,78,5,339-354,Thomas
Some observations on explosion development in process pipelines and implications for the selection and testing of explosion protection devices,2008,86,3,153-162,Thomas
An evaluation of new procedures for testing explosion arresters,1998,76,4,277-285,Thomas
An experimental study of flame acceleration and deflagration to detonation transition in representative process piping,2010,88,2,75-90,Thomas
Overpressure development during the combustion of a hydrogen-air mixture partial filling a confined space,2010,88,1,24-27,Thomas
An experimental investigation of the coupling between gaseous explosion pressures and a water volume in a closed vessel,2010,88,1,20-23,Thomas
Calculating the benefit to workers of averting a radiation exposure lasting longer than the working lifetime,2009,87,3,161-174,Jones
The effect of the exposure time on the value of a manSievert averted,2009,87,4,227-231,Jones
Incorporating the 2007 recommendations of the International Commission on Radiation Protection into the J-value analysis of nuclear safety systems,2009,87,4,245-253,Jones
Extending the J-value framework for safety analysis to include the environmental costs of a large accident,2010,88,5,297-317,Jones
The limits to risk aversion: Part 2: The permission point and worked examples,2010,88,6,396-406,Jones
The limits to risk aversion: Part 1. The point of indiscriminate decision,2010,88,6,381-395,Jones
The trade-offs embodied in J-value safety analysis,2010,88,3,147-167,Jones
The Life Extension Achieved by Eliminating a Prolonged Radiation Exposure,2006,84,5,344-354,Thomas
The Extent of Regulatory Consensus on Health and Safety Expenditure: Part 2: Applying the J-Value Technique to Case Studies Across Industries,2006,84,5,337-343,Thomas
The Extent of Regulatory Consensus on Health and Safety Expenditure: Part 1: Development of the J-Value Technique and Evaluation of Regulators' Recommendations,2006,84,5,329-336,Thomas
Analytical Techniques for Faster Calculation of the Life Extension Achieved by Eliminating a Prolonged Radiation Exposure,2007,85,3,230-240,Jones
Hazards equal trips or alarms or both,2009,87,1,3-13,Timms
Dust explosions: How should the influence of humidity be taken into account?,2009,87,1,14-20,Perrin
Loss prevention programmes of the hazardous work place review and inspection act of taiwan,2007,85,2,133-138,Shu
Emergency response plan for boiler explosion with toxic chemical releases at Nan-Kung industrial park in central Taiwan,2008,86,6,415-420,Shu
Planning an emergency response centre in southern Taiwan science park,2007,85,2,125-132,Shu
Nourishing and Poisoning a 'Safety Culture',2001,79,3,167-173,Tweeddale
Benefits of Fire Compartmentation in Chemical Warehouses,2004,82,5,331-340,Rew
An Improved γ-Analysis Method for Process Security Analysis,2006,84,2,92-100,Uygun
Flixborough: the Explosion and its Aftermath,2004,82,2,105-127,Venart
Prediction of Minimum Flash Point Behaviour for Binary Mixtures,2006,84,1,1-9,Rogers
SDG-based HAZOP analysis of operating mistakes for PVC process,2009,87,1,40-46,Zhao
Data mining for failure diagnosis of process units by learning probabilistic networks,1997,75,4,210-216,Wang
The Impact of Data Uncertainty in Determining Safety Integrity Level,2004,82,6,393-397,Wang
Analysing the Past Planning the Future for the Hazard of Management,2002,80,1,47-54,Ward
The S2S training and assessment tool for unexpected reactors: Structure and knowledge base,2008,86,1,49-54,Sales
COMAH and the Environment: Lessons Learned from Major Accidents 1999-2000,2002,80,1,40-46,Whitfield
Addressing emerging risks using carbon capture and storage as an example,2011,89,6,463-471,Paltrinieri
Hazards from carbon dioxide capture transport and storage,2011,89,6,482-491,Wardman
Sustainable Development and IChemE,2000,78,4,236,Wilkinson
Stratified propane-air explosions in a duct vented geometry: effect of concentration ignition and injection position,2007,85,2,153-161,Willacy
Studies on Principle and Prevention of Explosion in Butadiene Systems,2002,80,6,305-309,Li
Prioritization of environmental issues in offshore oil and gas operations: A hybrid approach using fuzzy inference system and fuzzy analytic hierarchy process,2011,89,1,22-34,Khan
Fire-extinguishing effectiveness of 1-bromo-333-trifluoropropene/inert gaseous mixture evaluated by cup burner method,2007,85,2,147-152,Lin
Experimental study of the interation between the water mists and pvc fire,2007,85,1,39-44,Yongfeng
Fire and explosion characteristics of 3-methyl pyridine at 270°c with high oxygen concentrations,2007,85,3,251-255,Shu
Quantitative risk analysis of toxic gas release caused poisoning--A CFD and dose-response model combined approach,2010,88,4,253-262,Zhang
Modification of Evacuation Time Computational Model for Stadium Crowd Risk Analysis,2007,85,6,541-548,Zhang
Experimental measurement and numerical analysis of binary hydrocarbon mixture flammability limits,2009,87,2,94-104,Zhao
Numerical modeling of water spray suppression of conveyor belt fires in a large-scale tunnel,2015,95,,93-101,Smith
Early fire detection for underground diesel fuel storage areas,2018,119,,69-74,Zhou
Reducing the risk of oxygen-related fires and explosions in hospitals treating Covid-19 patients,2021,ePub,ePub,ePub,Wood
A programmable logic controller based remote pipeline monitoring system,2021,149,,894-904,Aziz
A probabilistic-based model for predicting pipeline third-party hitting rate,2021,148,,333-341,Gong
Failure assessment of corrosion affected pipeline networks with limited failure data availability,2022,157,,306-319,Aryai
Reliability assessment of pitting corrosion of pipeline under spatiotemporal earthquake including spatial-dependent corrosion growth,2021,148,,166-178,Zhang
Failure probability analysis of the urban buried gas pipelines using Bayesian networks,2017,111,,678-686,Khan
Study on corrosion reliability of oil/gas pipelines based on enhanced Hamacher Operator and Bayesian Assessment,2017,111,,569-581,Peng
Accident case data-accident causation model driven safety training method: targeted safety training empowered by historical accident data in coal industry,2024,182,,1208-1226,Xueming
Intelligence-led accident prevention and its application in petrochemical enterprises,2024,184,,690-702,Wang