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�I <br /> 100 H = Henry's Law Coefficient <br /> (at In M3/mole) <br /> I <br /> v <br /> 10 propylene <br /> r • <br /> isobutane <br /> C <br /> • TP Z+ <br /> n-butane �.O/b"i� �r7g <br /> y7P�P !p <br /> 1.0 O ee <br /> \X I-Pentene <br /> v <br /> npentane <br /> t <br /> n <br /> o cyclopentane. <br /> E •1,2-dimethylbutane <br /> Q n-he.anc <br /> / •isopropylctltcr <br /> °1 c = �� dimelhylpenlanes methylcyclopentane <br /> N 0.1 •benzene <br /> o > melhylhexanes• 1,2-dichloroethan <br /> C trimethylpentanes <br /> 0 <br /> n <br /> j •toluene t-butylmethylether• <br /> 11,r a'`c9 4 ethylbenzene se •1,2-0ibromoethane <br /> Pe <br /> 0.011 methyloelanea \ ,seraeS d <br /> 0� 1 <br /> I xylenes <br /> V <br /> N <br /> O <br /> ij <br /> Incrrasingly Mobile <br /> 0.001 m Ground Water <br /> b. O� 01 001 <br /> •letraethyllead >> ,rte •Z• <br /> ` 0.001 0.01 0.1 1.0 10 100 1,000 <br /> Aqueous Solubility (m.mole/1) <br /> �. Figure 3. Vapor pressures, solubilities, and corresponding <br /> Henry's Law constants for major constituents of <br /> gasoline. <br /> r <br /> v <br /> 1 v <br />