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Peabody Weacern <br />Paradox Hydrology Syscem <br />Water Quality Reporc <br />Sice YSAL1 <br />Loc -35160.902 -9544,476 <br />E1 ev 7174.93 <br />Field Parameters <br />Field Ph S.U. <br />Temperature C <br />Conductivity U[9i0S/CM <br />Depth To Water FT <br />Lnboratory Parameters <br />Alk As CaCO3, Ph 4.6 MG/L <br />Alk, Bicarb As CaCO3 MG/L <br />Alk, Carb As CaCO3 MG/L <br />Alk, Nydrox As CaCO3 MG/L <br />Aluminum, Dissolved MG/L <br />Arsenic, Dissolved UG/L <br />Barium, Dissolved UG/L <br />Die solved UC/L <br />ity UMS /CM2 <br />is solved UG/L <br />MG/L <br />A6 CaCO3 MC/L <br />Dissolved MG/L <br />Dl ssolved MG/L <br />NiC ke 1, Dissolved UG/L <br />Ammonia NiCrogen~' MG/L <br />Nitrate NiCrogen~d MG/L <br />Nitrite Nitrogen_N MG/L <br />Nitrate /NiCr1Ce Nitrog¢n_N MG/L <br />Ph Ac 25 Deg. Cent. S.U. <br />Phosphorus, OrChophos MG/L <br />Potassium, Dissolved MG/L <br />Selenium, Dissolved UC/L <br />Silver, Dissolved UG/L <br />Sodium, Dissolved MC/L <br />Solids, Dissolved MG/L <br />Solids, Suspended MG/L <br />Sulfate MG/L <br />Sulfide MG/L <br />Zinc, Dissolved MG/L <br />sits rbonate A6 HCO3 MG/L <br />Carbonate Ae CO3 MG/L <br />Hydroxi de AB OH MG/L <br />Phosphe to Ae PO4 MG/L <br />Ca tion_Anion Balance PERCENT <br />Sar RATIO <br />Solids, Diae. (Ca lc) MG/L <br />Sum Of Anions MEQ/L <br />Sum OE Cations MEQ/L <br />Tde Ratio ANAL/CALC <br />Condition2yprom 10/01/98 To 9/30 /99...WELL <br />10/06/98 <br />< <br /> <br /> <br />B <br />e <br />B <br />< <br />< <br />7.56 <br />10.40 <br />1020.00 <br />4.91 <br />316.00 <br />316.00 <br />2.00 < <br />2.00 < <br />.03 < <br />1.00 < <br />77.00 <br />70.00 <br />3.00 < <br />113.00 <br />10.D0 <br />10.00 < <br />1050.00 <br />10.00 < <br />.30 B <br />547.00 <br />O1 <br />40.00 < <br />63.50 <br />02 B <br />.20 < <br />1.00 < <br />10.00 < <br />OS < <br />.13 < <br />O1 < <br />.13 < <br />8.10 <br />.06 <br />4.20 <br />1.00 < <br />5.00 < <br />29.90 <br />700.00 <br />82.00 <br />290.00 <br />13 8 <br />.O1 B <br />386.00 <br />2.00 < <br />2.00 < <br />.16 <br />-2.40 <br />.47 <br />696.00 <br />12.70 <br />12.10 <br />I.O1 <br />5/20/99 <br />7.6R <br />6.40 <br />1010.00 <br />1.17 <br />28R .1 <br />2RB .I <br />2.I <br />2.i <br />1 <br />1.1 <br />74 .I <br />50.1 <br />3.1 <br />112.1 <br />10.1 <br />10.1 <br />1080.1 <br />10.1 <br />522.1 <br />1 <br />40.1 <br />SB .'. <br />1.1 <br />10.1 <br />7.' <br />3.' <br />1.1 <br />6.I <br />36 .' <br />750.1 <br />72. i <br />320.1 <br />352.1 <br />2.1 <br />2.i <br />-2.. <br />719.1 <br />12.1 <br />12 .'. <br />1.1 <br />(~ <br />