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Multiscale modeling for process safety applications /
Featuring worked out examples, case studies, and a question bank to aid understanding and involvement, this valuable resource demonstrates the implementation of multiscale modeling techniques on process safety applications. --
| Clasificación: | Libro Electrónico |
|---|---|
| Autores principales: | , , |
| Formato: | Electrónico eBook |
| Idioma: | Inglés |
| Publicado: |
Amsterdam :
Elsevier,
[2016]
|
| Temas: | |
| Acceso en línea: | Texto completo |
Tabla de Contenidos:
- Front Cover; Multiscale Modeling for Process Safety Applications; Copyright; Contents; Preface; Acknowledgments; 1
- INTRODUCTION; REFERENCES; 2
- PROCESS SAFETY; 2.1 FIRE; 2.1.1 THE FIRE TRIANGLE; 2.1.2 IGNITION PHENOMENA; 2.1.3 FLAMMABILITY LIMITS OF GASES AND VAPORS; 2.1.4 TYPES OF FIRES; 2.1.4.1 Diffusion fires; Jet fires; Natural fires; Pool fires; Fireballs; 2.1.4.2 Premixed fires; Flash fires; 2.1.5 FIRE RISK ANALYSIS; 2.2 EXPLOSION; 2.2.1 DEFLAGRATION AND DETONATION; 2.2.2 EXPLOSION ENERGY; 2.2.2.1 Energy of chemical explosions; 2.2.2.2 Energy of mechanical explosions
- Brode's equation (Brode, 1959)Isentropic expansion; Isothermal expansion; Thermodynamic availability; 2.2.3 EXPLOSION TYPES; 2.2.3.1 Vapor cloud explosion; 2.2.3.2 Boiling liquid expanding vapor explosion; 2.2.3.3 Dust explosion; Explosibility classification; Minimum ignition temperature; Minimum explosive concentration; Minimum ignition energy; Explosion pressure characteristics; 2.2.4 EXPLOSION PREVENTION; 2.2.4.1 Inerting; Vacuum purging; Pressure purging; Combined pressure-vacuum purging; Sweep-through purging; 2.2.4.2 Controlling static electricity; 2.2.4.3 Ventilation; 2.3 TOXIC EFFECTS
- 2.3.1 HOW TOXIC SUBSTANCES ENTER THE ORGANISM2.3.2 PARTICLE CLASSIFICATION; 2.3.2.1 Dimensionality; 2.3.2.2 Particle morphology; 2.3.2.3 Particle composition; 2.3.2.4 Particle uniformity and agglomeration; 2.3.3 TOXIC SUBSTANCES; 2.3.4 TOXICITY ASSESSMENT; 2.3.4.1 Noncancer effect; 2.3.4.2 Cancer effect; 2.3.5 RISK ASSESSMENT; 2.3.6 HYGIENE STANDARDS; 2.3.6.1 ERPG; 2.3.6.2 IDLH; 2.3.6.3 EEGL; 2.3.6.4 PEL; 2.3.6.5 TXDS; 2.3.6.6 RMP; 2.3.7 HAZARD ASSESSMENT METHODOLOGY; 2.3.8 SOURCE TERM; 2.3.9 GAS DISPERSION; 2.3.9.1 Workbooks/correlations; 2.3.9.2 Integral models; 2.3.9.3 Shallow layer models
- 2.3.9.4 Computational fluid dynamics2.3.10 CONCENTRATION FLUCTUATIONS; 2.3.11 MITIGATION: TERRAIN, BARRIERS, SPRAYS, SHELTER, AND EVACUATION; 2.3.12 PLANT LAYOUT; 2.3.13 COMPUTER AIDS; 2.4 PRESENT APPROACH TO PROCESS SAFETY; 2.4.1 RISK AND HAZARD; 2.4.2 METHODOLOGY IN RISK ASSESSMENT; 2.4.2.1 Nodes in risk assessment; 2.4.2.2 Teams and information required for a risk assessment; 2.4.3 QUANTITATIVE RISK ASSESSMENT; 2.4.4 SCALABILITY IN RISK ASSESSMENT METHODOLOGIES; 2.4.5 PROBABILITY BASED APPROACHES; 2.4.5.1 Fault tree analysis; 2.4.5.2 Event tree analysis; 2.4.5.3 Bow-tie plots
- 2.4.5.4 Failure modes and effects analysis2.4.5.5 Bayesian networks; 2.4.6 CONSEQUENCE-BASED APPROACHES; 2.4.6.1 Fire consequence modeling; Impact on personnel; Impact on structures; Impact on Electrical Equipment; Impact on the environment; 2.4.6.2 Probit analysis: dose-response modeling; 2.4.7 QUALITATIVE AND SEMI-QUANTITATIVE APPROACHES; 2.4.7.1 Layer of protection analysis; 2.4.7.2 Risk matrix; 2.4.7.3 HAZOP; 2.4.7.4 What-if analysis; 2.4.7.5 Checklist; 2.4.7.6 What-if/checklist; 2.4.7.7 Dow fire and explosion index; 2.5 PROCESS SAFETY CHALLENGES AND LOOKING AT THE FUTURE