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The lower flammability limit (LFL) and upper flammability limit (UFL) are important safety limits which describe the minimum and maximum volume fraction in air, respectively, that a flammable substance can burn if ignited. If the range of concentration of benzene in air in which ignition could take place is 1.4 - 8.0 vol%, what would be the corresponding temperatures for air saturated with benzene in the vapour space of a storage tank assuming a total pressure in the vapour space of 100 kPa?
For air saturated with benzene, partial pressure of benzene would be equiavlent to vapor pressure of benzene in air.
a) Now for LFL, vol% of benezne = 1.4 mol%, partial pressure of benzene = total pressure * mol fraction of benzene
since for vapor phase, mole fraction of a component is same as volume fraction of the component.
partial pressure of benzene = 100*1.4/100 = 1.4 kPa or 1.4*7.5 mmHg = 10.5 mmHg
Now using antonie equation for benzene, T (0C)= B/(A-Log10p) -C where p is in mmHG, for benzene we know from literature that A = 6.88, B = 1196.8 & C = 219.16
On solving the above equation for p = 10.5 mm Hg, T = -14.88 DegC
a) Now for HFL, vol% of benezne = 8 mol%, partial pressure of benzene = total pressure * mol fraction of benzene
since for vapor phase, mole fraction of a component is same as volume fraction of the component.
partial pressure of benzene = 100*8/100 = 8 kPa or 8*7.5 mmHg = 60.0 mmHg
Now using antonie equation for benzene, T (0C)= B/(A-Log10p) -C where p is in mmHG, for benzene we know from literature that A = 6.88, B = 1196.8 & C = 219.16
On solving the above equation for p = 60.0 mm Hg, T = -15.4 DegC