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Flammability limit

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Flammability limits, also called flammable limits, give the proportion of combustible gases in a mixture, between which limits this mixture is flammable. Gas mixtures consisting of combustible, oxidizing, and inert gases are only flammable under certain conditions. The lower flammable limit (LFL) describes the leanest mixture that still sustains a flame, i.e. the mixture with the smallest fraction of combustible gas, while the upper flammable limit (UFL) gives the richest flammable mixture.

There is a quantitative difference between flammability limits and explosive limits. In an explosive mixture the fuel oxidizer mixture is closer to stoichiometric proportion. This difference has no practical application in safety engineering as the flammable vapor cloud is turbulent and the exact mixture of fuel and oxidizer varies greatly. Therefore, many references use the term flammability limit (LFL, UFL) and explosive limit (LEL, UEL) interchangeably.

Attaining the perfect combustible or explosive mixture between a fuel and air is important in internal combustion engines, for example in gasoline or diesel engines.

A deflagration is a propagation of a combustion zone at a velocity less than the speed of sound in the unreacted medium. A detonation is a propagation of a combustion zone at a velocity greater than the speed of sound in the unreacted medium. An explosion is the bursting or rupture of an enclosure or container due to the development of internal pressure from a deflagration or detonation as defined in NFPA 69.

NFPA 72 regulation about the Instrument & Electrical Installation for Fire & Gas Detector. As Instrument Engineer considered type of Fire & Gas Detector with process plant, such as Compressor plant, Loading Bay plant, and other plant to potential vaporizer of gas.

Limits

Lower Explosive Limit

Lower Explosive Limit (LEL): The lowest concentration (percentage) of a gas or a vapor in air capable of producing a flash of fire in presence of an ignition source (arc, flame, heat). At a concentration in air below the LEL there is not enough fuel to continue an explosion. Concentrations lower than the LEL are "too lean" to explode but may still deflagrate. Methane gas has a LEL of 4.4% (at 138 degrees C) by volume, meaning 4.4% of the total volume of the air consists of methane. At 20 degrees C the LEL is 5.1% by volume. If the atmosphere has less than 5.1% methane, an explosion cannot occur even if a source of ignition is present. When methane (CH
4) concentration reaches 5.1% an explosion can occur if there is an ignition source. LEL concentrations vary greatly between combustible gases.

Percentage reading on combustible air monitors should not be confused with the LEL concentrations. Explosimeters designed and calibrated to a specific gas may show the relative concentration of the atmosphere to the LEL—the LEL being 100%. A 5% displayed LEL reading for methane, for example, would be equivalent to 5.1% multiplied by 5%, or approximately 0.25% methane by volume at 20 degrees C. Control of the explosion hazard is usually achieved by sufficient natural or mechanical ventilation, to limit the concentration of flammable gases or vapors to a maximum level of 25% of their Lower Explosive or Flammable Limit.

Upper Explosive Limit

Upper Explosive Limit (UEL): Highest concentration (percentage) of a gas or a vapor in air capable of producing a flash of fire in presence of an ignition source (arc, flame, heat). Concentration higher than UFL or UEL are "too rich" to burn.

Influence of temperature, pressure and composition

Flammability limits of mixtures of several combustible gases can be calculated using Le Chatelier's mixing rule for combustible volume fractions xi:

and similar for UEL.

Temperature, pressure, and the concentration of the oxidizer also influences flammability limits. Higher temperature results in lower LFL and higher UFL, while greater pressure increases both values. The effect of pressure is very small at pressures below 10 millibar and difficult to predict, since it has only been studied in internal combustion engines with a turbocharger.

Oxygen enriched atmospheres lower the LFL and increase the UFL. An atmosphere devoid of an oxidizer is neither flammable or explosive regardless of the fuel gas concentration. Increasing the fraction of inert gases in an air mixture raises the LFL and decreases the UFL.

Controlling explosive atmospheres

Controlling gas and vapor concentrations outside the explosive limits is a major consideration in occupational safety and health. Methods used to control the concentration of a potentially explosive gas or vapor include use of sweep gas, an unreactive gas such as nitrogen or argon to dilute the explosive gas before coming in contact with air. Use of scrubbers or adsorption resins to remove explosive gases before release are also common. Gases can also be maintained safely at concentrations above the UEL, although a breach in the storage container can lead to explosive conditions or intense fires.

Dusts

Dusts also have upper and lower explosion limits, though the upper limits are hard to measure and of little practical importance. Lower explosive limits for many organic materials are in the range of 10–50 g/m³, which is much higher than the limits set for health reasons, as is the case for the LEL of many gases and vapours. Dust clouds of this concentration are hard to see through for more than a short distance, and normally only exist inside process equipment.

Explosion limits also depend on the particle size of the dust involved, and are not intrinsic properties of the material. In addition, a concentration above the LEL can be created suddenly from settled dust accumulations, so management by routine monitoring, as is done with gases and vapours, is of no value. The preferred method of managing combustible dust is by preventing accumulations of settled dust through process enclosure, ventilation, and surface cleaning. However, lower explosion limits may be relevant to plant design.

Examples

The flammable/explosive limits of some gases and vapors are given below. Concentrations are given in percent by volume of air.

  • Class IA liquids (Flash Point less than 73 °F (22.8 °C); Boiling Point less than 100 °F (37.8 °C) are NFPA 704 Flammability Rating 4
  • Classes IB (Flash Point less than 73 °F (22.8 °C); Boiling Point equal to or greater than 100 °F (37.8 °C)) and IC liquids (Flash Point equal to or greater than 73 °F (22.8 °C), but less than 100 °F (37.8 °C)) are NFPA 704 Flammability Rating 3
  • Classes II (Flash Point equal to or greater than 100 °F (37.8 °C), but less than 140 °F (60 °C) and IIIA liquids (Flash Point equal to or greater than 140 °F (60 °C), but less than 200 °F (93.3 °C)) are NFPA 704 Flammability Rating 2
  • Class IIIB liquids (Flash Point equal to or greater than 200 °F (93.3 °C) are NFPA 704 Flammability Rating 1
Substance LFL/LEL in %

by volume of air

UFL/UEL in %

by volume of air

NFPA Class Flash point Minimum Ignition Energy in mJ

expressed as percent by volume in air 

(Note, for many chemicals it

takes the least amount of 

ignition energy midpoint between 

the LEL and UEL.)[1]
Autoignition
Temperature
Acetaldehyde 4.0 57.0 IA -39 °C 0.37 175 °C
Acetic acid (glacial) 4 19.9 II 39 °C to 43 °C 463 °C
Acetic anhydride II 54 °C
Acetone 2.6–3 12.8–13 IB -17 °C 1.15 @ 4.5% 465 °C, 485 °C[2]
Acetonitrile IB 2 °C 524 °C
Acetyl chloride 7.3 19 IB 5 °C 390 °C
Acetylene 2.5 82 IA -18 °C 0.017 @ 8.5% (in pure oxygen 0.0002 @ 40%) 305 °C
Acrolein 2.8 31 IB -26 °C 0.13
Acrylonitrile 3.0 17.0 IB 0 °C 0.16 @ 9.0%
Allyl chloride 2.9 11.1 IB -32 °C 0.77
Ammonia 15 28 IIIB 11 °C 680 651 °C
Arsine 4.5–5.1[3] 78 IA Flammable gas
Benzene 1.2 7.8 IB -11 °C 0.2 @ 4.7% 560 °C
1,3-Butadiene 2.0 12 IA -85 °C 0.13 @ 5.2%
Butane, n-Butane 1.6 8.4 IA -60 °C 0.25 @ 4.7% 420–500 °C
n-Butyl acetate, Butyl acetate 1–1.7[4] 8–15 IB 24 °C 370 °C
Butyl alcohol, Butanol 1 11 IC 29 °C
n-Butanol 1.4[5] 11.2 IC 35 °C 340 °C
n-Butyl chloride, 1-chlorobutane 1.8 10.1 IB -6 °C 1.24
n-Butyl mercaptan 1.4[6] 10.2 IB 2 °C 225 °C
Butyl methyl ketone, 2-Hexanone 1[7] 8 IC 25 °C 423 °C
Butylene, 1-Butylene, 1-Butene 1.98[8] 9.65 IA -80 °C
Carbon disulfide 1.0 50.0 IB -30 °C 0.009 @ 7.8% 90 °C
Carbon Monoxide 12[9] 75 IA -191 °C Flammable gas 609 °C
Chlorine monoxide IA Flammable gas
1-Chloro-1,1-difluoroethane 6.2 17.9 IA -65 °C Flammable Gas
Cyanogen 6.0–6.6[10] 32–42.6 IA Flammable gas
Cyclobutane 1.8 11.1 IA -63.9 °C[11] 426.7 °C
Cyclohexane 1.3 7.8–8 IB -18 °C to -20 °C[12] 0.22 @ 3.8% 245 °C
Cyclohexanol 1 9 IIIA 68 °C 300 °C
Cyclohexanone 1–1.1 9–9.4 II 43.9–44 °C 420 °C[13]
Cyclopentadiene[14] IB 0 °C 0.67 640 °C
Cyclopentane 1.5–2 9.4 IB -37 to -38.9 °C[15][16] 0.54 361 °C
Cyclopropane 2.4 10.4 IA -94.4 °C[17] 0.17 @ 6.3% 498 °C
Decane 0.8 5.4 II 46.1 °C 210 °C
Diborane 0.8 88 IA -90 °C Flammable gas[18] 38 °C
o-Dichlorobenzene, 1,2-Dichlorobenzene 2[19] 9 IIIA 65 °C 648 °C
1,1-Dichloroethane 6 11 IB 14 °C
1,2-Dichloroethane 6 16 IB 13 °C 413 °C
1,1-Dichloroethene 6.5 15.5 IA -10 °C Flammable gas
Dichlorofluoromethane 54.7 Non flammable,[20] -36.1 °C[21] 552 °C
Dichloromethane, Methylene chloride 16 66 Non flammable
Dichlorosilane 4 - 4.7 96 IA -28 °C 0.015
Diesel fuel 0.6 7.5 IIIA >62 °C (143 °F) 210 °C
Diethanolamine 2 13 IB 169 °C
Diethylamine 1.8 10.1 IB -23 to -26 °C 312 °C
Diethyl disulfide 1.2 II 38.9 °C[22]
Diethyl ether 1.9–2 36–48 IA -45 °C 0.19 @ 5.1% 160–170 °C
Diethyl sulfide IB -10 °C[23]
1,1-Difluoroethane 3.7 18 IA -81.1 °C[24]
1,1-Difluoroethylene 5.5 21.3 -126.1 °C[25]
Diisobutyl ketone 1 6 49 °C
Diisopropyl ether 1 21 IB -28 °C
Dimethylamine 2.8 14.4 IA Flammable gas
1,1-Dimethylhydrazine IB
Dimethyl sulfide IA -49 °C
Dimethyl sulfoxide 2.6–3 42 IIIB 88–95 °C 215 °C
1,4-Dioxane 2 22 IB 12 °C
Epichlorohydrin 4 21 31 °C
Ethane 3[26] 12–12.4 IA Flammable gas -135 °C 515 °C
Ethanol, Ethyl Alcohol 3–3.3 19 IB 12.8 °C (55 °F) 365 °C
2-Ethoxyethanol 3 18 43 °C
2-Ethoxyethyl acetate 2 8 56 °C
Ethyl acetate 2 12 IA -4 °C 460 °C
Ethylamine 3.5 14 IA -17 °C
Ethylbenzene 1.0 7.1 15–20 °C
Ethylene 2.7 36 IA 0.07 490 °C
Ethylene glycol 3 22 111 °C
Ethylene oxide 3 100 IA −20 °C
Ethyl Chloride 3.8[27] 15.4 IA −50 °C
Ethyl Mercaptan IA
Fuel oil No.1 0.7[28] 5
Furan 2 14 IA -36 °C
Gasoline (100 Octane) 1.4 7.6 IB < −40 °C (−40 °F) 246–280 °C
Glycerol 3 19 199 °C
Heptane, n-Heptane 1.05 6.7 -4 °C 0.24 @ 3.4% 204–215 °C
Hexane, n-Hexane 1.1 7.5 -22 °C 0.24 @ 3.8% 225 °C, 233 °C[29]
Hydrogen 4/17[30] 75/56 IA Flammable gas 0.016 @ 28% (in pure oxygen 0.0012) 500–571 °C
Hydrogen sulfide 4.3 46 IA Flammable gas 0.068
Isobutane 1.8[31] 9.6 IA Flammable gas 462 °C
Isobutyl alcohol 2 11 28 °C
Isophorone 1 4 84 °C
Isopropyl alcohol, Isopropanol 2[32] 12 IB 12 °C 398–399 °C; 425 °C[33]
Isopropyl chloride IA
Kerosene Jet A-1 0.6–0.7 4.9–5 II >38 °C (100 °F) as jet fuel 210 °C
Lithium Hydride IA
2-Mercaptoethanol IIIA
Methane (Natural Gas) 4.4–5 15–17 IA Flammable gas 0.21 @ 8.5% 580 °C
Methyl acetate 3 16 -10 °C
Methyl Alcohol, Methanol 6–6.7[34] 36 IB 11 °C 385 °C; 455 °C[35]
Methylamine IA 8 °C
Methyl Chloride 10.7[36] 17.4 IA -46 °C
Methyl ether IA −41 °C
Methyl ethyl ether IA
Methyl ethyl ketone 1.8[37] 10 IB -6 °C 505–515 °C[38]
Methyl formate IA
Methyl mercaptan 3.9 21.8 IA -53 °C
Mineral spirits 0.7[39] 6.5 38–43 °C 258 °C
Morpholine 1.8 10.8 IC 31–37.7 °C 310 °C
Naphthalene 0.9[40] 5.9 IIIA 79–87 °C
Neohexane 1.19[41] 7.58 −29 °C 425 °C
Nickel tetracarbonyl 2 34 4 °C 60 °C
Nitrobenzene 2 9 IIIA 88 °C
Nitromethane 7.3 22.2 35 °C 379 °C
Octane 1 7 13 °C
iso-Octane 0.79 5.94
Pentane 1.5 7.8 IA -40 to -49 °C as 2-Pentane 0.18 @ 4.4% 260 °C
n-Pentane 1.4 7.8 IA 0.28 @ 3.3%
iso-Pentane 1.32[42] 9.16 IA 420 °C
Phosphine IA
Propane 2.1 9.5–10.1 IA Flammable gas 0.25 @ 5.2% (in pure oxygen 0.0021) 480 °C
Propyl acetate 2 8 13 °C
Propylene 2.0 11.1 IA -108 °C 0.28 458 °C
Propylene Oxide 2.3 36 IA
Pyridine 2 12 20 °C
Silane 1.5[43] 98 IA <21 °C
Styrene 1.1 6.1 IB 31–32.2 °C 490 °C
Tetrafluoroethylene IA
Tetrahydrofuran 2 12 IB -14 °C 321 °C
Toluene 1.2–1.27 6.75–7.1 IB 4.4 °C 0.24 @ 4.1% 480 °C; 535 °C[44]
Triethylborane -20 °C -20 °C
Trimethylamine IA Flammable gas
Trinitrobenzene IA
Turpentine 0.8[45] IC 35 °C
Vegetable oil IIIB 327 °C (620 °F)
Vinyl acetate 2.6 13.4 −8 °C
Vinyl chloride 3.6 33
Xylenes 0.9–1.0 6.7–7.0 IC 27–32 °C 0.2
m-Xylene 1.1[46] 7 IC 25 °C 525 °C
o-Xylene IC 17 °C
p-Xylene 1.0 6.0 IC 27.2 °C 530 °C

See also

References

  1. ^ Britton, L. G “Using Material Data in Static Hazard Assessment.” as found in NFPA 77 - 2007 Appendix B
  2. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  3. ^ Gases - Explosive and Flammability Concentration Limits
  4. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  5. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  6. ^ n-BUTYL MERCAPTAN ICSC: 0018
  7. ^ 2-HEXANONE ICSC:0489
  8. ^ Gases - Explosive and Flammability Concentration Limits
  9. ^ Gases - Explosive and Flammability Concentration Limits
  10. ^ Cyanogen
  11. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 211
  12. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 216
  13. ^ CYCLOHEXANONE ICSC: 0425
  14. ^ MSDS Cyclopentadiene
  15. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 221
  16. ^ CYCLOPENTANE ICSC: 0353
  17. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 226
  18. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 244
  19. ^ Walsh (1989) Chemical Safety Data Sheets, Roy. Soc. Chem., Cambridge.
  20. ^ Encyclopedia.airliquide.com
  21. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 266
  22. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 281
  23. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 286
  24. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 296
  25. ^ Yaws, Carl L.; Braker, William; Matheson Gas Data Book Published by McGraw-Hill Professional, 2001 pg. 301
  26. ^ Gases - Explosive and Flammability Concentration Limits
  27. ^ Gases - Explosive and Flammability Concentration Limits
  28. ^ Gases - Explosive and Flammability Concentration Limits
  29. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  30. ^ http://environmentalchemistry.com/yogi/periodic/H.html
  31. ^ Gases - Explosive and Flammability Concentration Limits
  32. ^ Gases - Explosive and Flammability Concentration Limits
  33. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  34. ^ Gases - Explosive and Flammability Concentration Limits
  35. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  36. ^ Gases - Explosive and Flammability Concentration Limits
  37. ^ Gases - Explosive and Flammability Concentration Limits
  38. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  39. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  40. ^ Gases - Explosive and Flammability Concentration Limits
  41. ^ Gases - Explosive and Flammability Concentration Limits
  42. ^ Gases - Explosive and Flammability Concentration Limits
  43. ^ Gases - Explosive and Flammability Concentration Limits
  44. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008
  45. ^ Combustibles
  46. ^ Working with modern hydrocarbon and oxygenated solvents: a guide to flammability American Chemistry Council Solvents Industry Group, pg. 7, January 2008

Further reading

  • David R. Lide, Editor-in-Chief; CRC Handbook of Chemistry and Physics, 72nd edition; CRC Press; Boca Raton, Florida; 1991; ISBN 0-8493-0565-9
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