Reservoir Fluid Study - Ntnu
lntertekRESERVOIR FLUID STUDYSM ENERGYWELL: RUSHFINAL REPORTPrepared forSM ENERGYBylntertek Westport ·rechnology Center6700 Portwest DriveHouston, Texas 77024(713) 479-8400 (Phone)(713) 864-9357 (Fax)www.westportl .comSeptember 9, 2014
, lntertekRESERVOIR FLUID STUDYWTC-14-00-1-119-SM ENERGY -RUSI-I - RECOMBINED FLUIDI · RESERVOIR FLUID STUDYTABLE OF CONTENTSList ofTablesList of FiguresIIiiiRESULTS AND DISCUSSIONSUMMARY2APPENDIX ASample Validation24APPENDIX 8Differential Liberation Material Balance28APPENDIXCDifferential Liberation - Compositional Analyses Of Liberated GasProject No.: WTC-14-00-1-11931
lntertekRESERVOIR FLUID STUDYWTC-14-00././29 - SM ENERG ' ·RUSH - RECOMBINED FLUIDLIST lC2C3C4CSC6C7CSC9SAMPLE COLLECTION DATACOMPOSITIONAL ANALYSIS OF RESERVOIR FLUIDOIL COMPRESSIBILITY @ 248.0 F ( 120.0 C)CONSTANT COMPOSITION EXPANSION@248.0 F (120.0 C)DIFFERENTIAL LIBERATION OIL PROPERTIES@248.0 F (120.0 C)DIFFERENTIAL LIBERATION GAS PROPERTIES@248.0 F (120.0 C)DIFFERENTIAL LIBERATION FLUID VISCOSITY @ 248.0 F ( 120.0 C)COMPOSITIONAL ANALYSIS OF LIBERATED GAS @ 248.0 F ( 120.0 C)COMPOSITIONAL ANALYSIS OF RESIDUAL OILCORRELATIONS OF MEASURED PVT LABORATORY DATASEPARATOR TEST CORRECTED DL OIL PROPERTIES @ 248.0 F (120.0 C)COMPOSITIONAL ANALYSIS OF RESERVOIR FLUIDCOMPOSITIONAL ANALYSIS OF FLASHED OILCOMPOSITIONAL ANALYSIS OF FLASHED GASDIFFERENTIAL LIBERATION @ 248.0 F (120.0 C) - MATERIAL BALANCEDIFFERENTIAL LIBERATION GAS COMPOSITION @2,915 psia (20.10 MPn)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 2,5 15 psia (17.34 MPn)DIFFERENTIAL LIBERATION GAS COMPOSITION @2, l 15 psia (14.58 MPn)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 1,715 psia (11.82 MPn)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 1,315 psia (9.06 MPa)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 915 psia (6.31 MPa)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 615 psia (4.24 MPa)DIFFERENTIAL LIBERATION GAS COMPOSITION @3 15 psia (2.17 MPa)DIFFERENTIAL LIBERATION GAS COMPOSITION @ 15 psi a (0.10 MPa )Project No.: 637383940ii
lntertekRESERVOIR FLUID STUDYH'TC-J.1-00-1-129 - SM ENERG}' - RUSI/ - RECOMBINED FLUIDLIST OF IGUREFIGUREFIGUREr-IGUREI2345CONSTANT COMPOSITION EXPANSION@248.0 F (120.0 C)DIFFERENTIAL LIBERATfON OIL DENSITY@248.0 F (120.0 C)DIFFERENTIAL LIBERATION OIL FORMATION VOLUME FACTOR @ 248.0 F ( 120.0 C)DIFFERENTIAL LIBERATION GAS-OIL RATIOS@248.0 F (120.0 C)DIFFERENTIAL LIBERATION OIL VISCOSITY @ 248.0 F ( 120.0 C)DIFFERENTIAL LIBERATION GAS DEVIATION FACTOR @ 248.0 F ( 120.0 C)67DIFFERENTIAL LIBERATION GAS VOLUME FACTORS@248.0 F (120.0 C)DIFFERENTIAL LIBERATION GAS GRAVITY @ 248.0 F ( 120.0 C)89DIFFERENTIAL LIBERATION GAS VISCOSITY @ 248.0 F (120.0 C)10 LIBERATED GAS COMPOSITION PROFILE @248.0 F (120.0 C)Bl DIFFERENTIAL LIBERATION@248.0 F (120.0 C) - MATERIAL BALANCEProject No. : H'TC-J.1-00-14291415161718192021222330iii
lntertekRESERVOIR FLUID STUDYll'TC-1./-00././29 - SM ENERGY - RUSH - RECOMBINED FLUIDRESULTS AND DISCUSSIONThe reservoir fluid study was conducted on a recombined sample prepared from separator oil andseparator gas collected from Well RUSH.The sample collection data is provided in Table I and the sample validation data of the reservoirfluid used in this study is given in Appendix A.Table 2 provides the compositional analysis of the RECOMBINED sample.The PVT cell was charged with a portion of the live oil sample and a constant compositionexpansion experiment (CCE) was performed on the oil. Table 3 provides the CCE results of theaverage compressibility of the reservoir fluid at pressures above the bubblepoint. Table 4 containsthe complete CCE results with the exception of the data already presented in Table 3. Figure Ishows the relative total volume (V/Vsat) data and Y-function with respect to pressure.Table 5 contains various property measurements performed on the differentially liberated oil belowthe bubblepoint including live oil density, oil formation volume factor and gas-oil ratios, which areshown in Figures 2 through 4, respectively.Table 6 contains a summary of the properties of the differentially liberated gas including gasgravities, deviation factors, gas formation volume factors and gas expansion factors. The gasdeviation factor (Z), gas formation volume factor and gas expansion factor, and gas gravity areshown in Figures 6 through 8, respectively.Table 7 provides the results of the reservoir fluid viscosity measurements. This data is representedby Figures 5 and 9. Gas phase viscosity was calculated using the compositional data and the Lee,Gonzalez, Eakin correlation.Table 8 summarizes the effluent gas compositions from each pressure stage during the differentialliberation experiment. Figure 10 shows this data plotted on semi-log co-ordinates. Table 9presents the compositional analysis of the residual oil at completion of the experiment.Table to provides the correlations of the measured PVT Data. Table 11 provides the oil formationvolume factor and solution gas-oil ratio from differential liberation corrected from single-stagesepartor test parameters.Appendix B contains the material balance check performed for this experiment. It is displayed asformation volume factors so that the balance can be checked on a point by point basis. Appendix Ccontains the compositional analyses of the liberated gases from the differential liberation test.Project No.: JVTC-14-00././29I· I
lntertek'RESERVOIR FLUID STUDYll'TC-14-004429 - SM ENERGr - RUSI/ - RECOMBINED FLUIDSUMMARYMAIN PVT RESULTSINITIAL RESERVOIR CONDITIONSReservoir PressureReservoir Tern erature:5866 psia248.0 FCONSTANT COMPOSITION EXPANSION 248.0 FSaturation Pressure32901.1 1004E-05Compressibility @ Reservoir Pressure2.15276E-05Com ressibilit , Saturation PressureDIFFERENTIAL LIBERATION 6il 248.0 F (120.0 C)At Saturation PressureOil Fonnation Volume Factor1.7373Solution Gas-Oil Ratio1255.22Oil Density0.6181Oil Viscosity0.438At Ambient Pressure0.7938Residual Oil Density1.185Residual Oil ViscosityAt Stock Tank Conditions0.8341Residual Oil DensityAPI Gravity38.1SINGLE-STAGE SEPARATOR TESTAt Saturation PressureOil Fonnation Volume FactorSolution Gas-Oil RatioAt Stock Tank ConditionsResidual Oil DensityAPI GravityProject No.: IJ'TC-14-00-/.129120.0 Cpsia1psia"1sia"res.bbl/STBscf/STBg/cm3cp40.44 MPa120.0 c22.68 MPa11.61 OOE-03 MPa"13.1223E-03 MPa"1.7373223.56618.10.438res.m3/ m3m3/ m3kg/m3mPa.sg/cm3cp793.8 kg/m31.185 mPa.sg/cm3834.1 kg/m338.11.6648 res.bbl/STBI 020.61 scf/STB0.8309 g/cm338.81.6648 res.m3/m3181.77 m3/m3830.9 kg/m338.8I-2
lntertek RESERVOIR FLUID STUDYWTC-14-00././29 - SM ENERGY - RUSH - RECOMBINED FLUIDTABLE 1SAMPLE COLLECTION DATAProject File:Operator Name:Pool or Zone:Field or Area:Well Location:Fluid Sample:Sampling Company:Name of Sampler:Sampling Date:Sampling Point:Sampling Temperature:Sampling Pressure:WTC-14-004429SM ENERGYRUSHRECOMBINEDSM ENERGYSEPARATOR160 F35.00 psia71.1 c0.24 MPa248 F5866 psia120.0 c40.44 MPaReservoir Temperature:Reservoir Pressure:Initial Reservoir Pressure (Pi)Depth of Reported PiProject No.: lf'TC- 1./-00././29psiaNIAftNI AMPam
-lntertekRESERVOIR FLUID SfUDYWTC-1./-00./.119 - SM ENERGY - RUSH - RECOMBINED FLUIDTABLE2COMPOSITIONAL ANALYSIS OF RESERVOIR FLUIDComponentNameINitrogenCarbon DioxideHydrogen acontanes plusC 26C21C2sC29C30C31CnC33C34C3sC36 MoleFr 05410.00840.03010.0 1410.0 1890.02570.04210.04790.02770.02380.0 1950.0 60.00600.00530.00480.00440.00390.00370.003 10.00300.00270.00230.00220.00190.00170.00 160.00 140.0 1240.00140.00450.00000.08060.02470.02740.00560.020 10.01 0.03420.03170 .03020.02710 .02630.02630.02520.02090.01990.01870.01760.01670 .01530.01540.01310.01340.01240.01120.01070 .00980.00910.00870 .00810.1076Calculated PropertiesTotal SampleMolecular WeightC 87.04FractionMo lecular WeightMole FractionDensity (glee)199.580.35250.8367C 7 FractionMolecula r WeightMole FractionDensity (glee)208.500.32680.8427C 11 FractionMolecular WeightMole FractionDensity (glee)294.320.16570.8817.,.,,.,. -.,,., uo----2 c uo e c ce caaaaaacoauueacacn6eac5c6a1.0000Project No.: WTC-1./-00././191.0000I-4
lntertekW-RESERVOIR FLUID STUDYIVTC-14-00./429 - SM ENERGr - RUSH - RECOMBINED FLUIDTABLE3OIL COMPRESSIBILITY @ 248.0 F (120.0 C)Pressure Ran2eFrom(psia)To(psia)801570155866501545154015351 ' 701558665015451540153515319-0 p Pressure 8I24.23'Psal - Saturation PressureProject No.: .68· P.salAverageCompressibility(psf1 )l.0448E-05I.I IOOE-05J.2616E-051.4608E-05l.5972E-05J.8133E-052.1 8 -osAverageCompressibility(MPa. 1 )l .5 153E-03l .6100E-03l.8299E-032.l 187E-032.3166E-032.6300E-03S: 28lt 03
lntertekRESERVOIR FLUID STUDYWTC-/.1-00./429 - SM ENERGJ' - RUSH - RECOMBINED FLUIDTABLE4CONSTANT COMPOSITION EXPANSION @ 248.0 F (120.0 C)Pressure(psia)80 1570 15586650154515401535153290 1046859672485RelativeVolume -Function(MPa)11 0.1018.8117.5216.2314.9513.6612.3711 50.9711110.9782560.9861320 .9951541.0000001.0232931.0506281.0829121.1213211. 47372.0760952.459 1273.0663284.158539Fluid 0.62110.6181 2.58762.53372.47982.42582.37 192.31802.26402.2IOI2. 15622.10222.04831.99441.94041.88651.8326Volume nt indicated pressure per volume at saturation pressure(1)[2}Y Function ((Psat-P)/P)/(Rclative Volume - I)Psat - Saturation PressureProject No.: ll'TC-1./· 00././291-6
lntertek'RESERVOIR FLUID STUDYWTC-14-004429 - S!lil ENERGJ' - RUSH - RECOMBINED FLUIDTABLESDIFFERENTIAL LIBERATION OIL PROPERTIES @ 248.0 F (120.0 C)IOil Formatio nT otal Format io nVolume F a ctorVolume Fa ctorIll121(os ia )(MPa)O .7289gi6llBl0 'ii.W7B1 41.21921.1 6671.0578PressureS91Piitl1 58883.20764.46086.528112.4645152.402611Gas-Oil 5.221255.221255.221255.221255.221255.22[!SSa .00Gas-O il Rat ioSolutionLibe 001 S 000.000.000.000.000.000.001I1ruooJ 56Density of Residual Oil 0.8341 g/cm3 (834.1 kg/m3) @ 60 F (288.7K)API Gravity ofResiduol Oil 38.1l I J Barrels (Cubic melers) ofoil ot indicated pressure ond temperature per barrel (cubic meter) of residual oil @ 60 F (288.7 K).[2] Tolal barrels (cubic meters) of oil and liberated gas at the indicated pressure and temperature per barrel (cubic meter) of residual oil @ 60 F (288.7 K).l'sat - Saturation PressureStandard conditions: 60 F (288.7 K) (c/l 14.696 psia (0.101325 MP11).-Project No.: WTC-14-0044291- 7
lntertek'RESERVOIR FLUID STUDYWTC-14-004429 - SM ENERG ' - RUSH - RECOMBINED FLUIDTABLE6DIFFERENTIAL LIBERATION GAS PROPERTIES @ 248.0 F (120.0 C)Gas GravityIncrementalCumulative{Air 1)(Air 1)Pressure(osla)[801570155866501545154015351532 1 !P.il'il 4434.5831.1327.6824.2321.6820.1017.3414.58I 1.829.066.314.242.170. 10I 78510.8819IGasDensity(g/cmiGas DeviationFactorGas FormationVolume FactorGas 44120.34996.50173.43150.29633.30717.1701.477Cubic feet (meters) of gos nt indicated pressure and temperature per cubic feet (meter) @ standard conditionsCubic feel (meters) of gos @ standard conditions per cubic feet (meter) @ indicated pressure and temperature.Psot - Saturation pressure- Standard conditions: 60 F (288.7 K) @l 14.696 psia (0.101325 MP11)lIJ[2]Project N o.: WTC-14-00./4291- 8
lntertekRESERVOIR FLUID STUDYJl'TC-14-00././29- SM ENERGY - RUSH - RECOMBINED FLUIDTABLE 7DIFFERENTIAL LIBERATION FLUID VISCOSITY @248.0 F (120.0 C)PressureIL.-(psis)CMPa )58515000400035003290 Psat sat - Saturation PressureProj ect No.: ll'TC-14-00././29Oil Viscosity(cp mPa.s)-Gas cositv 90.014380.01347O.Ol I0622.4726.2330.5935.8241.5047.9954.7566.59107.07
-lntertek·flRESERVOIR FLUID STUDYWTC-l -00-/.119·SM E.\'ERG r · RUSH· RECOMBINED FLUIDTABLESCOMPOSITIONAL ANALYSIS OF LIBERATED GAS@ 248.0 F (120.0 C)ComponentN2C02H2SClC2C3i·C4n·C4i.CSn·CSC6C7 0.00470.00540.00440.0120Differential Liberation Sta2e Pressure (psia/MPa)1315615915315159.066.314.240.102. 170.00640.01330.00000.78590.09470.051 1250.00010.01 0.03780.06301.0000 1.0000 1.0000 1.0000 1.0000 1.0000 J.0000Standard Conditions22.2021 .6422.0422.5022.6643.9226.430.7788 0.7664 0.7472 0.7611 0.7769 0.7823 0.91251.5163GrnviCalculated Pro rties of C7 ·@l Standard ConditionsMW(g/mol)101.78 101.84 102.27101.55 1101.25 1102.21 1103.74 1101.08 1100.61Densitv Ce/cc)0.7338 0.7338 0.7347 0.7336 0.7329 0.7348 0.7370 0.7324 0.7315Total1.00001.0000IProject No.: WTC- 14-0044291·10
lntertekRESERVOIR FLUID STUDYWTC-1./-00-/.129 - SM ENERG)' - RUSfl - RECO.\JBINED FLUIDProject No.: ll'TC-1./-00././29
lntertekRESERVOIR FLUID STUDYWTC-14-004-129 - SM ENERGY - RUSH - RECOMBINED FLUID'TABLE 10CORRELATIONS OF MEASURED PVT LABORATORY DATA--· . -. - --··-- --- ---·. -·--. -· ·---- . .-·. - . . . - .----y (-0.024833*x" 2 0.968804*x 1.041243)/( I .03 I 856*x 0.956503)R Squared 0.986075(P Psat)y (0.494648*x"2 0.544879*x l.314038)/(2.358709*x -0.009661)Relative Volume (V/Vsat)R Squared 0.999994DIFFERENTIAL LIBERATION (@, 248.0 F 1120.0 n(P Psat)r-(0.025927*x"2 0.760329*x 0.702912)/(1.190159*x 1.210596)Live Oil Density (glee)R Squared 0.994970(P Psat)y (-0.198838*x" 2 1.04543 I x 0.055006)/(1 .382887*x 0.068979)Live Oil Density (glee)R Sauared 0.999173(P Psat) y (-0.028047*x"2 l.355188*x I .346279)/(1.190159*x 1.210596)Oil FVF [I]R Squared 0.986075(P Psat)y (0.494727*x"2 0.828654*x -0.047454)/(0.794263*x -0.044923)Oil FVF [I]R Sauared 0.994520(P Psat)y (651.752832*x" 2 -42.179461*x 0.358224)/(3.080190*x -0.218130)GOR [2]R Sauared 0.995781(P Psat)y (0.090 I 84*x" 2 0.886312 x 0.343334)/(1.6 78630*x 1.501444)Oil Viscosity (cp mPa.s)R Squared 0.999870{P Psat)y (-0.722154*x"2 1.562558* : 0.229496)/(2.366382* : 0.189006)Oil Viscosity (cp mPa.s)R Sauared 0 .999863is the measured parameter and x P/Psat, dimensionlessy[I] Barrels (Cubic meters) ofoil at indicated pressure and temperature per barrel (cubic meter) of residual oil @ 60 F (288.7 K).r11 Cubic feet (meters) of l!.as at indicated oressure and temoerature oer cubic feet (meter) (@ standard conditionsRelative Volume (V/ Vsat)Project No.: WTC-14-00-1429(P Psat)I - 12
lntertek"RESERVOIR FLUID STUDYWTC-14-004429- SM ENERG)' - RUSH - RECOMBINED FLUIDTABLE 11SEPARATOR TEST CORRECTED DL O IL PROPERTIES @ 248.0 F (120.0 C)Oil Formation Volume 824.23s2 J' t1 l .5811.829.066.314.242.170 1.21921.16671.0578G ns-Oil 7901.59941.61671.62861.64 171.6567u: 22I!l 6.070.00Gas-Oil RntioMeasuredC 11020.611020.611020.6 1JI\1 618 15.00672.24535.24401.38279.20155.8469. .580.00181.77181.77181.77181.77181.77181.77181.77I 00.00 'IDensity of Residual Oil 0.8341 sfcm3 (834.1 kg/m3) @ 60 F (288.7K)API Gravity ofResidual Oil 38.1[I] Barrels (Cubic meters) of oil at indicated pressure and temperature per barrel (cubic meter) of residual oil @ 60 F (288.7 K).[2] Total barrels (cubic meters) of oil and liberated gas at the indicated pressure and temperature per barrel (cubic meter) of residual oil @ 60 F (288.7 K).Psnt - Saturation PressureStandard conditions: 60 F (288.7 K) (ti! 14.696 psin (0.101325 MPa).-Project No.: WTC-14-0044291-13
lntertekYIRESERVOIR FLUID STUDYW/'C-l./·OOU19 SAi ENERGJ' - RUSH - RECOMBINED FLUIDFIGURE ICONSTANT COMPOSITION EXPANSION @ 248.0 F (120.0 I---------·----'IIIIIItIIIItI IIIIIIIIIIIIIIIIIIIIIIII 0ILJ -c:r--t::}.' :t -----;c.:1' ;;::;:.:.::.:.:;r-'-i:::.:.:::::::r'1------------ - - 1- - -w---- ---- ---IIIII-- --------- ---------- ------·---'-- *·- I.I.I---------t--------- ----------t----------t----------t---------- ---------i---------1IIIIIII1.00III1.50I---------- --------- ---------- ---------4----------f---------- --------- ---------IIIIIIIIIIIIIIIII'IIIII'IIItIIIIII- -- ----- --------- ---------- ----------r--------- ·- ---------r--------- --------IIIIIII ---------·---------- --------- ---------IIt----- ----------·--------.IIIIIIIII.IIIII'a;.:!IIIII,. 3.002.00IIIII --- ---------- I2.50IIIII0::IIIIt'al"'iiIIII3.50 t----i---------- --------- ----------t----------t----------t---------- ---------i---------1IIIIII4.00"' 40005000600070008000--------- ---------- -------- ---------- ---------4----------t---------- --------- 0010000.009000Pressure (psia)-0- Rclatlvc Volume - - Y-FunctionProject No.: WTC-14-00././29I - 14
lntertekRESERVOIR FLUID STUDYllTC-1 ./-00./.129 - SM ENERGY - RUSH - RECOMBINED FLUIDFIGURE2DIFFERENTIAL LIBERATION OIL DENSITY @ 248.0 F (120.0 C)0.85JI0.80 ''I'''. . . II1ttIII.,III IIIIIIIIIIIIIttI:IIIIIIIIIII ---------- ---------- -------,----------,----------,---------t0.75III. III0.70IIIIIIIIIIIIII IIIII:I:III:III:IIIII IIIII0.6001000IIIII1·IIIIIIIIIIIII:III:IIttII,.,. - .,, - ------ ---------IIIIIIIIIII2000IIII300040005000Pressure (psia)Project No.: I IIIIII--- --------- ---------.&.----------'---------- ---------- ---------- ---------IIIIIIIII0.65I6000700080009000
lntertekRESERVOIR FLUID STUDYJJ'1C-14-00-/.129 - SM ENERGJ' - RUS/-1 - RECOMBINED FLUIDFIGURE3DIFFERENTIAL LIBERATION OIL FORMATION VOLUME FACTOR1.80248.0 F (120.0 C)IIiI1.70I,,.co1.60--JS.ti)-. - ---------- ---------- ---------- ---------- ---------IIItlIIIIIII---------- III:IIII:IItIIII- ---------- ---------- ---------- ---------- ---------- ---------- :II:IIIIIIIIIIIIIII: :IIi:I:Il IIIIIIIIII1.30IIIII--------- -------- ---------- ---------- ---------- ---------- ---------- ------·--- ---------'IIIIIIIIIIIII E0IIIII:I(.I., IIIII---------- ---------- -------- -------- ---------- ---------- ---------- ---------- -------'IIIIIII1.500E 0IIIIIffIIIIul'3II)I---------- ----------.,.'I!-.0II---------- ---------- ---------- ItII1.20IIIItI IIIIIII----- ---------- ---------- ---------- ---------- ---------- ---------- ---------- ---------IIIIIIII0IIIII IIIIIIIIIIIIIIIIIIIIIIttIII IIIIII--------- ---------- ---------- ---------- ---------- ---------- ----------t----------t---------1IIIII 00Pressure (psia)Project No.: WTC-14-00.J./29I· 16
lntertek'RESERVOIR FLUID STUDYWTC-14-004429 - SM ENERGY - RUSH - RECOMBINED FLUIDFIGURE 4DIFFERENTIAL LIBERATION GAS-OIL RATIOS@ 248.0 F (120.0 C)1400I1200IIII-------- ----------t----------i-----------:----------- IIII. I ---------- ----------·---------- - III- ----.I ---------- 1IIIIII1IijtIIIIIIIIIIIIIIIII ----------4----------- ----------f---------- ----------4----------- IIII----------i------III---------- ----------T·---------, ----·-- -r---· - r-· ------ ItIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIIII II IIIIII II-----.L.- ------- ------L---------- ---------1I - ----- ---- I --- ------ - ----tIIIII200ItII IIII---------- ----------·---------- ---------- ---------- -·-------IIIIIIIII04000II IIIIII Pressure (psia) Solut ionProject No.: WTC-14-004429 LiberatedI - 17
lntertekRESERVOIR FLUID STUDYll'TC-1./-00././19 - SA/ ENERG " - RUSf-1 · RECOMBINED FLUIDFIGURESDIFFERENTIAL LIBERATION OIL VISCOSITY @ 248.0 F (120.0 IIIIIII::::IIII----L--- - --- II A ----------- -------------.L.------------- - ---------- 4 ----------- 1III0.80- u0III----------·--- --- - --·------------- ----------- ---t-------------- -------------·---- -------1IIIIIII "'IIIt------------ ------------- -·---------- ---·--·--·---.,.----· - - -. r -- T - -II0'III-------------t--------0 .6{) . IIIIIIIII0.20 -6IIIIIIIIII IIII------------- -------------t------------- -1II0.40IIII.JIIIIIIIIII--t------------- ------IIIIIIII IIIIIIaIIIIII-----.-------------- -------------f- ---r-------------T------ ------- ----- - - ---- ------------- -------------T----------- e (psia)Project No.: ll'TC-1./-00././19I - 18
lntertekRESERVOIR FLUID STUDY11'TC-/.l-OO.U19 - SA,/ ENERGY - RUSfl - RECOMBINED FLUIDFIGURE 6DIFFERENTIAL LIBERATION GAS DEVIATION FACTOR @ 248.0 F (120.0 C)I 02:IIIIII 00II.0IIfII I IIIIIt IIIIIIIIIIII0 tIIIJfIIIII-------- ------------- -------------- ------------. 'I -------------·---------- -ItIII:·;;:cIIIIII· II). -------------·-------------I--- -------------- ------------- -------------- ------------ -------------{------------ lIIIf096uc:su.cf---------1-------------- ------------- -------------- --------------t-------------- -------------098NII-------------1-------------- ------------- -------------- ------------i------------- IIIIIIIIIIIIIIIIIIIIIIIIIIIIIlI------------- --------------r-- --- .,. - ----------- ------------- 'IIIIIIII0860Pressure (psia)Project No.: ll'TC-14-004419250030003500
lntertek"RESERVOIR FLUID STUDYll'TC- 14-00././29 - SM ENERGY - RUSH - RECOMBINED FLUIDFIGURE 7DIFFERENTIAL LIBERATION GAS VOLUME FACTORS @ 248.0 F(l20.0 C)180IIIIIII160------------4--------- ----t------------- ------------- --------M· 40------------ ------------- -------------4-----M-------- -------III0,60IIIIIIIIIIIIIIIIIIIIIIIIIIII0.50 - -ItI120 ,-.I ----------t-------------- -------------r-----------1III0.40 . ---II ;:::;u. 1IIII l:.L.I'801IIIIII Q.II60II)(UJc"' '.8------ -------'40tIIII0. 10200100015002000250030000)500Pressure (psia) FonnationProject No.: JJ'TC-/.1-00././29 ExpansionI 20
lntertekRESERVOIR FLUID STUDYIJ'TC-1 ./-004./19 - SM ENERGY - RUSH - RECOMBINED FLUIDFIGURESDIFFERENTIAL LIBERATION GAS GRAVITY @ 248.0 F (120.0 C)1.60IIIIIIe1.40III IIIIIIIIIIIIII1IIIItItIIIIIII------------ -------------- -------------- --------------·-------------- -------------- -------------'IIIIIIIIIIIIIII 20IIItItIII----·---- -------------- IIIIIIIIIIIIIIIIIIaIII1.!::I. 1.00 0ttII------ -------------- -------------- -------------- -------------- -------------- IIIIIIIII---------- --------------t--------------t-------------- ----------- -i--------------i·;;:: I0 060IIIIIItII-------------- --------------t-------------- --------:SII:III III"' ----------- -------------- -------------- -------------- II'It:IIIIII020II:IIIII IItII------------- -------------- ssure (psia)Project No.: WTC-14-004419I- 2l
lntertekRESERVOIR FLUID STUDYll'TC-1-1-00.J.129 - SM ENERGr - RUSH - RECOMBINED FLUIDFIGURE9DIFFERENTIAL LIBERATION GAS VISCOSITY @ 248.0 F (120.0 C)0.025IIIIIIIIIIII:IIIIIIIII IIII-------------·------------- -------------- -------------f------------- -------- -------------·----- ------ -------------- ------------ III----------- ·----------0.015IIIIII:I-- ----- IItItItIII1IIII--- --------·--------- -- -·-------·- - ------------- ------------- -------------- -------f-------------i-------------- --- --------f------------- -------------- -----------1IIIII0.005IIIIIIIIIIt II :IIIIIIItIIIII'IIIII'Ii:IIIII IIIt0.0000500IOOO150020002500300035-00Pressure (psia)Project No.: ll'TC- /.1-00-1-129I - 22
lntertekRESERVOIR FLUID STUDYll'TC-14-00././29 - SM ENERGY - RUSH - RECOMBINED FLUIDFIGURE 10LIBERATED GAS COMPOSITION PROFILE @ 248.0 F (120.0 C)t.000II IIIIIII0. 100III--- ------------- -------------- ------------- --------------'c.9tiJ:0.010Q)0 ,II:'''''IIIIII----- -- - - -- L ---------.&.-----·- -·------- ---- '"'- ressure (psia)Project No.: ll'TC-1./-00././291- 23
lntertekRESERVOIR FLUID STUDYWTC-1-1-00-/.129-SM ENERGY - RUSH - RECOMBINED FLUIDAPPENDIX ASAMPLE VALIDATIONProject No. : WTC-1./-00-1429
---1ntertekRESERVOIR FLUID STUDYWTC-14-004429 - SM ENERGY - RUSH - RECOMBINED FLUIDTABLE AlCOMPOSITIONAL ANALYSIS OF RESERVOIR FLUIDComponentNameNitrogenCarbon DioxideHydrogen anen-PentaneHexanesHeptanesOctanesNonanesDecan esU
lntertek RESERVOIR FLUID STUDY ll'TC-1./-00././29 -SM ENERGY -RUSH -RECOMBINED FLUID RESULTS AND DISCUSSION The reservoir fluid study was conducted on a recombined sample prepared from separator oil and separator gas collected from Well RUSH. The sample collection data is provided in Table I and the sample validation data of the reservoir
modesto livermore FREEPORT REGIONAL WATER FACILITY S o u t h . Briones Reservoir Upper San Leandro Reservoir Chabot Reservoir San Antonio Reservoir Reservoir Calaveras Reservoir Crystal Springs Reservoir San Andreas Reservoir Bethany Reservoir . cooking, bathing, filling swimming pools
Reservoir characterization is a combined technology associated with geostatistics, geophsics, petrophysics, geology and reservoir engineering and the main goals of reservoir characterization research are to aid field de velopment and reservoir management teams in describing the reservoir in sufficient detail, developing 3D/4D data for reservoir
L M A B CVT Revision: December 2006 2007 Sentra CVT FLUID PFP:KLE50 Checking CVT Fluid UCS005XN FLUID LEVEL CHECK Fluid level should be checked with the fluid warmed up to 50 to 80 C (122 to 176 F). 1. Check for fluid leakage. 2. With the engine warmed up, drive the vehicle to warm up the CVT fluid. When ambient temperature is 20 C (68 F .
environment. To optimize the effectiveness of each reservoir, we must be able to predict the rate of reservoir sedimentation processes, especially reservoir-sediment trap efficiency. Reservoir-sediment trap efficiency is the fraction of the sediment transported into a reservoir that is deposited in that reservoir, usually expressed as a percentage.
Reservoir Characteristics Number of Flowing Fluids in the Reservoir: The mathematical expressions that are used to predict the volumetric performance and pressure behavior of the reservoir vary in forms and complexity depending upon the number of mobile fluids in the reservoir. There are generally three cases of flowing systems:
Fluid Mechanics Fluid Engineers basic tools Experimental testing Computational Fluid Theoretical estimates Dynamics Fluid Mechanics, SG2214 Fluid Mechanics Definition of fluid F solid F fluid A fluid deforms continuously under the action of a s
Jul 09, 2015 · Tiny-Fogger/Tiny F07, Tiny-Compact/Tiny C07 Tiny-Fluid 42 Tiny FX Tiny-Fluid 42 Tiny S Tiny-Fluid 43 Unique 2.1 Unique-Fluid 43 Viper NT Quick-Fog Fluid 44 Viper NT Regular-Fog Fluid 45 Viper NT Slow-Fog Fluid 46 Martin K-1 Froggy’s Fog K-razy Haze Fluid 47 Magnum 2000 Froggy’s Fog Backwood Bay Fluid 48
Nama Mata Kuliah : Akuntansi Keuangan Lanjutan Kode Mata Kuliah : AKM 145001 Semester : 5 (lima) Sks/jam perminggu : 3 SKS/ 6 jam Jurusan/ Program Studi : Jurusan Akuntansi/ DIV Akuntansi Manajemen Dosen Pengampu : 1. Novi Nugrahani, SE., M.Ak., Ak 2. Drs. Bambang Budi Prayitno, M.Si., Ak 3. Marlina Magdalena, S.Pd. MSA Capaian Pembelajaran Lulusan yang dibebankan pada mata kuliah :Setelah .
