Index1 Input File

2 Solution History

3 Main

Input File$ Generated by PRO/II Keyword Generation System <version 9.0>$ Generated on: Tue Jun 19 15:47:30 2012TITLE DIMENSION ENGLISH, TEMP=C, PRES=PA, WT=KG SEQUENCE SIMSCI CALCULATION TVPBASIS=37.7778, RVPBASIS=APINCOMPONENT DATA LIBID 1,BUTANE/2,1BUTENE/3,T2BUTENE/4,C2BUTENE/5,IBUTANE/6,CP/ & 7,CYPENTEN/8,3M1BUTEN/9,2M1BUTEN/10,TPND/11,1PENTENE/ & 12,C2PENTEN/13,T2PENTEN/14,PPLN/15,IPENTANE/16,PENTANE/ & 17,M12B/18,2M2BUTEN/19,H2, BANK=SIMSCI,PROCESS ASSAY FIT=ALTERNATE, CONVERSION=API94, CURVEFIT=CURRENT, & KVRECONCILE=TAILSTHERMODYNAMIC DATA METHOD SYSTEM=SRK, SET=SRK01, DEFAULTSTREAM DATA PROPERTY STREAM=NAFTA, TEMPERATURE=90, PRESSURE=1.39E6, PHASE=M, & COMPOSITION(WT,KG/H)=1,734.83/2,830.09/3,1301.83/4,1419.77/ & 5,72.58/6,226.35/7,3913.21/8,635.04/9,6104.5/11,2599.13/ & 12,5928.6/13,9062.7/15,14719.3/16,3651.48/18,20135.3 PROPERTY STREAM=NAFTA+H2, TEMPERATURE=65, PRESSURE=1.39E6, PHASE=M, & COMPOSITION(WT,KG/H)=1,734.83/2,830.09/3,1301.83/4,1419.77/ & 5,72.56/6,226.35/7,3913.21/8,635.04/9,5529.36/10,1029.67/ & 11,2599.13/12,5402.38/13,8133.05/14,526.18/15,14719.3/ & 16,3651.48/17,517.1/18,20135.3/19,26 NAME NAFTA,NAFTA/NAFTA+H2,NAFTA+H2UNIT OPERATIONS HXRIG UID=02-E-01 TYPE TEMA=AEU, ORIENTATION=HORI, FLOW=COUN TUBES FEED=NAFTA, M=S2, LENGTH=16, OD=0.8, BWG=14, PASS=4, & PATTERN=30, PITCH=1.25, MATERIAL=CS, DPUNIT=34474 SHELL FEED=NAFTA+H2, M=S4, MATERIAL=CS, FOUL=0.0022, & DPUNIT=34474, ID=23 BAFFLE CUT=25, SPACING=10 SNOZZLE TYPE=CONV, ID=4,8 TNOZZLE ID=4,8 HXCALC DPSMETHOD=BELL, DPTMETHOD=BBM, HTCMETHOD=CHEN HCURVE UID=HC1 ISOTHERMAL STREAM=NAFTA, TEMP=90,81.33, DP=0, POINTS=3 ISOTHERMAL STREAM=NAFTA+H2, TEMP=69,77.92, DP=0, POINTS=3 PROPERTY ALL,SUMMARYEND

Index

Solution History SIMULATION SCIENCES INC. R PAGE H-1 PROJECT PRO/II VERSION 9.0 ELEC V7.0 PROBLEM CALCULATION HISTORY 06/19/12

*** PROBLEM SOLUTION BEGINS FEED FLASH COMPLETE ** WARNING ** The ideal gas enthalpy of BUTANE was extrapolated. ** WARNING ** The ideal gas enthalpy of 1BUTENE was extrapolated. ** WARNING ** The ideal gas enthalpy of T2BUTENE was extrapolated. ** WARNING ** The ideal gas enthalpy of C2BUTENE was extrapolated. ** WARNING ** The ideal gas enthalpy of IBUTANE was extrapolated. ** WARNING ** The ideal gas enthalpy of CP was extrapolated. ** WARNING ** The ideal gas enthalpy of CYPENTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of 3M1BUTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of 2M1BUTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of TPND was extrapolated. ** WARNING ** The ideal gas enthalpy of 1PENTENE was extrapolated. ** WARNING ** The ideal gas enthalpy of C2PENTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of T2PENTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of PPLN was extrapolated. ** WARNING ** The ideal gas enthalpy of IPENTANE was extrapolated. ** WARNING ** The ideal gas enthalpy of PENTANE was extrapolated. ** WARNING ** The ideal gas enthalpy of M12B was extrapolated. ** WARNING ** The ideal gas enthalpy of 2M2BUTEN was extrapolated. ** WARNING ** The ideal gas enthalpy of H2 was extrapolated. UNIT 1 SOLVED - '02-E-01 ' *** PROBLEM SOLUTION REACHED *** THIS RUN USED 39.36 PRO/II SIMULATION UNITS *** RUN STATISTICS STARTED 15:46:45 06/19/12 NO ERRORS FINISHED 15:46:46 06/19/12 19 WARNINGS RUN TIMES NO MESSAGES INTERACTIVE 0 MIN, 0.01 SEC CALCULATIONS 0 MIN, 1.49 SEC TOTAL 0 MIN, 1.50 SEC

Index

=========

HcurveIn (Summary) UOM HC1Name HC1Description HC1Thermodynamic System SRK01Temperature[HCURVE1] C DATA1 90 DATA2 85.665 DATA3 81.3300000000001Temperature[HCURVE2] C DATA1 69.0000000000001 DATA2 73.46 DATA3 77.9200000000001Pressure[HCURVE1] Pa DATA1 1390000 DATA2 1390000 DATA3 1390000Pressure[HCURVE2] Pa DATA1 1390000 DATA2 1390000 DATA3 1390000Vapor Molar Rate[HCURVE1] kg-mol / hr DATA1 0 DATA2 0 DATA3 0Vapor Molar Rate[HCURVE2] kg-mol / hr DATA1 1.33880318712 DATA2 1.47785533884 DATA3 1.7257358574Liquid Molar Rate[HCURVE1] kg-mol / hr DATA1 1026.48666168 DATA2 1026.48666168 DATA3 1026.48666168Liquid Molar Rate[HCURVE2] kg-mol / hr DATA1 1039.51779588 DATA2 1039.37874372 DATA3 1039.1308632

kg-mol / hr DATA1 0 DATA2 0 DATA3 0

kg-mol / hr DATA1 0 DATA2 0 DATA3 0Vapor Enthalpy[HCURVE1] BTU / hr DATA1 0 DATA2 0 DATA3 0Vapor Enthalpy[HCURVE2] BTU / hr DATA1 12648.4555714367 DATA2 15744.3631266468

Index

Free Water Molar Rate[HCURVE1]

Free Water Molar Rate[HCURVE2]

DATA3 20656.3078516862Liquid Enthalpy[HCURVE1] BTU / hr DATA1 14005445.3126836 DATA2 13244171.7456827 DATA3 12493175.4645233Liquid Enthalpy[HCURVE2] BTU / hr DATA1 10550769.9827498 DATA2 11297154.2642125 DATA3 12052190.0479594Water Phase Enthalpy[HCURVE1] BTU / hr DATA1 0 DATA2 0 DATA3 0Water Phase Enthalpy[HCURVE2] BTU / hr DATA1 0 DATA2 0 DATA3 0Total Enthalpy[HCURVE1] BTU / hr DATA1 14005445.3126836 DATA2 13244171.7456827 DATA3 12493175.4645233Total Enthalpy[HCURVE2] BTU / hr DATA1 10563418.4383827 DATA2 11312898.6290827 DATA3 12072846.3556575Latent Heat[HCURVE1] BTU / kgLatent Heat[HCURVE2] BTU / kg DATA1 266.144234925028 DATA2 218.573928970864 DATA3 200.817433605672Vapor Molar Entropy[HCURVE1] BTU / C kg-mol DATA1 0 DATA2 0 DATA3 0Vapor Molar Entropy[HCURVE2] BTU / C kg-mol DATA1 247.625277709325 DATA2 259.87169051997 DATA3 273.163048167877Liquid Molar Entropy[HCURVE1] BTU / C kg-mol DATA1 462.979026690425 DATA2 460.924553295547 DATA3 458.873179819157Liquid Molar Entropy[HCURVE2] BTU / C kg-mol DATA1 448.386661896006 DATA2 450.489970238659 DATA3 452.609827592744Total Molar Entropy[HCURVE1] BTU / C kg-mol DATA1 462.979026690425 DATA2 460.924553295547 DATA3 458.873179819157Total Molar Entropy[HCURVE2] BTU / C kg-mol DATA1 448.128432316645 DATA2 450.219321744735 DATA3 452.312305556082

Vapor Mass Rate[HCURVE1] kg / hr DATA1 0 DATA2 0 DATA3 0Vapor Mass Rate[HCURVE2] kg / hr DATA1 25.821973602 DATA2 31.7011568688 DATA3 41.082603264Liquid Mass Rate[HCURVE1] kg / hr DATA1 71334.730008 DATA2 71334.730008 DATA3 71334.730008Liquid Mass Rate[HCURVE2] kg / hr DATA1 71376.828012 DATA2 71370.948816 DATA3 71361.567396Free Water Mass Rate[HCURVE1] kg / hr DATA1 0 DATA2 0 DATA3 0Free Water Mass Rate[HCURVE2] kg / hr DATA1 0 DATA2 0 DATA3 0Mw of Vapor[HCURVE1] DATA1 0 DATA2 0 DATA3 0Mw of Vapor[HCURVE2] DATA1 19.28735594 DATA2 21.45078482 DATA3 23.80584669Mw of Liquid[HCURVE1] DATA1 69.49406424 DATA2 69.49406424 DATA3 69.49406424Mw of Liquid[HCURVE2] DATA1 68.66340171 DATA2 68.66693133 DATA3 68.67428339Dry Vapor Sp Gr[HCURVE1] DATA1 0 DATA2 0 DATA3 0Dry Vapor Sp Gr[HCURVE2] DATA1 0.6659078836 DATA2 0.7406016026 DATA3 0.8219115691Dry Liquid Sp Gr[HCURVE1] DATA1 0.6527355934 DATA2 0.6527355934 DATA3 0.6527355934Dry Liquid Sp Gr[HCURVE2] DATA1 0.6518001953

DATA2 0.6518087782 DATA3 0.6518265319Vapor Mole Fraction[HCURVE1]Vapor Mole Fraction[HCURVE2]Liquid Mole Fraction[HCURVE1] fraction DATA1 1 DATA2 1 DATA3 1Liquid Mole Fraction[HCURVE2] fraction DATA1 0.9987137487 DATA2 0.9985801547 DATA3 0.9983420042Vapor Mass Fraction[HCURVE1] fraction DATA1 0 DATA2 0 DATA3 0Vapor Mass Fraction[HCURVE2] fraction DATA1 0.0003616388693 DATA2 0.0004439773156 DATA3 0.0005753652456Liquid Mass Fraction[HCURVE1] fraction DATA1 1 DATA2 1 DATA3 1Liquid Mass Fraction[HCURVE2] fraction DATA1 0.9996383611 DATA2 0.9995560227 DATA3 0.9994246348Dry Vapor LV Fraction[HCURVE1] fraction DATA1 0 DATA2 0 DATA3 0Dry Vapor LV Fraction[HCURVE2] fraction DATA1 0.0005937624498 DATA2 0.0006892405764 DATA3 0.0008478108324Dry Liquid LV Fraction[HCURVE1] fraction DATA1 1 DATA2 1 DATA3 1Dry Liquid LV Fraction[HCURVE2] fraction DATA1 0.9994062376 DATA2 0.9993107594 DATA3 0.9991521892

HxRig (Summary) UOM 02-E-01HX Name 02-E-01HX Description 02-E-01Shell Side Thermo Method SRK01Tube Side Thermo Method SRK01Shell Side Feed Stream(s) NAFTA+H2Shell Side Product Stream(s) S4Tube Side Feed Stream(s) NAFTATube Side Product Stream(s) S2

1

1

4Tube Side Coefficient(User Input) BTU/hr-ft2-F DEFAULT

hr-ft2-F/BTU 0.002Shell Side Coefficient(User Input) BTU/hr-ft2-F DEFAULTShell Side Fouling Resistance hr-ft2-F/BTU 0.0022Duty BTU / hr 1949055.05567456LMTD C 13.55811416LMTD Correction factor (Ft) 0.8688005302U Value with Fouling BTU/hr-ft2-F 108.55386653658U Value without Fouling BTU/hr-ft2-F 222.798671423993Exchanger Area ft2 846.815409405509U*A BTU/hr-F 91925.0869244608Tube Bundle Weight kg 2134.742671Empty Shell Weight kg 3153.621862Tube Side product temperature C 78.7849857000001Tube Side pressure drop per shell Pa 34473.8Tube Side Feed Pressure Pa 1390000Tube Side Product Pressure Pa 1355526.2Shell Side Product Temperature C 76.605857Shell Side Pressure Drop per Shell Pa 34473.8Shell Side Feed Pressure Pa 1390000Shell Side Product Pressure Pa 1355526.2Area per shell ft2 846.738878184773

Stream (Summary) UOM NAFTAName NAFTADescription NAFTAPhase LiquidThermodynamic System SRK01Total Molar Rate kg-mol / hr 1026.48666168Total Mass Rate kg / hr 71334.730008Temperature C 90Pressure Pa 1390000Total Molecular Weight 69.49406424Total Specific Enthalpy BTU / kg 196.334174264971Total Cp 2.615390001Total Molar Component Rates kg-mol / hr BUTANE 12.6425842128 1BUTENE 14.7946297464 T2BUTENE 23.2024152096 C2BUTENE 25.3044506916 IBUTANE 1.24872251004 CP 3.22737489576 CYPENTEN 57.447076788 3M1BUTEN 9.0546152148 2M1BUTEN 87.04002672 TPND 0 1PENTENE 37.059275088

Number of Shells in Series(User Input)

Number of Shells in Parallel(User Input)

Number of Tube Passes per Shell(User Input)

Tube Side Fouling Resistance(User Input)

C2PENTEN 84.53198502 T2PENTEN 129.219043392 PPLN 0 IPENTANE 204.0091767 PENTANE 50.609364336 M12B 0 2M2BUTEN 287.095921092 H2 0Total Molar Component Fractions fraction BUTANE 0.01231636483 1BUTENE 0.01441288065 T2BUTENE 0.02260371818 C2BUTENE 0.02465151437 IBUTANE 0.001216501448 CP 0.00314409823 CYPENTEN 0.05596475719 3M1BUTEN 0.008820976982 2M1BUTEN 0.08479411374 TPND 0 1PENTENE 0.03610302643 C2PENTEN 0.08235078757 T2PENTEN 0.1258847759 PPLN 0 IPENTANE 0.198745083 PENTANE 0.04930347975 M12B 0 2M2BUTEN 0.2796879218 H2 0Vapor Molar Rate kg-mol / hr N/AVapor Mass Rate kg / hr N/AVapor Molecular Weight N/AVapor Mole Fraction fraction N/AVapor Specific Enthalpy BTU / kg N/AVapor CP N/AVapor Composition fraction BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/A

Vapor Component Rate kg-mol / hr BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/ATotal Liquid Molar Rate kg-mol / hr 1026.48666168Total Liquid Mass Rate kg / hr 71334.730008Total Liquid Molecular Weight 69.49406424Total Liquid Mole Fraction fraction 1Total Liquid Specific Enthalpy BTU / kg 196.334174264971Total Liquid CP 2.615390001Total Liquid Composition fraction BUTANE 0.01231636483 1BUTENE 0.01441288065 T2BUTENE 0.02260371818 C2BUTENE 0.02465151437 IBUTANE 0.001216501448 CP 0.00314409823 CYPENTEN 0.05596475719 3M1BUTEN 0.008820976982 2M1BUTEN 0.08479411374 TPND 0 1PENTENE 0.03610302643 C2PENTEN 0.08235078757 T2PENTEN 0.1258847759 PPLN 0 IPENTANE 0.198745083 PENTANE 0.04930347975 M12B 0 2M2BUTEN 0.2796879218 H2 0Total Liquid Component Rate kg-mol / hr BUTANE 12.6425842128 1BUTENE 14.7946297464 T2BUTENE 23.2024152096 C2BUTENE 25.3044506916 IBUTANE 1.24872251004 CP 3.22737489576 CYPENTEN 57.447076788

3M1BUTEN 9.0546152148 2M1BUTEN 87.04002672 TPND 0 1PENTENE 37.059275088 C2PENTEN 84.53198502 T2PENTEN 129.219043392 PPLN 0 IPENTANE 204.0091767 PENTANE 50.609364336 M12B 0 2M2BUTEN 287.095921092 H2 0Liqud Molar Rate kg-mol / hr N/ALiquid Cp N/ALiquid Molecular Weight N/ALiquid Mole Fraction fraction N/ALiquid Molar Enthalpy BTU / kg-mol N/ALiquid Composition fraction BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/ALiquid Component Rate kg-mol / hr BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A

M12B N/A 2M2BUTEN N/A H2 N/ADecant Water Mole Rate kg-mol / hr N/ADecant Water Moleculat Weight N/AWater Mole Fraction fraction N/ADecant Water Molar Enthalpy BTU / kg-mol N/ADecant Water Cp N/ALiquid1 Mole Rate kg-mol / hr N/ALiquid1 Mole Frac fraction N/ALiquid1 Molecular Weight N/ALiquid1 Molar Enthalpy BTU / kg-mol N/ALiquid1 Cp N/ALiquid1 Composition fraction BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/ALiquid1 Component Rate kg-mol / hr BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/ALiquid2 Mole Rate kg-mol / hr N/A

Liquid2 Mole Frac fraction N/ALiquid2 Molecular Weight N/ALiquid2 Molar Enthalpy BTU / kg-mol N/ALiquid1 Cp N/ALiquid2 Composition fraction BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/ALiquid2 Component Rate kg-mol / hr BUTANE N/A 1BUTENE N/A T2BUTENE N/A C2BUTENE N/A IBUTANE N/A CP N/A CYPENTEN N/A 3M1BUTEN N/A 2M1BUTEN N/A TPND N/A 1PENTENE N/A C2PENTEN N/A T2PENTEN N/A PPLN N/A IPENTANE N/A PENTANE N/A M12B N/A 2M2BUTEN N/A H2 N/A

NAFTA+H2 S2 S4NAFTA+H2 S2 S4NAFTA+H2 S2 S4

Mixed Liquid MixedSRK01 SRK01 SRK01

1040.85659916 1026.48666168 1040.8565991671402.649984 71334.730008 71402.649984

65 78.7849857000001 76.6058571390000 1355526.2 1355526.2

68.59989171 69.49406424 68.59989171138.645406611946 169.011393570034 165.942196178416

2.434307199 2.526418782 2.518282692

12.6425842128 12.6425842128 12.642584212814.7946297464 14.7946297464 14.794629746423.2024152096 23.2024152096 23.202415209625.3044506916 25.3044506916 25.30445069161.24837841484 1.24872251004 1.248378414843.22737489576 3.22737489576 3.22737489576

57.447076788 57.447076788 57.4470767889.0546152148 9.0546152148 9.054615214878.839485992 87.04002672 78.839485992

15.1158592404 0 15.115859240437.059275088 37.059275088 37.059275088

77.028962184 84.53198502 77.028962184115.963779096 129.219043392 115.963779096

7.7244775668 0 7.7244775668204.0091767 204.0091767 204.0091767

50.609364336 50.609364336 50.6093643367.5911804892 0 7.5911804892

287.095921092 287.095921092 287.09592109212.8975924196 0 12.8975924196

0.01214632661 0.01231636483 0.012146326610.0142138982 0.01441288065 0.0142138982

0.02229165403 0.02260371818 0.022291654030.02431117861 0.02465151437 0.024311178610.00119937599 0.001216501448 0.00119937599

0.003100691198 0.00314409823 0.0031006911980.05519211466 0.05596475719 0.05519211466

0.008699195663 0.008820976982 0.0086991956630.07574481061 0.08479411374 0.075744810610.01452251852 0 0.01452251852

0.0356045925 0.03610302643 0.03560459250.07400535504 0.08235078757 0.07400535504

0.111411869 0.1258847759 0.1114118690.007421269723 0 0.007421269723

0.1960012329 0.198745083 0.19600123290.04862280199 0.04930347975 0.04862280199

0.007293204937 0 0.0072932049370.2758265848 0.2796879218 0.2758265848

0.01239132502 0 0.012391325021.28607620112 N/A 2.2670546000422.5119948688 N/A 53.4670218

17.50440203 N/A 23.584355580.001235594031 N/A 0.002178066221

483.019206964533 N/A 500.3722602506022.884779721 N/A 2.556155265

0.006681592334 N/A 0.0087499298160.008777412668 N/A 0.01144960187

0.01169403058 N/A 0.015491348640.01188926354 N/A 0.01580805759

0.000848118148 N/A 0.0010912645490.0004657562134 N/A 0.0006704937423

0.00978798214 N/A 0.013960413310.002715813768 N/A 0.00371377445

0.01765586649 N/A 0.024582329290.002556487155 N/A 0.0035666580780.008541597849 N/A 0.01188771595

0.01478710512 N/A 0.020909164830.02265429699 N/A 0.03201964096

0.001236704713 N/A 0.0017413119320.04965550651 N/A 0.06871105074

0.009932218953 N/A 0.013997218430.001326861174 N/A 0.001872740559

0.05283857506 N/A 0.075124943780.7659548106 N/A 0.6746523415

0.0085930368876 N/A 0.0198365686380.01128842154 N/A 0.0259568725932

0.0150394144176 N/A 0.03511973318760.0152904988908 N/A 0.0358377296724

0.00109074456576 N/A 0.002473956316440.00059899798152 N/A 0.0015200459226

0.0125880908868 N/A 0.031649019210.003492743454 N/A 0.00841932945

0.0227067896988 N/A 0.0557294826960.00328783728852 N/A 0.008085808602

0.010985145714 N/A 0.02695010113440.0190173439728 N/A 0.0474022183320.0291351522132 N/A 0.0725902743240.0015904964988 N/A 0.0039476492244

0.063860765184 N/A 0.1557717036480.0127735904196 N/A 0.0317324584368

0.00170644457772 N/A 0.00424560510.067954433868 N/A 0.170312349384

0.985076253 N/A 1.529473694041039.57052328 1026.48666168 1038.58954488

71380.137996 71334.730008 71349.18296468.66310309 69.49406424 68.698152550.998764406 1 0.9978219338

138.536797433321 169.011393570034 165.6915838909642.434165129 2.526418782 2.518254311

0.01215308716 0.01231636483 0.012153740340.0142206238 0.01441288065 0.01421993216

0.02230476459 0.02260371818 0.022306497880.02432654604 0.02465151437 0.02432973939

0.001199810539 0.001216501448 0.0011996119780.003103950935 0.00314409823 0.003105995883

0.05524828514 0.05596475719 0.055282116060.00870659784 0.008820976982 0.0087100779430.07581667376 0.08479411374 0.075856489130.01453732197 0 0.01454643320.03563807274 0.03610302643 0.035656362190.07407861527 0.08235078757 0.07412125449

0.111521673 0.1258847759 0.1115851680.007428920788 0 0.007433668051

0.1961822805 0.198745083 0.19627908450.04867066698 0.04930347975 0.04869838342

0.007300586035 0 0.0073050368370.2761024483 0.2796879218 0.2762646805

0.01145907462 0 0.01094572807

12.6339911748 12.6425842128 12.62274764414.7833413236 14.7946297464 14.768672871623.1873757956 23.2024152096 23.167295478

25.289160192 25.3044506916 25.26861296161.24728767028 1.24872251004 1.245904458483.22677589788 3.22737489576 3.22585484976

57.434488668 57.447076788 57.415427748

9.0511224696 9.0546152148 9.04619588478.816779208 87.04002672 78.783756516

15.1125714036 0 15.107773431637.04828994 37.059275088 37.032324984

77.009944824 84.53198502 76.981559976115.934643936 129.219043392 115.891188804

7.7228870688 0 7.7205299184203.94531594 204.0091767 203.85340498850.596590744 50.609364336 50.5776318847.5894740424 0 7.5869348832

287.027966664 287.095921092 286.92560872811.9125161936 0 11.3681187396

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