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f <br /> too H Henry's Law Coefficient <br /> (mn1•M3/mole) <br /> prupyltne <br /> to <br /> isobutane /q <br /> a <br /> mbutar,t <br /> ,/ I-penlene . <br /> � rnptntane <br /> i <br /> L <br /> R cyclop Cr,tanc e <br /> 0 1,2•dirrcihytbutane <br /> Qn-hexane f a itupr[isYlcthtr <br /> i ... _ <br /> w u " dn,ellrviPcn,anrs nlcl ly cyclopentanes <br /> .. •bC1lf erlC <br /> 1,2-d¢hloroethanr <br /> ! o cT thylhr•xanes. <br /> N 7 <br /> 0. t rune thyl pen lanes <br /> C <br /> Ek <br /> etoluene t•flu lYfnit thylttiler• <br /> 4 <br /> elhylbeezenc •1.2-dihromaethane/ t <br /> ♦e°s4 f,c�d v <br /> 0.01 Ine111yt(3001111S {•pari • <br /> u • xylcncs <br /> I, J <br /> 7. <br /> O� <br /> fncrnasingly Mobite <br /> d.oat n Ground Water <br /> o° <br /> 0 /ol o <br /> .telraclhyl read - - - <br /> d.00t 0.01 a.1 1.0 to 100 1.O00 <br /> Aqueom Solubility (rn rnOte/i) <br /> t <br /> t Figure 4. Vapor pressures, solubilities and corresponding <br /> Henry's Law constants for major constituents of <br /> gasoline. <br />