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AI <br /> 100 H = Henry s Law Coefficient <br /> (Mill-W/hole) <br /> Propylene <br /> 10 <br /> Isobutane �q <br /> C, <br /> N7 PFJ <br /> n butane l Ova. qv <br /> 1�1 <br /> OO d 11-1 <br /> 1 0 1 1 pentene <br /> q <br /> d1 n pentane <br /> m <br /> E <br /> cyclopentane• <br /> 0 1 2 dimethytbutane <br /> En hexan� • Isopropylethcr <br /> Q . <br /> 0 c ° �� drmethylpentanes melhylcyclopentane •benzene <br /> N o `r 1 2dichlorocthan <br /> .. w o methylhexanes• <br /> u > <br /> Cl- c lrrrnelhylpentanes <br /> zi <br /> OL •toluene t butylmethylether• <br /> m /9 <br /> ethylbenzene •1 2-drbromoethane <br /> • \C`` a�0 Pa S <br /> C O <br /> 001 <br /> methyloelanes �� �O y <br /> lens <br /> o <br /> O <br /> III vasrnrlly Moble <br /> 0001- m Ground Water <br /> O,\ O~ ODO <br /> O p O <br /> •if Iraethyllead <br /> 0 001 001 0 1 1 0 10 100 1 000 <br /> Niticous Solubrllly (in mole/0 <br /> Figure 1-3 Vapor pressures, solubilities, and corresponding <br /> Henry's Law constants for major constituents of <br /> gasoline. <br />