Note: ‘Page numbers followed by “f” indicate figures, “t” indicate tables’.
atomistic simulation-based approaches,
148–149
practical considerations,
149
Atmospheric interest
Autoignition temperature (AIT),
Automatic pressure tracking adiabatic calorimeter (APTAC),
176
Calculated adiabatic reaction temperature (CART),
156
Chaos theory techniques
runaway reaction
continuous real-time evaluation,
301
parametric sensitivity,
300
Chemical Engineering Thermodynamics and Hazard Evaluation (CHETAH),
157–159, 164–166
Computational fluid dynamics (CFD),
dispersion of flammable gases
simulated flammable materials, types,
231–232
geometry representation,
215
soot formation model,
219
QRA
temporal and spatial scales,
211, 212t
toxic dispersion/HVAC design
published validation studies,
259–262
transport equation and physical models,
212, 212f, 213t
Consequence based approaches
fire consequence modeling,
72–74
electrical equipment, impact on,
73–74
environment, impact on,
74
personnel, impact on,
72–73
structures, impact on,
73
probit analysis, dose–response modeling,
74, 75t
Conserved scalar model,
216
Continuous process monitoring,
303
Coupling of length scales (CLS),
407
Critical adiabatic flame temperature (CAFT),
126–127
Deflagration to detonation transition (DDT),
21, 246–249
Design Institute for Emergency Relief Systems (DIERS),
296–297
Differential algebraic equations (DAE),
290–291
Diffusion fires
Discrete transfer method,
218
Dispersion of flammable gases
simulated flammable materials, types,
231–232
explosibility classification,
34, 34t
explosion pressure characteristics,
36–37
minimum explosive concentration,
35
minimum ignition energy,
36
minimum ignition temperature,
34–35
practical considerations,
188
Dynamic operator training simulator (DOTS),
294–295
Dynamic simulation
Equipment failure
Bayesian logic
sources of generic data,
321
exponential distribution,
311
failure rates without failure,
315–316
liquefied natural gas, risk assessment
mean time to failure,
311
probabilistic models,
310
Weibull distribution,
313
Explosion
vapor cloud explosion (VCE),
26–27
Explosion energy
chemical explosions,
22–24
mechanical explosions,
24–25
isentropic expansion,
24–25
thermodynamic availability,
25
Explosion modeling, CFD,
238
Explosive decomposition reaction
Exponential distribution,
311
Facility siting studies
risk-related equations,
343
weather conditions, Monte Carlo simulation of,
343–344
Finite element analysis (FEA)
thermomechanical response of structures
flame–wall interactions,
278
Fire
fire risk analysis (FRA),
19–20
Fire hazard analysis (FHA),
19
geometry representation,
215
soot formation model,
219
first principle calculations,
128–129
computational fluid dynamics,
53–54
workbooks/correlations,
53
Hartree-Fock (HF) method,
115
Hazard and operability study (HAZOP),
292–294
macroscale modeling approaches,
156–157
macroscale modeling approaches,
156–157
Highest occupied molecular orbital (HOMO),
116
Inerting
combined pressure–vacuum purging,
39–40, 40f
controlling static electricity,
41
pressure purging,
39, 39f
sweep-through purging,
40
Inherently safer design (ISD)
material design, multiscale modeling approach in,
372–383
QSPR methodology, hazardous materials risk evaluation by,
378–383, 379f
improve process safety, advantages to,
384–386
Monte Carlo methods application,
339–352
process control, multiscale modeling approach in,
366–371, 367f
model predictive control,
371
quantitative risk analysis
Integrated multi-scale approaches,
408f, 409
Isentropic expansion,
24–25
radiative heat flux iso-surface,
222f
Kinetic parameters prediction,
418
Liquefied natural gas (LNG)
methodology development
independent protection layer,
324, 325f
Lower flammability limit (LFL),
228, 411
Lower oxygen limit (LOL),
Lowest unoccupied molecular orbital (LUMO),
116
Lumping various modeling,
125
QSPR methodology, hazardous materials risk evaluation by,
378–383, 379f
improve process safety, advantages to,
384–386
Minimum energy path (MEP),
169
Minimum flash point behavior (MFPB),
135–136
Minimum ignition energy (MIE),
Modeling and Experimental Research into Gas Explosions (MERGE),
241
Molecular dynamics–based model,
415
atomistic simulation-based approaches,
148–149
practical considerations,
149
atomistic simulation-based approaches,
148–149
practical considerations,
188
first principle calculations,
128–129
heat of reaction/heat of formation,
155–167
macroscale modeling approaches,
156–157
quantum mechanics and molecular dynamics,
193–194, 194f
correlation-based model development,
122
geometry optimization,
121
first principle-based approaches,
169–174
macroscale modeling approaches,
168
practical considerations,
174
macroscale modeling approaches,
176–179
molecular dynamics simulations,
182–185
molecular modeling approaches,
179–185
practical considerations,
185
first principle calculations,
190–191
multiscale modeling techniques,
190–191
Moller-Plesset fourth order (MP4),
128
Monte Carlo methods application,
339–352
Multilinear regression (MLR),
138–139
Multiphase chemical reactions,
149
QSPR methodology, hazardous materials risk evaluation by,
378–383, 379f
material failure
atomistic level description,
331, 332f
characteristic length scales,
328, 328f
model predictive control,
371
Multivariate statistical analyses
continuous process monitoring,
303
principal component analysis,
304
vs. univariate statistical analyses,
303, 303f
quantum mechanics and molecular dynamics,
193–194, 194f
Nudge elastic band (NEB),
191
Occupational Safety and Health Administration (OSHA),
398
Operator training simulator (OTS),
294–295
Polydimethylsiloxane (PDMS),
183
Polymethyl methacrylate (PMMA),
184
Premixed fires, flash fires,
19
Principal component analysis (PCA),
304
Probabilistic risk assessment (PRA)
failure modes and effects analysis (FMEA),
69–70
Process control, multiscale modeling approach in,
366–371, 367f
model predictive control,
371
Process safety,
challenges and opportunities,
92–102
communication, lack of,
102
consequence-based approaches, deficiencies in,
93–94
explosion consequence modeling,
94
leading indicators, importance to,
101–102
probability-based approaches, disadvantages of,
93
protection analysis, layer of,
95–96
qualitative and semiquantitative techniques, disadvantages of,
95–96
deflagration and detonation,
21, 22f
fire risk analysis (FRA),
19–20
gases and vapors, flammability limits of,
7–9
present approach to,
60–82
consequence based approaches,
72–74
qualitative and semi-quantitative approaches,
74–82
quantitative risk analysis (QRA),
63
concentration fluctuations,
54
particle classification,
42–43
correlation-based model development,
122
geometry optimization,
121
Qualitative/semi-quantitative approaches,
74–82
Chernobyl Nuclear Power Plant,
87–88
current regulations,
84–85
Dow Fire and Explosion Index (DF&EI),
82, 83f–84f
hazards and operability (HAZOP),
79–80, 81f
layer of protection analysis (LOPA),
76–77, 76f
major industrial incidents, characteristics of,
91, 91f
St. Herblain disaster,
88
Quantitative risk analysis (QRA)
Quantitative structure–activity relationship (QSAR),
, 397–400
correlation-based model development,
122
geometry optimization,
121
correlation-based model development,
122
geometry optimization,
121
molecular descriptors,
380
statistical evaluation,
381
first principle-based approaches,
169–174
macroscale modeling approaches,
168
practical considerations,
174
Reactive empirical bond-order (REBO),
182
Reactive molecular dynamic (RMD),
182
Reactive system screening tool (RSST),
176
Regional modeling system for aerosol and deposition (REMSAD),
144
Reynolds-averaged Navier–Stokes (RANS) equations,
234
Risk assessment
methodology in
barrier identification,
62
barrier performance analysis,
62–63
hazards identification,
62
risk characterization,
63
teams and information required for,
63
quantitative risk assessment (QRA),
63
Soot-band emission assumption,
218
Specific target organ toxicity-repeated exposure (STOT-RE),
400
Specific target organ toxicity-single exposure (STOT-SE),
400
Superheating energy (SE),
31
macroscale modeling approaches,
176–179
molecular dynamics simulations,
182–185
molecular modeling approaches,
179–185
practical considerations,
185
Topochemical indices (TCIs),
400
Topostructural indices (TSIs),
400
Total erythema score (TES),
400
Toxic effects
emergency exposure guidance levels (EEGL),
48
emergency response planning guidelines (ERPGs),
48
immediately dangerous to life or health (IDLH),
48
permissible exposure limits (PEL),
49
toxicity dispersion (TXDS),
49
Toxicity assessment,
45–46
Transition state theory (TST),
170–171
Upper flammability limit (UFL),
7–8, 228
Upper oxygen limit (UOL),
Vapor cloud explosion,
238
published validation studies,
241–242
Variational transition state theory (VTST),
418
first principle calculations,
190–191
multiscale modeling techniques,
190–191
Weibull distribution,
313