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Millones de Pies Cúbicos por Día (MMPCD) 2004 55.9 2005 121.7 2006 143.2 2007 232.2 2008 301.3 2009 315.1 2010 669.3 2011 1066 2012 1113.7 2013 1153.8 2014 1213.6 Fuente: PeruPetro. Elaboración propia RESERVAS DE GAS NATURAL 2003-2013 (MILES DE MILLONES DE PIES CUBICOS - BCP) AÑO PROBADAS PROBABLES POSIBLES DESARROLLADAS NO DESARROLLADAS TOTAL PROBADAS 2003 564 8159 8723 7333 12606 2004 3420 8069 11489 5166 13169 2005 3392 8536 11928 6817 11612 2006 4284 7558 11842 6830 11570 2007 4174 7647 11821 6832 11218 2008 6221 5980 12201 6256 12644 2009 9742 2261 12002 14007 19251 2010 10027 2435 12462 10622 20554 2011 9015 3685 12700 8835 7544 2012 10604 4772 15376 7709 5142 2013 9964 5083 15047 6507 5363 2004 2005 2006 2007 2008 0 200 400 600 800 1000 1200 1400 55.9 121.7 143.2 232.2 301. Producción Fiscaliz Período: 2004 - Millones de Pies Cúbicos por Día (MMPCD)

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Datos CamiseaMillones de Pies Cbicos por Da (MMPCD)200455.92005121.72006143.22007232.22008301.32009315.12010669.32011106620121113.720131153.820141213.6Fuente: PeruPetro. Elaboracin propiaRESERVAS DE GAS NATURAL 2003-2013(MILES DE MILLONES DE PIES CUBICOS - BCP)AOPROBADASPROBABLESPOSIBLESRECURSOSTOTALDESARROLLADASNO DESARROLLADASTOTAL PROBADAS2003564815987237333126062866220043420806911489516613169298242005339285361192868171161230357200642847558118426830115703024220074174764711821683211218298712008622159801220162561264431101200997422261120021400719251326537791320101002724351246210622205543404777685201190153685127008835754448647777262012106044772153767709514279787108014201399645083150476507536378286105203

DensidadDensidad del gas naturalnotacion*10^-6*10^-17900000D-0179000000.790.079COMPOSICIN GAS NATURALdenotacion cientifica=1.0E-060.000001notar, cientifica numerosComponente % Molarctes BWR*ctesCZB0A0C0bacTloThiC0Thic1c2c3c4c5Nitrgeno0.7870.1074260d-01106760.3.8165782d+09.2327700d-022543.46.7380614d+08.1272000d-03.5300000d-020024428.204.5969191d+0900000Dixido de carbono0.2420.4991091 d-01277379.8.1404080d+11.4124070d 0213863.44.1511650d+11.8466750d-04.5393795d-02185.19249.722107495.3.1404080d+11-45523.556410.90705-1.8345281.40608036d-02n-.35715229d-05Metano 88.3670.4260090d-01187966.5.2287011d+10.3380183d-025005.791.2578892d+09.1243668d-03.6000246d-288.72160.9463810.054.2287011d+101156.585122.430422-0.19660009.83585195d-03n-1.4082303d-05Etano10.4200.6277381d-01421081.1819794d+11.1112248d 0134975.72.3320337d+11.2434045d-03.1180048d-0188.72235.94111892.84.1819795d+11-115.58784.13720066n-.26136501d-01.70916299d-04n-.77287552d-07Propano0.1690.9731520d-01696362.2.5150139d+11.2250097d-0196032.18.1307179d+11.6072144d-03.2200091d 0188.72283.16183657.63.5150139d+11224.77276-0.27168015.40766214d-02n-24567358d-04.36696788d-07Isobutano 0.00630.13754691036866.8612441d+11.4243716d-01196343.6.2898188d+11.1074148d-02.3400144d-01163.3269.272215799.1.8612441d+11-46903.055447.81248-2.108841.49127655d-02n-.45387795d-05n-Butano 0.00520.12436341021878.1006030d+12.2999982d-01190737.5.3206134d+11.1101390d-02.3400144d-01164.77294.271219928.4.1006030d+12-21614.603196.75588-0.87321324.19092915d-02n-.16522697d-05Isopentano 0.00070.1600561296603.1769537d+12.6681485d-01380622.8.7042554d+11.1700106d-02.4630206d-01182.87285.941828222.2.1769536d+12-31661.795277.34169-1.2012055.25899463d-02n-.22291006d-05n-Pentano 0.00080.15675411234134.2149415d+12.6681485d-01412907.5.8351451d+11.1810113d-02.4750203d+01183.88349.83797193.520.2149415d+12-7288.382556.467595-0.20786825.37376742d-03n-.26587363d-06Hexano0.00100.17781671462927.3363485d+121091355721148.8.1532908d+12.2811034d-02.666878d-01186.01349.83524832.9.3363485d+12-763504713.2050984n-.17389375d-01.46383657d-04n-.49742039d-07Heptano0.00070.19900911775356.4808841d+120.15196041050278.2502893d+12.4356386d-02.9000388d-01187.16372.05536598.05.4808841d+121925.1615-16.788424.80255078d-01n-.17616065d-03.14121718d-06Octano 0.00040.1518031490560.7306480d+120.28471212112782.4568033d+12.4365266d-02.9574765d-01262.22568.53717592.42.7306480d+121024.9385-2.1607919.13762442d-0200

Componente % Molarfraccion Molarctes BWR*ctesCZB0A0C0bacTloThiC0Thic1c2c3c4c5Nitrgeno0.78700.00790.0000000107106760.3816.57820.00000000232543.4673.806140.00000000010.00000000530024428.204596.919100000Dixido de carbono0.24200.00240.0000000499277379.814040.80.000000004113863.4415116.50.00000000010.0000000054185.19249.722107495.314040.8-45523.556410.90705-1.83452810.0000000041-0Metano 88.36700.88370.0000000426187966.52287.0110.00000000345005.791257.88920.00000000010.00000000688.72160.9463810.0542287.011-1156.585122.430422-0.196600090.0000000008-0Etano10.42000.10420.000000062842108118197.940.000000011134975.7233203.370.00000000020.000000011888.72235.94111892.8418197.95-115.58784.13720066-0.00000002610.0000000001-0Propano0.16900.00170.0000000973696362.251501.390.000000022596032.1813071.790.00000000060.00000002288.72283.16183657.6351501.39224.77276-0.271680150.0000000041-00Isobutano 0.00630.00010.1375469103686686124.410.0000000424196343.628981.880.00000000110.000000034163.3269.272215799.186124.41-46903.055447.81248-2.1088410.0000000049-0n-Butano 0.00520.00010.124363410218781006030.00000003190737.532061.340.00000000110.000000034164.77294.271219928.4100603-21614.603196.75588-0.873213240.0000000019-0Isopentano 0.00070.00000.1600561296603176953.70.0000000668380622.870425.540.00000000170.0000000463182.87285.941828222.2176953.6-31661.795277.34169-1.20120550.0000000026-0n-Pentano 0.00080.00000.15675411234134214941.50.0000000668412907.583514.510.00000000180.0000047502183.88349.83797193.52214941.5-7288.382556.467595-0.207868250.0000000004-0Hexano0.00100.00000.17781671462927336348.51091355721148.8153290.80.00000000280.0000000667186.01349.83524832.9336348.5-763504713.2050984-0.00000001740-0Heptano0.00070.00000.19900911775356480884.10.15196041050278250289.30.00000000440.00000009187.16372.05536598.05480884.11925.1615-16.7884240.0000000803-0.00000000020Octano 0.00040.00000.15180314905607306480.28471212112782456803.30.00000000440.0000000957262.22568.53717592.427306481024.9385-2.16079190.000000001400100.00011.0000*Presion= PaVolumen= m3/(k*mol)Tempratura=KunidadesCn=Pa(K*m3)/kmol)2temperatura: Ken Perry pag 481Datos InicialesTemperatura (C)15Temperatura (K)288.15Presin (atm)1metano 100%Presin (bar)1.01325densidad inicialPresion dadapresion calculadaerrorPresin (Pa)101324.9965828140.0424101325101242.525548040.0008139596R (PA*m3)/(Kmol*K)8314.330.04230.00316263210.042350.00198827430.04240.0008139259inicial0.04210.042450.0003604133densidad inicialPresion dadapresion calculadaerror0.04250.00153474310.04212101325100934.7232949940.0038517316ref metanoMezcla0.04214101325100982.6739761690.0033784952B00.00002132980.04216101325101030.6246907460.002905258419.5733405436A021.35761941410.04218101325101078.5754387410.00243202136.500726607C07.56748749240.0422101325101126.526220170.00195878390.1098671082b0.13775739720.04222101325101174.4770350480.00148554622.4725727731a2.6579140950.04224101325101222.4278833910.00101230811.7784168978c2.08867570220.04226101325101270.3787652160.00053906970.07612164510.08003991470.04228101325101318.3296805380.00006583090.00827345870.00898981480.0423101325101366.2806293730.00040740810.04232101325101414.2316117360.00088064750.04234101325101462.1826276440.00135388730.04236101325101510.1336771130.00182712730.04238101325101558.0847601580.00230036770.0424101325101606.0358767940.0027736085densidad (kmol/m3)

Propiedades

PROPIEDADES TERMOFISICAS DE SUSTANCIAS PURAS Esta base de datos est copiada de "The Properties of Gases and Liquids, 4th. Edition", por Reid, Prausnitz y Poling, McGraw Hill, 1987.

NUMERO COMPONENTEFORMULAMASA MOLEC.TEMP.TEMP.TEMP.PRESIONVOLUMEN COMPRES.FACTORMOMENTO VISCOSIDAD LIQUIDADH FORM.DG FORM.H VAPORIZ. CAPACIDAD CALORIFICA GAS IDEALEC. PRESION CONSTANTES PARA EC DE PRESION DE VAPOR T MIN.T MAX. EC. DE ANTOINE PARA PRESION DE VAPORT MIN.T MAX. EC.DE HARLACHER PARA PRESION DE VAPOR DENSIDAD LIQ.TEMP.REF. PARAPARAM.SOLUBILIDADVOLUMEN LIQUIDOFUSIONEBULL.CRITICACRITICACRITICOCRITICAACENTRICODIPOLAR log (m)=B*(1/T-1/C) (Gas ideal,298K)(TB)CP = A + B T + C T2 + D T3VAPORVP AVP BVP CVP D PARA PRESION DE VAPOR ln PS = A - B/(T+C) PARA EC. DE ANTOINE ln PS = A + B/T + C ln T + D PS/(T2)@TDENLIQDEN (298,15 K) (298,15 K)kg/kmolKKKbarcm3/mol--Debyes T en [K], m en cp kJ/mol kJ/molkJ/mol T en [K], CP en [J/mol K] PS en [bar] , PC en [bar] , T en [K] , TC en [K] PS en [kPa] , T en [K]KK PS en [kPa] , T en [K]g/cm3K [J/m3]0.5 m3/kmol(TF)(TB)(TC)(PC)(VC)(ZC)(w)(DIPM)(B)(C)(DHf)(DGf)(DHV)(A)(B)(C)(D)(A)(B)(C)(TMIN)(TMAX)(A)(B)(C)(D)(LIQDEN)(TDEN) (d) (VL)Ec. 1 :ln (PS/PC) = (1-X)-1 [A X + B X1,5 + C X3 + D X6] ;X = 1 - T/TC = 1 - TR TB = temperatura ebullicin normal normalEc. 2 :ln PS = A - B/T + C ln T + D PS/T2 TT = temperatura punto tripleEc. 3 :ln PS = A - B/(T + C) LH = lquido hipottico (298,15 K, 1 bar)(A)(B)(C)(D)(TMIN)(TMAX)56NITROGENON228.01363.377.4126.233.989.80.2900.0390.090.3046.410.0000.0005.5773.1150E+01-1.3570E-022.6800E-05-1.1680E-081-6.096761.13670-1.04072-1.9330663.0126.212.9190588.72-6.6054.090.029.912-924.86-3.0750.2640.80478.19081.9LH0.034707TB99DIOXIDO DE CARBONOCO244.010216.6304.173.893.90.2740.2390.0578.08185.24-393.800-394.60017.1541.9800E+017.3440E-02-5.6020E-051.7150E-081-6.956261.19695-3.126142.99448217.0304.120.57463103.39-0.16154.0204.050.715-3146.64-3.5720.70314564LH0.037417TT116METANOCH416.04390.7111.6190.446.099.20.2880.0110.0114.1457.60-74.900-50.8708.1801.9250E+015.2130E-021.1970E-05-1.1320E-081-6.004351.18850-0.83408-1.2283391.0190.413.2091897.84-7.1693.0120.028.160-1300.61-2.6410.4420.425111.711618LH0.037831TB168ETANOC2H630.07089.9184.6305.448.8148.30.2850.0990.0156.6095.57-84.740-32.95014.7075.4090E+001.7810E-01-6.9380E-058.7130E-091-6.343071.01630-1.19116-2.03539133.0305.413.64851511.42-17.16130.0199.00.548183.012375LH0.055205TB206PROPANOC3H844.09485.5231.1369.842.5203.00.2810.1530.0222.67133.41-103.900-23.49018.774-4.2240E+003.0630E-01-1.5860E-043.2150E-081-6.722191.33236-2.13868-1.38551145.0369.813.71081872.46-25.16164.0249.041.477-3266.92-4.1791.8100.582231.013091LH0.075642TB258N-BUTANOC4H1058.124134.8272.7425.238.0255.00.2740.1990.0265.84160.20-126.200-16.10022.3939.4870E+003.3130E-01-1.1080E-04-2.8220E-091-6.887091.15157-1.99873-3.13003170.0425.213.66302154.90-34.42195.0290.046.319-4065.57-4.7812.6800.579293.014470TB0.096647TB259ISOBUTANOC4H1058.124113.6261.4408.236.5263.00.2830.1830.1302.51170.20-134.600-20.90021.297-1.3900E+003.8470E-01-1.8460E-042.8950E-081-6.955791.50090-2.52717-1.49776165.0408.213.52292032.73-33.15187.0280.044.126-3771.21-4.5092.5700.557293.014027TB0.097704TB311N-PENTANOC5H1272.151143.4309.2469.733.7304.00.2630.2510.0313.66182.45-146.500-8.3700.258-3.6260E+004.8730E-01-2.5800E-045.3050E-081-7.289361.53679-3.08367-1.02456195.0469.713.81812477.07-39.94220.0330.054.667-4827.08-5.3133.6800.626293.0144390.116126379N-HEXANOC6H1486.178177.8341.9507.530.1370.00.2640.2990.0362.79207.09-167.300-0.16728.853-4.4130E+005.8200E-01-3.1190E-046.4940E-081-7.467651.44211-3.28222-2.50941220.0507.513.82142697.55-48.78245.0370.055.264-5587.42-5.8854.7780.659293.0149890.131287429N-HEPTANOC7H16100.205182.6371.6540.327.4432.00.2630.3490.0436.73232.53-187.9008.00031.698-5.1460E+006.7620E-01-3.6510E-047.6580E-081-7.674681.37068-3.53620-3.20243240.0540.313.85852911.32-56.51270.0400.059.261-6303.87-6.3736.0000.684293.0152030.147113483N-OCTANOC8H18114.232216.4398.8568.824.9492.00.2590.3980.0473.70251.71-208.60016.40034.413-6.0960E+007.7120E-01-4.1950E-048.8550E-081-7.912111.38007-3.80435-4.50132260.0568.813.92743120.29-63.63292.0425.064.624-7100.69-7.0537.3100.703293.0153530.163655

compresibilidad ZPseudoreducidas corregidaComponente % MolarMasa molecularFraccion molarTemp. CriticaPresion CriticaPresion CriticaVol. CriticaCompres. CriticaFactor AcentricoTemp. CriticaPresion Criticakg/kmolTc (K)Pc (bar)Pc (Pascal)cm3/mol(ZC)(w)Tc (K)Pc (Pascal)Nitrgeno0.78728.0130.0078699921126.233.933943875.089.80.2900.039125.733803313.9Dixido de carbono0.24244.0100.0024199976304.173.873764600.093.90.2740.239303.673637836.4Metano 88.36716.0430.8836691163190.446.046001550.099.20.2880.011189.945875289.2Etano10.42030.0700.1041998958305.448.848838650.0148.30.2850.099304.948755078.6Propano0.16944.0940.0016899983369.842.542455175.0203.00.2810.153369.342395178.4Isobutano 0.00658.1240.0000629999425.238.037996875.0255.00.2740.199424.737950174.9n-Butano 0.00558.1240.0000519999408.236.536477000.0263.00.2830.183407.736430300.8Isopentano 0.00172.1500.000007187.833.333300000.00.2700.210187.333207335.9n-Pentano 0.00172.1510.000008469.733.733741225.0304.00.2630.251469.233703684.2Hexano0.00186.1780.00001507.530.130100000.0370.00.2640.299507.030069004.9Heptano0.001100.2050.000007540.327.427357750.0432.00.2630.349539.827331288.9Octano 0.000114.2320.000004568.824.924900000.0492.00.2590.398568.324877122.8100.000117.7212661197H2S0.0000

Datos a IngresarTemperatura (C)15Temperatura (K)288.15Presin (atm)2Presin (Pa)196133densidad (kmol/m3)0.0424R (Pa*m3)/(Kmol*K)8314.33Masa molar aparente (Kg/kmol)=17.7212661197Gravedad Especifica (SG)=0.61107814210.6118654341

Calculo de la presion y temperatura pseudocriticas (Standling)Calculo de la presion y temperatura pseudocriticas (Standling corregida por Katz)Presion Pseudocritica (Psc)=46261914.3717606Fsk0.5225922295Presion Pseudocritica (Psc)46140112.2083986Temperatura Pseudocritica (Tsc)=202.4915420085Temperatura Pseudocritica (Tsc)201.968949779Calculo de la presion y temperatura pseudoreducidas (Standling)Calculo de la presion y temperatura pseudoreducidas (Standling corregida por Katz)Presion Pseudoreducida (Psr)=0.0042396214Presion Pseudoreducida (Psr)0.0042508132Temperatura Pseudoreducida (Tsr)=1.4230223996Temperatura Pseudoreducida (Tsr)1.4267044529PerryCalculo de Z:Berthelot Ecuacion=0.9981201887Berthelot Ecuacion=0.9981347182Metodo de Papay, J.=0.9994012973Metodo de Papay, J.=0.9994046917Metodo de Brill, JP0.9992264403Metodo de Brill, JP0.9992293919a0.3725565376a0.3748325418b0.0012423997b0.0012420696c0.0829722444c0.0826131146d1.7613944882d1.7641532909-1.7613944882-1.7641532909para mas calculos de Z, revisar perry a partir de pag 80Metodo Starling0.5745792992a10.3265a2-1.07a3-0.5339a40.01569a5-0.05165a60.5475a7-0.7361a80.1844a90.1056a100.6134a110.721

Z = Vreal Videal

ViscosidadLee, Gonzales y EakinDatos a IngresarTemperatura (C)15Temperatura (R)518.67Presin (atm)1Presin (Pa)98066.5densidad (g/cm3)0.0007496096R (Pa*m3)/(Kmol*K)8314.33densidad (kmol/m3)0.0423Masa molar aparente (Kg/kmol)17.7212661197K0.0003431728densidad (g/m3)749.6095568647A6.4295236787B1.3671809471Viscosidadcp1070892.53752667dinamicagr*m/s10708.9253752667Transporte actualMMPCD=1270m3/s=1868736202.25247D intero (18")m aprox=0.45Aream2=0.159043095velocidadcm/s=4152747116.11659Reynolds=130808878.330865f laminar=ERROR:#REF!Dimetro nominal (in)Rugosidad (um)f turbulento1830f inicialf calculadoerror2423.60.17740.17707036120.00185816663224.10.17730.17707036120.00129519893410.160.17720.17707036120.00073159570.17710.17707036120.00016735610.1770.17707036120.00039752110.17690.17707036120.0009630370.17680.17707036120.0015291925

Presion 1tuberia 18" punto 4tuberia 24" punto 2tuberia 18" punto 1 densidad (kg mol/m3)0.0423P barP1-P2P barP1-P2P barP1-P2P barP1-P2pi3.141592404000000454500000404000000404000000d1 (m) 18"0.45P inicialP calculadaErrorP barQkQ(k+1)ConvergenciaQkQ(k+1)ConvergenciaQkQ(k+1)Convergenciad1 (m) 24"0.6100000240655381663190000000481310763326380000001361361.77264711480.0021357256699.4699.45287912490.0000756007361361.77264711480.0021357256z0.99922644031000000000000010000024065538166319000000046131076332638000000100000000000001361.1361.67246083750.0015828157699.405699.44787878260.0000613038361.1361.67246083750.0015828157R (Pa*m3)/(K*mol)8.3144722000000000000010000024065538166319000000044131076332638000000200000000000001361.2361.57233003440.0010297526699.41699.44287851180.0000470067361.2361.57233003440.0010297526T (K)293.153000000000000010000024065538166319000000042131076332638000000300000000000001361.3361.47225465940.0004765363699.415699.43787831250.0000327096361.3361.47225465940.0004765363f0.184000000000000010000024065538166319000000040131076332638000000400000000000001361.4361.37223466640.0000768331699.42699.43287818470.0000184123361.4361.37223466640.0000768331L (m)15000000000000010000024065538166319000000038131076332638000000500000000000001361.5361.27227000950.0006303556699.425699.42787812840.000004115361.5361.27227000950.0006303556Caudal (m3/s)1868736202.252476000000000000010000024065538166319000000036131076332638000000600000000000001361.6361.17236064280.0011840312699.43699.42287814350.0000101825361.6361.17236064280.00118403127000000000000010000024065538166319000000034131076332638000000700000000000001361.7361.07250652040.00173786699.435699.41787823020.00002448361.7361.07250652040.001737868000000000000010000024065538166319000000032131076332638000000800000000000001361.8360.97270759650.002291842699.44699.41287838830.0000387777361.8360.97270759650.002291842Pascal = Kmol/m*s^29000000000000010000024065538166319000000030131076332638000000361.9360.87296382540.0028459771699.445699.40787861790.00005307541060.825361.9360.87296382540.002845977110000000000000010000024065538166319000000028131076332638000000362360.77327516140.0034002653699.45699.4028789190.0000673733362360.77327516140.003400265311000000000000010000024065538166319000000026131076332638000000362.1360.67364155880.0039547066699.455699.39787929160.0000816713362.1360.67364155880.003954706612000000000000010000024065538166319000000024131076332638000000362.2360.57406297190.0045093011699.46699.39287973570.0000959693362.2360.57406297190.0045093011130000000000000100000240655381663190000000221310763326380000003.1808619362.3360.47453935530.0050640488699.465699.38788025120.0001102675362.3360.47453935530.0050640488140000000000000100000240655381663190000000201310763326380000005.6548656699.47699.38288083820.000124565815000000000000010000024065538166319000000018131076332638000000699.475699.37788149670.00013886411600000000000001000001.5040961354320000000000000000001700000000000001000001.4156198921340000000000000000001800000000000001000001.3369743426360000000000000000001900000000000001000001.266607271912000000000000001000001.203276908312100000000000001000001.145978007912200000000000001000001.093888098512300000000000001000001.046327746412400000000000001000001.002730756912500000000000001000000.962621526712600000000000001000000.92559762181

Hoja1compresorspeed7600rpmspeed8000rpmspeed9000rpmvolumen flowhead (kj/kg)%efficienciavolumen flowhead (kj/kg)%efficienciavolumen flowhead (kj/kg)%efficiencia062770687708277130054.0877136060.9777155076.9777140053.9878.5140060.4777160076.7777150052.9879150059.9778170075.9778160052.7879160057.9879180074.9779170049.980170056.9879190073.9779180047.9879180055.9880200071.9780190045.9879190053.9880210069.9780200043.9878200051.9879220067.9779210040.0877210049.9879230065.9779220037.9976220046.9878240063.9778230035.9973.5230043.9876250059.9776240031.9970240041.4874260057.9874280000250036.9972270053.9876.5259033.9970280049.9874310001290045.9872295042.9870355001speed10000rpmvolumen flowhead (kj/kg)%efficiencia010177170095.9677180095.4677.5190094.4678200093.9678.5210091.9679220089.9679230087.9679240086.9780250084.9780260081.9779270079.9779280075.9779290073.9778300069.9777310065.9776320061.9775330057.9872340053.9870405001

Curvas-RPMSpeedrpm4500450045004500450045004500h (m)Q (m3/h)

Hoja5Curva de Compresor PC Chiquintirca

1xD10P3S Siemens1xD10P3S SiemensHead CurveEficienciaHead CurveEficienciaft-lbf/lbmRPMft3/s%RPMm3/hmetros%148007125238071252344.63419.0980147407125248171252446.58417.3981146007125268271252650.46413.4382144107125278371252752.40408.0583141207125308471253058.22399.8384125007125388471253873.74353.9684119507125408371254077.63338.3983115007125428271254281.51325.6482109507125438171254383.45310.0781105007125448071254485.39297.3380102007125457971254587.33288.837998407125467871254689.27278.6478168307600258076002548.52476.5780167007600268176002650.46472.8981166007600288276002854.34470.0682163607600308376003058.22463.2683160007600338476003364.04453.0784143007600418476004179.57404.9384136507600438376004383.45386.5283130507600458276004587.33369.5382125007600468176004689.27353.9681121007600488076004893.15342.6380116507600497976004995.09329.8979112507600507876005097.03318.5678190008075278080752752.40538.0280188508075288180752854.34533.7781187508075308280753058.22530.9482185008075338380753364.04523.8683180008075368480753669.86509.7084163008075438480754383.45461.5684156008075468380754689.27441.7483148208075488280754893.15419.6682142008075498180754995.09402.1081137508075518080755198.97389.3680133008075527980755300.91376.6179128508075537880755402.85363.8778213008550298085502956.28603.1580212508550318185503160.16601.7381210008550338285503364.04594.6582207008550358385503567.92586.1683201908550398485503975.68571.7284183508550468485504689.27519.6184176008550488385504893.15498.3883168508550518285505198.97477.1482162008550528185505300.91458.7381156008550548085505504.79441.7480151808550557985505606.74429.8579146008550567885505708.68413.4378236509295328092953262.10669.6980236009295338192953364.04668.2881234009295358292953567.92662.6182230009295388392953873.74651.2983222509295428492954281.51630.0584207009295488492954893.15586.1684197509295518392955198.97559.2683190009295538292955402.85538.0282181009295558192955606.74512.5381175009295578092955810.62495.5480170009295587992955912.56481.3979164809295607892956116.44466.6678261509500348095003465.98740.4980260509500368195003669.86737.6581258009500388295003873.74730.5782254009500418395004179.57719.2583245009500468495004689.27693.7684234009500518495005198.97662.6184222009500548395005504.79628.6383212009500568295005708.68600.3282204009500588195005912.56577.6681196009500608095006116.44555.0180190009500627995006320.32538.0279185009500637895006422.26523.8678289509975378099753771.80819.7780288009975388199753873.74815.5381284509975418299754179.57805.6182278009975458399754587.33787.2183246009975578399755810.62696.5983237509975598299756014.50672.5382227909975618199756218.38645.3481220009975638099756422.26622.9780213009975657999756626.14603.1579206009975667899756728.08583.3378

graficosPotencia vs Caudal% speed% torqueAltura vs Caudal055Eficiencia vs Caudal1050Preson vs tiempo2045caudal vs tiempo3050Altura vs tiempo40555060607070858010593150P succion (bar)P descarga (bar)Capacidad (ACT_m3/h)Head (m)Fluid Head (kj/kg)Duty (kj/hr)Rpmeficiencia adiabatica %eficiencia poliprotica %Caudal final

7777.817328124.11.21794850006006.22446.3445607778.6273082472.423903600060012.99913.22558.27779.447278369.43.622858800060020.41220.7145567781.077234610.65.988769300060037.637.992493.87783.567161966.49.477635500060071.78372.0655457784.987122116511.42559900060098.00698.034598.8P succion (bar)P descarga (bar)Capacidad (ACT_m3/h)Head (m)Fluid Head (kj/kg)Duty (kj/hr)Rpmeficiencia adiabatica %eficiencia poliprotica %Caudal final

8084.0773285835.7227823000100035.39935.795038080808080807786

DemandaCONSUMO TOTAL DE GAS NATURAL CAMISEA (MMPCD)Home

AOMESGeneradores ElctricosIndustrialesGNVResidenciales y ComercialesTotal2004Aug-040.3215.040.000.0015.37Sep-0428.2314.970.000.0043.20Oct-0443.6115.040.000.0058.65Nov-0451.3415.580.000.0166.93Dec-0434.1314.870.000.0149.002005Jan-0538.5215.150.000.0153.68Feb-0532.9715.640.000.0148.63Mar-0537.0716.030.000.0153.11Apr-0539.5217.140.000.0156.67May-0565.7717.800.000.0183.58Jun-0580.8418.720.000.0199.57Jul-0586.4620.090.000.02106.57Aug-0580.1021.630.000.02101.75Sep-0587.1021.980.000.02109.11Oct-0536.9719.910.000.0356.91Nov-0568.2127.740.000.0596.00Dec-0571.4227.620.000.0599.092006Jan-0640.8930.040.000.0670.99Feb-0653.6532.430.000.0786.14Mar-0621.7231.430.000.0853.23Apr-0612.5434.710.000.1147.36May-0645.4635.870.000.1581.48Jun-0693.4736.600.510.18130.76Jul-06100.9836.130.680.19137.97Aug-06102.1446.390.910.25149.69Sep-0683.9958.011.060.34143.40Oct-0677.1254.531.350.36133.35Nov-0671.3242.881.670.66116.54Dec-0675.6744.232.040.36122.302007Jan-0786.3349.991.950.42138.68Feb-0787.2248.682.710.44139.05Mar-07100.0447.003.530.48151.05Apr-0789.4053.333.270.52146.52May-07100.9457.054.050.58162.62Jun-07127.8862.933.860.62195.29Jul-07151.7861.584.190.55218.10Aug-07158.0066.715.270.66230.64Sep-07152.3166.426.920.71226.35Oct-07148.7571.297.570.70228.32Nov-07154.2472.568.390.63235.83Dec-07147.1367.319.420.61224.472008Jan-0891.1167.229.330.69168.34Feb-08138.6972.1910.470.77222.12Mar-08142.0372.1410.840.78225.78Apr-08140.8669.2612.321.13223.57May-08171.1473.3513.061.06258.61Jun-08193.2078.9914.181.08287.46Jul-08195.9076.4715.631.69289.69Aug-08196.0475.9116.591.10289.63Sep-08192.5082.6317.811.27294.21Oct-08183.5778.7319.271.40282.97Nov-08186.8979.0220.131.87287.91Dec-08181.5876.8722.981.20282.632009Jan-09161.3968.6717.640.92248.62Feb-09144.9266.0021.241.08233.24Mar-09163.5478.3122.701.12265.67Apr-09147.2879.1322.501.19250.10May-09167.4786.8422.891.37278.57Jun-09191.7978.8123.891.25295.75Jul-09193.0181.7223.161.24299.13Aug-09190.5785.3423.611.34300.86Sep-09188.0288.2223.941.44301.62Oct-09185.1287.2628.501.49302.37Nov-09177.9484.3628.451.64292.38Dec-09169.5380.2630.211.58281.582010Jan-10182.0082.6928.401.15294.24Feb-10198.4886.6130.251.20316.54Mar-10194.1489.3231.091.23315.78Apr-10178.2493.1131.061.19303.60May-10220.7697.9932.461.19352.40Jun-10268.0299.6530.001.19398.86Jul-10274.6784.4832.511.29392.96Aug-10280.0891.8135.961.43409.28Sep-10296.2093.4536.271.44427.36Oct-10279.9496.3237.341.49415.08Nov-10288.9498.2438.711.54427.43Dec-10224.8496.3038.881.55361.572011Jan-11219.9996.7538.011.51356.26Feb-11258.03102.0940.331.61402.06AoDemanda (MMPCD)Mar-11232.20102.1240.491.61376.421200446.63Apr-11232.37105.7242.851.71382.642200580.39May-11261.66108.5641.531.90413.6532006106.10Jun-11305.99105.2139.571.80452.5742007191.41Jul-11307.54107.7743.131.90460.3452008259.41Aug-11327.54112.7746.732.37489.4262009279.16Sep-11320.04116.9846.952.38486.3572010367.93Oct-11319.14113.2246.392.35481.1182011435.62Nov-11305.78122.8350.572.56481.7592012492.52Dec-11277.71111.0853.592.48444.87102013539.402012Jan-12252.89107.7452.142.41415.18112014587.00Feb-12300.47113.4254.302.51470.69122015625.32*Mar-12302.07116.4758.292.65479.48132016708.31*Apr-12283.27110.0756.062.87452.28142017765.53*May-12293.17115.9355.043.68467.83152018822.75*Jun-12335.10121.9363.253.46523.73162019879.97*Jul-12342.89114.0163.893.49524.27172020937.19*Aug-12329.01112.5260.663.31505.49182021994.41*Sep-12317.72110.3470.083.83501.971920221051.63*Oct-12348.20110.3470.083.83532.462020231108.85*Nov-12320.15112.3572.003.85508.352120241166.06*Dec-12345.00114.6065.003.86528.462220251223.28**Proyectado

Hoja4

ProyectoPK InicialPK FinalLongitud (m)ClaseFactor de diseoEspesor (pulg)Loop Costa700317705999568230.50.688705999711184518510.720.469711184716180499630.50.6887161807266641048410.720.469726664729270260630.50.6882895373064569961331032

Hoja6Compresor RepresentativoCompresor ChinquintircaEficienciaPIDEnergia CnusmidaPresionFlujoEficienciaPIDEnergia CnusmidaPresionFlujoEnergiaCaudal%%kJ/hBarMMPCD%%kJ/hBarMMPCDkJ/hMMPCD725241600078.71785.40.000009755441100011569.325758085115.5057210483200080.29820789.47000975108823000115138.611121605222.77547220966400083.19881752017650000115277.31498283530072301450000085.84935191061023008428620.18821848645437.316272401933000088.31983753026470000115414.832584565652.034672502416000090.641027754035290000115553.143307165866.486671602899000092.871067755044110000115691.4540297651080.9386717033820000951106756052940000115829.7647523651295.390671803866000097.061142757061760000115967.9754749651509.842671904349000099.0511777580705800001151106862197651724.7386711004832000010112097590794100001151244969423651939.1906751008823000011513831076649652153.6426