Calculos Fluidos .Assis

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Calculos Fluido

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CAPACIDADE DE REVESTIMENTO CAP. DESL. PROF. VOL. REV VOL. DESL bbl/m bbl/m m bbls bbls 20 0.1328 0.023 0.00 0.00 23 0.1292 0.027 0.00 0.00 45 0.1023 0.0538 0.00 0.00 36 0.2536 0.0416 0.00 0.00 44 0.2443 0.05 1880.00 459.28 94.00 54 0.2322 0.063 0.00 0.00 68 0.4912 0.0789 1033.00 507.41 81.50 133 1.12 0.1567 0.00 0.00 319 2.498 0.3696 0.00 0.00 TOTAL 966.69 CAPACIDADE DE POO DIAMETRO CAP PROF. VOLUME DIAMETRO CAP pol bbl/m m bbls POL bbl/m 8.5 0.2303 1583.00 364.56 4.5 0.0467 12.25 0.4783 0.00 5 0.0583 17.5 0.976 0.00 5 0.0283 26 2.154 0.00 6.75 0.0252 36 4.13 0.00 7.75 0.0287 TOTAL 364.56 8 0.0287 9.5 0.0287 DIAMETRO PESO pol 7 7 7 9.625 9.625 9.625 13.375 20 30

ANTONIO DE ASSISTEC. FLUIDOS MI DRILLING

CAPACIDADE DE TOBOS DESL PROF bbl/m m 0.01789 0.0214 280.00 0.06 1174.00 0.12 105.00 0.1627 0.1753 0.02589 TOTAL VAZO B bbl/min

CAP-VOL VOL-DESL bbls bbls 0.00 0.00 16.32 5.99 33.22 70.44 2.65 12.60 0.00 0.00 0.00 0.00 0.00 0.00 52.19 89.03 TEMPO RETORNO minuto #DIV/0!

CAPACIDADEDO POO SEM COLUNA CAPACIDADE DO POO COM COLUNA CAPACIDADE DO ANULAR

1331 1242 1190

TEMPO SUP/BROCA minuto #DIV/0!

DIAMETRO pol 13 3/8

12 1/4

CAPACIDADE DO ANULAR OD CAP. PROF. pol bbl/m m 7 3/4 0.2998 6 3/4 0.346 5 0.4115 4 1/2 0.4267 7 3/4 0.2868 6 3/4 0.333 5 0.3986 4 1/2 0.4137

VOLUME bbls 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

DIAMETRO OD pol 9 5/8

8 1/2

CAPACIDADE ANULAR CAP PROF pol bbl/m m 6 3/4 0.099 5 0.1664 4 1/2 0.1797 6 3/4 0.0848 5 0.1506 4 1/2 0.1588

VOLUME bbls 0.00 0.00 0.00 0.00 0.00 0.00 0.00

DIAMETRO pol 20

17 1/2

CAPACIDADE DO ANULAR OD CAP PROF. pol bbl m 9 1/2 0.8304 8 0.9141 7 3/4 0.9266 6 3/4 0.9728 5 1.0384 4 1/2 1.0535 9 1/2 0.6884 8 0.7721 7 3/4 0.7846 6 3/4 0.8308 5 0.8963 4 1/2 0.9114

VOLUME bbls 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

PH psi 0.00

PRESSO HIDROSTTICA FATOR PROF m 0.17

PESO lb/gal 9.70

PH psi 160.00

CALCULO DO PESO ESPECIFICO FATOR PROF PESO m lb/gal 0.17 2800.00 0.34

P. CIRC. lb/gal 10.04

SALINIDADE E RAZO PARAFINA/GUA VOL NITRATO 4.00 % DE GUA 32.00 % DE PARAFINA 55.00 % DE SLIDO 13.00 SALINIDADE NaCl 170984 % GUA CORRIGIDA 34.3 %SOLIDO CORRIGIDA 10.7 R. PARAFINA 61.6 R GUA 38.4 BARITA pc 77.7 BARITA sc 95.4CALCAREO CALCAREO

ml % % % ppm % % % %V FINAL C

192368

NaCl/mg/l

PESO I lb/gal 9.70

PESO F lb/gal 10.50

AUMENTO DE DENSIDADE V INICIAL V FINAL BARITA bbl bbl lb 200.00 206.7 10489.6

kg 8727.3

sc 290.9

bbl 217.5

CORREO DA PARAFINA VOLUME DE FLUIDO 512.00 RAZO PARAFINA DESEJADA 51.00 RAZO GUA DESEJADA 49.00 % DE PARAFINA 49.00 % DE GUA 51.00 VOLUME DE PARAFINA 20.9 VOLUME DE GUA

GUA

VOLUME DE FLUIDO P/ REDUZIR DENSIDADE PESO INICIAL 10.30 PESO FINAL 9.30 PESO DO FLUIDO P/ DILUIO 6.80 VOLUME INICIAL BBL 750.00 VOLUME DE DILUIO BBL 300.0 ESTOQUE DE GRANEIS TON PE LB 50.00 815.0 22671.6 7.00 257.6 3192.2 MISTURA DE FLUIDOS VOL 2 PESO 2 bbl lb/gal 1000.00 10.10

#DIV/0! TIPO BARITINA BENTONITA

REDUO DA SALINIDADE SAL FLUIDO SALIDADE GUA SAL DESEJADA % DE GUA VOLUME INICIAL VOLUME DILUIO #DIV/0!

SC 997.6 280.9

VOL 1 bbl 700.00

PESO 1 lb/gal 10.50

V FINAL bbl 1700.0

PESO F lb/gal 10.26

PESO DO VOLUME DE LAMA VOL. Bbls P. LAMA P. KG P. LB 2340.00 9.50 424391 933660 FLUIDO ABSORVIDO NO CASCALHO METROS PERF. CAPACIDADE VOL/CASCALHO PARAFINA/REORTA PARAF./CASCALHO LAMA CASCALHO CASCALHO MIDO LAMA ABSORVIDA M BBL/M BBL % % % BBL BBL 118.00 0.98 115 42.00 3.10 5.5 122 7

mg/l lb/bbl ppm

CONVERSO 314446 140000.00 110.00 49.16 261767 116546 CONTAMINANTE MAGNSIO mg/l CLCIO mg/l 600.00

PESO/SALINIDADE lb/gal 10.01 pe/(gr/cc) 1.2012 lb/bbl 420.44 BARRILHA LB/BBL 0.0 0.6

TEMPERATURA C 49.0 F 120.0 DUPLEX

F 120.2 C 48.9

DADOS VOLUMTRICO BOMBA DE LAMA TRIPLEX DIMETRO CAMISA POL 6.00 COMPRIMENTO DO PISTO POL 12.00 EFICINCIA VOLUMTRICA % 98.00 DESCARGA VOLUMTRICA GAL/STK 4.406 DESCARGA VOL. REAL GAL/STK 4.274 DESCARGA VOL. REAL BBL/STK 0.102 DIMETRO DA HASTE POL

0.000 0.000 0.000

VOL 1 bbl 469.4

MISTURA DE FLUIDOS PESO/VOLUME FIXO PESO 1 VOL 2 PESO 2 V. FINAL lb/gal bbl lb/gal bbl 13.2 56.6 6.7 526.0

P. FINAL lb/gal 12.5

VOL. PREPARAR BENTONITA SODA CAUSTICA VOLUME FINAL

CONVENCIONAL bbl 700 lb/bbl 25 lb/bbl 0.3 bbl

318.2 3.8 717.9

lb 17500.0

pe 260.0

FLUIDO SINTTICO VOL A PREPARAR bbl 100 PARAFINA % (bbl) 70 NOVA MUL lb/bbl (tb) 8 MI MOD lb/bbl (tb) 2 CAL HIDRATADA lb/bbl (sc) 10 VERSA HRP lb/bbl (tb) SALMORA % (bbl) 30 BARITINA pe3/sc/lb PESO DESEJADO lb/gal 9 ARGILA lb/bbl 2 VOLUME FINAL

64.3 2.0 0.5 22.7 0.0 27.6 50.9 4.1 8.1

ANTONIO ASSIS QUIMICO MI DRILLING

5597

STA VOL. GUA BENTONITA SODA CAUSTICA AMIDO BARITINA VOL. FINAL FLUIDO A BASE GUA DOCE/SALGADA VOL. A FABRICAR bbl VOL. FINAL bbl BENTONITA lb/bbl (sc) SODA CAUSTICA lb/bbl (sc) CMC AV AS lb/bbl (sc) GOMA XATANA lb/bbl (sc) CMC ADS lb/bbl (sc) KLA GARD lb/bbl (tb) SAL GROSSO lb/bbl (sc) BARRILHA lb/bbl (sc) DETERGENTE lb/bbl (bd) POLISTAR 60 lb/bbl (sc) POLISAL T (AMIDO) lb/bbl (sc) KCL lb/bbl (sc) BARITINA sc/50 kg PESO INICIAL/FINAL lb/gal

FLUIDO A BASE GUA DOCE/SALGADA VOL. A FABRICAR bbl VOL. FINAL bbl 0.0 BENTONITA lb/bbl (sc 0.0 SODA CAUSTICA lb/bbl (sc) 0.0 CMC AV AS lb/bbl (sc) 0.0 GOMA XATANA lb/bbl (sc) 0.0 CMC ADS lb/bbl (sc) 0.0 KLA GARD lb/bbl (bd) 0.0 SAL GROSSO lb/bbl (sc) 0.0 BARRILHA lb/bbl (sc) 0.0 DETERGENTE lb/bbl (bd) 0.0 POLISTAR 60 lb/bbl (sc) 0.0

FLUIDO 100% PARAFINA VOL. A FABRICAR bbl PARAFINA bbl CLAYTONE lb/bbl GELTONE II lb/bbl VERSA HRP lb/bbl NOVA MOD lb/bbl CAL HIDRATADA lb/bbl ECOTROL lb/bbl CALCAREO FINO lb/bbl VOLUME FINAL bbl VOL C/ CALCAREO bbl FLUIDO FLOPRO PESO DO FLUIDO VOL A FABRICAR bbl MI TROL lb/bbl DUO VIS lb/bbl CALCITA 2,44 lb/bbl MI LUB LPH lb/bbl PEROXIDO Mg lb/bbl

0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 FLUIDO BR MUL VOL A FABRICAR PARAFINA SALMOURA NOVA MUL ECOTRL CAL HIDRATADA VERSA HRP

9.1 2500.0 8.0 1.8 30.0 10.5 1.0

363.6 81.8 1136.4 59.7 45.5

sc sc sc tb sc

BARRILHA lb/bbl BICARBONATO lb/bbl KCL lb/bbl 15.8 SAL lb/bbl MI BAC 40 lb/bbl 0.5 OXIDO MAGNESIO lb/bbl 1.0 BARITINA sc/kg PESO I e PESO F lb/gal VOL DE MATERIAL bbl VOL FINAL C/BARIT bbl VOL DE CADIT bbl VOL AGUA DOCE bbl Obs: No consta volume do MI Lub LPH

0.0 0.0 359.3 0.0 28.4 45.5 0.0 197.3 2500.0 214.0 2088.6

sc sc sc sc bd sc 0.0 bbl bbl bbl

VG 69 CALCITA BARITINA PESO 1 e PESO F VOL. DE MATERIAL

SALMOURA VOL FABRICADO VOL DE GUA SAL VOL MATERIAL

ALPHDRILL PESO DO FLUIDO lb/gal 9.2 lb/gal VOL. A FABRICAR bbl 3400.0 bbl AGUA INDUSTRIAL bbl 2547.6 bbl BICARBONATO NA lb/bbl 0.3 15.5 sc CIDO CIRICO lb/bbl 0.3 7.7 sc DUO VIS lb/bbl 1.5 92.7 sc FILTRAPAC lb/bbl 0.5 30.9 sc ULTRAPAC lb/bbl 1.0 68.1 sc CADIT bbl 474.7 bbl KCL lb/bbl 15.8 488.4 sc CALCITA 2,44 lb/bbl 30.0 1545.5 sc ULTRAHIB lb/bbl 10.0 77.4 tb ALPHAFREE lb/bbl 7.0 59.4 tb BARITINA sc 386.4 sc PESO 1 E PESO 2 9.2 9.4 lb/gal VOL DE MATERIAL bbl 377.7 bbl Obs: 1 % vol = 3,5 lb/bbl (Ultrahib e Alpafree)

FLUIDO SINTTICO VOL A FABRICAR PARAFINA SAL NOVA MUL ECOTRL CAL HIDRATADA VERSA HRP VG 69 CALCITA BARITINA AGUA INDUSTRIAL VOL. DE MATERIAL VOLUME FINAL TOTAL

ANTONIO ASSIS QUIMICO MI DRILLING

bbl lb/bbl lb/bbl lb/bbl lb/gal bbl

50.0 0.0 0.0 0.0 10.6

sc 0.0 0.0 0.0 59.8 54.2

lb 0.0

6582.3

BASE GUA DOCE/SALGADA 600 616.7 0.0 3.3 5.5 8.7 5.5 7.2 0.0 0.0 0.0 0.0 48.0 0.0 186.7 9.5 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00

0.3 0.5 0.8 0.5 6

4

8.9

CUSTO BBL M3

FLUIDO BR MUL bbl bbl bbl lb/bbl lb/bbl lb/bbl lb/bbl

4260.0 60.0 40.0 6.0 1.0 5.0 1.0

2317.0 1544.6 64.5 85.4 484.1 9.7

CONCENTRAO FINAL DE FLOPRO Marerial Utilizado LB/BBL Embalagem MI Trol 6.97 sc/25 kg Duo Vis 1.57 sc/25 kg Calcita 26.13 sc/30 kg Perxido 0.79 Bar/22,7kg KCl 13.77 sc/50 kg

lb/bbl lb/bbl sc 8.0 bbl

1.0 30.0 9.0

85.4 1936.4 2167.6 398.4

Sal MI Bac 40 xido Mg MI Lubegua doce

0.00 0.44 0.87 9.15 370 370.0 2870.0

Salmoura Volume fabricado Volume total SALMOURA bbL bbL sc bbl 400.0 345.8 345.5 54.2

sc/50 kg sc/20 kg sc/25 kg tb/200 kg bbl bbl bbl

FLUIDO SINTTICO bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl lb/bbl bbl 4076.0 145.3 39.7 9.0 1.0 5.0 1.0 2.0 70.6 0.7

VOLUME FINAL TOTAL

CONCENTRAO FINAL SINTTICO Material1 M. gasto Conc Final Embalagem 2211.1 150 bbl 460.4 11.71 sc/50 kg 92.6 22 10.49 tb/180kg 81.7 2 0.97 sc/22,7kg 463.2 210 6.85 sc/20 kg 9.3 1 1.06 tb/203kg 163.4 16 2.07 sc/22,7kg 0.0 630 9.61 sc/30kg 2616.4 228 72.33 sc/50 kg 1275.6 14.71 bbl 616.6 99.9 bbl 4325.9

TESTE DE ABSORO PROFUNDIDADE DA SAPATA PESO DA LAMA ORIGINAL PESO EQUIVALENTEMXIMO MXIMO PRESSO MXIMA BOMBEIO PRESSO ESTABILIZADA PRESSO DE ABSORO GRADIENTE DE ABSORO PESO EQ. DE ABSORO M LB/GAL LB/GAL PSI PSI PSI PSI/M LB/GAL 2000.00 9.50 11.00 510.00 789.00 4019.00 2.01 11.82

ANTONIO ASSISQUIMICO MI

FLUIDO CAMAI VOL. DESEJADO PESO DESEJADO VOLUME SOL. KCL VOLUME CADIT VOL. AGUA MAR SAFE SCAV NA MI WET 70 MI BAC 40 PESO CADIT 540.0 9.1 124.2 142.7 273.1 0.6 5.2 2.7 9.8

DETERMINAO K+ VOL. FILTRADO V. FILTRADO QAS ION POTASSIO (K+) CL- DO KCL KCL DETERMINAO NACL V. GASTO AGNO CLORETO TOTAL CL- NACL NACL FLUIDO CAINJ VOL. DESEJADO CL. AMONIO MI WET 70 MI BAC 40 VOLUME DE GUA 0.0 0.0 0.0 0.0 0.0 0.0 9.9 6000.0 5.3 48.0 10.0

155.1

PREPARO SOLUO KCL KCL TIPO I 155 AGUA DO MAR 541 VOL FABRICADO 550 FLUIDO CA