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Explosion and fire (3 injured, potential offsite consequences) [[electronic resource] ] : First Chemical Corporation, Pascagoula, Mississippi, October 13, 2002 / / U.S. Chemical Safety and Hazard Investigation Board
Explosion and fire (3 injured, potential offsite consequences) [[electronic resource] ] : First Chemical Corporation, Pascagoula, Mississippi, October 13, 2002 / / U.S. Chemical Safety and Hazard Investigation Board
Pubbl/distr/stampa [Washington, D.C.] : , : U.S. Chemical Safety and Hazard Investigation Board, , [2003]
Descrizione fisica 77 pages : digital, PDF file
Collana Investigation report / U.S. Chemical Safety and Hazard Investigation Board
Soggetto topico Industrial accidents - Investigation - Mississippi - Pascagoula
Chemicals - Fires and fire prevention - Mississippi - Pascagoula
Chemicals - Fires and fire prevention
Industrial accidents - Investigation
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Altri titoli varianti Explosion and fire
Record Nr. UNINA-9910697413303321
[Washington, D.C.] : , : U.S. Chemical Safety and Hazard Investigation Board, , [2003]
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Pubbl/distr/stampa New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Descrizione fisica 1 online resource (482 p.)
Disciplina 660.2804
660/.2804
Soggetto topico Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention
ISBN 1-282-77417-4
9786612774171
0-470-92504-3
1-59124-664-4
0-470-92503-5
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing
4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance
4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer
5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures
5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment
Record Nr. UNINA-9910143237903321
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Pubbl/distr/stampa New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Descrizione fisica 1 online resource (482 p.)
Disciplina 660.2804
660/.2804
Soggetto topico Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention
ISBN 1-282-77417-4
9786612774171
0-470-92504-3
1-59124-664-4
0-470-92503-5
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing
4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance
4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer
5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures
5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment
Record Nr. UNISA-996212662303316
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Materiale a stampa
Lo trovi qui: Univ. di Salerno
Opac: Controlla la disponibilità qui
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities [[electronic resource]]
Pubbl/distr/stampa New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Descrizione fisica 1 online resource (482 p.)
Disciplina 660.2804
660/.2804
Soggetto topico Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention
ISBN 1-282-77417-4
9786612774171
0-470-92504-3
1-59124-664-4
0-470-92503-5
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing
4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance
4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer
5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures
5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment
Record Nr. UNINA-9910830023703321
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities
Guidelines for fire protection in chemical, petrochemical, and hydrocarbon processing facilities
Pubbl/distr/stampa New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Descrizione fisica 1 online resource (482 p.)
Disciplina 660.2804
660/.2804
Soggetto topico Chemical plants - Fires and fire prevention
Chemicals - Fires and fire prevention
ISBN 1-282-77417-4
9786612774171
0-470-92504-3
1-59124-664-4
0-470-92503-5
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Fire Protection in Chemical, Petrochemical, and Hydrocarbon Processing Facilities; CONTENTS; Preface; Acknowledgments; Acronyms; 1 Introduction; 1.1. Scope; 1.2. Who Will Benefit from This Guideline?; 1.2.1. What Is Fire Protection?; 1.2.2. Examples; 1.3. Relation to Other CCPS Guidelines and Resources; 2 Management Overview; 2.1. Management Commitment; 2.2. Integration with Other Management Systems; 2.3. Balancing Protection; 2.4. Cost-Benefit; 3 Fire Protection Strategy; 3.1. Key Factors in a Fire Protection Strategy; 3.1.1. Acceptable Loss; 3.1.2. Cost of Fires
3.1.3. Insurance Coverage3.1.4. Installed Systems versus Emergency Response; 3.1.5. Prescriptive versus Performance-Based Design; 3.2. Developing a Fire Protection Strategy; 3.3. Integration with Other Management Systems; 3.4. Integration with the Lifecycle of a Facility; 3.4.1. Design; 3.4.2. Construction and Commissioning; 3.4.3. Operations; 3.4.4. Decommissioning; 4 Overview of Fire Prevention Elements; 4.1. Audit Program; 4.1.1. The Audit Process; 4.1.2. Qualifications and Staffing; 4.1.3. Frequency of Audits; 4.1.4. Application to Fire Protection; 4.2. Layout and Spacing
4.3. Control of Ignition Sources4.3.1. Electrical Area Classification; 4.3.2. Personal Ignition Sources; 4.3.3. Hot Work; 4.3.4. Static Electricity; 4.4. Employee Training; 4.5. Housekeeping; 4.5.1. Housekeeping Program; 4.5.2. Process Area Housekeeping; 4.5.3. Dust Control; 4.5.4. Inappropriate Storage and Handling; 4.5.5. Housekeeping and Equipment; 4.5.6. Cleaning Materials; 4.6. Incident Investigation; 4.6.1. Incident Investigation Process; 4.6.2. Application to Fire Prevention; 4.7. Inherently Safer Design; 4.8. Plant Maintenance; 4.8.1. Poor Maintenance
4.8.2. Good Maintenance Program Elements4.9. Management of Change; 4.9.1. Personnel Changes; 4.9.2. Process Changes; 4.9.3. Maintenance Turnarounds; 4.10. Material Hazards; 4.10.1. Materials Hazard Evaluation Program; 4.10.2. Material Safety Data Sheets; 4.11. Alarm and Surveillance; 4.11.1. Security; 5 Fire Hazard Analysis; 5.1. Hazardous Chemicals and Processes; 5.2. Recognize What You Want to Understand; 5.3. Identification of Inventories; 5.4. Define Fire Scenarios; 5.5. Calculate Potential Fire Hazard; 5.5.1. Ignition and Combustion; 5.5.2. Heat Transfer
5.5.3. Fire Growth and Heat Release5.5.4. Solid Materials; 5.5.5. Enclosure Effects; 5.6. Flash Fires; 5.7. Fireballs; 5.8. Liquid or Pool Fires; 5.8.1. Uelease Rate; 5.8.2. Pool Size; 5.8.3. Flame Height; 5.8.4. Duration of Burning Pools; 5.8.5. Heat Transfer; 5.8.6. Convective Heat Transfer above the Plume; 5.9. Gas and Jet Fires; 5.9.1. Estimating Discharge Rates; 5.9.2. Jet Flame Size; 5.9.3. Heat Transfer; 5.9.4. Radiative Exposure; 5.10. Solid Fires; 5.11. Fire Impact to Personnel, Structures, and Equipment; 5.11.1. Impact to Personnel; 5.11.2. Impact to Structures
5.11.3. Thermal and Nonthermal Impact on Electrical and Electronic Equipment
Record Nr. UNINA-9910876775003321
New York, NY, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2003
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards
Edizione [2nd ed.]
Pubbl/distr/stampa Hoboken, New Jersey : , : Wiley, , 2010
Descrizione fisica 1 online resource (458 p.)
Disciplina 660.2804
660/.2804
Collana CCPS concept book Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards.
Soggetto topico Chemical plants - Fires and fire prevention
Chemical plants - Safety measures
Pressure vessels - Safety measures
Chemicals - Fires and fire prevention
Explosions - Prevention
Soggetto genere / forma Electronic books.
ISBN 1-118-20987-7
1-283-37163-4
9786613371638
0-470-64043-X
1-61583-627-6
0-470-64044-8
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Vapor Cloud Explosion, Pressure Vessel Burst, BLEVE, and Flash Fire Hazards; CONTENTS; List of Tables; List of Figures; Glossary; Acknowledgements; 1. INTRODUCTION; 2. MANAGEMENT OVERVIEW; 2.1. Flash Fires; 2.2. Vapor Cloud Explosions; 2.3. Pressure Vessel Bursts; 2.4. BLEVEs; 2.5. Prediction methodologies; 3. CASE HISTORIES; 3.1. Historical experience; 3.2. Flash fires; 3.2.1. Donnellson, Iowa, USA: Propane Fire; 3.2.2. Lynchburg, Virginia, USA: Propane Fire; 3.2.3. Quantum Chemicals, Morris, Illinois, USA: Olefins Unit Flash Fire; 3.3. Vapor Cloud Explosions
3.3.1. Flixborough, UK: Vapor Cloud Explosion in Chemical Plant3.3.2. Port Hudson, Missouri, USA: Vapor Cloud Explosion after Propane Pipeline Failure; 3.3.3. Jackass Flats, Nevada, USA: Hydrogen-Air Explosion during Experiment; 3.3.4. Ufa, West-Siberia, USSR: Pipeline Rupture Resulting In a VCE; 3.3.5. Phillips, Pasadena, Texas USA: Propylene HDPE Unit VCE and BLEVEs; 3.3.6. BP, Texas City, Texas USA: Discharge from Atmospheric Vent Resulting in a VCE; 3.4. Pressure Vessel Burst; 3.4.1. Kaiser Aluminum, Gramercy, Louisiana USA: Alumina Process Pressure Vessel Burst
3.4.2. Union Carbide Seadrift, Texas USA: Ethylene Oxide Distillation Column Pressure Vessel Burst3.4.3. Dana Corporation, Paris, Tennessee USA: Boiler Pressure Vessel Burst; 3.5. BLEVE; 3.5.1. Procter and Gamble, Worms, Germany: Liquid CO2 Storage Vessel Explosion; 3.5.2. San Juan Ixhuatepec, Mexico City, Mexico: Series of BLEVEs at LPG Storage Facility; 3.5.3. San Carlos de la Rapita, Spain: Propylene Tank Truck Failure; 3.5.4. Crescent City, Illinois, USA: LPG Rail Car Derailment; 3.5.5. Kingman, Arizona USA: LPG Railroad Tank Car BLEVE; 4. BASIC CONCEPTS
4.1. Atmospheric Vapor Cloud Dispersion4.2. Ignition; 4.3. Thermal Radiation; 4.3.1. Point-Source Model; 4.3.2. Solid-Flame Model; 4.4. Explosions - VCE; 4.4.1. Deflagration; 4.4.2. Detonation; 4.5. Blast Effects; 4.5.1. Manifestation; 4.5.2. Blast Loading; 4.5.3. Ground Reflection; 4.5.4. Blast Scaling; 5. FLASH FIRES; 5.1. Overview of Experimental Research; 5.1.1. China Lake and Frenchmen Flats cryogenic liquid tests; 5.1.2. Maplin Sands Tests; 5.1.3. Musselbanks Propane Tests; 5.1.4. HSE LPG Tests of Flash Fires and Jet Fires; 5.2. Flash-Fire Radiation Models; 5.3. Sample Calculations
6. VAPOR CLOUD EXPLOSIONS6.1. Introduction; 6.1.1. Organization of Chapter; 6.1.2. VCE Phenomena; 6.1.3. Definition of VCE; 6.1.4. Confinement and Congestion; 6.2. Vapor Cloud Deflagration Theory and Research; 6.2.1. Laminar Burning Velocity and Flame Speed; 6.2.2. Mechanisms of Flame Acceleration; 6.2.3. Effect of Fuel Reactivity; 6.2.4. Effect of Confinement; 6.2.5. Effect of Congestion; 6.2.6. Effects of Other Factors; 6.2.7. University of Leeds Correlation; 6.2.8. TOO GAME Correlation; 6.2.9. Shell CAM Correlation; 6.3. Vapor Cloud Detonation Theory and Research
6.3.1. Direct Initiation of Vapor Cloud Detonations
Record Nr. UNINA-9910139403303321
Hoboken, New Jersey : , : Wiley, , 2010
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards
Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards
Edizione [2nd ed.]
Pubbl/distr/stampa Hoboken, New Jersey : , : Wiley, , 2010
Descrizione fisica 1 online resource (458 p.)
Disciplina 660.2804
660/.2804
Collana CCPS concept book Guidelines for vapor cloud explosion, pressure vessel burst, BLEVE, and flash fire hazards.
Soggetto topico Chemical plants - Fires and fire prevention
Chemical plants - Safety measures
Pressure vessels - Safety measures
Chemicals - Fires and fire prevention
Explosions - Prevention
ISBN 1-118-20987-7
1-283-37163-4
9786613371638
0-470-64043-X
1-61583-627-6
0-470-64044-8
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Vapor Cloud Explosion, Pressure Vessel Burst, BLEVE, and Flash Fire Hazards; CONTENTS; List of Tables; List of Figures; Glossary; Acknowledgements; 1. INTRODUCTION; 2. MANAGEMENT OVERVIEW; 2.1. Flash Fires; 2.2. Vapor Cloud Explosions; 2.3. Pressure Vessel Bursts; 2.4. BLEVEs; 2.5. Prediction methodologies; 3. CASE HISTORIES; 3.1. Historical experience; 3.2. Flash fires; 3.2.1. Donnellson, Iowa, USA: Propane Fire; 3.2.2. Lynchburg, Virginia, USA: Propane Fire; 3.2.3. Quantum Chemicals, Morris, Illinois, USA: Olefins Unit Flash Fire; 3.3. Vapor Cloud Explosions
3.3.1. Flixborough, UK: Vapor Cloud Explosion in Chemical Plant3.3.2. Port Hudson, Missouri, USA: Vapor Cloud Explosion after Propane Pipeline Failure; 3.3.3. Jackass Flats, Nevada, USA: Hydrogen-Air Explosion during Experiment; 3.3.4. Ufa, West-Siberia, USSR: Pipeline Rupture Resulting In a VCE; 3.3.5. Phillips, Pasadena, Texas USA: Propylene HDPE Unit VCE and BLEVEs; 3.3.6. BP, Texas City, Texas USA: Discharge from Atmospheric Vent Resulting in a VCE; 3.4. Pressure Vessel Burst; 3.4.1. Kaiser Aluminum, Gramercy, Louisiana USA: Alumina Process Pressure Vessel Burst
3.4.2. Union Carbide Seadrift, Texas USA: Ethylene Oxide Distillation Column Pressure Vessel Burst3.4.3. Dana Corporation, Paris, Tennessee USA: Boiler Pressure Vessel Burst; 3.5. BLEVE; 3.5.1. Procter and Gamble, Worms, Germany: Liquid CO2 Storage Vessel Explosion; 3.5.2. San Juan Ixhuatepec, Mexico City, Mexico: Series of BLEVEs at LPG Storage Facility; 3.5.3. San Carlos de la Rapita, Spain: Propylene Tank Truck Failure; 3.5.4. Crescent City, Illinois, USA: LPG Rail Car Derailment; 3.5.5. Kingman, Arizona USA: LPG Railroad Tank Car BLEVE; 4. BASIC CONCEPTS
4.1. Atmospheric Vapor Cloud Dispersion4.2. Ignition; 4.3. Thermal Radiation; 4.3.1. Point-Source Model; 4.3.2. Solid-Flame Model; 4.4. Explosions - VCE; 4.4.1. Deflagration; 4.4.2. Detonation; 4.5. Blast Effects; 4.5.1. Manifestation; 4.5.2. Blast Loading; 4.5.3. Ground Reflection; 4.5.4. Blast Scaling; 5. FLASH FIRES; 5.1. Overview of Experimental Research; 5.1.1. China Lake and Frenchmen Flats cryogenic liquid tests; 5.1.2. Maplin Sands Tests; 5.1.3. Musselbanks Propane Tests; 5.1.4. HSE LPG Tests of Flash Fires and Jet Fires; 5.2. Flash-Fire Radiation Models; 5.3. Sample Calculations
6. VAPOR CLOUD EXPLOSIONS6.1. Introduction; 6.1.1. Organization of Chapter; 6.1.2. VCE Phenomena; 6.1.3. Definition of VCE; 6.1.4. Confinement and Congestion; 6.2. Vapor Cloud Deflagration Theory and Research; 6.2.1. Laminar Burning Velocity and Flame Speed; 6.2.2. Mechanisms of Flame Acceleration; 6.2.3. Effect of Fuel Reactivity; 6.2.4. Effect of Confinement; 6.2.5. Effect of Congestion; 6.2.6. Effects of Other Factors; 6.2.7. University of Leeds Correlation; 6.2.8. TOO GAME Correlation; 6.2.9. Shell CAM Correlation; 6.3. Vapor Cloud Detonation Theory and Research
6.3.1. Direct Initiation of Vapor Cloud Detonations
Record Nr. UNINA-9910830788803321
Hoboken, New Jersey : , : Wiley, , 2010
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado
Autore Woodward John Lowell
Pubbl/distr/stampa Hoboken, N.J., : Wiley, c2010
Descrizione fisica 1 online resource (392 p.)
Disciplina 665.7/730289
665.7730289
Altri autori (Persone) PitbladoRobin
Soggetto topico Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment
Flammable liquids - Accidents - Risk assessment
Chemicals - Fires and fire prevention
Chemical plants - Accidents - Simulation methods
Soggetto genere / forma Electronic books.
ISBN 1-282-54984-7
9786612549847
0-470-59023-8
0-470-59022-X
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks
2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues
4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack
5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline)
5.7.3 Blowdown of Type 3 Breach (Underwater Level)
Record Nr. UNINA-9910140606103321
Woodward John Lowell  
Hoboken, N.J., : Wiley, c2010
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado
LNG risk based safety [[electronic resource] ] : modeling and consequence analysis / / John L Woodward and Robin Pitblado
Autore Woodward John Lowell
Pubbl/distr/stampa Hoboken, N.J., : Wiley, c2010
Descrizione fisica 1 online resource (392 p.)
Disciplina 665.7/730289
665.7730289
Altri autori (Persone) PitbladoRobin
Soggetto topico Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment
Flammable liquids - Accidents - Risk assessment
Chemicals - Fires and fire prevention
Chemical plants - Accidents - Simulation methods
ISBN 1-282-54984-7
9786612549847
0-470-59023-8
0-470-59022-X
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks
2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues
4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack
5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline)
5.7.3 Blowdown of Type 3 Breach (Underwater Level)
Record Nr. UNINA-9910830217303321
Woodward John Lowell  
Hoboken, N.J., : Wiley, c2010
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
LNG risk based safety : modeling and consequence analysis / / John L Woodward and Robin Pitblado
LNG risk based safety : modeling and consequence analysis / / John L Woodward and Robin Pitblado
Autore Woodward John Lowell
Pubbl/distr/stampa Hoboken, N.J., : Wiley, c2010
Descrizione fisica 1 online resource (392 p.)
Disciplina 665.7/730289
Altri autori (Persone) PitbladoRobin
Soggetto topico Liquefied natural gas - Safety measures
Flammable gases - Accidents - Risk assessment
Flammable liquids - Accidents - Risk assessment
Chemicals - Fires and fire prevention
Chemical plants - Accidents - Simulation methods
ISBN 1-282-54984-7
9786612549847
0-470-59023-8
0-470-59022-X
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto LNG RISK BASED SAFETY; CONTENTS; Preface; 1 LNG Properties and Overview of Hazards; 1.1 LNG Properties; 1.2 Hazards of LNG with Respect to Public Risk; 1.2.1 Flash Fire, Pool Fire, or Jet Fire; 1.2.2 Outdoor Vapor Cloud Explosions; 1.2.3 Enclosed Vapor Cloud Explosions; 1.2.4 Asphyxiation; 1.2.5 Freeze Burns; 1.2.6 RPT Explosions; 1.2.7 Roll Over; 1.3 Risk Analysis Requires Adequate Modeling; 1.4 Flammability; 1.5 Regulations in Siting Onshore LNG Import Terminals; 1.5.1 U.S. Marine LNG Risk and Security Regulation; 1.5.2 U.S. Land-Based LNG Risk and Security Regulation
1.5.3 European and International Regulations1.6 Regulation for Siting Offshore LNG Import Terminals; 1.7 Controversial Claims of LNG Opponents; 2 LNG Incidents and Marine History; 2.1 LNG Ship Design History; 2.1.1 Initial Design Attempts; 2.1.2 Tank Materials; 2.1.3 Insulation Materials; 2.1.4 Tank Design; 2.2 Designs and Issues-First Commercial LNG Ships; 2.2.1 Membrane Technology; 2.2.2 Gaztransport Solution; 2.2.3 Spheres; 2.2.4 LNG Carriers for the Asian Trade; 2.2.5 Current State of LNG Tankers; 2.3 LNG Trade History; 2.3.1 European Trade; 2.3.2 Asian Trade; 2.3.3 Temporary Setbacks
2.3.4 Revival of LNG with Worldwide Supply-Demand Pinch of Petroleum2.3.5 Supply History; 2.3.6 Some Economic Factors; 2.4 LNG Accident History; 2.5 Summary of LNG History and Relevant Technical Developments; 3 Current LNG Carriers; 3.1 Design Requirements; 3.2 Membrane Tanks; 3.2.1 Tank Design and Insulation; 3.2.2 Dimensions and Capacity; 3.2.3 Tank Materials and Insulation; 3.2.4 Pressure and Vacuum Relief; 3.2.5 Design Issues; 3.3 Moss Spheres; 3.3.1 Typical Dimensions and Capacity; 3.3.2 Insulation and Tank Materials; 3.3.3 Pressure and Vacuum Relief; 3.3.4 Design Issues
4 Risk Analysis and Risk Reduction4.1 Background; 4.2 Risk Analysis Process; 4.2.1 Hazard Identification; 4.3 Frequency: Data Sources and Analysis; 4.3.1 Generic Data Approach; 4.4 Frequency: Predictive Methods; 4.4.1 FTA; 4.4.2 Event Tree Analysis; 4.5 Consequence Modeling; 4.6 Ignition Probability; 4.7 Risk Results; 4.7.1 Risk Presentation; 4.7.2 Risk Decision Making; 4.8 Special Issues-Terrorism; 4.9 Risk Reduction and Mitigation Measures for LNG; 5 LNG Discharge on Water; 5.1 Type 1-Above Water Breaches at Sea; 5.1.1 Ship-to-Ship Collisions; 5.1.2 Weapons Attack
5.2 Type 2-At Waterline Breaches at Sea5.2.1 Grounding or Collision; 5.2.2 Explosive-Laden Boat Attack; 5.3 Type 3-Below Waterline Breaches at Sea; 5.4 Discharges from Ship's Pipework; 5.5 Cascading Failures at Sea; 5.5.1 Sloshing Forces; 5.5.2 Explosion in Hull Chambers; 5.5.3 RPT in Hull Chambers; 5.5.4 Cryogenic Temperature Stresses on Decks and Hull; 5.5.5 Cascading Events Caused by Fire; 5.6 Initial Discharge Rate; 5.7 Time-Dependent Discharge (Blowdown); 5.7.1 Blowdown for Type 2 Breach (at Waterline); 5.7.2 Blowdown for Type 1 Breach (above Waterline)
5.7.3 Blowdown of Type 3 Breach (Underwater Level)
Record Nr. UNINA-9910876948703321
Woodward John Lowell  
Hoboken, N.J., : Wiley, c2010
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui