CALCULO DEL M(P)

DETERMINACION DEL FACTOR Z, Ug, Bg,

Gravedad Especifica = 0.69

SO MOLECULAR DEL GAS = 19.9893

Presion Temperatura Temperatura Ppc Tpc Ppr Tpr A

Psi (oF) (oR) Psi (oR)

0 145 605 665.042 380.659 0 1.589 0.464

200 145 605 665.042 380.659 0.301 1.589 0.464

400 145 605 665.042 380.659 0.601 1.589 0.464

600 145 605 665.042 380.659 0.902 1.589 0.464

800 145 605 665.042 380.659 1.203 1.589 0.464

1000 145 605 665.042 380.659 1.504 1.589 0.464

1200 145 605 665.042 380.659 1.804 1.589 0.464

1400 145 605 665.042 380.659 2.105 1.589 0.464

1600 145 605 665.042 380.659 2.406 1.589 0.464

1800 145 605 665.042 380.659 2.707 1.589 0.464

2000 145 605 665.042 380.659 3.007 1.589 0.464

N X Y X^2 X^3 X^4 XY X^2*Y

1 0 0 0 0 0 0 0

2 200 3 40000 8000000 1.60E+09 661.33425788 132266.85158

3 400 13 160000 64000000 2.56E+10 5303.8473277 2121538.9311

4 600 30 360000 216000000 1.30E+11 17932.250028 10759350.017

5 800 53 640000 512000000 4.10E+11 42509.218786 34007375.029

6 1000 83 1000000 1000000000 1.00E+12 82861.656048 82861656.048

7 1200 119 1440000 1728000000 2.07E+12 142573.1328 171087759.36

8 1400 161 1960000 2744000000 3.84E+12 224874.57538 314824405.54

9 1600 208 2560000 4096000000 6.55E+12 332549.28911 532078862.58

10 1800 260 3240000 5832000000 1.05E+13 467867.50327 842161505.89

11 2000 316 4000000 8000000000 1.60E+13 632560.50439 1265121009

Sumatorias 11000 1246 15400000 242000000004.05328E+13 1949693.31 3255155729

0 200 400 600 800 1000 1200 1400 1600 1800 20000

50

100

150

200

250

300

350

f(x) = 7.52705356241549E-05 x² + 0.00940351274914038 x − 1.51524973043131

Determinación del m(P)

Presión

m (p

)

B C D FACTOR DENSIDAD X Y K

Z lb/pc

0 0.068 0.983 1 0 5.330 1.334 122.157

0.081 0.068 0.983 0.979 0.629 5.330 1.334 122.157

0.172 0.068 0.983 0.956 1.288 5.330 1.334 122.157

0.273 0.068 0.983 0.933 1.980 5.330 1.334 122.157

0.383 0.068 0.983 0.910 2.705 5.330 1.334 122.157

0.504 0.068 0.983 0.889 3.463 5.330 1.334 122.157

0.633 0.068 0.983 0.869 4.250 5.330 1.334 122.157

0.773 0.068 0.983 0.852 5.059 5.330 1.334 122.157

0.922 0.068 0.983 0.837 5.882 5.330 1.334 122.157

1.081 0.068 0.983 0.826 6.711 5.330 1.334 122.157

1.250 0.068 0.983 0.817 7.535 5.330 1.334 122.157

Ecuacion Simultaneas

Eliminacion de Gauss-Jordan

11

11000

15400000

24200000000 11 11000 15400000

4.05328E+13 11000 15400000 24200000000

1949693.3114 15400000 24200000000 40532800000000

3255155729

1245.9371418 Resolviendo el sistema de Ecuaciones

0 -48400000 -9.680E+10

0 -96800000000 -2.087E+14

0 -7.30878720000001E+020

Los Valores determinado son:

8E-05 0.009

A B

DETERMINACION DE LOS MÍNIMOS CUADRADOS

ΣN ΣX ΣX^2 = ΣY

ΣN ΣX ΣX^2 ΣX^3 = ΣXY

ΣX ΣX^2 ΣX^3 ΣX^4 = ΣX^2Y

ΣX^2

ΣX^3

ΣX^4

ΣXY

ΣX^2Y

ΣY

0 200 400 600 800 1000 1200 1400 1600 1800 20000

50

100

150

200

250

300

350

f(x) = 7.52705356241549E-05 x² + 0.00940351274914038 x − 1.51524973043131

Determinación del m(P)

Presión

m (p

)

VISCOSIDAD Bg P/UZ DEL M(P) M(P) acum M(P)

CP scf/cf PSI/CP PSI/CP PSI/CP MMPSI^2/CP

0.0122 0 0 0 0

0.0124 11.938 16533 3306671 3306671 3

0.0126 24.444 33231 9952947 13259618 13

0.0129 37.575 49906 16627465 29887083 30

0.0132 51.346 66341 23249440 53136523 53

0.0137 65.731 82284 29725133 82861656 83

0.0142 80.656 97462 35949288 118810944 119

0.0147 96.007 111607 41813753 160624697 161

0.0153 111.635 124486 47218609 207843306 208

0.0160 127.365 135929 52083085 259926391 260

0.0168 143.011 145840 56353861 316280252 316

1245.9371418

1949693.3114

3255155729

Resolviendo el sistema de Ecuaciones

-7741317.865

-16619281035

-5.50136E+16

Los Valores determinado son:

-1.515

C

Ejemplo 4,1

Se tiene una prueba icronal y se desa conocer el potencial del reservorio y el IPR par los metodos: Simplificad, Jones blount Claze y LIT.

Datos

Pr= 10477 Psi Prof= 14300 pies

Tr= 270 ºF API= 59

Tc= 95 ºF SGg= 0.65

Choque Caudal Gas

Ch/64" hr psia psia MMscf/d BPD

estatica inicial 24 10477 9044

flujo 1 12 12 7815 5950 4.817 72

flujo 2 16 12 6009 4380 6.296 88

flujo 3 20 12 4865 3350 7.337 98

flujo 4 24 12 3978 2460 8.08 109

flujo extendido 16 38 6188 4500 6.281 89

Determinar las relaciones Gas-petroleo

Caudal Caudal RGC YIELD

Gas Condensado

MMscf/d BPD PC/BBl BBl/MMPC

4.817 72 66902.78 14.95

6.296 88 71545.45 13.98

7.337 98 74867.35 13.36

8.08 109 74128.44 13.49

6.281 89 70573.03 14.17

promedios 71603.41 13.97 monofasico

CALCULO DE LA PRESIÓN DE ROCIO

K1= 346.77647

K2= 0.09741

K3= -0.29478

K4= -0.04783

K5= 0.28126

K6= 0.00068

K7= 1.90633

Determinación de la presión de Rocio K8= 8.41763

Ecuación 1 %C7= 0.98940

Ecuación 2 %C7= 1.10648

Pd = 2480.72 psi

CALCULO DEL M(P)

DETERMINACION DEL FACTOR Z, Ug, Bg,Dg

Gravedad Especifica = 0.65

PESO MELECULAR DEL GAS = 18.8266

Presion Temperatura Temperatura Ppc Tpc Ppr Tpr

periodo de flujo

Duracion periodo

Presion (Pwf) Fondo

Presion (Pwh) Cabeza

Caudal Condensado

)764(

3

275

87

1KK CKTrK

K

K

APIKC

GCRkPd

8207.0

8207.0

102607

706807

SGgGCRC

GCRC

Psi (oF) (oR) Psi (oR)

0 270 730 667.705 371.29125 0 1.966

1125 270 730 667.705 371.29125 1.685 1.966

1406 270 730 667.705 371.29125 2.106 1.966

1758 270 730 667.705 371.29125 2.633 1.966

2197 270 730 667.705 371.29125 3.291 1.966

2746 270 730 667.705 371.29125 4.113 1.966

3433 270 730 667.705 371.29125 5.142 1.966

4291 270 730 667.705 371.29125 6.427 1.966

5364 270 730 667.705 371.29125 8.034 1.966

6705 270 730 667.705 371.29125 10.042 1.966

8382 270 730 667.705 371.29125 12.553 1.966

10477 270 730 667.705 371.29125 15.691 1.966

N X Y X^2 X^3 X^4 XY

1 0 0 0 0 0 0

2 1125 83 1265533.44692 1423673632 160157490526593665.8677263

3 1406 130 1977396.01081 2780612562.433910094983556182313.223394

4 1758 200 3089681.26689 5430883911 9546130330947 352426.649

5 2197 307 4827626.97951 10607195139 2.3305982E+13 675273.925953

6 2746 465 7543167.15548 20717178005 5.6899371E+13 1278262.74668

7 3433 693 11786198.6804 40463238291 1.3891448E+14 2379902.15182

8 4291 1011 18415935.4382 79029762288 3.3914668E+14 4337377.36291

9 5364 1437 28774899.1222 154355004469 8.2799482E+14 7710423.67465

10 6705 1992 44960779.8784 301474618103 2.0214717E+15 13356835.4369

11 8382 2695 70251218.56 588817613482 4.9352337E+15 22588668.3192

12 10477 3572 109767529 1150034401333 1.204891E+16 37421194.9463

Sumatorias 47885.16276 12586 302659965.5 2.35513E+12 2.04069E+16 90376344.3

presion DP^2/Qg Diferencial Del M(p)/Qg Qg^2 Del M(p)-bQg^

P^2 M(p) Del M(p)

MMPsi^2 Mmpsia^2/MMsMmpsi^2/cp Mmpsi^2/cpMmpsi^2/MMscfd MMscfd^2

109.77 3653

48.69 10.11 2373 1280 265.781 23.203 752

73.66 11.70 1626 2027 321.926 39.640 1124

86.10 11.73 1204 2449 333.752 53.832 1223

93.94 11.63 904 2749 340.175 65.286 1262

71.48 11.38 1696 1957 311.615 39.451 1059

sumatoria 8504 1261.633 181.961 4360

METODO SMPLIFICADO (FETKOVICH)

Pseudo Potencial

1 10 100 1000

0.10

1.00

10.00

100.00

1000.00Prueba Isocronal metodo Simplificado

ISOCRONAL

Linear (ISOCRONAL)

CAUDAL DE GAS (MMpcd)

Dif

ere

nc

ial

de

Pre

sio

n (

PS

I^2

)

0 2000 4000 6000 8000 10000 120000

5001000150020002500300035004000

f(x) = 1.51193729148208E-05 x² + 0.204377713162504 x − 148.03665392984

Determinación del m(P)

Presión

m (p

)

n= 0.7871

C= 0.0000043 MMpcd/Psi^2

Qg= 9.13 MMpcd

METODO JONES BLOUNT GLAZE

Determinacion de coeficientes "A", "B" y AOF

valores validos 4

A 0.465209185

B 8.3157 Mmpsia^2/Mmscfd

B' 12.43 Mmpsia^2/Mmscfd

B'/B 1.494211175

AOF Tras. 8.834 Mmscfd

METODO ANALISI LIT (Pseudo Presiones)

Coeficientes Laminar e Turbulento "A" e "B"

1 10 100 1000

0.10

1.00

10.00

100.00

1000.00Prueba Isocronal metodo Simplificado

ISOCRONAL

Linear (ISOCRONAL)

CAUDAL DE GAS (MMpcd)

Dif

ere

nc

ial

de

Pre

sio

n (

PS

I^2

)

4.5 5 5.5 6 6.5 7 7.5 8 8.5-0.09

1.91

3.91

5.91

7.91

9.91

11.91

13.91

f(x) = 0.45627773074275 x + 8.31568392036408

Metodo de Jones Blount and Glaze

Metodo de Jones Blount and GlazeLinear (Metodo de Jones Blount and Glaze)

Caudal de Gas (MMpcd)

Dp

/Qg

(p

si^

2/M

Mp

cd

)

Coeficiente Laminar A 164.3435929 MMpsia^2/cp/MMscfd

A' 168.56 MMpsia^2/cp/MMscfd

Coeficiente Turbulento B 22.776 MMpsia^2/cp/(MMscfd)^2

Potencial transiente AOF trans. 9.56 Mmscfd

Potencial Estabilizado AOF Est. 9.49 Mmscfd

Ecuacion del pseudo potencial

164.3435929 22.77641183

Metodos Simplicado Blount blaze

10477 0 0 3653

9429 2.471 2.230 3123

8382 4.087 3.901 2627

7334 5.376 5.212 2164

6286 6.428 6.257 1734

5238 7.283 7.089 1338

4191 7.962 7.738 974

3143 8.480 8.226 644

2095 8.844 8.567 347

1048 9.061 8.768 83

0 9.133 8.834 0

Pseudo PresionPresion

AsumidaCaudal

(MMscfd)Caudal

(MMscfd)M(P)

(MmPSI/cp)

1 10 100

1

10

100

1000

10000

Metodo Analisis LIT

Metodo Analisis LITLinear (Metodo Analisis LIT)

Qg (MMpcd)

Del

M(p

)-b

Qg

^2

0 2 4 6 8 10 120

2000

4000

6000

8000

10000

12000

IPR

Simplificado Jones Blount Glaze Metodo LIT

Qo (MMscfd)

P (P

si)

wfR pmpm scq2scq

0 2 4 6 8 10 120

2000

4000

6000

8000

10000

12000

IPR

Simplificado Jones Blount Glaze Metodo LIT

Qo (MMscfd)

P (P

si)

Se tiene una prueba icronal y se desa conocer el potencial del reservorio y el IPR par los metodos: Simplificad, Jones blount Claze y LIT.

Caudal agua

BPD

6

11

17

17

10

A B C D FACTOR DENSIDAD X

Z gr/cc

0.613 0 0.038 1.128 1 0 5.039

0.613 0.34704907269 0.038 1.128 0.9550106625 0.0453441292 5.039

0.613 0.454 0.038 1.128 0.94689075516 0.05716621299 5.039

0.613 0.599 0.038 1.128 0.93895000176 0.07206208862 5.039

0.613 0.798 0.038 1.128 0.933046906 0.09064750362 5.039

0.613 1.074 0.038 1.128 0.93270902832 0.11335042632 5.039

0.613 1.462 0.038 1.128 0.94381286055 0.14002109211 5.039

0.613 2.015 0.038 1.128 0.97474575712 0.16947202196 5.039

0.613 2.811 0.038 1.128 1.0351956198 0.19946970794 5.039

0.613 3.972 0.038 1.128 1.13341716533 0.22772966373 5.039

0.613 5.681 0.038 1.128 1.2743345313 0.25318382222 5.039

0.613 8.224 0.038 1.128 1.46204878854 0.27584654659 5.039

X^2*Y Ecuacion Simultaneas

0 Eliminacion de Gauss-Jordan

105370289.835

256368697.264 12

619477561.771 47885.162764

1483702517.83 302659965.539

3510726504.48 2355134181216 12 47885.162764

8170450073.9 2.0406935E+16 47885.162764 302659965.539

18613330998 90376344.3044 302659965.5392355134181216

41360439726 745072229723

89561321518 12586.2490983 Resolviendo el sistema de Ecuaciones

189329182384 0 -1338930774

392061859452 0 -1.376869E+13

7.45072E+11

0

Los Valores determinado son:

2E-05

Gas

MMscfd

4.817

6.296

7.337

8.08

6.281

26.53

DETERMINACION DE LOS MÍNIMOS CUADRADOS

ΣN ΣX

ΣN ΣX ΣX^2

ΣX ΣX^2 ΣX^3

ΣX^2

ΣX^3

ΣX^4

ΣXY

ΣX^2Y

ΣY

1 10 100 1000

0.10

1.00

10.00

100.00

1000.00Prueba Isocronal metodo Simplificado

ISOCRONAL

Linear (ISOCRONAL)

CAUDAL DE GAS (MMpcd)

Dif

ere

nc

ial

de

Pre

sio

n (

PS

I^2

)

0 2000 4000 6000 8000 10000 120000

5001000150020002500300035004000

f(x) = 1.51193729148208E-05 x² + 0.204377713162504 x − 148.03665392984

Determinación del m(P)

Presión

m (p

)

1 10 100 1000

0.10

1.00

10.00

100.00

1000.00Prueba Isocronal metodo Simplificado

ISOCRONAL

Linear (ISOCRONAL)

CAUDAL DE GAS (MMpcd)

Dif

ere

nc

ial

de

Pre

sio

n (

PS

I^2

)

4.5 5 5.5 6 6.5 7 7.5 8 8.5-0.09

1.91

3.91

5.91

7.91

9.91

11.91

13.91

f(x) = 0.45627773074275 x + 8.31568392036408

Metodo de Jones Blount and Glaze

Metodo de Jones Blount and GlazeLinear (Metodo de Jones Blount and Glaze)

Caudal de Gas (MMpcd)

Dp

/Qg

(p

si^

2/M

Mp

cd

)

Delta M(p)

Mmpsi/cp MMscfd

0 0

529 2.414

1026 4.011

1489 5.246

1919 6.254

2315 7.101

2679 7.822

3009 8.439

3306 8.969

3570 9.422

3653 9.560

Caudal de Gas

1 10 100

1

10

100

1000

10000

Metodo Analisis LIT

Metodo Analisis LITLinear (Metodo Analisis LIT)

Qg (MMpcd)

Del

M(p

)-b

Qg

^2

0 2 4 6 8 10 120

2000

4000

6000

8000

10000

12000

IPR

Simplificado Jones Blount Glaze Metodo LIT

Qo (MMscfd)

P (P

si)

0 2 4 6 8 10 120

2000

4000

6000

8000

10000

12000

IPR

Simplificado Jones Blount Glaze Metodo LIT

Qo (MMscfd)

P (P

si)

Y K VISCOSIDAD Bg P/UZ DEL M(P) M(P) acum

CP scf/cf PSI/CP PSI/CP PSI/CP

1.392 148.706 0.01487 0 0 0 0

1.392 148.706 0.01592 57.042 74013 83261561 83261561

1.392 148.706 0.01633 71.914 90928 46388088 129649648

1.392 148.706 0.01693 90.653 110605 70849209 200498857

1.392 148.706 0.01777 114.033 132517 106836926 307335783

1.392 148.706 0.01896 142.593 155274 158082314 465418097

1.392 148.706 0.02061 176.144 176501 227803721 693221818

1.392 148.706 0.02276 213.193 193423 317496919 1010718737

1.392 148.706 0.02537 250.929 204268 426660403 1437379139

1.392 148.706 0.02827 286.480 209293 554608584 1991987723

1.392 148.706 0.03130 318.500 210103 703042859 2695030581

1.392 148.706 0.03440 347.010 208297 876716574 3571747155

Ecuacion Simultaneas

Eliminacion de Gauss-Jordan

302659965.538815 12586.2490983

2355134181216.05 90376344.3044

2.04069349893033E+016 745072229723

Resolviendo el sistema de Ecuaciones

-1.377E+13 -481821545

-1.533E+17 -5.131513E+12

-1.56547480861652E+025 -2.3669E+20

Los Valores determinado son:

0.204 -148.037

ΣX^2 = ΣY

ΣX^3 = ΣXY

ΣX^4 = ΣX^2Y

M(P)

MMPSI^2/CP

0

83

130

200

307

465

693

1011

1437

1992

2695

3572

ejemplo 4.2

Se desea conocer el maximo potemcial del reservorio y el IPR con datos de reservorio para los siguientes metodos:

Datos de Reservorio

Presion de Reservorio 10477 psia Gravedad Especifica del 0.65

Temperatura de Reservorio 270 o F Gravedad del Condensado 59

Temperatura Fluyente en Ca 95 o F Relacion Gas Condendado 71603.41

Espesor Neto Permeable 62 pies Relacion Gas Agua 475224

Espesor Perforado 48 pies Viscosidad del liquido 0.67

Prof. 14300 pies Saturacion de agua 0.6

RESERVORIO DE GAS SECO

METODO DE JONES BLOUNT & GLAZE

RESERVORIO Keff*Swi*Krg*Sw

Sistema Multifasico

Pr^2-Pwf^2 = Aq^2+Bq 0.31

A=3.16*10^-12 Be SGg Tr Zr / hp^2 Rw

B= 1.424* 10^3 u Tr Zr (ln (0.472 Re/RW) +S) / K h

Be= 2.33*10^10/ k ^1.201

Beta psi^-1 1.81710E+10

PRESION Term. Turb. Term. Flujo Pr^2-Pwf^2

ASUMIDA Darcy

PSIA A B PSI^2

10477 0.0521 17590.89 0

9429 0.0505 16659.76 20855831

8382 0.0481 15295.58 39516310

7334 0.0453 13740.43 55981440

6286 0.0424 12123.51 70251219

5238 0.0395 10523.77 82325647

4191 0.0368 9004.41 92204724

3143 0.0347 7635.66 99888451

2095 0.0333 6502.63 105376828

1048 0.0328 5684.76 108669854

0 0.0331 5214.63 109767529

DETERMINACION DEL FACTOR Z, Ug, Bg,Dg

SG cond. = 0.7428

SG mescla = 0.6869

PESO MELECULAR DEL GAS = 19.8940009222081

Presion Temperatura Ppc

Psi (oF) (oR) Psi

10477 10477 270 730 665.2531

9429 9967 270 730 665.2531

8382 9208 270 730 665.2531

7334 8324 270 730 665.2531

6286 7376 270 730 665.2531

5238 6397 270 730 665.2531

4191 5408 270 730 665.2531

3143 4423 270 730 665.2531

2095 3461 270 730 665.2531

1048 2557 270 730 665.2531

0 1808 270 730 665.2531

Se desea conocer el maximo potemcial del reservorio y el IPR con datos de reservorio para los siguientes metodos:

Radio de pozo 0.35 pies Penetracion de la Bala

Radio de Drene 1000 pies Rp

Pc/Bbl Permeabilidad del Gas 1.23 md Densidad de las Perf

Pc/Bbl Dano de Formacion 17 Tipo de perforacion s

% Permeabilidad relativa a 0.25 % Porosidad

% Saturacion irrecidual 0.25 % Rc

PERFORACIONES (BLOUNT GLAZE)

Sistema Multifasico

Pr^2-Pwf^2 = Aq^2+Bq

A= 3.16*10^-12 Be SGg Tr Zr (1/Rp - 1/Rc) / Lp^2

B= 1.424*10^3 u Tr Zr (ln Rc/ Rp) / Kp Lp

Be = 2.33*10^10/ Kp^1.201

Beta psi^-1 5.6934664E+10

CAUDAL Termino Termino Caud./Perf. PRESION

CALCULADO Fluy.Fondo

MMPCD A B MPCD PSI

0.000 5401.5 140618.93 0.0 10477

1.247 5230.9 133175.65 2.2 9413

2.563 4979.3 122270.61 4.4 8343

4.021 4689.9 109838.97 7.0 7266

5.682 4387.2 96913.55 9.9 6175

7.606 4089.3 84125.45 13.2 5061

9.843 3816.3 71979.92 17.1 3901

12.385 3593.8 61038.31 21.5 2628

15.046 3450.0 51981.06 26.1 824

17.372 3402.2 45443.10 30.2 #NUM!

18.803 3432.1 41684.99 32.6 #NUM!

Tpc Ppr Tpr A B

(oR)

379.9301 15.7489 1.9214 0.5983 9.0751

379.9301 14.9822 1.9214 0.5983 8.3388

379.9301 13.8420 1.9214 0.5983 7.3013

379.9301 12.5127 1.9214 0.5983 6.1771

379.9301 11.0873 1.9214 0.5983 5.0730

379.9301 9.6160 1.9214 0.5983 4.0422

379.9301 8.1287 1.9214 0.5983 3.1119

379.9301 6.6483 1.9214 0.5983 2.2971

379.9301 5.2019 1.9214 0.5983 1.6078

379.9301 3.8432 1.9214 0.5983 1.0563

379.9301 2.7176 1.9214 0.5983 0.6699

0.88 pies

0.021 pies

12 balas/pie

0.4 %

0.18 %

0.063 pies Los Valores determinado son:

2E-05 0.204

A B

METODO DE DARCY METODO DE LA PSEUDO PRESION

Qg=703*10E-6*Kg*Hn*(Pr^2-Pwf^2)/(Ug*Tr*Zr*(ln(Rd/Rw)-3/4+S))) Qg=703*10^ -6*k*h(m(p)r-m(p)f)/Tr*(ln(Rd/Rw)-0.75+S+Dq)

Factor de Coseny= f (1+7*(rw/(2fh))^0.5*cos(f*90))

f= 0.774193548387097

-0.05102165381862

CAUDAL Caud./Perf. PRESION SEUDOPRESION CAUDAL

CALCULADO Fluy.Fondo ASUMIDA (M(p)) CALCULADO

MMPCD MPCD PSI PSIA/cp MMPCD

0.000 0.0 10477 3653 0.000

0.970 1.7 9417 3123 1.606

2.002 3.5 8353 2627 3.112

3.158 5.5 7283 2164 4.517

4.491 7.8 6204 1734 5.821

6.063 10.5 5109 1338 7.024

7.936 13.8 3981 974 8.127

10.139 17.6 2773 644 9.129

12.559 21.8 1272 347 10.030

14.815 25.7 #NUM! 83 10.831

16.314 28.3 #NUM! 11.082

C D FACTOR DENSIDAD X

Z grs/cc

0.0412 1.1028 1.46062406309838 0.29177038177565 5.04962494072893

0.0412 1.1028 1.41449457175231 0.28661747075083 5.04962494072893

0.0412 1.1028 1.34645200741522 0.27818776204321 5.04962494072893

0.0412 1.1028 1.26820858160016 0.26698672172556 5.04962494072893

0.0412 1.1028 1.18634519584964 0.25289787562826 5.04962494072893

0.0412 1.1028 1.10580001872216 0.23531428622167 5.04962494072893

0.0412 1.1028 1.03197664444856 0.2131483577987 5.04962494072893

0.0412 1.1028 0.97179976869642 0.18512306038859 5.04962494072893

0.0412 1.1028 0.932918054326197 0.15088693689189 5.04962494072893

0.0412 1.1028 0.91999139942224 0.11304194442374 5.04962494072893

0.0412 1.1028 0.928066797082348 0.07923720597188 5.04962494072893

-148.037

C

Qg=703*10^ -6*k*h(m(p)r-m(p)f)/Tr*(ln(Rd/Rw)-0.75+S+Dq)

Factor de Coseny= f (1+7*(rw/(2fh))^0.5*cos(f*90))

Caud./Perf. PRESION

Fluy.Fondo

MPCD PSI

0.0 10477

2.8 9407

5.4 8333

7.8 7255

10.1 6172

12.2 5080

14.1 3973

15.8 2830

17.4 1562

18.8 #NUM!

19.2 #NUM!

Y K VISCOSIDAD Bg

CP PCS/pc pc/PCS

1.39007501185421 146.73551580902 0.03649856721233 347.348198488586 0.00287895548142

1.39007501185421 146.73551580902 0.03569390075014 341.213736345623 0.00293071436898

1.39007501185421 146.73551580902 0.03442719669896 331.178296437164 0.00301952154099

1.39007501185421 146.73551580902 0.03283494108986 317.843628429207 0.00314620118371

1.39007501185421 146.73551580902 0.03097019291834 301.071071595658 0.00332147487535

1.39007501185421 146.73551580902 0.0288417275506 280.138076045619 0.00356966826543

1.39007501185421 146.73551580902 0.02644307646984 253.749875644021 0.00394088863083

1.39007501185421 146.73551580902 0.02381201714472 220.386185648254 0.00453748948492

0.000 2.000 4.000 6.000 8.000 10.000 12.000 14.000 16.000 18.000 20.0000

2000

4000

6000

8000

10000

12000Comparacion del Metodo IPR

Metodo Blount Glaze

Metodo de Darcy

Metodo Pseudo Presion

Blount Glaze con Perf.

Darcy con Perf.

Pseudo Presion con Perf.

Caudal MMPCD

Pres

ion

Psi

1.39007501185421 146.73551580902 0.02112380182347 179.628601730927 0.00556704216569

1.39007501185421 146.73551580902 0.01872641469995 134.57471423342 0.00743081644792

1.39007501185421 146.73551580902 0.01702828573907 94.3306876458925 0.0106010040312

0.000 2.000 4.000 6.000 8.000 10.000 12.000 14.000 16.000 18.000 20.0000

2000

4000

6000

8000

10000

12000Comparacion del Metodo IPR

Metodo Blount Glaze

Metodo de Darcy

Metodo Pseudo Presion

Blount Glaze con Perf.

Darcy con Perf.

Pseudo Presion con Perf.

Caudal MMPCD

Pres

ion

Psi