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f <br /> EXPLOSIONS 921-85� ';"- <br /> Table 13-8 Combustion Properties of Common Flammable Gases <br /> .1 071. Limits of <br /> Flammability <br /> Percent by Air Needed Air Needed <br /> Btu Volume in Air Specific to Burn to Burn Ignition Temp <br /> per 113 MJ/m3 Gravity 1 ft;of Gas 1 m3 of Gas <br /> Gas (gross) (gross) Lower Upper (air = 1.0) (ft) (m3) °F °C <br /> Natural gas <br /> High inert type' 958-1051 35.7-39.2 4.5 14.0 0.660-0.708 9.2 9.2 - - <br /> High methane type 1008-1071 37.6-39.9 4.7 15.0 0.590-0.614 10.2 10.2 900-1170 482-632 <br /> High Btu type` 1071-1124 39.9-41.9 4.7 14.5 0.620-0.719 9.4 9.4 - - <br /> Blast furnace gas 81-111 3.0-4.1 32.2 71.3 1.04-1.00 0.8 0.8 <br /> Coke oven gas 575 21.4 4.4 34.0 0.38 4.7 4.7 - - <br /> Propane (commercial) 2516 93.7 2.15 9.6 1.52 24.0 24.0 01-100 ' 493-604 <br /> (k.,.' Butane (commercial) 3300 122.9 1.9 8.5 2.0 31.0 31.0 900-1000 482-538 <br /> Sewage gas 670 24.9 6.0 17.0 0.79 6.5 6.5 - - <br /> Acetylenei 1499 208.1 2.5 81.0 0.91 11.9 11.9 581 305 <br /> Hydrogen 325 12.1 4.0 75.0 0.07 2.4 2.4 932 500 ' <br /> Anhydrous ammonia 386 14.4 16.0 25.0 0.60 8.3 8.3 1204 651 <br /> Carbon monoxide 314 11.7 12.5 74.0 0.97 2.4 2.4 1128 609 <br /> ethylene 1600 59.6 2.7 36.0 0.98 14.3 14.3 914 490 <br /> Methyl acetylene, 2450 91.3 3.4 10.8 1.48 - - 850 454 <br /> propadiene,stabilized`[ <br /> 'Typical composition C114 71.9-83.2%;N2 6.3-16.20% <br /> ['Typical composition (''114 87.6-95.79o;N2 0.1-2.39% <br /> `Typical composition CH4 85.0-90.1%;N2 1.2-7.5% <br /> dMAPP®Gas from the NFPA Fire Protection Handbook, l7th edition,Table 3-7C <br /> does not burn until it is mixed with air during the explosion's A natural gas leak in the first story of a multistory structure <br /> venting phase or negative pressure phase, thereby producing may well be manifested in an explosion with an epicenter in <br /> the characteristic following fire. an upper story. The natural gas, being lighter than air, will <br /> When optimum (i.e., most violent) explosions occur, it is have a tendency to rise through natural openings and may <br /> almost always at mixtures near or just above the stoichiometric even migrate inside walls. The gas will continue to disperse <br /> mixture (i.e.,slightly fuel rich).This is the optimum mixture. in the structure until an ignition source is encountered. <br /> These mixtures produce the most efficient combustion and, An LP-Gas leak on the first story of a house, if it is not,. <br /> therefore, the highest flame speeds, rates of pressure rise, ignited there, can travel away from the source and,due to its <br /> maximum pressures,and consequently the most damage.Post- density, will tend to migrate downward. The gas may collect ,- <br /> explosion fires can occur if there are pockets of overly rich in lower areas of the house and concentrate.. <br /> mixture. Ignition of the gas will only occur if the concentration is <br /> For common lighter-than-air gases in residential buildings, within the flammable limits and in contact with a competent <br /> an explosion involving an optimum concentration will some- ignition source (one with enough energy). <br /> times result in some destructive shattering effects of wooden Whether lighter-or heavier-than-air gases are involved,there[ <br /> structural materials. may be evidence of the passage of flame where the fuel air <br /> layer was.Scorching,blistering of paintwork,and showing of <br /> 13-8.2.2* Vapor Density. The vapor density of the gas or "tidemarks" are indicators of this type of phenomena The: <br /> ~ vapor fuel can have a marked effect on the nature of the operation of heating and air-conditioning systems,temper;( <br /> explosion damage to the confining structure.This is especially ture gradients,and the effects of wind on a building can cause <br /> true in dwellings and other buildings. mixing and movement that can reduce the effects,of vapof <br /> I leavier-than-air gases and vapors(i.e.,vapor density greater density.Vapor density effects are greatest in still-air conditions,: <br /> than 1.0), such as from ignitible liquids and LP-Gases, tend Full-scale testing of the distribution of flammable gas cone, <br /> to settle to lower areas.Lighter-than-air gases,such as natural centrations in rooms has shown that near stoichiometric coh' <br /> gas,tend to rise and collect in upper areas.For example,signs centrations of gas wou'dc <br /> d dev the location of tht< <br /> of postblast burning in pocketed areas between ceiling joists leak and either(1) the cel an-air gases or(2)11;' <br /> may be indicative of a lighter-than-air fuel rather than heavier- the floor for heavier-thar3' so reported that <br /> than-air gases or vapors.(See 4-17.9.)Due to their higher mobil- a heavier-than-air gas tha. evel would create <br /> ity and tendency to escape upward, lighter-than-air gases are a greater concentration at the gas would. <br /> less likely to produce hazardous situations than heavier-than- slowly diffuse upward. t e relationship is' <br /> air gases, which can pool in basements, crawl spaces, wells, true for a lighter-than-air g height.VentilaL: <br /> and tanks.' tion,both natural and mechanical,can ch'atige the movement <br /> 1998 Edltlo y, <br /> a , <br />