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r -rs N0116 JVW'i011 <br /> � <br /> r <br /> z <br /> COE'YRI(;IIT 1'.)90 Version 1.1 <br /> L11vironmentnl Svstems unci Technologies, Inc. <br /> 130,x 10157, Dlackshur4, VA 2.1062-0157 USA <br /> (703)-552-0685 x <br /> TPH AS DIESEL CONTAMINATION <br /> TOTAL ,MASS OF THE SPILL - .10406E+05 [KG1 <br /> AIR FLOW RATE _ . 1223.1E+07 [L/DAY1 <br /> TEMPERATURE = 15.55556 DEGREES C <br /> MINIMUM TIME STEP - 2.00000 �DAYSI <br /> DAYSMAXIMUM TIME STEP - 50.00000TOTAL VENTING TIME = 1825.00000 DAYS <br /> C'RA'CK-NICOLSON FACTOR - .70 <br /> j . <br /> CUSIPOUND MOLECULAR VAPOR BOILING <br /> WEIGHT PRESSURE TEMPERATURE <br /> (GM/MOLE1 (ATM) DEGREES C <br /> benzene 78.10 .08117 80.00 <br /> s . ` toluene 92.10 .02304 111.00 <br /> ethylbenzene 116.00 00451 136.20 <br /> xylenes 1(16.20 .00642 138.56 <br /> xylenes <br /> 1=8.20 .00010 218.00 <br /> -qpht!thylnaphthalene 142.20 OD004 241.00 <br /> -n-hexylbenzene 162.35 .00007 226.00 <br /> C13 153.00 .00003 255.00 <br /> Ci4 159.50 .00000 297.00 <br /> " C15 186.DO .00000 337.00 <br /> i C16 202.00 .00000 371.50 <br /> C16 216.00 .00000 409.00 <br /> C18 232.00 .00000 477.00 <br /> C19 245.00 .00000 177.00 <br /> 3,4-benzpyrene 252.00 .00000 497.00 <br /> C21 276.00 .00000 550.00 <br /> COMPOUND MOLE MASS TOTAL TOTAL <br /> FRACTION FRACTION MASS (KG) MOLES <br /> benzene 006049 .003000 .31218E+02 .39972E+03 <br /> toluene .025819 .015100 .15713E+03 .17061E+04 <br /> ethylbenzene .015748 .015600 .16233E+03 .10406E+04 <br /> xylenes 073400 .049500 .51510E+03 .48503E+01 <br /> _ naphthalene .116449 .094800 .98649E+03 .76949E+04 <br /> methylnaphthalene .148396 .134000 .13914E+04 .98059E+04 <br /> 116398 .120000 .12487E+04 .76915E+04 <br /> -- n-hexylbenzene C13 . 131951 .128200 .13340E+04 .87193E+04 <br /> C14 .129141 .130800 .13611E+04 .85336E+04 <br /> -- (.15 .092962 .109800 .11126E+04 .61429E+04 <br /> C16 .055117 .070700 .73570E+03 .36421E+04 <br /> C17 .016951 .06,1400 .67015E+03 .31025E+04 <br /> C18 .021789 .032100 .33403E+03 .14398E+04 <br /> C19 .010027 .015600 .16233E+03 .66259E+03 <br /> 3,4-benzpyrene .0016?9 ; pg�p0 .85329E+02 .3090 .95329E+02 16E+03 <br /> C21 <br /> -•TME _ .00000 DAPS <br /> - - - -- <br /> ----...,.86080E+05THE TOTAL MASS OF HYDROCARBONS = .10406E+05[KGI <br /> % CUMULATIVE MASS CHANGE = 00000[%1 <br /> % MASS CHANGE FOR DELTA T - .00000 11 <br /> TIME = 2.00000 DAYS <br /> .,-- <br />