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Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Pubbl/distr/stampa New York, : DIERS, c1992
Descrizione fisica 1 online resource (576 p.)
Disciplina 660.281
Altri autori (Persone) FisherH. G
Soggetto topico Chemical plants - Safety measures
Relief valves
ISBN 1-282-81740-X
9786612817403
0-470-93831-5
1-59124-780-2
0-470-93830-7
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Emergency Relief System Design Using DIERS Technology: The Design Institute for Emergency Relief Systems (DIERS) Project Manual; Contents; Preface; Introduction; 1. Overview; 2. Design Institute for Emergency Relief Systems (DIERS); 3. A Strategy for Major Accidental Release Prevention; 4. A Strategy for Emergency Relief System Design; 5. An Approach to Emergency Relief System Design Assessment; 6. Two-Phase Vapor-Liquid Flow; 7. Two-Phase Vapor-Liquid Flow Onset and Disengagement; 8. Two-Phase Vapor-Liquid Hydrodynamics; 9. DlERS Bench-Scale Apparatus
10. Runaway Reaction Emergency Relief System Design Computer Program11. References; Appendix A. DlERS Committees; Appendix B. DlERS Sponsors; Appendix C. DIERS Contractors; Chapter I. Vapor Disengagement Dynamics; 1. Overview; 1-1. Vapor Disengagement Dynamics; 1-2. Design Considerations; 2. Detailed Discussion; 2-1. Open Literature References; 2-2. Project Manual; 3. References; Appendix I-A. The Coupling Equation and Flow Models; Appendix I-B. Best Estimate Procedure to Calculate Two-Phase Vapor-Liquid Flow Onset/Disengagement; Appendix I-C. Fluid Behavior in Venting Vessels
Appendix I-D. Energy and Material Balance Derivations for Emergency Pressure Relief of VesselsAnnex I-D1. Internal Energy and Venting Calculations; Chapter II. Pressure Relief System Flow; 1. Introduction; 1-1. Scope; 1-2. Organization; 1-3. Special Terminology; 2. Recommended Design Methods; 2-1. Newtonian Flow; 2-2. Complex Fluids; 2-3. Useful Approximations; 3. Technology Base; 3-1. General Flow Equations; 3-2. Nozzle Flow Models; 3-3. Sharp Reductions; 3-4. Pressure Recovery/Expansions/Equilibrations; 3-5. Pipe Flow; 3.6. Application to Pressure Relief System Elements; 3-7. Networks
3-8. Complex Fluids4. Nomenclature; 5. Acknowledgments; 6. References; Appendix II-A. Thermophysical Property Requirements; Appendix II-B. Equilibrium Flash Calculations; Appendix II-C. Model Parameters for Pipe Entrance Sections; Appendix II-D. Computer Routines in SAFIRE Program; Appendix II-E. Example Problems; Appendix II-F. Generalized Correlations and Design Charts; Chapter III. DIERS Phase III Large-Scale Integral Tests; 1. Summary; 2. Introduction; 2-1. Program Objectivcs; 2-2. Program Description; 3. Test Configurations; 4. Test Results; 4-1. Tests T1 to T8
4-2. Tests V32-W1 to V32-W84-3. Tests T9, T10, T11, T14, and T25; 4-4. Tests T12 and T13; 4-5. Test T20; 4-6. Tests T17 and T18; 4-7. Tests T21, T22, T23, and T24; 4-8. ICRE Tats 32-6 to 32-11; 4-9. ICRE Tests 2000-1 to 2000-5; 4-10. ICRE Tests 32-14, 32-15, and 32-18; 5. Acknowledgments; 6. References; Appendix III-A. Test Configurations; Appendix III-B. Experimental Results and Model Comparisons; Appendix III-C. Kinetics Model for Styrene Polymerizations; Chapter IV. High Viscosity Flashing Two-Phase Flow; 1. Introduction; 1-1. General Discussion of High Viscosity Flow in Relief Systems
1-2. Why High Viscosity Systems Require Special Consideration
Record Nr. UNISA-996217752803316
New York, : DIERS, c1992
Materiale a stampa
Lo trovi qui: Univ. di Salerno
Opac: Controlla la disponibilità qui
Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Pubbl/distr/stampa New York, : DIERS, c1992
Descrizione fisica 1 online resource (576 p.)
Disciplina 660.281
Altri autori (Persone) FisherH. G
Soggetto topico Chemical plants - Safety measures
Relief valves
ISBN 1-282-81740-X
9786612817403
0-470-93831-5
1-59124-780-2
0-470-93830-7
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Emergency Relief System Design Using DIERS Technology: The Design Institute for Emergency Relief Systems (DIERS) Project Manual; Contents; Preface; Introduction; 1. Overview; 2. Design Institute for Emergency Relief Systems (DIERS); 3. A Strategy for Major Accidental Release Prevention; 4. A Strategy for Emergency Relief System Design; 5. An Approach to Emergency Relief System Design Assessment; 6. Two-Phase Vapor-Liquid Flow; 7. Two-Phase Vapor-Liquid Flow Onset and Disengagement; 8. Two-Phase Vapor-Liquid Hydrodynamics; 9. DlERS Bench-Scale Apparatus
10. Runaway Reaction Emergency Relief System Design Computer Program11. References; Appendix A. DlERS Committees; Appendix B. DlERS Sponsors; Appendix C. DIERS Contractors; Chapter I. Vapor Disengagement Dynamics; 1. Overview; 1-1. Vapor Disengagement Dynamics; 1-2. Design Considerations; 2. Detailed Discussion; 2-1. Open Literature References; 2-2. Project Manual; 3. References; Appendix I-A. The Coupling Equation and Flow Models; Appendix I-B. Best Estimate Procedure to Calculate Two-Phase Vapor-Liquid Flow Onset/Disengagement; Appendix I-C. Fluid Behavior in Venting Vessels
Appendix I-D. Energy and Material Balance Derivations for Emergency Pressure Relief of VesselsAnnex I-D1. Internal Energy and Venting Calculations; Chapter II. Pressure Relief System Flow; 1. Introduction; 1-1. Scope; 1-2. Organization; 1-3. Special Terminology; 2. Recommended Design Methods; 2-1. Newtonian Flow; 2-2. Complex Fluids; 2-3. Useful Approximations; 3. Technology Base; 3-1. General Flow Equations; 3-2. Nozzle Flow Models; 3-3. Sharp Reductions; 3-4. Pressure Recovery/Expansions/Equilibrations; 3-5. Pipe Flow; 3.6. Application to Pressure Relief System Elements; 3-7. Networks
3-8. Complex Fluids4. Nomenclature; 5. Acknowledgments; 6. References; Appendix II-A. Thermophysical Property Requirements; Appendix II-B. Equilibrium Flash Calculations; Appendix II-C. Model Parameters for Pipe Entrance Sections; Appendix II-D. Computer Routines in SAFIRE Program; Appendix II-E. Example Problems; Appendix II-F. Generalized Correlations and Design Charts; Chapter III. DIERS Phase III Large-Scale Integral Tests; 1. Summary; 2. Introduction; 2-1. Program Objectivcs; 2-2. Program Description; 3. Test Configurations; 4. Test Results; 4-1. Tests T1 to T8
4-2. Tests V32-W1 to V32-W84-3. Tests T9, T10, T11, T14, and T25; 4-4. Tests T12 and T13; 4-5. Test T20; 4-6. Tests T17 and T18; 4-7. Tests T21, T22, T23, and T24; 4-8. ICRE Tats 32-6 to 32-11; 4-9. ICRE Tests 2000-1 to 2000-5; 4-10. ICRE Tests 32-14, 32-15, and 32-18; 5. Acknowledgments; 6. References; Appendix III-A. Test Configurations; Appendix III-B. Experimental Results and Model Comparisons; Appendix III-C. Kinetics Model for Styrene Polymerizations; Chapter IV. High Viscosity Flashing Two-Phase Flow; 1. Introduction; 1-1. General Discussion of High Viscosity Flow in Relief Systems
1-2. Why High Viscosity Systems Require Special Consideration
Record Nr. UNINA-9910830776803321
New York, : DIERS, c1992
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Emergency relief system design using DIERS technology [[electronic resource] ] : the Design Institute for Emergency Relief Systems (DIERS) project manual / / H.G. Fisher ... [et al.]
Pubbl/distr/stampa New York, : DIERS, c1992
Descrizione fisica 1 online resource (576 p.)
Disciplina 660.281
Altri autori (Persone) FisherH. G
Soggetto topico Chemical plants - Safety measures
Relief valves
ISBN 1-282-81740-X
9786612817403
0-470-93831-5
1-59124-780-2
0-470-93830-7
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Emergency Relief System Design Using DIERS Technology: The Design Institute for Emergency Relief Systems (DIERS) Project Manual; Contents; Preface; Introduction; 1. Overview; 2. Design Institute for Emergency Relief Systems (DIERS); 3. A Strategy for Major Accidental Release Prevention; 4. A Strategy for Emergency Relief System Design; 5. An Approach to Emergency Relief System Design Assessment; 6. Two-Phase Vapor-Liquid Flow; 7. Two-Phase Vapor-Liquid Flow Onset and Disengagement; 8. Two-Phase Vapor-Liquid Hydrodynamics; 9. DlERS Bench-Scale Apparatus
10. Runaway Reaction Emergency Relief System Design Computer Program11. References; Appendix A. DlERS Committees; Appendix B. DlERS Sponsors; Appendix C. DIERS Contractors; Chapter I. Vapor Disengagement Dynamics; 1. Overview; 1-1. Vapor Disengagement Dynamics; 1-2. Design Considerations; 2. Detailed Discussion; 2-1. Open Literature References; 2-2. Project Manual; 3. References; Appendix I-A. The Coupling Equation and Flow Models; Appendix I-B. Best Estimate Procedure to Calculate Two-Phase Vapor-Liquid Flow Onset/Disengagement; Appendix I-C. Fluid Behavior in Venting Vessels
Appendix I-D. Energy and Material Balance Derivations for Emergency Pressure Relief of VesselsAnnex I-D1. Internal Energy and Venting Calculations; Chapter II. Pressure Relief System Flow; 1. Introduction; 1-1. Scope; 1-2. Organization; 1-3. Special Terminology; 2. Recommended Design Methods; 2-1. Newtonian Flow; 2-2. Complex Fluids; 2-3. Useful Approximations; 3. Technology Base; 3-1. General Flow Equations; 3-2. Nozzle Flow Models; 3-3. Sharp Reductions; 3-4. Pressure Recovery/Expansions/Equilibrations; 3-5. Pipe Flow; 3.6. Application to Pressure Relief System Elements; 3-7. Networks
3-8. Complex Fluids4. Nomenclature; 5. Acknowledgments; 6. References; Appendix II-A. Thermophysical Property Requirements; Appendix II-B. Equilibrium Flash Calculations; Appendix II-C. Model Parameters for Pipe Entrance Sections; Appendix II-D. Computer Routines in SAFIRE Program; Appendix II-E. Example Problems; Appendix II-F. Generalized Correlations and Design Charts; Chapter III. DIERS Phase III Large-Scale Integral Tests; 1. Summary; 2. Introduction; 2-1. Program Objectivcs; 2-2. Program Description; 3. Test Configurations; 4. Test Results; 4-1. Tests T1 to T8
4-2. Tests V32-W1 to V32-W84-3. Tests T9, T10, T11, T14, and T25; 4-4. Tests T12 and T13; 4-5. Test T20; 4-6. Tests T17 and T18; 4-7. Tests T21, T22, T23, and T24; 4-8. ICRE Tats 32-6 to 32-11; 4-9. ICRE Tests 2000-1 to 2000-5; 4-10. ICRE Tests 32-14, 32-15, and 32-18; 5. Acknowledgments; 6. References; Appendix III-A. Test Configurations; Appendix III-B. Experimental Results and Model Comparisons; Appendix III-C. Kinetics Model for Styrene Polymerizations; Chapter IV. High Viscosity Flashing Two-Phase Flow; 1. Introduction; 1-1. General Discussion of High Viscosity Flow in Relief Systems
1-2. Why High Viscosity Systems Require Special Consideration
Record Nr. UNINA-9910841192603321
New York, : DIERS, c1992
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Energy optimization in process systems / Stanislaw Sieniutycz, Jacek Jeżowski
Energy optimization in process systems / Stanislaw Sieniutycz, Jacek Jeżowski
Autore Sieniutycz, Stanislaw
Pubbl/distr/stampa Amsterdam [etc.], : Elsevier, 2009
Descrizione fisica XVII, 751 p. ; 24 cm
Disciplina 660
660.281
Altri autori (Persone) Jezowski, Jacek
Soggetto topico Processi chimici - Controllo - Modelli matematici
ISBN 9780080451411
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Record Nr. UNISANNIO-NAP0465458
Sieniutycz, Stanislaw  
Amsterdam [etc.], : Elsevier, 2009
Materiale a stampa
Lo trovi qui: Univ. del Sannio
Opac: Controlla la disponibilità qui
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Edizione [2nd ed.]
Pubbl/distr/stampa New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Descrizione fisica 1 online resource (786 p.)
Disciplina 660.2804
660.281
Soggetto topico Chemical plants - Risk assessment
ISBN 1-282-78332-7
9786612783326
0-470-93542-1
1-59124-456-0
0-470-93541-3
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation
2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background
3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk
4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data
5.1.1. Types of Data
Record Nr. UNISA-996212666303316
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Materiale a stampa
Lo trovi qui: Univ. di Salerno
Opac: Controlla la disponibilità qui
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Edizione [2nd ed.]
Pubbl/distr/stampa New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Descrizione fisica 1 online resource (786 p.)
Disciplina 660.2804
660.281
Soggetto topico Chemical plants - Risk assessment
ISBN 1-282-78332-7
9786612783326
0-470-93542-1
1-59124-456-0
0-470-93541-3
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation
2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background
3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk
4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data
5.1.1. Types of Data
Record Nr. UNINA-9910830665503321
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Guidelines for chemical process quantitative risk analysis [[electronic resource]]
Edizione [2nd ed.]
Pubbl/distr/stampa New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Descrizione fisica 1 online resource (786 p.)
Disciplina 660.2804
660.281
Soggetto topico Chemical plants - Risk assessment
ISBN 1-282-78332-7
9786612783326
0-470-93542-1
1-59124-456-0
0-470-93541-3
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Chemical Process Quantitative Risk Analysis; Contents; Preface; Preface to the First Edition; Acknowledgments; Acknowledgments to the First Edition; Management Overview; Organization of the Guidelines; Acronyms; 1 Chemical Process Quantitative Risk Analysis; 1.1. CPQRA Definitions; 1.2. Component Techniques of CPQRA; 1.2.1. Complete CPQRA Procedure; 1.2.2. Prioritized CPQRA Procedure; 1.3. Scope of CPQRA Studies; 1.3.1. The Study Cube; 1.3.2. Typical Goals of CPQRAs; 1.4. Management of Incident Lists; 1.4.1. Enumeration; 1.4.2. Selection; 1.4.3. Tracking
1.5. Applications of CPQRA1.5.1. Screening Techniques; 1.5.2. Applications within Existing Facilities; 1.5.3. Applications within New Projects; 1.6. Limitations of CPQRA; 1.7. Current Practices; 1.8. Utilization of CPQRA Results; 1.9. Project Management; 1.9.1. Study Goals; 1.9.2. Study Objectives; 1.9.3. Depth of Study; 1.9.4. Special User Requirements; 1.9.5. Construction of a Project Plan; 1.9.6. Project Execution; 1.10. Maintenance of Study Results; 1.11. References; 2 Consequence Analysis; 2.1. Source Models; 2.1.1. Discharge Rate Models; 2.1.2. Flash and Evaporation
2.1.3. Dispersion Models2.2. Explosions and Fires; 2.2.1. Vapor Cloud Explosions (VCE); 2.2.2. Flash Fires; 2.2.3. Physical Explosion; 2.2.4. BLEVE and Fireball; 2.2.5. Confined Explosions; 2.2.6. Pool Fires; 2.2.7. Jet Fires; 2.3. Effect Models; 2.3.1. Toxic Gas Effects; 2.3.2. Thermal Effects; 2.3.3. Explosion Effects; 2.4. Evasive Actions; 2.4.1. Background; 2.4.2. Description; 2.4.3. Example Problem; 2.4.4. Discussion; 2.5. Modeling Systems; 2.6. References; 3 Event Probability and Failure Frequency Analysis; 3.1. Incident Frequencies from the Historical Record; 3.1.1. Background
3.1.2. Description3.1.3. Sample Problem; 3.1.4. Discussion; 3.2. Frequency Modeling Techniques; 3.2.1. Fault Tree Analysis; 3.2.2. Event Tree Analysis; 3.3. Complementary Plant-Modeling Techniques; 3.3.1. Common Cause Failure Analysis; 3.3.2. Human Reliability Analysis; 3.3.3. External Events Analysis; 3.4. References; 4 Measurement, Calculation, and Presentation of Risk Estimates; 4.1. Risk Measures; 4.1.1. Risk Indices; 4.1.2. lndividual Risk; 4.1.3. Societal Risk; 4.1.4. lnjury Risk Measures; 4.2. Risk Presentation; 4.2.1. Risk Indices; 4.2.2. lndividual Risk; 4.2.3. Societal Risk
4.3. Selection of Risk Measures and Presentation Format4.3.1. Selection of Risk Measures; 4.3.2. Selection of Presentation Format; 4.4. Risk Calculations; 4.4.1. lndividual Risk; 4.4.2. Societal Risk; 4.4.3. Risk Indices; 4.4.4. General Comments; 4.4.5. Example Risk Calculation Problem; 4.4.6. Sample Problem Illustrating That F-N Curves Cannot Be Calculated from lndividual Risk Contours; 4.5. Risk Uncertainty, Sensitivity, and Importance; 4.5.1. Uncertainty; 4.5.2. Sensitivity; 4.5.3. Importance; 4.6. References; 5 Creation of CPQRA Data Base; 5.1. Historical incident Data
5.1.1. Types of Data
Record Nr. UNINA-9910840981603321
New York, : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c2000
Materiale a stampa
Lo trovi qui: Univ. Federico II
Opac: Controlla la disponibilità qui
Guidelines for safe automation of chemical processes [[electronic resource]]
Guidelines for safe automation of chemical processes [[electronic resource]]
Pubbl/distr/stampa New York, N.Y., : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c1993
Descrizione fisica 1 online resource (450 p.)
Disciplina 660.281
660.28150289
660/.2815/0289
Soggetto topico Chemical processes - Automation - Safety measures
ISBN 1-282-81738-8
9786612817380
0-470-93825-0
1-59124-641-5
0-470-93824-2
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Nota di contenuto Guidelines for Safe Automation of Chemical Processes; CONTENTS; List of Figures; List of Tables; Preface; Glossary; Acronyms; 1. INTRODUCTION; 1.0 Objective; 1.1 Scope; 1.2 Limitations; 1.3 Overview of the Contents; 2. THE PLACE OF AUTOMATION IN CHEMICAL PLANT SAFETY.. .A DESIGN PHILOSOPHY; 2.0 Chemical Plant Operations in Transition; 2.1 Plant Automation; 2.2 A Framework for Chemical Process Safety; 2.3 Chemical Plant Safety System Development; 2.4 Safety System Design Philosophy; 2.5 References; 3. TECHNIQUES FOR EVALUATING INTEGRITY OF PROCESS CONTROL SYSTEMS; 3.0 Introduction
3.1 Safety and Integrity Evaluation Techniques3.2 Typical Process Hazard Review Activities and Outputs; 3.3 System Integrity Evaluation Criteria and Certification Methods; 3.4 Emerging Documents; 3.5 References; 4. SAFETY CONSIDERATIONS IN THE SELECTION AND DESIGN OF BASIC PROCESS CONTROL SYSTEMS; 4.0 Introduction; 4.1 BPCS Technology Selection; 4.2 Signals; 4.3 Field Measurements; 4.4 Final Control Elements; 4.5 Process Controllers; 4.6 Operator/Control System Interfaces; 4.7 Communication Considerations in typical PES Architectures; 4.8 Electrical Power Distribution Systems
4.9 Control-System Grounding for Personnel and Signal Protection4.10 Batch Control with Regulatory and Discrete Control; 4.11 Software Design and Data Structures; 4.12 Advanced Computer-Control Strategies; 4.13 Administrative Actions; 4.14 References; 5. SAFETY CONSIDERATIONS IN THE SELECTION AND DESIGN OF SAFETY INTERLOCK SYSTEMS (SISs); 5.0 Introduction; 5.1 SIS Design Issues; 5.2 Perform SIS Requirements Analysis; 5.3 SIS Technology Selection; 5.4 Select SIS Architecture; 5.5 Select SIS Equipment; 5.6 Perform SIS DESIGN; 5.7 References
6. ADMINISTRATIVE ACTIONS TO ENSURE CONTROL SYSTEM INTEGRITY6.0 Introduction; 6.1 Communication of Procedures; 6.2 Maintenance Facilities Planning; 6.3 Testing Bpcs Hardware And Software; 6.4 SIS and Alarm Test Procedures; 6.5 Testing Frequency Requirements; 6.6 Installed Test Connections and Necessary Bypasses; 6.7 Plant Operations Training with Installed Controls; 6.8 Documentation of the BPCS and SIS; 6.9 Audit Program to Keep Emphasis on BPCS/SIS Maintenance and Documentation Activities; 6.10 Simulation; 6.11 Process Control Organization and Staffing; 6.12 References
7. AN EXAMPLE: THESE GUIDELINES APPLIED TO THE SAFE AUTOMATION OF A BATCH POLYMERIZATION REACTOR7.0 Introduction; 7.1 Project Definition; 7.2 Hazard Identification; 7.3 Process Design Strategy; 7.4 SIS Integrity Level Selection; 7.5 Design of the BPCS; 7.6 Risk Assessment and Control; 7.7 Design And Validation of the SIS; 7.8 Installation and Testing; 7.9 Administrative Procedures to Maintain Integrity; 7.10 Approach for Automation of an Existing Facility; 7.11 References; 8. THE PATH FORWARD . . . TO MORE AUTOMATED, SAFE CHEMICAL PLANTS; 8.0 Introduction
8.1 Governmental Regulations and Industry Initiatives
Record Nr. UNISA-996212702303316
New York, N.Y., : Center for Chemical Process Safety of the American Institute of Chemical Engineers, c1993
Materiale a stampa
Lo trovi qui: Univ. di Salerno
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INDUSTRIAL processing with membranes / edited by Robert E. Lacey and Sidney Loeb
INDUSTRIAL processing with membranes / edited by Robert E. Lacey and Sidney Loeb
Pubbl/distr/stampa New York : J. Wiley and sons, 1972
Descrizione fisica X, 348 p. : ill. ; 23 cm
Disciplina 660.281
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione ita
Record Nr. UNINA-990000035130403321
New York : J. Wiley and sons, 1972
Materiale a stampa
Lo trovi qui: Univ. Federico II
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Integrated design and simulation of chemical processes / Alexandre C. Dimian
Integrated design and simulation of chemical processes / Alexandre C. Dimian
Autore DIMIAN, Elsevier
Pubbl/distr/stampa Amsterdam [etc.] : Elsevier, 2003
Descrizione fisica XVI, 698 p. : ill. ; 25 cm
Disciplina 660.281
Soggetto topico Processi chimici
ISBN 0-444-82996-2
Formato Materiale a stampa
Livello bibliografico Monografia
Lingua di pubblicazione eng
Record Nr. UNISA-990003012540203316
DIMIAN, Elsevier  
Amsterdam [etc.] : Elsevier, 2003
Materiale a stampa
Lo trovi qui: Univ. di Salerno
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