Ipr Pozos de Petroleo
33
DATOS BASICOS : Rsb= 350 Pc/Bbl Pr= 3000 Psi API= 30 Rd 912 pies Tr. = 200 o F Rw 0.354 pies SGg = 0.7 Kr 30 md Tsep= 83.5 oF Kro 0.25 md Psep= 230 Psi ht 40 pies Daño S 0 hp 20 pies RGA 0 Pc/Bbl SGo = 0.876 Tr= 660 o R Pb(psi) Standing 2006 Lasater 2599 2979 Vasquez 2095 2237 Glazo 1854 Presion Asumida Rs Fact. Bo Visc. Uo Densd. Pet Psi Pc/Bbls Bo (Bl/BF) cp Lb/Pc 3000 350 1.2106 1.278 46.65 2834 350 1.2129 1.266 46.74 2669 350 1.2153 1.253 46.83 2503 350 1.2179 1.241 46.93 2338 350 1.2207 1.229 47.04 2172 350 1.2236 1.216 47.15 Presion burb. 2006 350 1.2269 1.20 47.28 1841 316 1.2112 1.28 47.62 1675 283 1.1958 1.36 47.97 1510 250 1.1808 1.45 48.32 1344 218 1.1662 1.54 48.66 1178 187 1.1522 1.65 48.99 1013 156 1.1388 1.76 49.32 847 127 1.1259 1.88 49.63 682 98 1.1137 2.02 49.93 516 71 1.1022 2.16 50.22 100 150 200 250 300 350 400 Relacion de Solubilidad Rs
description
Ejercicios
Transcript of Ipr Pozos de Petroleo
DATOS BASICOS :
Rsb= 350 Pc/Bbl Pr= 3000 PsiAPI= 30 Rd 912 pies
Tr. = 200 o F Rw 0.354 pies
SGg = 0.7 Kr 30 md
Tsep= 83.5 oF Kro 0.25 md
Psep= 230 Psi ht 40 piesDaño S 0 hp 20 piesRGA 0 Pc/Bbl
SGo = 0.876Tr= 660 o R
Pb(psi)Standing 2006Lasater 2599 2979
Vasquez 2095 2237Glazo 1854
Presion Asumida Rs Fact. Bo Visc. Uo Densd. Pet
Psi Pc/Bbls Bo (Bl/BF) cp Lb/Pc3000 350 1.2106 1.278 46.652834 350 1.2129 1.266 46.742669 350 1.2153 1.253 46.832503 350 1.2179 1.241 46.932338 350 1.2207 1.229 47.042172 350 1.2236 1.216 47.15
Presion burb. 2006 350 1.2269 1.20 47.281841 316 1.2112 1.28 47.621675 283 1.1958 1.36 47.971510 250 1.1808 1.45 48.321344 218 1.1662 1.54 48.661178 187 1.1522 1.65 48.991013 156 1.1388 1.76 49.32847 127 1.1259 1.88 49.63682 98 1.1137 2.02 49.93516 71 1.1022 2.16 50.22
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
Factor A para Bo 0.0331 e visc. Sat.= d visc. Sat.= c visc. Sat.= b visc. Sat.=z vis. Pet Muerto 2.4255y vis. Pet Muerto 266.38x vis. Pet Muerto 0.5616uod= 2.644
1.309 0.385 0.030 0.7401.184 0.348 0.027 0.755
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
1.0000
1.0500
1.1000
1.1500
1.2000
1.2500
Factor Volumetrico
Factor Volumetrico
Presion
Bo
Bb
l/B
f
1.058 0.311 0.024 0.7700.935 0.275 0.022 0.7870.815 0.240 0.019 0.8050.698 0.205 0.016 0.8240.584 0.172 0.013 0.8440.474 0.139 0.011 0.8650.368 0.108 0.008 0.8880.267 0.078 0.006 0.913
Tr= 200 oFAPI= 30
SGg= 0.7PRROPIEDADES DEL GAS
Gravedad Especifica = 0.7PESO MELECULAR DEL GAS = 20.2748
Presion Temperatura Ppc Tpc PprPsi (oF) (oR) Psi (oR)
3000 200 660 664.37 382.97 4.51552834 200 660 664.37 382.97 4.26632669 200 660 664.37 382.97 4.01702503 200 660 664.37 382.97 3.76782338 200 660 664.37 382.97 3.51852172 200 660 664.37 382.97 3.26932006 200 660 664.37 382.97 3.02001841 200 660 664.37 382.97 2.77071675 200 660 664.37 382.97 2.52151510 200 660 664.37 382.97 2.27221344 200 660 664.37 382.97 2.02301178 200 660 664.37 382.97 1.77371013 200 660 664.37 382.97 1.5245847 200 660 664.37 382.97 1.2752682 200 660 664.37 382.97 1.0259516 200 660 664.37 382.97 0.7767
B120
Jlrivero: Para que funcione Tarner tiene que trabajar bajo rango
Standing. Pb= 18 (Rsb/SGg)^0.83 * 10^fracSGo= 0.88 frac= 0.00091 Tr - 0.0125 APIfrac= -0.193Pb= 2006 Psi
Darcy Blount GlazeCompresb. Co Qo Beta A B Qo
1/Psi BPD 1/psi Coef. Laminar Cof. Trb. BPD1.3398075E-05 0 380060531 1.2935 4.22115E-06 01.3808261E-05 129 380060531 1.2834 4.245013E-06 1291.4252713E-05 260 380060531 1.2734 4.27046E-06 2601.4736497E-05 393 380060531 1.2636 4.297705E-06 3931.5265811E-05 528 380060531 1.2539 4.327008E-06 5271.5848333E-05 665 380060531 1.2443 4.358688E-06 664
1.2792E-05 804 380060531 1.2349 4.393141E-06 8021.2698E-05 812 2033973825 155.3134 2.308389E-05 8101.2605E-05 820 2033973825 163.1475 2.2663E-05 8181.2515E-05 829 2033973825 171.6145 2.225653E-05 8271.2427E-05 838 2033973825 180.7672 2.18649E-05 8361.2343E-05 847 2033973825 190.6601 2.148863E-05 8451.2261E-05 857 2033973825 201.3466 2.112841E-05 8551.2183E-05 867 2033973825 212.8716 2.078514E-05 8651.2109E-05 878 2033973825 225.2579 2.046009E-05 8761.2039E-05 888 2033973825 238.4783 2.015514E-05 886
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
a visc. Sat.=
-0.2321-0.2122
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000 2834.40006895333
2668.80013790666
2503.20020685999
2337.60027581332
2172.00034476665
2006.40041371999
1840.80048267332
1675.20055162665
1509.60062057998
1344.00068953331
1178.40075848664
1012.80082743997
847.200896393303
681.600965346634
516.001034299965
1.0000
1.0500
1.1000
1.1500
1.2000
1.2500
Factor Volumetrico
Factor Volumetrico
Presion
Bo
Bb
l/B
f
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
44.00
45.00
46.00
47.00
48.00
49.00
50.00
51.00
Densidad lb/pc
Densidad lb/pc
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
0
0.000002
0.000004
0.000006
0.000008
0.00001
0.000012
0.000014
0.000016
0.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
-0.1918-0.1713-0.1509-0.1304-0.1102-0.0902-0.0706-0.0516
Tpr A B C D Z Densidadgrs/cc
1.7234 0.52446687 1.8148384802 0.05635685 1.0183121784 0.8635 0.15931.7234 0.52446687 1.6725205434 0.05635685 1.0183121784 0.8607 0.15101.7234 0.52446687 1.5351648856 0.05635685 1.0183121784 0.8591 0.14241.7234 0.52446687 1.4027584323 0.05635685 1.0183121784 0.8590 0.13361.7234 0.52446687 1.2752903265 0.05635685 1.0183121784 0.8602 0.12461.7234 0.52446687 1.1527516624 0.05635685 1.0183121784 0.8629 0.11541.7234 0.52446687 1.0351352359 0.05635685 1.0183121784 0.8670 0.10611.7234 0.52446687 0.922435313 0.05635685 1.0183121784 0.8726 0.09671.7234 0.52446687 0.8146474138 0.05635685 1.0183121784 0.8796 0.08731.7234 0.52446687 0.7117681153 0.05635685 1.0183121784 0.8878 0.07801.7234 0.52446687 0.6137948698 0.05635685 1.0183121784 0.8974 0.06871.7234 0.52446687 0.5207258408 0.05635685 1.0183121784 0.9080 0.05951.7234 0.52446687 0.4325597566 0.05635685 1.0183121784 0.9196 0.05051.7234 0.52446687 0.3492957799 0.05635685 1.0183121784 0.9320 0.04171.7234 0.52446687 0.2709333955 0.05635685 1.0183121784 0.9450 0.03311.7234 0.52446687 0.1974723138 0.05635685 1.0183121784 0.9584 0.0247
LasaterPb= 18 (Rsb/SGg)^0.83 * 10^frac Mayor a 40Menor igual a 40frac= 0.00091 Tr - 0.0125 API Mo= 360 330
yg2= 0.520 0.498 C1C2
yg2 > 0.60 yg2<=0.60 C3
Pb SGg/Tr= 2.76 2.40Pb= 2599 2979 psi
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
44.00
45.00
46.00
47.00
48.00
49.00
50.00
51.00
Densidad lb/pc
Densidad lb/pc
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
0
0.000002
0.000004
0.000006
0.000008
0.00001
0.000012
0.000014
0.000016
0.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
X Y K VISCOSIDAD Bg BgCP scf/cf cf/scf
5.19668739 1.36066252 132.559645 0.0203 186.0778 0.005375.19668739 1.36066252 132.559645 0.0197 176.3890 0.005675.19668739 1.36066252 132.559645 0.0191 166.3801 0.006015.18685853 1.36262829 132.559645 0.0185 156.0857 0.006415.18685853 1.36262829 132.559645 0.0180 145.5479 0.006875.18685853 1.36262829 132.559645 0.0174 134.8155 0.007425.18685853 1.36262829 132.559645 0.0169 123.9431 0.008075.18685853 1.36262829 132.559645 0.0164 112.9884 0.008855.18685853 1.36262829 132.559645 0.0160 102.0109 0.009805.18685853 1.36262829 132.559645 0.0156 91.0693 0.010985.18685853 1.36262829 132.559645 0.0152 80.2194 0.012475.18685853 1.36262829 132.559645 0.0148 69.5115 0.014395.18685853 1.36262829 132.559645 0.0145 58.9893 0.016955.18685853 1.36262829 132.559645 0.0142 48.6878 0.020545.18685853 1.36262829 132.559645 0.0139 38.6323 0.025895.18685853 1.36262829 132.559645 0.0137 28.8383 0.03468
Vasques and Beggs
a= 0.816API <=30 API >30 API <=30 API>30 b= 0.1327.62 56.18 -0.51 c= -0.9890.914328 0.84246 -0.4711.172 10.393 Pb= 2095 2237
Glaso
10.98 3.268Pb= 1854
Se realizo una prueba de flujo tras flujo de cuatro puntos, cuya zona perforada es de 20 pies y su presion estatica es 4453 psi, Determinar los siguientes puntos
1.- Determinar la constante de Flujo laminar y turbulento C,D2. Determinar el maximo potencial AOF3. Determinar el C¨/C analizando todos los indicadores propuesto4. Según los indicadores recomendar si es posibles algunos trabajos a realizar 5.Determinar el maximo potencial si incrementamos las perforaciones al doble 6. Construir el IPR sin incrementar e incrementados las perforaciones
Pr= 4453 psi 19829209Tr= 180 oF
hp1= 30 pieshp2= 60 pies
Prueba Caudal Flujo Presion Fluyente Pr-Pwf/QoNo BPD PSI PSI/BPD1 545 4427 0.047712 672 4418 0.052083 746 4412 0.054964 822 4405 0.05839
Flujo estabilizado 650 4400 0.08154
C1= 0.0266D1= 0.00004AOF1= 10224 BPDC¨= 0.0265999999999999C¨/C= 1.000D2= 0.00001AOF2= 19814 BPD
500 550 600 650 700 750 800 8500.01
0.02
0.03
0.04
0.05
0.06
0.07
Metodo de Jones Blount Glaze
Metodo de Jones Blount GlazeLinear (Metodo de Jones Blount Glaze)
Caudal de Petroleo (BPD)
Pr-
Pw
f /
Qo
(P
si/
BP
D)
C=0.0266 PSI/BPD
0 2000 4000 6000 8000 10000 12000 14000 160000
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
f(x) = − 0.00002 x² − 0.0266 x + 4453R² = 1f(x) = − 0.00004 x² − 0.0266000000000005 x + 4453R² = 1
Sensibilidad de la Relacion del Indice de Productividad
Caudal con perf. Inic.Polynomial (Caudal con perf. Inic.)Caudal con incremento de Perf.Polynomial (Caudal con incremento de Perf.)
Caudal de Petroleo( BPD)
Pre
sio
n P
wf
( P
SI )
declinacion 0.2Construcion del IPR Metodo de Jones Bloun Glaze
Presion Asumida Caudal de Petroleo Caudal de Petroleosimple perf. Doble perf.
Pwf (psi) BPD BPD4453 0 03562 4398 82002850 6007 114012280 7046 134711824 7781 149391459 8325 160241167 8737 16845934 9053 17476747 9299 17967598 9491 18350478 9642 18651383 9761 18889306 9855 19078245 9930 19227196 9989 19346157 10037 19440125 10074 19515
0 2000 4000 6000 8000 10000 12000 14000 160000
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
f(x) = − 0.00002 x² − 0.0266 x + 4453R² = 1f(x) = − 0.00004 x² − 0.0266000000000005 x + 4453R² = 1
Sensibilidad de la Relacion del Indice de Productividad
Caudal con perf. Inic.Polynomial (Caudal con perf. Inic.)Caudal con incremento de Perf.Polynomial (Caudal con incremento de Perf.)
Caudal de Petroleo( BPD)
Pre
sio
n P
wf
( P
SI )
Pr^2-Pwf^2psi^2
230880310485363465425184469209
AOFtr= 10200 BPD Construcion del IPR Metodo SimplificadoAOFest= 9100 BPD Presion Asumida
n= 0.673Ctrans.= 0.12515767 BPD/PSI^2 Pwf (psi)
Cest.= 0.11166027 BPD/PSI^3 44533562285022801824
500 550 600 650 700 750 800 8500.01
0.02
0.03
0.04
0.05
0.06
0.07
Metodo de Jones Blount Glaze
Metodo de Jones Blount GlazeLinear (Metodo de Jones Blount Glaze)
Caudal de Petroleo (BPD)
Pr-
Pw
f /
Qo
(P
si/
BP
D)
C=0.0266 PSI/BPD
0 2000 4000 6000 8000 10000 12000 14000 160000
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
f(x) = − 0.00002 x² − 0.0266 x + 4453R² = 1f(x) = − 0.00004 x² − 0.0266000000000005 x + 4453R² = 1
Sensibilidad de la Relacion del Indice de Productividad
Caudal con perf. Inic.Polynomial (Caudal con perf. Inic.)Caudal con incremento de Perf.Polynomial (Caudal con incremento de Perf.)
Caudal de Petroleo( BPD)
Pre
sio
n P
wf
( P
SI )
100 1000 10000 10000010000
100000
1000000
10000000
100000000
f(x) = 553.131488128106 x − 20156.7323440089R² = 0.376594989673289
Metodo de Simplificado
Prueba de Flujo
Linear (Prueba de Flujo)
Caudal de Petroleo(BPD)
Pr^
2-P
wf^
2
AOFtran=10200 bpd
AOFest.=9100 BPD
145911679347475984783833062451961571251008064514133
0 2000 4000 6000 8000 10000 12000 14000 160000
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
f(x) = − 0.00002 x² − 0.0266 x + 4453R² = 1f(x) = − 0.00004 x² − 0.0266000000000005 x + 4453R² = 1
Sensibilidad de la Relacion del Indice de Productividad
Caudal con perf. Inic.Polynomial (Caudal con perf. Inic.)Caudal con incremento de Perf.Polynomial (Caudal con incremento de Perf.)
Caudal de Petroleo( BPD)
Pre
sio
n P
wf
( P
SI )
100 25001500 3600
25000 352583500 362569
11258 32541587
Construcion del IPR Metodo SimplificadoCaudal de Petroleo Caudal de Petroleo
Transiente EstabilizadoBPD BPD
0 05128 45757155 63838313 74169014 8042
100 1000 10000 10000010000
100000
1000000
10000000
100000000
f(x) = 553.131488128106 x − 20156.7323440089R² = 0.376594989673289
Metodo de Simplificado
Prueba de Flujo
Linear (Prueba de Flujo)
Caudal de Petroleo(BPD)
Pr^
2-P
wf^
2
AOFtran=10200 bpd
AOFest.=9100 BPD
9449 84309723 86749896 8829
10006 892710076 898910121 902910149 905510168 907110179 908110187 908810192 909210195 909510197 909710198 909810199 909910199 909910199 909910200 9100
100 1000 10000 1000001000
10000
100000
1000000
Reservorio III Reservorio II Reservorio I Reserv. III-IIPr= 4313 Pr= 3000 Pr= 2200Qo= 500 Qo= 1370 Qo= 1451Pwf= 3919 Pwf= 1760 Pwf= 1500IP= 1.27 IP= 1.10 IP= 2.07 IP=Presion (psi) Qo (BPD) Presion (psi) Qo (BPD) Presion (psi) Qo (BPD) Presion (psi)
4313 0 3000 0 2200 0 37024000 397 2500 552 2000 415 33023000 1666 2000 1105 1800 829 25352000 2935 1500 1657 1500 1451 17671000 4204 1000 2210 1000 2487 1000500 4839 500 2762 500 3524 500
0 5473 0 3315 0 4560 0
0 1000 2000 3000 4000 5000 6000 7000 8000 9000 10000 11000 12000 13000 14000
0
500
1000
1500
2000
2500
3000
3500
IPR COMPUESTO
Presion (psi)
Qo BPD
Pre
sio
n p
si
Reserv. (III-II)-I
2.3738 Presion QwQo (BPD) Presion (psi) Qo (BPD) Fondo
0 3002 0950 2695 1364
2771 2192 36004593 1643 60446414 1000 89017601 500 111258788 0 13348
2000 6002500 8003000 1200
0 1000 2000 3000 4000 5000 6000 7000 8000 9000 10000 11000 12000 13000 14000
0
500
1000
1500
2000
2500
3000
3500
IPR COMPUESTO
Presion (psi)
Qo BPD
Pre
sio
n p
si
DATOS BASICOS :
Rsb= 350 Pc/Bbl Pr= 3000 PsiAPI= 30 Rd 912 pies
Tr. = 165 Rw 0.354 pies
Tem. Superf. 90 oF Kr 30 md
SGg = 0.7 Kro 0.25 md
Tsep= 83.5 oF ht 40 piesPsep= 230 Psi hp 20 piesDaño S 10
RGA 0 Pc/Bbl o F
Profundidaf 5000 pies Presion Cab. 104 Psi
SGo = 0.876 Presion Fondo 837.7 Psi
Tr= 625 o R
Prof. Temp Presion Cal. PresionPies o F Psi Asum. Frac. burbuja Psi
0 90 104 -0.293 1593417 93 164 -0.290 1605833 97 224 -0.287 1617
1250 100 284 -0.284 16281667 104 344 -0.281 16402083 107 404 -0.277 16522500 111 464 -0.274 16642917 114 524 -0.271 16763333 118 584 -0.268 16883750 121 644 -0.265 17014167 125 704 -0.262 17134583 128 764 -0.258 17265000 165 838 -0.225 1865
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
Factor A para Bo 0.0271 e visc. Sat.= d visc. Sat.= c visc. Sat.= b visc. Sat.= a visc. Sat.=z vis. Pet Muerto 2.4255y vis. Pet Muerto 266.38
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
1.0000
1.0500
1.1000
1.1500
1.2000
1.2500
Factor Volumetrico
Factor Volumetrico
Presion
Bo
Bb
l/B
f
x vis. Pet Muerto 0.7024uod= 4.039
1.309 0.385 0.030 0.740 -0.23211.156 0.340 0.027 0.758 -0.20771.003 0.295 0.023 0.778 -0.18260.854 0.251 0.020 0.799 -0.15740.709 0.208 0.016 0.822 -0.13230.569 0.167 0.013 0.847 -0.10740.434 0.128 0.010 0.874 -0.08300.307 0.090 0.007 0.903 -0.05920.188 0.055 0.004 0.934 -0.03660.081 0.024 0.002 0.965 -0.0159
Tr= 165 oFAPI= 30
SGg= 0.7PRROPIEDADES DEL GAS
Gravedad Especifica = 0.7PESO MELECULAR DEL GAS = 20.2748
Presion Temperatura Ppc Tpc Ppr TprPsi (oF) (oR) Psi (oR)
3000 165 625 664.37 382.97 4.5155 1.63202811 165 625 664.37 382.97 4.2307 1.63202622 165 625 664.37 382.97 3.9458 1.63202432 165 625 664.37 382.97 3.6610 1.63202243 165 625 664.37 382.97 3.3761 1.63202054 165 625 664.37 382.97 3.0913 1.63201865 165 625 664.37 382.97 2.8064 1.63201675 165 625 664.37 382.97 2.5216 1.63201486 165 625 664.37 382.97 2.2367 1.63201297 165 625 664.37 382.97 1.9519 1.63201108 165 625 664.37 382.97 1.6670 1.6320918 165 625 664.37 382.97 1.3822 1.6320729 165 625 664.37 382.97 1.0973 1.6320540 165 625 664.37 382.97 0.8125 1.6320351 165 625 664.37 382.97 0.5276 1.6320161 165 625 664.37 382.97 0.2428 1.6320
B120
Jlrivero: Para que funcione Tarner tiene que trabajar bajo rango
Standing. Pb= 18 (Rsb/SGg)^0.83 * 10^fracSGo= 0.88 frac= 0.00091 Tr - 0.0125 APIfrac= -0.22485Pb= 1865 Psi
Pb(psi)Standing 1865Lasater 2461 2821
Vasquez 1973 2125Glazo 1788
DarcyPresion Asumida Rs Fact. Bo Visc. Uo Densd. Pet Compresb. Co Qo
Psi Pc/Bbls Bo (Bl/BF) cp Lb/Pc 1/Psi BPD3000 350 1.1887 1.765 47.56 1.134E-05 02811 350 1.1908 1.746 47.64 1.1743E-05 452622 350 1.1930 1.726 47.73 1.2186E-05 912432 350 1.1955 1.707 47.83 1.2676E-05 1382243 350 1.1981 1.687 47.93 1.322E-05 1862054 350 1.2010 1.667 48.05 1.383E-05 2351865 350 1.2041 1.65 48.17 1.2554E-05 2841675 309 1.1854 1.79 48.61 1.2441E-05 2871486 268 1.1668 1.94 49.04 1.2330E-05 2901297 228 1.1490 2.12 49.47 1.2222E-05 2931108 189 1.1319 2.32 49.89 1.2119E-05 296918 152 1.1157 2.55 50.30 1.2021E-05 299729 116 1.1004 2.80 50.69 1.1928E-05 302540 82 1.0862 3.08 51.05 1.1842E-05 305351 50 1.0731 3.38 51.39 1.1764E-05 308161 22 1.0616 3.71 51.69 1.1695E-05 311
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
0
50
100
150
200
250
300
350
400
Relacion de Solubilidad
Relacion de Solubilidad
Presion
Rs
3000
2834
.400
0689
5333
2668
.800
1379
0666
2503
.200
2068
5999
2337
.600
2758
1332
2172
.000
3447
6665
2006
.400
4137
1999
1840
.800
4826
7332
1675
.200
5516
2665
1509
.600
6205
7998
1344
.000
6895
3331
1178
.400
7584
8664
1012
.800
8274
3997
847.
2008
9639
3303
681.
6009
6534
6634
516.
0010
3429
9965
1.0000
1.0500
1.1000
1.1500
1.2000
1.2500
Factor Volumetrico
Factor Volumetrico
Presion
Bo
Bb
l/B
f
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
44.00
45.00
46.00
47.00
48.00
49.00
50.00
51.00
Densidad lb/pc
Densidad lb/pc
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
00.0000020.0000040.0000060.0000080.00001
0.0000120.0000140.0000160.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
A B C D Z Densidad Xgrs/cc
0.48436464087739 2.09900386 0.0639293 0.99249618 0.8330 0.1744 5.2803480.48436464087739 1.90670648 0.0639293 0.99249618 0.8285 0.1643 5.2803480.48436464087739 1.72279249 0.0639293 0.99249618 0.8261 0.1537 5.2803480.48436464087739 1.54713705 0.0639293 0.99249618 0.8259 0.1426 5.186858530.48436464087739 1.37963957 0.0639293 0.99249618 0.8280 0.1312 5.186858530.48436464087739 1.22022038 0.0639293 0.99249618 0.8325 0.1194 5.186858530.48436464087739 1.06881756 0.0639293 0.99249618 0.8395 0.1075 5.186858530.48436464087739 0.9253841 0.0639293 0.99249618 0.8488 0.0956 5.186858530.48436464087739 0.7898853 0.0639293 0.99249618 0.8605 0.0836 5.186858530.48436464087739 0.66229637 0.0639293 0.99249618 0.8744 0.0718 5.186858530.48436464087739 0.54260036 0.0639293 0.99249618 0.8902 0.0602 5.186858530.48436464087739 0.43078629 0.0639293 0.99249618 0.9077 0.0490 5.186858530.48436464087739 0.32684753 0.0639293 0.99249618 0.9263 0.0381 5.186858530.48436464087739 0.23078048 0.0639293 0.99249618 0.9458 0.0276 5.186858530.48436464087739 0.14258344 0.0639293 0.99249618 0.9654 0.0176 5.186858530.48436464087739 0.06225581 0.0639293 0.99249618 0.9846 0.0079 5.18685853
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
00.0000020.0000040.0000060.0000080.00001
0.0000120.0000140.0000160.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
LasaterPb= 18 (Rsb/SGg)^0.83 * 10^frac Mayor a 40Menor igual a 40frac= 0.00091 Tr - 0.0125 API Mo= 360 330
API <=30yg2= 0.520 0.498 C1 27.62
C2 0.914328yg2 > 0.60 yg2<=0.60 C3 11.172
Pb SGg/Tr= 2.76 2.40Pb= 2461 2821 psi
Blount GlazeBeta A B Qo Estimulacion
1/psi Coef. Laminar Cof. Trb. BPD S=0380060531 4.2245 4.1483E-06 0 0380060531 4.1849 4.1703E-06 45 109380060531 4.1457 4.1939E-06 91 220380060531 4.1069 4.2195E-06 138 333380060531 4.0687 4.2474E-06 186 447380060531 4.0310 4.2779E-06 235 564380060531 3.9940 4.3116E-06 284 683
2033973825 511.4631 2.2563E-05 287 6902033973825 548.1743 2.206E-05 290 6962033973825 589.1566 2.1579E-05 292 7032033973825 634.9794 2.112E-05 295 7102033973825 686.2593 2.0687E-05 298 7182033973825 743.5954 2.0279E-05 302 7252033973825 807.3962 1.9899E-05 305 7322033973825 877.4212 1.9552E-05 308 7402033973825 951.4223 1.9247E-05 311 747
0 100 200 300 400 500 600 700 8000
500
1000
1500
2000
2500
3000
3500
Comportamiento del Indice de Productividad
IPR con Daño
IPR estimulado
Caudal de Petroleo BPD
Pre
sio
n P
si
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
0.000
0.500
1.000
1.500
2.000
2.500
Viscosidad cp
Viscosidad cp
3000 2834.4000689533
3
2668.8001379066
6
2503.2002068599
9
2337.6002758133
2
2172.0003447666
5
2006.4004137199
9
1840.8004826733
2
1675.2005516266
5
1509.6006205799
8
1344.0006895333
1
1178.4007584866
4
1012.8008274399
7
847.20089639330
3
681.60096534663
4
516.00103429996
5
44.00
45.00
46.00
47.00
48.00
49.00
50.00
51.00
Densidad lb/pc
Densidad lb/pc
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
00.0000020.0000040.0000060.0000080.00001
0.0000120.0000140.0000160.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
Y K VISCOSIDAD Bg BgCP scf/cf cf/scf
1.3439304 125.662903 0.0208 203.6977 0.004911.3439304 125.662903 0.0200 191.8784 0.005211.3439304 125.662903 0.0192 179.4826 0.00557
1.36262829 125.662903 0.0181 166.5686 0.006001.36262829 125.662903 0.0174 153.2171 0.006531.36262829 125.662903 0.0167 139.5295 0.007171.36262829 125.662903 0.0161 125.6235 0.007961.36262829 125.662903 0.0155 111.6271 0.008961.36262829 125.662903 0.0150 97.6708 0.010241.36262829 125.662903 0.0145 83.8798 0.011921.36262829 125.662903 0.0141 70.3660 0.014211.36262829 125.662903 0.0137 57.2215 0.017481.36262829 125.662903 0.0133 44.5136 0.022471.36262829 125.662903 0.0131 32.2821 0.030981.36262829 125.662903 0.0128 20.5384 0.048691.36262829 125.662903 0.0127 9.2665 0.10792
3000
2834
.4000
6895
333
2668
.8001
3790
666
2503
.2002
0685
999
2337
.6002
7581
332
2172
.0003
4476
665
2006
.4004
1371
999
1840
.8004
8267
332
1675
.2005
5162
665
1509
.6006
2057
998
1344
.0006
8953
331
1178
.4007
5848
664
1012
.8008
2743
997
847.2
0089
6393
303
681.6
0096
5346
634
516.0
0103
4299
965
00.0000020.0000040.0000060.0000080.00001
0.0000120.0000140.0000160.000018
Compresibilidad 1/psi
Compresibilidad 1/psi
presion
com
pre
sib
ilid
ad
Vasques and Beggs Glaso
a= 0.816API >30 API <=30 API>30 b= 0.13 10.7156.18 -0.54 c= -0.989 Pb=0.84246 -0.5010.393 Pb= 1973 2125
0 100 200 300 400 500 600 700 8000
500
1000
1500
2000
2500
3000
3500
Comportamiento del Indice de Productividad
IPR con Daño
IPR estimulado
Caudal de Petroleo BPD
Pre
sio
n P
si
3.2521788
0 1000 2000 3000 4000 5000 60000
20
40
60
80
100
120
140
160
180
f(x) = 0.0109505494505495 x + 85.9505494505495R² = 0.823168317864191
Chart Title
ll
Linear (ll)
0 1000 2000 3000 4000 5000 60000
20
40
60
80
100
120
140
160
180
f(x) = 0.0109505494505495 x + 85.9505494505495R² = 0.823168317864191
Chart Title
ll
Linear (ll)
0 1000 2000 3000 4000 5000 60000
100
200
300
400
500
600
700
800
900
f(x) = 0.145083956043956 x + 102.343956043956R² = 0.99979537103084
Chart Title
presi
Linear (presi)
0 1000 2000 3000 4000 5000 60000
100
200
300
400
500
600
700
800
900
f(x) = 0.145083956043956 x + 102.343956043956R² = 0.99979537103084
Chart Title
presi
Linear (presi)
0 1000 2000 3000 4000 5000 60000
20
40
60
80
100
120
140
160
180
f(x) = 0.0109505494505495 x + 85.9505494505495R² = 0.823168317864191
Chart Title
TEMP.
Linear (TEMP.)
PROF
TE
MP
0 1000 2000 3000 4000 5000 60000
20
40
60
80
100
120
140
160
180
f(x) = 0.0109505494505495 x + 85.9505494505495R² = 0.823168317864191
Chart Title
TEMP.
Linear (TEMP.)
PROF
TE
MP
1 110 10
100 1001000 1000
10000100000
1000000
12250
25632416552143
100025
1 10 100 10001
10
100
1000
1 10 100 10001
10
100
1000
