Page 757 - Dust Explosions in the Process Industries
P. 757

710  Index

            Flame propagation (continued)           Grain dust
              turbulent, 325-367                      experiments, 306,393,420
                acceleration, 351-363                 explosions
                in closed vessels, 332-341              Iowa (1980), 169-171
                models, 325-329,363-367                 Kambo (1976), 163-165
                overview, 330-3 32                      Minnesota (1980), 168-169
                research, 600-602,604606                Missouri (1980), 166-167
                safe gap for dust clouds, 346-351       Oslo (1976), 165, 166
                systematic comparative studies, 344-346   Oslo (1987), 165, 166
                in unconfined geometries, 341-344       recent, 25
              zero gravity conditions, theory of, 284-287   Stavanger (1970), 160-162
            Flame stability systems, 385, 387, 388      Stavanger (1988), 162-163
            Flame stretch phenomena, 598                Texas (1981), 171-172
            Flame types                               literature survey, 133-134
              Nusselt, 268                            use of liquid additives, 114-115
              in premixed gas, 268-270              Grewer-furnaceflammability test, 496
              volatile, 268                         Gruber et al. venting theory, 463-464
            Flameproof enclosures, 567-568,576      Gutterman and Ranz gas velocity gradient,
            Flammability                                  225-226
              data, 685
              tests, 493-498
            Flexible big bags, 617-618
            Flour dusts                             Halons (as suppressants), 106, 108
                                                    Harmonized gas and dust standards, 550,551,
              explosion in Turin (1785), 157-160
              literature survey, 133-134                  556,565,567
            Fluidized bed experiments, 226,268, 280,465, 602   Hartmann apparatushomb
                                                      American Society for Testing and Materials
            Frank-Kamenetskii’sconstant, 386, 389,390,    and, 535
                  397,402
            Friction                                  bag filters experiments and, 450
                                                      closed vessels laboratory tests and, 534,535
              definition, 14
              as hazard, 13                           description of, 241
              as ignition source, 592                 dispersion air valve, 336
              tests, 515                              dispersion system of, 480,481
              wall, 355                               dust concentrationand, 35,36, 243, 308
            “Friction sparks,” 13,64,419,515, 592     dust explosion venting and, 460,461
            Frictional heat, 60                       explosibility tests and, 489
                                                      explosion pressure, 337
                                                      explosion violence and, 638
            Galleries, experiments in, 367-369        fixed vent ratio and, 431
            Gas explosions                            laboratory test, 526-529
              risks from heated dust, 490492          laminar flame propagation in closed vessels
              smoldering, 12                              theories and, 296,297
                Malmo (1989), 181-182,  183           oxygen content in atmosphere,541
                Stavanger (1985), 177-178             particle size and, 30, 31, 33, 34
                Tomylovo (1987-1989),  178-180        Rust method and, 437
              turbulent studies, 344-346              tests, 336,433
            Gas flow, turbulent, 234-239              turbulent dust flames in closed vessels studies
            Gas inerting systems, 68-69                   and, 334,337
              for aluminum and magnesium powder or dust,   vent sizing methods and, 434,450
                  139                               Haswell coal mine explosion, 20-21,256
              partial, 69                           Hazard analysis/surveys, 124-127
            Gaseous product generation risk, 491      classificationsystem, 543
            Gases versus dusts, 550-551               minimum mass of dust, 621-622
            German and Swiss closed bombs, 521        reduction possibilities, 61-62,67-68
            Glow temperature, 684                     research, 610-611,634
            Godbert-Greenwaldfurnace, 424,425,426,   Hazard and Operability Studies (HAZOP), 124,
                  499-501,504,541                         125
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