Index

Note: ‘Page numbers followed by “f” indicate figures, “t” indicate tables’.
A
Aerosol formation, 144–149, 145f
atomistic simulation-based approaches, 148–149
practical considerations, 149
Atmospheric interest
aim, 422
context, 421
general methodology, 422
Autoignition temperature (AIT), 7
Automatic pressure tracking adiabatic calorimeter (APTAC), 176
B
Boiling liquid expanding vapor explosion (BLEVE), 16–17, 221, 243–245
Brode’s equation, 24
C
Calculated adiabatic reaction temperature (CART), 156
Carcinogen, 398
Chaos theory techniques
runaway reaction
continuous real-time evaluation, 301
infinitesimal volume V, 302, 302f
Lyapunov exponent, 301
parametric sensitivity, 300
protection and prevention, 298–300
warning detection system, 298–300
Chemical Engineering Thermodynamics and Hazard Evaluation (CHETAH), 157–159, 164–166
Chemical equilibrium, 129–131
Computational fluid dynamics (CFD), 2
application, 262–267
dispersion of flammable gases
CFD codes, 237, 237t
geometry representation, 230–231, 231f
parameters, 229, 229f
published validation dispersion, 235–237, 236f–237f
simulated flammable materials, types, 231–232
source models, 232
turbulent model, 234–235, 234f
UFL and LFL, 228, 228f
erosion/corrosion, 376–378, 377f
explosion modeling, 238
BLEVE, 243–245
dust explosion, 249–254
vapor cloud explosion, 238–242
fire modeling, 214–215
CFD codes, 220, 220t
combustion model, 216–217
fires, types, 214
fuel source, 219
geometry representation, 215
jet fires, 221–225
pool fires, 225–227
radiation model, 217–219
radiative probit function, 219–220
soot formation model, 219
turbulent model, 215–216
preprocessor, 211, 212f
QRA
application, 353–366
temporal and spatial scales, 211, 212t
toxic dispersion/HVAC design
CFD codes, 237t, 262
CFD data, probit function, 258–259
dispersion, 254–255
geometry representation, 256–257
published validation studies, 259–262
research, 254
source model, 257–258
toxic materials, 258
turbulence model, 257
transport equation and physical models, 212, 212f, 213t
Computational model, 138
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
Cool flames, 132
COSMO theory, 129–130
Coupling of length scales (CLS), 407
Critical adiabatic flame temperature (CAFT), 126–127
D
Deflagration to detonation transition (DDT), 21, 246–249
Density functional theory, 115–116, 121
Design Institute for Emergency Relief Systems (DIERS), 296–297
Differential algebraic equations (DAE), 290–291
Diffusion fires
fireballs, 16–17
jet fires, 9–11
natural fires, 11–12
pool fires, 12–16
Discrete transfer method, 218
Dispersion of flammable gases
CFD codes, 237, 237t
geometry representation, 230–231, 231f
parameters, 229, 229f
simulated flammable materials, types, 231–232
source models, 232
turbulent model, 234–235, 234f
UFL and LFL, 228, 228f
validation dispersion, 235–237, 236f–237f
Dust explosion, 32–37, 33f, 186–188, 249
combustion model, 250–251
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
published CFD studies, 251–254
turbulence model, 250
Dynamic operator training simulator (DOTS), 294–295
Dynamic simulation
blowdown studies, 296–298
depressurization, 296–298
HAZOP, 292–294
operator training, 294–295, 294f, 296f
E
Eddy break-up model, 217
Equipment failure
bathtub curve, 309, 310f
Bayesian logic
application, 319–321
die roll example, 318, 319t
expert judgment, 317
generic data, 316–317
plant-specific data, 316–317
sources of generic data, 321
expert judgment, 311
exponential distribution, 311
failure rates without failure, 315–316
frequentist, 310–311
gamma distribution, 311–313
liquefied natural gas, risk assessment
applications, 322
LOPA, 322
methodology development, 322–324
lognormal distribution, 314–315
mean time to failure, 311
multiscale models, 327
corrosion, 333–336
material failure, 328–333
normal distribution, 314
probabilistic models, 310
subjectivist, 310–311
Weibull distribution, 313
ERPG, 258
Explosion
prevention, 37–41
inerting, See Inerting
types, 25–37
boiling liquid expanding vapor explosion (BLEVE), 27–32, 29f–30f, 32f
dust explosion, 32–37, 33f
vapor cloud explosion (VCE), 26–27
Explosion energy
chemical explosions, 22–24
mechanical explosions, 24–25
Brode’s equation, 24
isentropic expansion, 24–25
isothermal expansion, 25
thermodynamic availability, 25
Explosion modeling, CFD, 238
BLEVE, 243–245
dust explosion, 249–254
vapor cloud explosion, 238–242
Explosive decomposition reaction
aim, 416
context, 416
general methodology, 416–418
Exponential distribution, 311
F
Facility siting studies
mathematical formulation, 341–342, 341t, 342f
objective function, 343
problem description, 340–341
results, 344
risk-related equations, 343
weather conditions, Monte Carlo simulation of, 343–344
Fiber damage, 284
Finite element analysis (FEA)
algebraic equation, 276, 277f
damage detection, 283–284
dispersion modeling, 286–287, 287f
heat release rate, 285–286, 286f
irregular mesh, 276, 277f
meshing, 275–276, 276f
storage and transportation, 281–283, 282f–283f
thermomechanical response of structures
composite material, 279, 280f
flame–wall interactions, 278
total strain, 278, 278f
Young’s modulus, 279, 280f
Fire
fire risk analysis (FRA), 19–20
types, 9–19, 214
diffusion fires, See Diffusion fires
premixed fires, See Premixed fires
Fire hazard analysis (FHA), 19
Fire modeling, CFD, 214–215
CFD codes, 220, 220t
combustion model, 216–217
fires, types, 214
fuel source, 219
geometry representation, 215
jet fires, 221–225
pool fire, 225–227
radiation model, 217–219
radiative probit function, 219–220
soot formation model, 219
turbulent model, 215–216
FLACS, 232
Flammability limits, 125–135, 126t
chemical equilibrium, 129–131
first principle calculations, 128–129
Flash point, 135–144, 137t, 139f
first principle-based approaches, 140–143, 140f
practical considerations, 143–144
Flux method, 218
Force field, 183–184
Froude number, 13
Fuel-rich core, 12
G
Gamma distribution, 311–313
Gas dispersion, 53–54
computational fluid dynamics, 53–54
integral models, 53
shallow layer models, 53
workbooks/correlations, 53
Gray gas assumption, 218
H
Hartree-Fock (HF) method, 115
Hazard and operability study (HAZOP), 292–294
Heat of formation, 155–167
choosing descriptors, 162–163, 163f
first principle-based approaches, 163–166, 165t
macroscale modeling approaches, 156–157
molecular group activity, 157–162, 158f, 159t, 160f
practical considerations, 166–167
Heat of reaction, 155–167
choosing descriptors, 162–163, 163f
first principle-based approaches, 163–166, 165t
macroscale modeling approaches, 156–157
molecular group activity, 157–162, 158f, 159t, 160f
practical considerations, 166–167
Highest occupied molecular orbital (HOMO), 116
Hydroxylamine, 179, 179f
I
Inerting
combined pressure–vacuum purging, 39–40, 40f
controlling static electricity, 41
pressure purging, 39, 39f
sweep-through purging, 40
vacuum purging, 38, 38f
ventilation, 41
Inherently safer design (ISD)
material design, multiscale modeling approach in, 372–383
corrosion prediction, 372–378
erosion/corrosion, CFD modeling of, 376–378, 377f
QSPR methodology, hazardous materials risk evaluation by, 378–383, 379f
tribo-corrosion, 373–376, 374f–375f
mesoscale reactor design, 384–392
improve process safety, advantages to, 384–386
potential processes for, 386–387, 387f–388f
techniques needed for, 387–392, 388f–391f
Monte Carlo methods application, 339–352
facility siting studies, See Facility siting studies
reliability engineering, 346–352
transportation safety, 344–346, 346f–347f
process control, multiscale modeling approach in, 366–371, 367f
control strategies, 371
kinetic Monte Carlo methods, 370–371, 370f
model building, 368, 368f
model predictive control, 371
model reduction, 369–370, 369t
quantitative risk analysis
CFD application, 353–366, 353f
Integrated multi-scale approaches, 408f, 409
Interfacial damage, 284
Isentropic expansion, 24–25
Isothermal expansion, 25
J
Jet fires, 221f, 223f
CFD codes, 221–223
gas phase jet fires, 221
hazards, 221
heat loads, 224, 225f
jet deflection, 223, 224f
jet impingement, 224, 225f
radiative heat flux iso-surface, 222f
K
Kinetic Monte Carlo methods, 370–371, 370f
Kinetic parameters prediction, 418
KisTHelP, 172, 173f
L
Lead dioxide, 414–415
Liquefied natural gas (LNG)
applications, 322
LOPA, 322
methodology development
Bayesian–LOPA method, 323, 323f
HAZOP, 322–323
independent protection layer, 324, 325f
initiating events, 326f
LOPA incident scenarios, 324, 327t
NFPA 59A and EN 1473, 323–324
Lower flammability limit (LFL), 228, 411
Lower oxygen limit (LOL), 8
Lowest unoccupied molecular orbital (LUMO), 116
Lumping various modeling, 125
M
Material design, 372–383
corrosion prediction, 372–378
erosion/corrosion, CFD modeling of, 376–378, 377f
QSPR methodology, hazardous materials risk evaluation by, 378–383, 379f
tribo-corrosion, 373–376, 374f–375f
Matrix damage, 284
Meshing, 275–276
Mesoscale reactor design, 384–392
improve process safety, advantages to, 384–386
potential processes for, 386–387, 387f–388f
techniques needed for, 387–392, 388f–391f
Minimum energy path (MEP), 169
Minimum flash point behavior (MFPB), 135–136
Minimum ignition energy (MIE), 6
Modeling and Experimental Research into Gas Explosions (MERGE), 241
Molecular dynamics–based model, 415
Molecular modeling, 407–408
aerosol formation, 144–149, 145f
atomistic simulation-based approaches, 148–149
practical considerations, 149
atomistic simulation-based approaches, 148–149
dust explosion, 186–188
practical considerations, 188
flammability limits, 125–135, 126t
chemical equilibrium, 129–131
first principle calculations, 128–129
flash point, 135–144, 137t, 139f
first principle-based approaches, 140–143, 140f
practical considerations, 143–144
heat of reaction/heat of formation, 155–167
choosing descriptors, 162–163, 163f
first principle-based approaches, 163–166, 165t
macroscale modeling approaches, 156–157
molecular group activity, 157–162, 158f, 159t, 160f
practical considerations, 166–167
molecular dynamics, 122–124, 124t
nanotoxicity, 192–195, 193f
challenges, 192–193
QSAR/QSPR, 194–195, 195f
quantum mechanics and molecular dynamics, 193–194, 194f
practical considerations, 131–135
composition effect, 132
pressure effects, 133–135, 134f
temperature effects, 133, 133f
QSPR/QSAR, 118–122, 119f
correlation-based model development, 122
data set, 120–121
geometry optimization, 121
molecular descriptors, 121–122
quantum mechanics/ab initio approaches, 114–117, 116f, 117t
reaction rate, 167–174, 167t
first principle-based approaches, 169–174
fun fact, 168
macroscale modeling approaches, 168
practical considerations, 174
transition state theory, 169–174, 170f–171f
reactive hazards, 150–155, 151t, 152f
reactivity hazard assessment criterion, 153–155, 153t
thermal runaway reactions, 174–185
first principle calculations, 179–182, 179f
macroscale modeling approaches, 176–179
molecular dynamics simulations, 182–185
molecular modeling approaches, 179–185
parametric sensitivity, 176–179, 177f–178f
practical considerations, 185
water reactive chemicals, 188–191
approaches, 189
challenges, 189–190
first principle calculations, 190–191
multiscale modeling techniques, 190–191
Moller-Plesset fourth order (MP4), 128
Monte Carlo methods application, 339–352
facility siting studies, See Facility siting studies
reliability engineering, 346–352
transportation safety, 344–346, 346f–347f
Multi-CASE program, 404
Multilinear regression (MLR), 138–139
Multiphase chemical reactions, 149
Multiscale models, 1–2, 327
corrosion, 333–336
material design, 372–383
corrosion prediction, 372–378
erosion/corrosion, CFD modeling of, 376–378, 377f
QSPR methodology, hazardous materials risk evaluation by, 378–383, 379f
tribo-corrosion, 373–376, 374f–375f
material failure
atomistic level description, 331, 332f
characteristic length scales, 328, 328f
crack propagation dynamics, 331–332, 333f
crystal deformation, 330, 331f
energy density, 329–330
energy-strain curve, 328–329, 329f
process control, 366–371, 367f
control strategies, 371
kinetic Monte Carlo methods, 370–371, 370f
model building, 368, 368f
model predictive control, 371
model reduction, 369–370, 369t
Multivariate statistical analyses
classification, 304
continuous process monitoring, 303
principal component analysis, 304
vs. univariate statistical analyses, 303, 303f
Mutation, 398
N
Nanotoxicity, 192–195, 193f
challenges, 192–193
QSAR/QSPR, 194–195, 195f
quantum mechanics and molecular dynamics, 193–194, 194f
Nudge elastic band (NEB), 191
O
Occupational Safety and Health Administration (OSHA), 398
Operator training simulator (OTS), 294–295
P
Polydimethylsiloxane (PDMS), 183
Polymethyl methacrylate (PMMA), 184
POLYRATE, 172
Pool fire, 225–227
Premixed fires, flash fires, 19
Principal component analysis (PCA), 304
Probabilistic risk assessment (PRA)
Bayesian networks, 70–72, 70f
bow-tie plots, 69, 69f
event tree analysis, 66–69, 68f
failure modes and effects analysis (FMEA), 69–70
fault tree analysis, 65–66, 67f
Process control, multiscale modeling approach in, 366–371, 367f
control strategies, 371
kinetic Monte Carlo methods, 370–371, 370f
model building, 368, 368f
model predictive control, 371
model reduction, 369–370, 369t
Process safety, 2
challenges and future, 82–103
challenges and opportunities, 92–102
communication, lack of, 102
consequence-based approaches, deficiencies in, 93–94
explosion consequence modeling, 94
HAZOP approach, 96
inherently safer design (ISD), 96–101, 96f
leading indicators, importance to, 101–102
organizations, 92–93, 92t
probability-based approaches, disadvantages of, 93
protection analysis, layer of, 95–96
qualitative and semiquantitative techniques, disadvantages of, 95–96
explosion, 20–41, 21t
deflagration and detonation, 21, 22f
explosion energy, See Explosion energy
types, See Explosion, types
fire, 5–20
fire risk analysis (FRA), 19–20
gases and vapors, flammability limits of, 7–9
ignition phenomena, 6–7
triangle, 5–6, 6f
types, 9–19
present approach to, 60–82
consequence based approaches, 72–74
probabilistic risk assessment (PRA), See Probabilistic risk assessment (PRA)
qualitative and semi-quantitative approaches, 74–82
quantitative risk analysis (QRA), 63
risk and hazard, 60–62
risk assessment, methodology in, See Risk assessment, methodology in
scalability, 64
toxic effects, 41–59
computer aids, 59, 60t
concentration fluctuations, 54
gas dispersion, See Gas dispersion
hazard assessment methodology, 49, 50t–51t
hygiene standards, 47–49, 47t
organism, 42, 43f
particle classification, 42–43
plant layout, 58–59, 59t
risk assessment, 46–47
source term, 51, 52f
terrain/barriers/sprays/shelter and evacuation, 54–57, 55f, 56t–58t
toxicity assessment, See Toxicity assessment
toxic substances, 44–45
Q
QSPR/QSAR, 118–122, 119f
correlation-based model development, 122
data set, 120–121
geometry optimization, 121
molecular descriptors, 121–122
Qualitative/semi-quantitative approaches, 74–82
Bhopal disaster, 86–87
Buncefield disaster, 89–90, 90f
checklist, 82
Chernobyl Nuclear Power Plant, 87–88
current regulations, 84–85
Dow Fire and Explosion Index (DF&EI), 82, 83f–84f
Flixborough disaster, 86
Fukushima disaster, 90
hazards and operability (HAZOP), 79–80, 81f
layer of protection analysis (LOPA), 76–77, 76f
major industrial incidents, characteristics of, 91, 91f
Naples disaster, 87
Piper Alpha disaster, 88
risk matrix, 77–78, 77f–79f
Seveso disaster, 86
St. Herblain disaster, 88
Texas city disaster, 89
Warffum disaster, 89
what-if analysis, 80
Quantitative risk analysis (QRA)
CFD application, 353–366, 353f
Quantitative structure–activity relationship (QSAR), 2, 397–400
case studies, 400–404
acute toxicity (LC50), 400–401
eye irritation, 403–404, 404t
skin irritation and corrosivity, 401–403, 402f–403f
correlation-based model development, 122
data set, 120–121
geometry optimization, 121
industrial hygiene, 397–400
molecular descriptors, 121–122
Quantitative structure–property relationship (QSPR), 2, 187–188, 378–383, 379f
correlation-based model development, 122
data set, 120–121
geometry optimization, 121
hazardous materials risk evaluation by, 378–383, 379f
data preprocessing, 380
flash point, 381–383, 382f–383f
molecular descriptors, 380
multivariate analysis, 380–381
statistical evaluation, 381
molecular descriptors, 121–122
R
Radiant heating, 15
Reaction heat, 418
Reaction rate, 167–174, 167t
first principle-based approaches, 169–174
fun fact, 168
macroscale modeling approaches, 168
practical considerations, 174
transition state theory, 169–174, 170f–171f
Reactive chemicals, 150
Reactive empirical bond-order (REBO), 182
Reactive hazards, 150–155, 151t, 152f
reactivity hazard assessment criterion, 153–155, 153t
Reactive molecular dynamic (RMD), 182
Reactive system screening tool (RSST), 176
ReaxFF, 182–183
Regional modeling system for aerosol and deposition (REMSAD), 144
Reliability engineering, 346–352
applications, 350, 350f, 350t–351t
example, 348–349, 349f, 349t
features, 351–352, 351f
number of trials, 352, 353t
Reynolds-averaged Navier–Stokes (RANS) equations, 234
Reynolds number, 9–10
Risk assessment
methodology in
barrier identification, 62
barrier performance analysis, 62–63
exposure assessment, 63
hazards identification, 62
nodes in, 63
risk characterization, 63
teams and information required for, 63
quantitative risk assessment (QRA), 63
scalability, 64
S
Soot-band emission assumption, 218
Specific target organ toxicity-repeated exposure (STOT-RE), 400
Specific target organ toxicity-single exposure (STOT-SE), 400
Strouhal number, 14
Superheating energy (SE), 31
T
Thermal runaway reactions, 174–185
first principle calculations, 179–182, 179f
macroscale modeling approaches, 176–179
molecular dynamics simulations, 182–185
molecular modeling approaches, 179–185
parametric sensitivity, 176–179, 177f–178f
practical considerations, 185
Topochemical indices (TCIs), 400
Topostructural indices (TSIs), 400
Total erythema score (TES), 400
Toxic effects
hygiene standards, 47–49, 47t
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
RMP, 49
toxicity dispersion (TXDS), 49
Toxicity assessment, 45–46
cancer effect, 46
noncancer effect, 45–46
Transition state theory (TST), 170–171
Tribo-corrosion, 373–376, 374f–375f
U
Upper flammability limit (UFL), 7–8, 228
Upper oxygen limit (UOL), 8
V
Vapor cloud explosion, 238
CFD codes, 242, 243t
combustion model, 240–241
geometry representation, 238–240
published validation studies, 241–242
turbulence model, 240
Variational transition state theory (VTST), 418
W
Water reactive chemicals, 188–191
approaches, 189
challenges, 189–190
first principle calculations, 190–191
multiscale modeling techniques, 190–191
Weibull distribution, 313


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