Ejercicio 1 Ejercicio 2 Ejercicio 3 Ejercicio 4 Ejercicio 5 Ejercicio 6 Ejercicio 7 Ejercicio 8.
ejercicio con 2 circuitos.xlsx
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METODO DE LA TEORÍA LINEAL
Elaboración de Circuitossistema de Ecuaciones
PRIMERA ITERACION
1.1. Cáculo de coeficientes de fricción DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.1Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 2.0371785078
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 442,865 7.0832238 7.08322382 0.01993141210.019931 0.000400 442,865 7.6579913 7.657991319 0.01705180120.017052 0.000400 442,865 7.6391124 7.639112433 0.01713618710.017136 0.000400 442,865 7.6397261 7.639726057 0.01713343450.017133 0.000400 442,865 7.6397061 7.639706106 0.017133524
Tubería (3-4)Longitud= 500 Caudal 0.1Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 3.1830914184
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 553,581 7.1102984 7.110298405 0.01977991150.01978 0.000500 553,581 7.5526238 7.552623801 0.0175309033
0.017531 0.000500 553,581 7.5422778 7.542277825 0.01757903170.017579 0.000500 553,581 7.5425184 7.542518415 0.0175779102
0.017578 0.000500 553,581 7.5425128 7.542512819 0.0175779363
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.1 2.037178508(1-6) 300 0.2 0.1 3.183091418(2-3) 450 0.25 0.1 2.037178508(3-4) 500 0.2 0.1 3.183091418(4-5) 400 0.15 0.1 5.658829188(2-5) 250 0.25 0.1 2.037178508(5-6) 300 0.2 0.1 3.183091418
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.0050.74 -136.16 0.00 0.00 0.00
0 0 67.35 226.94 -800.116M INVERSA
-0.380190638 0.4781396689 0.4721119 0.451800947 0.380-0.619809362 -0.478139669 -0.472112 -0.45180095 -0.380-0.012186549 -0.016727599 0.9235116 0.722145163 0.012-0.012186549 -0.016727599 -0.076488 0.722145163 0.0120.012186549 0.0167275991 0.0764884 0.277854837 -0.012186549-0.368004089 -0.505132732 -0.4514 -0.27034422 0.36800408880.380190638 0.5218603311 0.5278881 0.548199053 0.619809362
SEGUNDO ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.17115819Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 3.4867978533
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 758,000 7.3439665 7.343966485 0.0185412337
0.018541 0.000400 758,000 7.75605 7.756049972 0.01662335970.016623 0.000400 758,000 7.7471456 7.747145641 0.01666159440.016662 0.000400 758,000 7.7473371 7.747337084 0.0166607710.016661 0.000400 758,000 7.747333 7.747332968 0.0166607887
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.068918687Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 2.1937448012
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 381,521 6.9289579 6.928957926 0.02082879530.020829 0.000500 381,521 7.4859862 7.485986195 0.01784440030.017844 0.000500 381,521 7.4685491 7.468549124 0.01792782140.017928 0.000500 381,521 7.4690897 7.469089695 0.01792522640.017925 0.000500 381,521 7.4690729 7.469072932 0.0179253069
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.17115819 3.486797853(1-6) 300 0.2 0.12884181 4.101152609(2-3) 450 0.25 0.08391869 1.709573449(3-4) 500 0.2 0.06891869 2.193744801(4-5) 400 0.15 0.05608131 3.173545728(2-5) 250 0.25 0.0972395 1.980942255(5-6) 300 0.2 0.02884181 0.918061191
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.0084.45 -173.61 0.00 0.00 0.00
0 0 60.54 159.49 -458.304M INVERSA
-0.518867561 0.2287543362 0.2198031 0.19622259 0.128-0.481132439 -0.228754336 -0.219803 -0.19622259 -0.128-0.025668236 -0.038153312 0.8765661 0.651908372 0.006-0.025668236 -0.038153312 -0.123434 0.651908372 0.0060.025668236 0.0381533122 0.1234339 0.348091628 -0.00635508-0.493199324 -0.733092352 -0.656763 -0.45568578 0.12210894370.518867561 0.7712456638 0.7801969 0.80377741 0.8715359761
TERCERA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.209289616Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 4.2636030666
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 926,870 7.4255444 7.425544394 0.01813607910.018136 0.000400 926,870 7.7841104 7.784110363 0.0165037270.016504 0.000400 926,870 7.7775572 7.777557154 0.01653155010.016532 0.000400 926,870 7.7776765 7.777676479 0.01653104280.016531 0.000400 926,870 7.7776743 7.777674306 0.0165310521
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.0526409Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.6756079851
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 291,410 6.7797206 6.779720629 0.02175586740.021756 0.000500 291,410 7.4264996 7.426499614 0.0181314140.018131 0.000500 291,410 7.4018499 7.401849884 0.0182523780.018252 0.000500 291,410 7.4027766 7.402776612 0.01824780840.018248 0.000500 291,410 7.4027418 7.402741753 0.0182479802
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.20928962 4.263603067(1-6) 300 0.2 0.14071038 4.478940173(2-3) 450 0.25 0.0751409 1.530754275(3-4) 500 0.2 0.0526409 1.675607985(4-5) 400 0.15 0.0348591 1.972616899(2-5) 250 0.25 0.09914872 2.019836314(5-6) 300 0.2 -0.0092896 0.295696955
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
102.46 -189.01 0.00 0.00 0.000 0 54.27 124.02 -292.457
M. INVERSA-0.6122662 0.0558473047 0.0433728 0.014868656 -0.052-0.3877338 -0.055847305 -0.043373 -0.01486866 0.052
-0.043442736 -0.066991411 0.8250109 0.578236102 -0.004-0.043442736 -0.066991411 -0.174989 0.578236102 -0.0040.043442736 0.0669914106 0.1749891 0.421763898 0.0037144857-0.568823464 -0.877161285 -0.781638 -0.56336745 -0.048636131
0.6122662 0.9441526953 0.9566272 0.985131344 1.0523506167
CUARTA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.229323433Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 4.6717276929
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,015,593 7.4597486 7.459748604 0.01797014640.01797 0.000400 1,015,593 7.7955128 7.795512783 0.0164554826
0.016455 0.000400 1,015,593 7.7898355 7.789835521 0.0164794770.016479 0.000400 1,015,593 7.7899312 7.789931207 0.01647907210.016479 0.000400 1,015,593 7.7899296 7.789929594 0.016479079
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.044087266Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.4033379786
f Número de Denomin denomina G(f)
dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 244,059 6.6738111 6.673811131 0.02245185230.022452 0.000500 244,059 7.3817138 7.381713839 0.01835209250.018352 0.000500 244,059 7.3512223 7.351222331 0.01850465040.018505 0.000500 244,059 7.3525139 7.352513867 0.01849814990.018498 0.000500 244,059 7.3524591 7.352459122 0.0184984254
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.22932343 4.671727693(1-6) 300 0.2 0.14567657 4.637018299(2-3) 450 0.25 0.07033727 1.432895665(3-4) 500 0.2 0.04408727 1.403337979(4-5) 400 0.15 0.02466273 1.395621994(2-5) 250 0.25 0.10148617 2.067454386(5-6) 300 0.2 -0.0293234 0.933391683
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
111.91 -195.45 0.00 0.00 0.000 0 50.86 105.29 -212.266
M. INVERSA-0.657758221 -0.03437267 -0.049895 -0.08203162 -0.147-0.342241779 0.0343726704 0.0498948 0.082031618 0.147-0.059656007 -0.093813413 0.7792595 0.516470288 -0.013-0.059656007 -0.093813413 -0.22074 0.516470288 -0.0130.059656007 0.0938134127 0.2207405 0.483529712 0.0133159717-0.598102214 -0.940559258 -0.829154 -0.59850191 -0.1335039430.657758221 1.0343726704 1.0498948 1.082031618 1.1468199147
QUINTA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.239119671
Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 4.8712945357
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,058,977 7.4748093 7.474809346 0.01789780450.017898 0.000400 1,058,977 7.8004662 7.800466193 0.01643459030.016435 0.000400 1,058,977 7.7951541 7.795154095 0.0164569970.016457 0.000400 1,058,977 7.7952405 7.795240485 0.01645663230.016457 0.000400 1,058,977 7.7952391 7.79523908 0.0164566382
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.039558155Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.259172229
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 218,986 6.6062531 6.606253076 0.02291340260.022913 0.000500 218,986 7.3520309 7.352030895 0.01850058040.018501 0.000500 218,986 7.3175135 7.317513523 0.01867552990.018676 0.000500 218,986 7.3190812 7.319081202 0.01866753050.018668 0.000500 218,986 7.3190099 7.319009941 0.018667894
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.23911967 4.871294536(1-6) 300 0.2 0.14838033 4.723081534(2-3) 450 0.25 0.06768315 1.378826682(3-4) 500 0.2 0.03955815 1.259172229(4-5) 400 0.15 0.01981685 1.121401423(2-5) 250 0.25 0.10268652 2.09190763(5-6) 300 0.2 -0.0391197 1.245214875
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
116.53 -198.96 0.00 0.00 0.000 0 48.97 95.34 -173.889
M. INVERSA-0.68104883 -0.079947618 -0.097474 -0.13159578 -0.194-0.31895117 0.0799476184 0.0974739 0.13159578 0.194
-0.071206829 -0.112913556 0.7474475 0.475584587 -0.020-0.071206829 -0.112913556 -0.252552 0.475584587 -0.0200.071206829 0.1129135556 0.2525525 0.524415413 0.020265898-0.609842001 -0.967034063 -0.844921 -0.60718037 -0.1735647560.68104883 1.0799476184 1.0974739 1.13159578 1.1938306537
SEXTA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.243960196Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 4.9699046815
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,080,414 7.4818945 7.481894508 0.0178639230.017864 0.000400 1,080,414 7.8027823 7.802782307 0.01642483510.016425 0.000400 1,080,414 7.7976377 7.797637663 0.01644651550.016447 0.000400 1,080,414 7.7977199 7.797719905 0.01644616860.016446 0.000400 1,080,414 7.7977186 7.79771859 0.0164461741
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.0372017Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.1841641141
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 205,942 6.5670733 6.567073307 0.02318762520.023188 0.000500 205,942 7.33442 7.334419957 0.0185895319
0.01859 0.000500 205,942 7.2974649 7.297464886 0.0187782870.018778 0.000500 205,942 7.299209 7.299209047 0.01876931380.018769 0.000500 205,942 7.2991266 7.299126649 0.0187697376
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.2439602 4.969904681(1-6) 300 0.2 0.1497898 4.767946395
(2-3) 450 0.25 0.0662642 1.349920037(3-4) 500 0.2 0.0372017 1.184164114(4-5) 400 0.15 0.0174858 0.989491565(2-5) 250 0.25 0.103321 2.104833129(5-6) 300 0.2 -0.0439602 1.399293228
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
118.81 -200.78 0.00 0.00 0.000 0 47.96 90.15 -155.325
M.INVERSA-0.692980843 -0.103054653 -0.121754 -0.1569014 -0.217-0.307019157 0.1030546531 0.1217543 0.156901404 0.217-0.078281576 -0.12460497 0.7282949 0.451811318 -0.025-0.078281576 -0.12460497 -0.271705 0.451811318 -0.0250.078281576 0.1246049697 0.2717051 0.548188682 0.0245649683-0.614699266 -0.978449683 -0.850049 -0.60871272 -0.1928942760.692980843 1.1030546531 1.1217543 1.156901404 1.2174592445
SETIMA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.246373303Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 5.0190639721
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,091,101 7.4853435 7.485343482 0.01784746470.017847 0.000400 1,091,101 7.8039065 7.803906492 0.0164201033
0.01642 0.000400 1,091,101 7.7988424 7.79884236 0.01644143490.016441 0.000400 1,091,101 7.7989226 7.798922633 0.01644109640.016441 0.000400 1,091,101 7.7989214 7.79892136 0.0164411018
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.036003322Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.1460186561
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 199,308 6.545927 6.545927003 0.02333768020.023338 0.000500 199,308 7.3247943 7.324794318 0.01863842160.018638 0.000500 199,308 7.2864929 7.286492949 0.01883488190.018835 0.000500 199,308 7.2883375 7.288337481 0.01882534970.018825 0.000500 199,308 7.2882486 7.288248561 0.018825809
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.2463733 5.019063972(1-6) 300 0.2 0.1505017 4.79060661(2-3) 450 0.25 0.06553457 1.335056218(3-4) 500 0.2 0.03600332 1.146018656(4-5) 400 0.15 0.01634043 0.924676903(2-5) 250 0.25 0.10365123 2.111560593(5-6) 300 0.2 -0.0463733 1.47610462
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
119.95 -201.71 0.00 0.00 0.000 0 47.45 87.51 -146.170
M. INVERSA-0.699036019 -0.114744737 -0.134088 -0.16976413 -0.229-0.300963981 0.1147447368 0.1340882 0.169764127 0.229-0.082236091 -0.131140954 0.7176664 0.438814963 -0.027-0.082236091 -0.131140954 -0.282334 0.438814963 -0.0270.082236091 0.1311409536 0.2823336 0.561185037 0.0269821324-0.616799927 -0.983603783 -0.851755 -0.60857909 -0.2023755870.699036019 1.1147447368 1.1340882 1.169764127 1.2293577195
OCTVA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)
(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.247578814Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 5.0436223809
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,096,440 7.4870463 7.487046339 0.01783934720.017839 0.000400 1,096,440 7.8044607 7.804460746 0.01641777120.016418 0.000400 1,096,440 7.7994361 7.799436122 0.01643893160.016439 0.000400 1,096,440 7.7995154 7.799515435 0.01643859730.016439 0.000400 1,096,440 7.7995142 7.799514183 0.0164386026
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.035401008Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.1268464335
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 195,973 6.5349624 6.534962438 0.02341605930.023416 0.000500 195,973 7.3197701 7.319770128 0.01866401670.018664 0.000500 195,973 7.2807624 7.280762367 0.01886454290.018865 0.000500 195,973 7.2826604 7.282660374 0.01885471120.018855 0.000500 195,973 7.2825679 7.282567926 0.0188551899
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.24757881 5.043622381(1-6) 300 0.2 0.15085869 4.8019699(2-3) 450 0.25 0.06516663 1.327560633(3-4) 500 0.2 0.03540101 1.126846433(4-5) 400 0.15 0.01577087 0.89244645(2-5) 250 0.25 0.10381843 2.114966765(5-6) 300 0.2 -0.0475788 1.514477133
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.00
0.00 0.00 0.00 0.00 -1.00120.52 -202.17 0.00 0.00 0.00
0 0 47.18 86.18 -141.609M. INVERSA
-0.702089929 -0.120633517 -0.140316 -0.17626379 -0.235-0.297910071 0.1206335168 0.1403162 0.176263793 0.235-0.084333919 -0.134608706 0.7120401 0.43196512 -0.028-0.084333919 -0.134608706 -0.28796 0.43196512 -0.0280.084333919 0.1346087059 0.2879599 0.56803488 0.0282680335-0.61775601 -0.986024811 -0.852356 -0.60822891 -0.2070667140.702089929 1.1206335168 1.1403162 1.176263793 1.2353347471
NOVENA ITERACION DATOS DE IN GRESOTramo(1-2)(1-6)(2-3)(3-4)(4-5)(2-5)(5-6)
Tubería (1-2)Longitud= 350 Caudal 0.248181384Viscosidad= 0.00000115 Diámetro 0.25Ks 0.000100 Velocidad 5.0558978094
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000400 1,099,108 7.4878925 7.487892545 0.01783531540.017835 0.000400 1,099,108 7.804736 7.804735978 0.01641661330.016417 0.000400 1,099,108 7.7997309 7.799730929 0.0164376890.016438 0.000400 1,099,108 7.7998098 7.799809768 0.01643735670.016437 0.000400 1,099,108 7.7998085 7.799808526 0.0164373619
CIRCUITO IITubería (3-4)
Longitud= 500 Caudal 0.035099394Viscosidad= 0.00000115 Diámetro 0.2Ks 0.000100 Velocidad 1.1172458043
f Número de Denomin denomina G(f)dato Ks/d Rreynolds 1/fasumido DATO CALCULADO
0.001 0.000500 194,304 6.5293838 6.529383804 0.02345608920.023456 0.000500 194,304 7.3172052 7.31720519 0.01867710380.018677 0.000500 194,304 7.2778359 7.277835862 0.0188797173
0.01888 0.000500 194,304 7.2797615 7.279761455 0.01886973070.01887 0.000500 194,304 7.2796672 7.279667173 0.0188702195
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.24818138 5.055897809(1-6) 300 0.2 0.15103737 4.807657445(2-3) 450 0.25 0.06498221 1.323803549(3-4) 500 0.2 0.03509939 1.117245804(4-5) 400 0.15 0.01548654 0.876357033(2-5) 250 0.25 0.1039023 2.116675366(5-6) 300 0.2 -0.0481814 1.53365749
ELABORACION DE LA MATRIZ
-1.00 -1.00 0.00 0.00 0.001.00 0.00 -1.00 0.00 0.000.00 0.00 1.00 -1.00 0.000.00 0.00 0.00 1.00 1.000.00 0.00 0.00 0.00 -1.00
120.81 -202.40 0.00 0.00 0.000 0 47.05 85.51 -139.329
M.INVERSA-0.703624102 -0.123590193 -0.143447 -0.17953313 -0.238-0.296375898 0.1235901928 0.1434473 0.179533125 0.238-0.08541545 -0.136396638 0.7091411 0.428439735 -0.029-0.08541545 -0.136396638 -0.290859 0.428439735 -0.0290.08541545 0.1363966377 0.2908589 0.571560265 0.0289318569
-0.618208653 -0.987193555 -0.852588 -0.60797286 -0.209399170.703624102 1.1235901928 1.1434473 1.179533125 1.2383310265
METODO DE LA
Tramo Longitud Diámet Caudal Velocidad(1-2) 350 0.25 0.2482 5.055897809(1-6) 300 0.2 0.1510 4.807657445(2-3) 450 0.25 0.0650 1.323803549(3-4) 500 0.2 0.0351 1.117245804(4-5) 400 0.15 0.0155 0.876357033(2-5) 250 0.25 0.1039 2.116675366(5-6) 300 0.2 -0.0482 1.53365749
HARDY CROSSCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL
I (1-2) 300 0.25 0.156
I (2-5) 300 0.1 0.029I (5-6) 500 0.2 -0.034I (6-1) 400 0.25 -0.074
CIRCUITO TUBERÍA LONGIT DIAMETRO
II (2-3) 400 0.1 0.03674II (3-4) 200 0.25 -0.00326II (4-5) 300 0.1 -0.03326II (2-5) 300 0.15 -0.02939
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.1300 0.2 0.1450 0.25 0.1500 0.2 0.1400 0.15 0.1250 0.25 0.1300 0.2 0.1
Tubería (1-6)Longitud= 300 Caudal 0.1 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 3.18309142 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 553,581 7.1102984 7.1102984 0.01977991 0.0010.019779912 0.000500 553,581 7.5526238 7.5526238 0.0175309 0.01993140.017530903 0.000500 553,581 7.5422778 7.5422778 0.01757903 0.01705180.017579032 0.000500 553,581 7.5425184 7.5425184 0.01757791 0.0171362
0.01757791 0.000500 553,581 7.5425128 7.5425128 0.01757794 0.0171334
Tubería (4-5)Longitud= 400 Caudal 0.1 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 5.65882919 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 738,108 7.0820715 7.0820715 0.0199379 0.0010.019937898 0.000667 738,108 7.379619 7.379619 0.01836251 0.01993140.018362513 0.000667 738,108 7.375327 7.375327 0.01838389 0.01705180.018383891 0.000667 738,108 7.3753888 7.3753888 0.01838358 0.0171362
0.018383583 0.000667 738,108 7.3753879 7.3753879 0.01838359 0.0171334
f hfi Kmi HFI+km0.01713352 5.073806 0 50.738060.01757794 13.61628 0 136.16280.01713352 6.523465 10 67.349890.01757794 22.69379 0 226.93790.01838359 80.01164 0 800.11640.01713352 3.624147 0 36.241470.01757794 13.61628 0 136.1628
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q3-4 0.051.00 1.00 Q5-4 0.04
36.24 -136.16 Q2-5 0.01-36.241475 0 Q6-5 0.00
M INVERSA Qi+1 Nuevos0.002792178 8.95E-005 Q1-2 0.242316 0.17115819-0.00279218 -8.9E-005 Q1-6 0.157684 0.128841818.9500E-005 0.0008873 Q2-3 0.067837 0.083918698.9500E-005 0.0008873 Q34 0.037837 0.06891869-8.950E-005 -0.000887 Q54 0.012163 0.056081310.002702678 -0.000798 Q25 0.094479 0.0972395-0.00279218 -8.9E-005 Q65 -0.04232 0.02884181
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.1711582300 0.2 0.1288418450 0.25 0.0839187500 0.2 0.0689187400 0.15 0.0560813250 0.25 0.0972395300 0.2 0.0288418
Tubería (1-6)Longitud= 300 Caudal 0.1288418 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.10115261 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 713,244 7.2166485 7.2166485 0.01920122 0.001
0.019201223 0.000500 713,244 7.5888796 7.5888796 0.0173638 0.02028060.017363796 0.000500 713,244 7.5818207 7.5818207 0.01739614 0.01845440.017396143 0.000500 713,244 7.581954 7.581954 0.01739553 0.0184830.017395532 0.000500 713,244 7.5819515 7.5819515 0.01739554 0.0184825
Tubería (4-5)Longitud= 400 Caudal 0.0560813 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 3.17354573 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 413,941 6.859077 6.859077 0.02125537 0.0010.021255369 0.000667 413,941 7.3081891 7.3081891 0.01872322 0.02001750.018723216 0.000667 413,941 7.2975881 7.2975881 0.01877765 0.01707920.018777653 0.000667 413,941 7.2978368 7.2978368 0.01877637 0.01716690.018776373 0.000667 413,941 7.297831 7.297831 0.0187764 0.017164
f hfi Kmi HFI+km0.01666079 14.45367 0 84.446260.01739554 22.36877 0 173.61420.01848255 4.955768 10 60.544030.01792531 10.99208 0 159.4934
0.0187764 25.70228 0 458.30380.01716406 3.432927 0 35.303830.01923966 1.239746 0 42.98434
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
35.30 -42.98 Q25 0.01-35.303828 0 Q65 0
M INVERSA Qi+1 Nuevos0.002988624 0.0001478 Q1-2 0.247421 0.20928962-0.00298862 -0.000148 Q1-6 0.152579 0.140710380.000147846 0.0014086 Q2-3 0.0663631 0.07514090.000147846 0.0014086 Q34 0.0363631 0.0526409-0.00014785 -0.001409 Q54 0.0136369 0.03485910.002840777 -0.001261 Q25 0.1010579 0.09914872-0.00298862 -0.000148 Q65 -0.047421 -0.00928962
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2092896300 0.2 0.1407104450 0.25 0.0751409500 0.2 0.0526409400 0.15 0.0348591250 0.25 0.0991487300 0.2 -0.00929
Tubería (1-6)Longitud= 300 Caudal 0.1407104 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.47894017 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 778,946 7.2503813 7.2503813 0.01902297 0.0010.019022969 0.000500 778,946 7.5999521 7.5999521 0.01731324 0.02052050.017313238 0.000500 778,946 7.593801 7.593801 0.0173413 0.01851960.017341297 0.000500 778,946 7.5939089 7.5939089 0.0173408 0.01855390.017340804 0.000500 778,946 7.593907 7.593907 0.01734081 0.0185532
Tubería (4-5)Longitud= 400 Caudal 0.0348591 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 1.9726169 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 257,298 6.6219728 6.6219728 0.02280474 0.0010.022804745 0.000667 257,298 7.2224515 7.2224515 0.01917038 0.0199575
0.01917038 0.000667 257,298 7.2019101 7.2019101 0.01927989 0.01706010.019279892 0.000667 257,298 7.2026048 7.2026048 0.01927617 0.01714550.019276173 0.000667 257,298 7.2025813 7.2025813 0.0192763 0.0171427
f hfi Kmi HFI+km0.01653105 21.44288 0 102.45550.01734081 26.59575 0 189.01060.01855324 3.988451 10 54.273930.01824798 6.528308 0 124.0159
0.0192763 10.1948 0 292.45750.01714278 3.564631 0 35.952370.02245843 0.150129 0 -16.161
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
35.95 16.16 Q25 0.01-35.952368 0 Q65 0
M. INVERSA Qi+1 Nuevos0.003239323 0.0002298 Q1-2 0.2493573 0.22932343-0.00323932 -0.00023 Q1-6 0.1506427 0.145676570.000229843 0.0019899 Q2-3 0.0655336 0.070337270.000229843 0.0019899 Q34 0.0355336 0.04408727-0.00022984 -0.00199 Q54 0.0144664 0.024662730.00300948 -0.00176 Q25 0.1038236 0.10148617-0.00323932 -0.00023 Q65 -0.049357 -0.02932343
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2293234300 0.2 0.1456766450 0.25 0.0703373500 0.2 0.0440873400 0.15 0.0246627250 0.25 0.1014862300 0.2 -0.029323
Tubería (1-6)Longitud= 300 Caudal 0.1456766 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.6370183 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 806,438 7.2632048 7.2632048 0.01895586 0.0010.018955857 0.000500 806,438 7.604108 7.604108 0.01729432 0.02067350.017294318 0.000500 806,438 7.598285 7.598285 0.01732084 0.01856150.017320836 0.000500 806,438 7.5983841 7.5983841 0.01732038 0.01859960.017320384 0.000500 806,438 7.5983824 7.5983824 0.01732039 0.0185989
Tubería (4-5)Longitud= 400 Caudal 0.0246627 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 1.39562199 Ks
f Número de Denomin denomina G(f) f
dato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 182,038 6.4205477 6.4205477 0.02425805 0.0010.024258047 0.000667 182,038 7.1414356 7.1414356 0.0196078 0.01988660.019607804 0.000667 182,038 7.1098855 7.1098855 0.01978221 0.01703760.019782209 0.000667 182,038 7.1112426 7.1112426 0.01977466 0.01712030.019774659 0.000667 182,038 7.1111842 7.1111842 0.01977498 0.0171176
f hfi Kmi HFI+km0.01647908 25.66357 0 111.90990.01732039 28.47263 0 195.4510.01859887 3.503396 10 50.855010.01849843 4.641949 0 105.290.01977498 5.235058 0 212.26590.01711769 3.729221 0 36.74610.01920663 1.279297 0 -43.6271
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
36.75 43.63 Q25 0.01-36.746103 0 Q65 0
M. INVERSA Qi+1 Nuevos0.003365336 0.0003052 Q1-2 0.2489159 0.23911967-0.00336534 -0.000305 Q1-6 0.1510841 0.148380330.000305222 0.0024959 Q2-3 0.065029 0.067683150.000305222 0.0024959 Q34 0.035029 0.03955815-0.00030522 -0.002496 Q54 0.014971 0.019816850.003060113 -0.002191 Q25 0.1038869 0.10268652-0.00336534 -0.000305 Q65 -0.048916 -0.03911967
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2391197300 0.2 0.1483803450 0.25 0.0676832500 0.2 0.0395582400 0.15 0.0198168250 0.25 0.1026865300 0.2 -0.03912
Tubería (1-6)Longitud= 300 Caudal 0.1483803 Longitud=
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.72308153 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 821,405 7.2699003 7.2699003 0.01892096 0.0010.018920956 0.000500 821,405 7.6062663 7.6062663 0.01728451 0.02076590.017284505 0.000500 821,405 7.6006109 7.6006109 0.01731024 0.01858690.017310237 0.000500 821,405 7.6007057 7.6007057 0.0173098 0.01862750.017309805 0.000500 821,405 7.6007041 7.6007041 0.01730981 0.0186266
Tubería (4-5)Longitud= 400 Caudal 0.0198168 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 1.12140142 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 146,270 6.2819284 6.2819284 0.02534043 0.0010.025340434 0.000667 146,270 7.0812797 7.0812797 0.01994236 0.01985120.019942358 0.000667 146,270 7.0408624 7.0408624 0.02017197 0.01702640.020171969 0.000667 146,270 7.0428615 7.0428615 0.02016052 0.01710770.020160519 0.000667 146,270 7.0427625 7.0427625 0.02016109 0.0171051
f hfi Kmi HFI+km0.01645664 27.86499 0 116.53160.01730981 29.5213 0 198.9570.01862666 3.248837 10 48.969660.01866789 3.771435 0 95.3390.02016109 3.445925 0 173.8887
0.0171052 3.815173 0 37.15360.01868606 2.215127 0 -56.6244
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
37.15 56.62 Q25 0.01-37.153597 0 Q65 0
M. INVERSA Qi+1 Nuevos0.003423096 0.0003579 Q1-2 0.2488007 0.2439602-0.0034231 -0.000358 Q1-6 0.1511993 0.1497898
0.000357901 0.0028515 Q2-3 0.0648452 0.06626420.000357901 0.0028515 Q34 0.0348452 0.0372017-0.0003579 -0.002852 Q54 0.0151548 0.0174858
0.003065195 -0.002494 Q25 0.1039555 0.103321-0.0034231 -0.000358 Q65 -0.048801 -0.0439602
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2439602300 0.2 0.1497898450 0.25 0.0662642500 0.2 0.0372017400 0.15 0.0174858250 0.25 0.103321300 0.2 -0.04396
Tubería (1-6)Longitud= 300 Caudal 0.1497898 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.7679464 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 829,208 7.2733147 7.2733147 0.0189032 0.0010.018903196 0.000500 829,208 7.6073638 7.6073638 0.01727952 0.02081790.017279518 0.000500 829,208 7.6017929 7.6017929 0.01730485 0.01860130.017304854 0.000500 829,208 7.6018855 7.6018855 0.01730443 0.01864320.017304432 0.000500 829,208 7.601884 7.601884 0.01730444 0.0186423
Tubería (4-5)Longitud= 400 Caudal 0.0174858 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 0.98949156 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 129,064 6.1990796 6.1990796 0.02602229 0.0010.026022294 0.000667 129,064 7.0436234 7.0436234 0.02015616 0.01983280.020156158 0.000667 129,064 6.9974365 6.9974365 0.02042312 0.01702060.020423119 0.000667 129,064 6.9998999 6.9998999 0.02040875 0.01710120.020408747 0.000667 129,064 6.9997683 6.9997683 0.02040951 0.0170986
f hfi Kmi HFI+km0.01644617 28.98612 0 118.81490.01730444 30.07548 0 200.7845
0.01864236 3.116668 10 47.962760.01876974 3.353691 0 90.148850.02040951 2.71598 0 155.32490.01709871 3.860998 0 37.368960.01850277 2.769788 0 -63.0067
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
37.37 63.01 Q25 0.01-37.36896 0 Q65 0
M.INVERSA Qi+1 Nuevos0.003451366 0.0003899 Q1-2 0.2487864 0.2463733-0.00345137 -0.00039 Q1-6 0.1512136 0.15050170.000389879 0.003067 Q2-3 0.0648049 0.065534570.000389879 0.003067 Q34 0.0348049 0.03600332-0.00038988 -0.003067 Q54 0.0151951 0.016340430.003061487 -0.002677 Q25 0.1039815 0.10365123-0.00345137 -0.00039 Q65 -0.048786 -0.0463733
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2463733300 0.2 0.1505017450 0.25 0.0655346500 0.2 0.0360033400 0.15 0.0163404250 0.25 0.1036512300 0.2 -0.046373
Tubería (1-6)Longitud= 300 Caudal 0.1505017 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.79060661 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 833,149 7.2750199 7.2750199 0.01889434 0.0010.018894336 0.000500 833,149 7.6079112 7.6079112 0.01727703 0.02084540.017277032 0.000500 833,149 7.6023822 7.6023822 0.01730217 0.01860890.017302171 0.000500 833,149 7.6024738 7.6024738 0.01730175 0.01865150.017301754 0.000500 833,149 7.6024723 7.6024723 0.01730176 0.0186507
Tubería (4-5)Longitud= 400 Caudal 0.0163404 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 0.9246769 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 120,610 6.1532241 6.1532241 0.02641159 0.0010.026411589 0.000667 120,610 7.0222385 7.0222385 0.02027911 0.01982330.020279108 0.000667 120,610 6.972715 6.972715 0.02056819 0.01701760.020568194 0.000667 120,610 6.9754627 6.9754627 0.02055199 0.01709780.020551994 0.000667 120,610 6.97531 6.97531 0.02055289 0.0170953
f hfi Kmi HFI+km0.0164411 29.55326 0 119.9532
0.01730176 30.35733 0 201.70760.01865068 3.049772 10 47.445290.01882581 3.150489 0 87.505520.02055289 2.388486 0 146.17040.01709535 3.884956 0 37.481040.01842373 3.06905 0 -66.1814
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
37.48 66.18 Q25 0.01-37.481045 0 Q65 0
M. INVERSA Qi+1 Nuevos0.003465591 0.0004077 Q1-2 0.2487843 0.24757881-0.00346559 -0.000408 Q1-6 0.1512157 0.150858690.0004077 0.0031867 Q2-3 0.0647987 0.065166630.0004077 0.0031867 Q34 0.0347987 0.03540101-0.0004077 -0.003187 Q54 0.0152013 0.01577087
0.003057892 -0.002779 Q25 0.1039856 0.10381843-0.00346559 -0.000408 Q65 -0.048784 -0.04757881
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2475788300 0.2 0.1508587450 0.25 0.0651666
500 0.2 0.035401400 0.15 0.0157709250 0.25 0.1038184300 0.2 -0.047579
Tubería (1-6)Longitud= 300 Caudal 0.1508587 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.8019699 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 835,125 7.2758702 7.2758702 0.01888992 0.0010.01888992 0.000500 835,125 7.6081839 7.6081839 0.01727579 0.0208594
0.017275793 0.000500 835,125 7.6026758 7.6026758 0.01730083 0.01861280.017300835 0.000500 835,125 7.6027669 7.6027669 0.01730042 0.0186558
0.01730042 0.000500 835,125 7.6027653 7.6027653 0.01730043 0.0186549
Tubería (4-5)Longitud= 400 Caudal 0.0157709 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 0.89244645 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 116,406 6.1289404 6.1289404 0.0266213 0.0010.026621297 0.000667 116,406 7.0107582 7.0107582 0.02034558 0.01981840.020345577 0.000667 116,406 6.9594278 6.9594278 0.02064681 0.0170160.020646808 0.000667 116,406 6.9623341 6.9623341 0.02062958 0.01709610.020629575 0.000667 116,406 6.9621693 6.9621693 0.02063055 0.0170936
f hfi Kmi HFI+km0.0164386 29.83864 0 120.5218
0.01730043 30.49917 0 202.17040.01865495 3.016312 10 47.184410.01885519 3.050713 0 86.175890.02063055 2.233289 0 141.60850.01709366 3.897115 0 37.537790.01838683 3.224219 0 -67.7659
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.05
1.00 1.00 Q54 0.0437.54 67.77 Q25 0.01
-37.537792 0 Q65 0M. INVERSA Qi+1 Nuevos
0.003472763 0.0004171 Q1-2 0.248784 0.24818138-0.00347276 -0.000417 Q1-6 0.151216 0.151037370.000417143 0.00325 Q2-3 0.0647978 0.064982210.000417143 0.00325 Q34 0.0347978 0.03509939-0.00041714 -0.00325 Q54 0.0152022 0.015486540.00305562 -0.002833 Q25 0.1039862 0.1039023-0.00347276 -0.000417 Q65 -0.048784 -0.04818138
DATOS DE IN GRESOLongitud Diámetro Caudal
350 0.25 0.2481814300 0.2 0.1510374450 0.25 0.0649822500 0.2 0.0350994400 0.15 0.0154865250 0.25 0.1039023300 0.2 -0.048181
Tubería (1-6)Longitud= 300 Caudal 0.1510374 Longitud=Viscosida= 1.15E-006 Diámetro 0.2 Viscosida=Ks 0.000100 Velocidad 4.80765744 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000500 836,114 7.2762946 7.2762946 0.01888772 0.0010.018887716 0.000500 836,114 7.60832 7.60832 0.01727518 0.02086650.017275175 0.000500 836,114 7.6028223 7.6028223 0.01730017 0.01861470.017300168 0.000500 836,114 7.6029131 7.6029131 0.01729975 0.0186580.017299755 0.000500 836,114 7.6029116 7.6029116 0.01729976 0.0186571
Tubería (4-5)Longitud= 400 Caudal 0.0154865 Longitud=Viscosida= 1.15E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 0.87635703 Ks
f Número de Denomin denomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 0.000667 114,307 6.1164174 6.1164174 0.02673042 0.0010.026730419 0.000667 114,307 7.0047961 7.0047961 0.02038023 0.0198160.020380227 0.000667 114,307 6.9525233 6.9525233 0.02068784 0.0170153
0.020687838 0.000667 114,307 6.9555134 6.9555134 0.02067005 0.01709530.020670054 0.000667 114,307 6.9553421 6.9553421 0.02067107 0.0170927
f hfi Kmi HFI+km0.01643736 29.9818 0 120.8060.01729976 30.57028 0 202.4021
0.0186571 2.999609 10 47.053670.01887022 3.001342 0 85.509780.02067107 2.157719 0 139.32860.01709281 3.903221 0 37.566260.01836898 3.303195 0 -68.5575
ELABORACION DE LA MATRIZ
0.00 0.00 Q1-2 -0.4-1.00 0.00 Q1-6 0.080.00 0.00 Q2-3 0.030.00 0.00 Q34 0.051.00 1.00 Q54 0.04
37.57 68.56 Q25 0.01-37.566257 0 Q65 0
M.INVERSA Qi+1 Nuevos0.003476368 0.000422 Q1-2 0.2487839 0.24848263-0.00347637 -0.000422 Q1-6 0.1512161 0.151126750.000422009 0.0032827 Q2-3 0.0647976 0.064889910.000422009 0.0032827 Q34 0.0347976 0.0349485-0.00042201 -0.003283 Q54 0.0152024 0.015344460.003054359 -0.002861 Q25 0.1039863 0.10394428-0.00347637 -0.000422 Q65 -0.048784 -0.04848263
f hfi Kmi HFI+km0.01643736 29.9818 0 120.8060.01729976 30.57028 0 202.4021
0.0186571 2.999609 10 47.053670.01887022 3.001342 0 85.509780.02067107 2.157719 0 139.32860.01709281 3.903221 0 37.566260.01836898 3.303195 0 -68.5575
TEORIALINEAL
0.2482
Tubería (2-3)450 Caudal 0.1
Viscosida= 1.150E-006 Diámetro 0.250.000100 Velocidad 2.03717851
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000400 442,865 7.08322382 7.08322382 0.019931410.000400 442,865 7.65799132 7.65799132 0.01705180.000400 442,865 7.63911243 7.63911243 0.017136190.000400 442,865 7.63972606 7.63972606 0.017133430.000400 442,865 7.63970611 7.63970611 0.01713352
Tubería (2-5)250 Caudal 0.1 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.03717851 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 442,865 7.08322382 7.08322382 0.01993141 0.0010.000400 442,865 7.65799132 7.65799132 0.0170518 0.0197799120.000400 442,865 7.63911243 7.63911243 0.01713619 0.0175309030.000400 442,865 7.63972606 7.63972606 0.01713343 0.017579032
0.000400 442,865 7.63970611 7.63970611 0.01713352 0.01757791
Tubería (2-3)450 Caudal 0.0839187
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 4.74881514
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 619,411 7.02198752 7.02198752 0.02028056
0.000667 619,411 7.36122587 7.36122587 0.018454390.000667 619,411 7.3555216 7.3555216 0.018483020.000667 619,411 7.35561721 7.35561721 0.018482540.000667 619,411 7.3556156 7.3556156 0.01848255
Tubería (2-5)250 Caudal 0.0972395 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 1.98094226 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 430,640 7.06797781 7.06797781 0.02001749 0.0010.000400 430,640 7.65185656 7.65185656 0.01707915 0.0244277890.000400 430,640 7.63228066 7.63228066 0.01716688 0.018997650.000400 430,640 7.63292989 7.63292989 0.01716396 0.0192530270.000400 430,640 7.63290835 7.63290835 0.01716406 0.019238879
%18.21945438.4347535111.681768730.922317260.8799827
1.9256045410.473671
Tubería (2-3)450 Caudal 0.0751409
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 4.25209521
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 554,621 6.98080847 6.98080847 0.020520530.000667 554,621 7.34826042 7.34826042 0.018519570.000667 554,621 7.34146646 7.34146646 0.018553860.000667 554,621 7.3415916 7.3415916 0.018553230.000667 554,621 7.34158929 7.34158929 0.01855324
Tubería (2-5)250 Caudal 0.0991487 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.01983631 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 439,095 7.07858448 7.07858448 0.01995755 0.0010.000400 439,095 7.65612925 7.65612925 0.0170601 0.0324636190.000400 439,095 7.63703956 7.63703956 0.01714549 0.0217355420.000400 439,095 7.63766388 7.63766388 0.01714269 0.0225257130.000400 439,095 7.63764345 7.63764345 0.01714278 0.022451626
%8.736053413.409046856.8294302619.401598941.34320812.30322238
68.320164
Tubería (2-3)450 Caudal 0.0703373
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.98026574
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 519,165 6.95493845 6.95493845 0.020673470.000667 519,165 7.33996379 7.33996379 0.018561460.000667 519,165 7.33243423 7.33243423 0.01859960.000667 519,165 7.33258085 7.33258085 0.018598860.000667 519,165 7.332578 7.332578 0.01859887
Tubería (2-5)250 Caudal 0.1014862 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.06745439 Ks
Número de Denomin denomina G(f) f
Ks/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 449,447 7.09119423 7.09119423 0.01988663 0.0010.000400 449,447 7.66118071 7.66118071 0.01703761 0.0243418080.000400 449,447 7.64266131 7.64266131 0.01712028 0.0189690810.000400 449,447 7.64325686 7.64325686 0.01711761 0.0192196350.000400 449,447 7.6432377 7.6432377 0.01711769 0.019205886
%4.096792781.82218399
3.921376311.449247924.45338171.1689447125.0417175
Tubería (2-3)450 Caudal 0.0676832
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.83007412
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 499,575 6.93944277 6.93944277 0.02076590.000667 499,575 7.33493796 7.33493796 0.018586910.000667 499,575 7.32694884 7.32694884 0.018627460.000667 499,575 7.3271095 7.3271095 0.018626640.000667 499,575 7.32710627 7.32710627 0.01862666
Tubería (2-5)250 Caudal 0.1026865 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.09190763 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 454,763 7.09751515 7.09751515 0.01985123 0.0010.000400 454,763 7.66370137 7.66370137 0.0170264 0.0229624760.000400 454,763 7.64546467 7.64546467 0.01710772 0.018516460.000400 454,763 7.64604614 7.64604614 0.01710512 0.0186938540.000400 454,763 7.6460276 7.6460276 0.0171052 0.018685685
%1.984145610.94096823
2.14135986.3342668513.33107460.6140866711.0111555
Tubería (2-3)450 Caudal 0.0662642
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.74977788
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 489,101 6.93077059 6.93077059 0.02081790.000667 489,101 7.33210676 7.33210676 0.018601260.000667 489,101 7.32385425 7.32385425 0.018643210.000667 489,101 7.32402316 7.32402316 0.018642350.000667 489,101 7.3240197 7.3240197 0.01864236
Tubería (2-5)250 Caudal 0.103321 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.10483313 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 457,572 7.10081516 7.10081516 0.01983278 0.0010.000400 457,572 7.6650143 7.6650143 0.01702057 0.0224637790.000400 457,572 7.64692435 7.64692435 0.01710119 0.0183559090.000400 457,572 7.64749856 7.64749856 0.01709863 0.0185090320.000400 457,572 7.64748033 7.64748033 0.01709871 0.018502495
%0.979451370.473013481.113347793.328519817.009438790.318601515.20365499
Tubería (2-3)450 Caudal 0.0655346
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.70848949
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 483,716 6.9262001 6.9262001 0.020845390.000667 483,716 7.33060929 7.33060929 0.018608860.000667 483,716 7.32221617 7.32221617 0.018651550.000667 483,716 7.32238954 7.32238954 0.018650670.000667 483,716 7.32238596 7.32238596 0.01865068
Tubería (2-5)250 Caudal 0.1036512 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.11156059 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 459,035 7.10252167 7.10252167 0.01982325 0.0010.000400 459,035 7.66569243 7.66569243 0.01701756 0.0222461210.000400 459,035 7.64767814 7.64767814 0.01709782 0.0182864370.000400 459,035 7.64824862 7.64824862 0.01709527 0.0184293740.000400 459,035 7.64823055 7.64823055 0.01709535 0.018423486
%0.486920050.236638090.56461341
1.70140513.611471950.161050822.53371364
Tubería (2-3)450 Caudal 0.0651666
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.68766842
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 481,000 6.92386576 6.92386576 0.020859440.000667 481,000 7.32984304 7.32984304 0.018612750.000667 481,000 7.32137763 7.32137763 0.018655820.000667 481,000 7.32155331 7.32155331 0.018654930.000667 481,000 7.32154966 7.32154966 0.01865495
Tubería (2-5)250 Caudal 0.1038184 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.11496676 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 459,775 7.10338283 7.10338283 0.01981844 0.0010.000400 459,775 7.66603442 7.66603442 0.01701604 0.0221439410.000400 459,775 7.64805825 7.64805825 0.01709612 0.0182539570.000400 459,775 7.64862685 7.64862685 0.01709358 0.0183922020.000400 459,775 7.64860886 7.64860886 0.01709366 0.018386604
%0.242794240.118301790.283809790.859312171.835943160.080720991.25062846
Tubería (2-3)450 Caudal 0.0649822
Viscosida= 1.150E-006 Diámetro 0.150.000100 Velocidad 3.67723208
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000667 479,639 6.92268813 6.92268813 0.020866540.000667 479,639 7.32945611 7.32945611 0.018614720.000667 479,639 7.32095411 7.32095411 0.018657980.000667 479,639 7.32113097 7.32113097 0.018657080.000667 479,639 7.32112729 7.32112729 0.0186571
Tubería (2-5)250 Caudal 0.1039023 Longitud=
Viscosida= 1.150E-006 Diámetro 0.25 Viscosida=0.000100 Velocidad 2.11667537 Ks
Número de Denomin denomina G(f) fKs/d Rreynolds 1/f datoDATO CALCULADO asumido
0.000400 460,147 7.10381408 7.10381408 0.01981604 0.0010.000400 460,147 7.66620563 7.66620563 0.01701528 0.0220943840.000400 460,147 7.64824853 7.64824853 0.01709527 0.018238236
0.000400 460,147 7.6488162 7.6488162 0.01709273 0.0183742250.000400 460,147 7.64879825 7.64879825 0.01709281 0.018368766
%0.121233960.059142190.142233910.431747240.925933590.040385370.62134693
Tubería (5-6)300 Caudal 0.1
1.150E-006 Diámetro 0.20.000100 Velocidad 3.18309142
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 553,581 7.11029841 7.11029841 0.019779910.000500 553,581 7.5526238 7.5526238 0.01753090.000500 553,581 7.54227783 7.54227783 0.017579030.000500 553,581 7.54251841 7.54251841 0.01757791
Tubería (5-6)300 Caudal 0.0288418
1.150E-006 Diámetro 0.20.000100 Velocidad 0.91806119
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 159,663 6.39820159 6.39820159 0.024427790.000500 159,663 7.25521121 7.25521121 0.018997650.000500 159,663 7.20693312 7.20693312 0.019253030.000500 159,663 7.20958261 7.20958261 0.019238880.000500 159,663 7.209437 7.209437 0.01923966
Tubería (5-6)300 Caudal -0.0092896
1.150E-006 Diámetro 0.20.000100 Velocidad 0.29569695
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 51,426 5.5501093 5.5501093 0.032463620.000500 51,426 6.78288979 6.78288979 0.021735540.000500 51,426 6.6628606 6.6628606 0.022525710.000500 51,426 6.67384482 6.67384482 0.022451630.000500 51,426 6.67283383 6.67283383 0.02245843
Tubería (5-6)300 Caudal -0.0293234
1.150E-006 Diámetro 0.20.000100 Velocidad 0.93339168
Número de Denomin denomina G(f)
Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 162,329 6.40949166 6.40949166 0.024341810.000500 162,329 7.26067259 7.26067259 0.018969080.000500 162,329 7.21319096 7.21319096 0.019219640.000500 162,329 7.21577238 7.21577238 0.019205890.000500 162,329 7.21563183 7.21563183 0.01920663
Tubería (5-6)300 Caudal -0.0391197
1.150E-006 Diámetro 0.20.000100 Velocidad 1.24521488
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 216,559 6.59919008 6.59919008 0.022962480.000500 216,559 7.34887762 7.34887762 0.018516460.000500 216,559 7.3139263 7.3139263 0.018693850.000500 216,559 7.31552489 7.31552489 0.018685680.000500 216,559 7.31545171 7.31545171 0.01868606
Tubería (5-6)300 Caudal -0.0439602
1.150E-006 Diámetro 0.20.000100 Velocidad 1.39929323
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 243,355 6.67203923 6.67203923 0.022463780.000500 243,355 7.3809464 7.3809464 0.018355910.000500 243,355 7.35035222 7.35035222 0.018509030.000500 243,355 7.35165056 7.35165056 0.018502490.000500 243,355 7.35159542 7.35159542 0.01850277
Tubería (5-6)300 Caudal -0.0463733
1.150E-006 Diámetro 0.20.000100 Velocidad 1.47610462
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 256,714 6.70459965 6.70459965 0.022246120.000500 256,714 7.39495353 7.39495353 0.018286440.000500 256,714 7.36622032 7.36622032 0.018429370.000500 256,714 7.36739746 7.36739746 0.018423490.000500 256,714 7.3673492 7.3673492 0.01842373
Tubería (5-6)300 Caudal -0.0475788
1.150E-006 Diámetro 0.20.000100 Velocidad 1.51447713
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 263,387 6.72005052 6.72005052 0.022143940.000500 263,387 7.40152972 7.40152972 0.018253960.000500 263,387 7.37366051 7.37366051 0.01839220.000500 263,387 7.37478286 7.37478286 0.01838660.000500 263,387 7.37473763 7.37473763 0.01838683
Tubería (5-6)300 Caudal -0.0481814
1.150E-006 Diámetro 0.20.000100 Velocidad 1.53365749
Número de Denomin denomina G(f)Ks/d Rreynolds 1/fDATO CALCULADO
0.000500 266,723 6.72758284 6.72758284 0.022094380.000500 266,723 7.40471913 7.40471913 0.018238240.000500 266,723 7.37726663 7.37726663 0.01837423
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0
Velocidad #DIV/0!Denomin denomina G(f)
1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
Caudal 0Diámetro 0Velocidad #DIV/0!
Denomin denomina G(f)1/f
#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!#DIV/0! #DIV/0! #DIV/0!
PRIMERA ITERACION
1.1. Cáculo de coeficientes de fricción
Tubería (1-2)Longitud= 350 Caudal 0.15 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000100 Velocidad 3.0557677617 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 664,297 7.28568 7.285684 0.0188390643 0.0010.01884 ### 664,297 7.73525 7.735247 0.0167128947 0.0317880.01671 ### 664,297 7.72444 7.724436 0.0167597061 0.0215050.01676 ### 664,297 7.72469 7.724695 0.016758585 0.0222460.01676 ### 664,297 7.72469 7.724689 0.0167586118 0.022178
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.05 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000100 Velocidad 2.8294145941 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 369,054 6.80625 6.806252 0.0215865878 0.0010.02159 ### 369,054 7.28998 7.289976 0.0188168876 0.0337620.01882 ### 369,054 7.27745 7.277449 0.0188817243 0.0218790.01888 ### 369,054 7.27777 7.277771 0.0188800528 0.0228370.01888 ### 369,054 7.27776 7.277763 0.0188800958 0.022737
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
supuestoI (1-2) 350 0.25 0.150 3.055768I (2-5) 300 0.2 0.010 0.318309I (5-6) 450 0.25 -0.040 0.814871I (6-1) 500 0.2 -0.080 2.546473
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDADsupuesto
II (2-3) 400 0.15 0.050 2.829415II (3-4) 250 0.25 0.010 0.203718II (4-5) 300 0.2 -0.020 0.636618II (2-5) 500 0.15 -0.010 0.565883
SEGUNDA ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1573765462 Longitud=Viscosidad= 1.1E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.2060411756 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 703,079 7.12116 7.121158 0.0197196276 0.0010.01972 ### 703,079 7.4536 7.453605 0.017999783 0.024355
0.018 ### 703,079 7.44813 7.448127 0.0180262709 0.0199490.01803 ### 703,079 7.44822 7.448217 0.0180258353 0.02010.01803 ### 703,079 7.44822 7.448215 0.0180258425 0.020094
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0334531312 Longitud=Viscosidad= 1.1E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 1.8930555502 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 249,086 6.45988 6.459876 0.0239635755 0.0010.02396 ### 249,086 6.94896 6.948964 0.0207090379 0.0388220.02071 ### 249,086 6.93629 6.936292 0.0207847724 0.0241010.02078 ### 249,086 6.93662 6.936618 0.0207828189 0.0253110.02078 ### 249,086 6.93661 6.93661 0.0207828692 0.025179
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.157 3.206041I (2-5) 300 0.2 0.034 1.079813
I (5-6) 450 0.25 -0.033 0.664598I (6-1) 500 0.2 -0.073 2.311671
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.033 1.893056II (3-4) 250 0.25 -0.007 0.133371II (4-5) 300 0.2 -0.037 1.16332II (2-5) 500 0.15 -0.034 1.919668
TERCERA ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1557456685 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.1728172853 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 689,743 7.11429 7.114293 0.0197577079 0.0010.01976 ### 689,743 7.45145 7.451447 0.0180102089 0.0250940.01801 ### 689,743 7.4458 7.445799 0.0180375453 0.0201690.01804 ### 689,743 7.44589 7.445893 0.0180370883 0.0203550.01804 ### 689,743 7.44589 7.445891 0.0180370959 0.020347
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0367767772 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0811350052 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 271,452 6.49949 6.499489 0.0236723589 0.0010.02367 ### 271,452 6.962 6.962004 0.0206315336 0.0497180.02063 ### 271,452 6.95083 6.950832 0.0206979078 0.027376
0.0207 ### 271,452 6.9511 6.9511 0.0206963108 0.0294840.0207 ### 271,452 6.95109 6.951093 0.0206963491 0.029204
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.156 3.172817I (2-5) 300 0.2 0.029 0.922106I (5-6) 450 0.25 -0.034 0.697822I (6-1) 500 0.2 -0.074 2.363583
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.037 2.081135II (3-4) 250 0.25 -0.003 0.065663II (4-5) 300 0.2 -0.033 1.057526II (2-5) 500 0.15 -0.029 1.6393
CUARTA ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1561563144 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.181182875 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 691,561 7.11524 7.115241 0.01975244 0.0010.01975 ### 691,561 7.45175 7.451746 0.0180087655 0.024920.01801 ### 691,561 7.44612 7.446121 0.0180359838 0.0201170.01804 ### 691,561 7.44621 7.446215 0.0180355298 0.0202940.01804 ### 691,561 7.44621 7.446213 0.0180355374 0.020287
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0361300378 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0445371259 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 266,679 6.49145 6.491447 0.023731052 0.0010.02373 ### 266,679 6.95938 6.959378 0.0206471028 0.0464730.02065 ### 266,679 6.94791 6.94791 0.02071532 0.026440.02072 ### 266,679 6.94819 6.948189 0.0207136548 0.028274
0.02071 ### 266,679 6.94818 6.948182 0.0207136953 0.028042CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.156 3.181183I (2-5) 300 0.2 0.030 0.955764I (5-6) 450 0.25 -0.034 0.689456I (6-1) 500 0.2 -0.074 2.350512
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.036 2.044537II (3-4) 250 0.25 -0.004 0.078838II (4-5) 300 0.2 -0.034 1.078112II (2-5) 500 0.15 -0.030 1.699136
quinta ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1560813628 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.1796559779 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 691,230 7.11507 7.115068 0.0197533997 0.0010.01975 ### 691,230 7.45169 7.451691 0.0180090284 0.024960.01801 ### 691,230 7.44606 7.446062 0.0180362683 0.0201290.01804 ### 691,230 7.44616 7.446156 0.0180358137 0.0203080.01804 ### 691,230 7.44615 7.446154 0.0180358213 0.0203
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0363025963 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0543019137 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 267,952 6.49361 6.493613 0.0237152194 0.001
0.02372 ### 267,952 6.96009 6.960087 0.0206429004 0.0472510.02064 ### 267,952 6.9487 6.948699 0.0207106182 0.0266680.02071 ### 267,952 6.94897 6.948975 0.0207089716 0.0285670.02071 ### 267,952 6.94897 6.948968 0.0207090116 0.028323
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.156 3.179656I (2-5) 300 0.2 0.030 0.947885I (5-6) 450 0.25 -0.034 0.690983I (6-1) 500 0.2 -0.074 2.352898
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.036 2.054302II (3-4) 250 0.25 -0.004 0.075323II (4-5) 300 0.2 -0.034 1.072619II (2-5) 500 0.15 -0.030 1.68513
sexta ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1561024256 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.1800850641 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 691,323 7.11512 7.115117 0.0197531299 0.0010.01975 ### 691,323 7.45171 7.451707 0.0180089545 0.0249520.01801 ### 691,323 7.44608 7.446079 0.0180361883 0.0201260.01804 ### 691,323 7.44617 7.446172 0.0180357339 0.0203050.01804 ### 691,323 7.44617 7.446171 0.0180357415 0.020298
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0362727156 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0526110194 Ks
f Número deDenomindenomina G(f) f
dato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 267,732 6.49324 6.493239 0.0237179519 0.0010.02372 ### 267,732 6.95996 6.959964 0.0206436255 0.0471120.02064 ### 267,732 6.94856 6.948562 0.0207114295 0.0266270.02071 ### 267,732 6.94884 6.948839 0.0207097796 0.0285150.02071 ### 267,732 6.94883 6.948832 0.0207098197 0.028273
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.156 3.180085I (2-5) 300 0.2 0.030 0.949507I (5-6) 450 0.25 -0.034 0.690554I (6-1) 500 0.2 -0.074 2.352227
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.036 2.052611II (3-4) 250 0.25 -0.004 0.075931II (4-5) 300 0.2 -0.034 1.07357II (2-5) 500 0.15 -0.030 1.688012
setima ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1560989876 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.1800150261 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 691,308 7.11511 7.115109 0.019753174 0.0010.01975 ### 691,308 7.4517 7.451704 0.0180089665 0.0249540.01801 ### 691,308 7.44608 7.446076 0.0180362014 0.0201270.01804 ### 691,308 7.44617 7.44617 0.0180357469 0.0203060.01804 ### 691,308 7.44617 7.446168 0.0180357545 0.020298
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0362816217 Longitud=
Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0531149978 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 267,798 6.49335 6.493351 0.0237171371 0.0010.02372 ### 267,798 6.96 6.960001 0.0206434093 0.0471530.02064 ### 267,798 6.9486 6.948603 0.0207111875 0.0266390.02071 ### 267,798 6.94888 6.94888 0.0207095387 0.028530.02071 ### 267,798 6.94887 6.948873 0.0207095787 0.028288
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.156 3.180015I (2-5) 300 0.2 0.030 0.949114I (5-6) 450 0.25 -0.034 0.690624I (6-1) 500 0.2 -0.074 2.352337
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.036 2.053115II (3-4) 250 0.25 -0.004 0.07575II (4-5) 300 0.2 -0.034 1.073287II (2-5) 500 0.15 -0.030 1.687314
octava ITERACION
Tubería (1-2)Longitud= 350 Caudal 0.1570878256 Longitud=Viscosidad= 1.2E-006 Diámetro 0.25 Viscosida=Ks 0.000150 Velocidad 3.2001594221 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 695,687 7.11738 7.117378 0.019740579 0.0010.01974 ### 695,687 7.45242 7.452418 0.0180055169 0.0247980.01801 ### 695,687 7.44685 7.446846 0.0180324702 0.020080.01803 ### 695,687 7.44694 7.446939 0.0180320228 0.0202520.01803 ### 695,687 7.44694 7.446937 0.0180320303 0.020245
CIRCUITO IITubería (2-3)
Longitud= 400 Caudal 0.0362802749 Longitud=Viscosidad= 1.2E-006 Diámetro 0.15 Viscosida=Ks 0.000150 Velocidad 2.0530387874 Ks
f Número deDenomindenomina G(f) fdato Ks/d Rreynolds 1/f datoasumido DATO CALCULADO asumido
0.001 ### 267,788 6.49333 6.493334 0.0237172603 0.0010.02372 ### 267,788 6.96 6.959995 0.020643442 0.0471470.02064 ### 267,788 6.9486 6.948597 0.0207112241 0.0266370.02071 ### 267,788 6.94887 6.948873 0.0207095751 0.0285280.02071 ### 267,788 6.94887 6.948867 0.0207096151 0.028286
CALCULO DE CAUDALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
I (1-2) 350 0.25 0.157 3.200159I (2-5) 300 0.2 0.031 0.980633I (5-6) 450 0.25 -0.033 0.67048I (6-1) 500 0.2 -0.073 2.320861
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL VELOCIDAD
II (2-3) 400 0.15 0.036 2.053039II (3-4) 250 0.25 -0.004 0.075777II (4-5) 300 0.2 -0.034 1.07333II (2-5) 500 0.15 -0.03081 1.743347
RESULTADOS FINALESCIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL Altura de
I (1-2) 350 0.25 0.156 100I (2-5) 300 0.2 0.029I (5-6) 450 0.25 -0.034I (6-1) 500 0.2 -0.074
CIRCUITO TUBERÍA LONGIT DIAMETRO CAUDAL
II (2-3) 400 0.15 0.037II (3-4) 250 0.25 -0.003
Tubería (2-5) Tubería (5-6)300 Caudal 0.01 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000100 Velocidad 0.318309 Ks 0.000100
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000500 55,358 5.6088 5.608783 0.03179 0.001 ### 177,1460.000500 55,358 6.8191 6.819111 0.02151 0.023599 ### 177,1460.000500 55,358 6.7046 6.704606 0.02225 0.018279 ### 177,1460.000500 55,358 6.7148 6.714815 0.02218 0.018543 ### 177,1460.000500 55,358 6.7139 6.713899 0.02218 0.018528 ### 177,146
Tubería (3-4) Tubería (4-5)250 Caudal 0.01 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000100 Velocidad 0.203718 Ks 0.000100
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000400 44,286 5.4423 5.442322 0.03376 0.001 ### 147,6220.000400 44,286 6.7606 6.760646 0.02188 0.025292 ### 147,6220.000400 44,286 6.6173 6.617346 0.02284 0.019927 ### 147,6220.000400 44,286 6.6318 6.631826 0.02274 0.020154 ### 147,6220.000400 44,286 6.6304 6.630352 0.02275 0.020143 ### 147,622
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0167586 11.166261 0 74.44174 0.00738 0.1570.0221845 0.1718465 0 17.18465 0.00738 0.016547 0.0340.0185285 -1.128734 0 28.21834 0.00738 -0.0330.0177736 -14.6857 0 183.5712 0.00738 -0.073sumas -4.476324 303.4159
0.0073765f hfi Kmi HFI+km Correción Nuevo
Caudal0.0188169 20.474377 10 413.5679 -0.01655 0.0330.0218788 0.0462789 0 4.627887 -0.01655 -0.0070.0199273 -0.617446 0 30.8723 -0.01655 -0.0370.0215053 -1.169977 0 116.9977 -0.01655 -0.00738 -0.034sumas 18.733233 566.0658
-0.016547
Tubería (2-5) Tubería (5-6)300 Caudal 0.034 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 1.079813 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 187,794 6.4077 6.407734 0.02436 0.001 ### 144,4780.000750 187,794 7.0802 7.08017 0.01995 0.02523 ### 144,4780.000750 187,794 7.0535 7.05351 0.0201 0.019658 ### 144,4780.000750 187,794 7.0546 7.054551 0.02009 0.01991 ### 144,4780.000750 187,794 7.0545 7.054511 0.02009 0.019896 ### 144,478
Tubería (3-4) Tubería (4-5)250 Caudal -0.00655 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.133371 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 28,994 5.0753 5.075277 0.03882 0.001 ### 202,3170.000600 28,994 6.4415 6.441485 0.0241 0.02403 ### 202,3170.000600 28,994 6.2856 6.285572 0.02531 0.019853 ### 202,3170.000600 28,994 6.302 6.302014 0.02518 0.019989 ### 202,3170.000600 28,994 6.3003 6.300266 0.02519 0.019984 ### 202,317
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0180258 13.220954 0 84.00841 -0.00163 0.155750.020094 1.7912485 0 52.80272 -0.00163 -0.00332 0.029
Correción ΔQ=
Correción ΔQ=
0.0198972 -0.806274 0 24.71456 -0.00163 -0.034250.0192258 -13.09111 0 180.26 -0.00163 -0.07425sumas 1.1148215 341.7857
-0.001631f hfi Kmi HFI+km Correción Nuevo
Caudal0.020709 10.086869 10 303.3489 0.00332 0.03678
0.0241006 0.0218502 0 -3.337497 0.00332 -0.003220.0198528 -2.054053 0 56.20326 0.00332 -0.033220.0207042 -12.96254 0 382.1118 0.00332 0.001631 -0.029sumas -4.907872 738.3265
0.0033236
Tubería (2-5) Tubería (5-6)300 Caudal 0.029 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.922106 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 160,366 6.3127 6.312722 0.02509 0.001 ### 151,7000.000750 160,366 7.0414 7.041404 0.02017 0.024972 ### 151,7000.000750 160,366 7.0092 7.009154 0.02035 0.019575 ### 151,7000.000750 160,366 7.0106 7.010557 0.02035 0.019813 ### 151,7000.000750 160,366 7.0105 7.010496 0.02035 0.019801 ### 151,700
Tubería (3-4) Tubería (4-5)250 Caudal -0.00322 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.065663 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 14,275 4.4848 4.484807 0.04972 0.001 ### 183,9170.000600 14,275 6.0439 6.043858 0.02738 0.024449 ### 183,9170.000600 14,275 5.8238 5.823798 0.02948 0.019976 ### 183,9170.000600 14,275 5.8517 5.85168 0.0292 0.020132 ### 183,9170.000600 14,275 5.8481 5.848097 0.02924 0.020126 ### 183,917
f hfi Kmi HFI+km Correción Nuevo
Correción ΔQ=
Correción ΔQ=
Caudal0.0180371 12.956443 0 83.18975 0.00041 0.156160.0203471 1.3226861 0 45.65884 0.00041 0.000647 0.0300.0198012 -0.884616 0 25.82493 0.00041 -0.033840.0192076 -13.67277 0 184.1344 0.00041 -0.07384sumas -0.27826 338.8079
0.0004106f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206315 12.145118 10 332.4463 -0.00065 0.036130.0273761 0.006016 0 -1.86647 -0.00065 -0.003870.0199764 -1.708009 0 51.4101 -0.00065 -0.033870.0208599 -9.523786 0 328.7591 -0.00065 -0.00041 -0.030sumas 0.9193388 710.749
-0.000647
Tubería (2-5) Tubería (5-6)300 Caudal 0.030 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.955764 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 166,220 6.3347 6.334699 0.02492 0.001 ### 149,8820.000750 166,220 7.0505 7.05052 0.02012 0.025035 ### 149,8820.000750 166,220 7.0196 7.019608 0.02029 0.019595 ### 149,8820.000750 166,220 7.0209 7.020921 0.02029 0.019837 ### 149,8820.000750 166,220 7.0209 7.020865 0.02029 0.019824 ### 149,882
Tubería (3-4) Tubería (4-5)250 Caudal -0.00387 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.078838 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 17,139 4.6387 4.638715 0.04647 0.001 ### 187,4980.000600 17,139 6.1499 6.149879 0.02644 0.024362 ### 187,4980.000600 17,139 5.9471 5.947076 0.02827 0.019951 ### 187,4980.000600 17,139 5.9717 5.971695 0.02804 0.020102 ### 187,498
Correción ΔQ=
Correción ΔQ=
0.000600 17,139 5.9687 5.968669 0.02807 0.020096 ### 187,498
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0180355 13.02373 0 83.40188 -7E-005 0.156080.020287 1.416812 0 47.18574 -7E-005 -0.00017 0.030
0.0198247 -0.864555 0 25.54553 -7E-005 -0.033920.0192121 -13.52513 0 183.1589 -7E-005 -0.07392sumas 0.0508609 339.292
-7.50E-005f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206471 11.730563 10 326.8067 0.00017 0.03630.0264403 0.0083761 0 -2.164376 0.00017 -0.00370.0199507 -1.772874 0 52.34355 0.00017 -0.03370.0208229 -10.21356 0 340.1541 0.00017 7.5E-005 -0.030sumas -0.247497 717.14
0.0001726
Tubería (2-5) Tubería (5-6)300 Caudal 0.030 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.947885 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 164,850 6.3296 6.329645 0.02496 0.001 ### 150,2140.000750 164,850 7.0484 7.048431 0.02013 0.025023 ### 150,2140.000750 164,850 7.0172 7.017215 0.02031 0.019592 ### 150,2140.000750 164,850 7.0185 7.018547 0.0203 0.019832 ### 150,2140.000750 164,850 7.0185 7.01849 0.0203 0.01982 ### 150,214
Tubería (3-4) Tubería (4-5)250 Caudal -0.0037 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.075323 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 16,375 4.6004 4.600407 0.04725 0.001 ### 186,542
Correción ΔQ=
Correción ΔQ=
0.000600 16,375 6.1236 6.123616 0.02667 0.024385 ### 186,5420.000600 16,375 5.9166 5.916557 0.02857 0.019957 ### 186,5420.000600 16,375 5.942 5.941968 0.02832 0.02011 ### 186,5420.000600 16,375 5.9388 5.938809 0.02835 0.020104 ### 186,542
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0180358 13.011436 0 83.36316 2E-005 0.15610.0203008 1.3944934 0 46.82845 2E-005 3.0E-005 0.0300.0198203 -0.8682 0 25.59653 2E-005 -0.03390.0192113 -13.55202 0 183.3369 2E-005 -0.0739sumas -0.014286 339.1251
2.11E-005f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206429 11.840471 10 328.3114 -3E-005 0.036270.0266676 0.0077115 0 -2.085644 -3E-005 -0.003730.0199575 -1.755451 0 52.09453 -3E-005 -0.033730.0208314 -10.04995 0 337.4873 -3E-005 -2E-005 -0.030sumas 0.0427776 715.8076
-2.99E-005
Tubería (2-5) Tubería (5-6)300 Caudal 0.030 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.949507 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 165,132 6.3307 6.33069 0.02495 0.001 ### 150,1200.000750 165,132 7.0489 7.048863 0.02013 0.025027 ### 150,1200.000750 165,132 7.0177 7.01771 0.02031 0.019593 ### 150,1200.000750 165,132 7.019 7.019038 0.0203 0.019833 ### 150,1200.000750 165,132 7.019 7.018982 0.0203 0.019821 ### 150,120
Tubería (3-4) Tubería (4-5)250 Caudal -0.00373 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.075931 Ks 0.000150
Número deDenomindenomina G(f) f Número de
Correción ΔQ=
Correción ΔQ=
Ks/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 16,507 4.6072 4.607171 0.04711 0.001 ### 186,7080.000600 16,507 6.1283 6.12826 0.02663 0.024381 ### 186,7080.000600 16,507 5.922 5.921954 0.02851 0.019956 ### 186,7080.000600 16,507 5.9472 5.947224 0.02827 0.020109 ### 186,7080.000600 16,507 5.9441 5.944089 0.0283 0.020103 ### 186,708
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0180357 13.01489 0 83.37404 -3E-006 0.15610.0202979 1.3990728 0 46.90199 -3E-006 -9E-006 0.029820.0198215 -0.867175 0 25.5822 -3E-006 -0.03390.0192115 -13.54446 0 183.2869 -3E-006 -0.0739sumas 0.002332 339.1451
-3.44E-006f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206436 11.821403 10 328.0508 9E-006 0.036280.0266272 0.0078247 0 -2.099314 9E-006 -0.003720.0199563 -1.758462 0 52.13766 9E-006 -0.033720.0208296 -10.08352 0 338.0362 9E-006 3.4E-006 -0.02982sumas -0.012756 716.1254
8.91E-006
Tubería (2-5) Tubería (5-6)300 Caudal 0.030 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.949114 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 165,063 6.3304 6.330437 0.02495 0.001 ### 150,1360.000750 165,063 7.0488 7.048759 0.02013 0.025026 ### 150,1360.000750 165,063 7.0176 7.01759 0.02031 0.019592 ### 150,1360.000750 165,063 7.0189 7.01892 0.0203 0.019833 ### 150,1360.000750 165,063 7.0189 7.018863 0.0203 0.019821 ### 150,136
Tubería (3-4) Tubería (4-5)250 Caudal -0.00372 Longitud= 300
Correción ΔQ=
Correción ΔQ=
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.07575 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 16,467 4.6052 4.605161 0.04715 0.001 ### 186,6590.000600 16,467 6.1269 6.12688 0.02664 0.024382 ### 186,6590.000600 16,467 5.9204 5.92035 0.02853 0.019957 ### 186,6590.000600 16,467 5.9457 5.945663 0.02829 0.020109 ### 186,6590.000600 16,467 5.9425 5.94252 0.02832 0.020103 ### 186,659
f hfi Kmi HFI+km Correción Nuevo Caudal
0.0180358 13.014326 0 83.37227 0.00099 0.157090.0202986 1.3979625 0 46.88417 0.00099 1.3E-006 0.030810.0198214 -0.867342 0 25.58454 0.00099 -0.032910.0201878 -14.23407 0 192.6099 0.00099 -0.07291sumas -0.689123 348.4509
0.0009888f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206434 11.827085 10 328.1285 -1E-006 0.036280.0266392 0.0077909 0 -2.095241 -1E-006 -0.003720.0199566 -1.757564 0 52.1248 -1E-006 -0.03372
0.02083 -10.07538 0 337.9032 -1E-006 -0.00099 -0.03081sumas 0.0019287 716.0613
-1.35E-006
Tubería (2-5) Tubería (5-6)300 Caudal 0.031 Longitud= 450
Viscosida= 1.15E-006 Diámetro 0.2 Viscosida= 1.15E-0060.000150 Velocidad 0.980633 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000750 170,545 6.3503 6.350301 0.0248 0.001 ### 145,7560.000750 170,545 7.0569 7.056937 0.02008 0.025183 ### 145,7560.000750 170,545 7.027 7.026959 0.02025 0.019643 ### 145,7560.000750 170,545 7.0282 7.02821 0.02024 0.019892 ### 145,7560.000750 170,545 7.0282 7.028158 0.02024 0.019879 ### 145,756
Correción ΔQ=
Correción ΔQ=
Tubería (3-4) Tubería (4-5)250 Caudal -0.00372 Longitud= 300
Viscosida= 1.15E-006 Diámetro 0.25 Viscosida= 1.15E-0060.000150 Velocidad 0.075777 Ks 0.000150
Número deDenomindenomina G(f) f Número deKs/d Rreynolds 1/f dato Ks/d RreynoldsDATO CALCULADO asumido DATO CALCULADO
0.000600 16,473 4.6055 4.605465 0.04715 0.001 ### 186,6660.000600 16,473 6.1271 6.127089 0.02664 0.024382 ### 186,6660.000600 16,473 5.9206 5.920593 0.02853 0.019957 ### 186,6660.000600 16,473 5.9459 5.945899 0.02829 0.020109 ### 186,6660.000600 16,473 5.9428 5.942758 0.02832 0.020103 ### 186,666
f hfi Kmi HFI+km Correción Nuevo Caudal
0.018032 13.17701 0 83.88308 -0.00096 0.156120.020245 1.4884073 0 48.31307 -0.00096 -0.00046 0.02939
0.0198796 -0.819884 0 24.91128 -0.00096 -0.033880.0192225 -13.19316 0 180.946 -0.00096 -0.07388sumas 0.6523694 338.0534
-0.000965f hfi Kmi HFI+km Correción Nuevo
Caudal0.0206434 11.826225 10 328.1168 0.00046 0.036740.0266374 0.007796 0 -2.095857 0.00046 -0.003260.0199566 -1.7577 0 52.12675 0.00046 -0.03326
0.020797 -10.7386 0 348.5704 0.00046 0.000965 -0.02939sumas -0.662278 726.718
0.0004557
hfi+Kñi altura deNudo camino agua
13.0960724 1 100 100.0001.41977596 2 (1-2) 86.904-0.8439211 5 (1-2)+(2-5) 85.484-13.367757 6 (1-6) 86.632
12.0536772 3 (1-2)-(2-3) 74.8500.00684101 4 83.750
Correción ΔQ=
Correción ΔQ=
Tubería (5-6) Tubería (1-6)Caudal -0.04 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.8148714 Ks 0.000100 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.509578 6.5095777 0.023599 0.001 ### 442,865 7.0051 7.00517.396452 7.3964516 0.018279 0.0203782 ### 442,865 7.5147 7.51477.343611 7.3436111 0.018543 0.0177082 ### 442,865 7.5005 7.50057.346671 7.3466709 0.0185276 0.0177754 ### 442,865 7.5009 7.50097.346493 7.3464934 0.0185285 0.0177735 ### 442,865 7.5009 7.5009
Tubería (4-5) Tubería (2-5)Caudal -0.02 Longitud= 500 CaudalDiámetro 0.15 Viscosida= 1.15E-006 DiámetrVelocidad 1.13176584 Ks 0.000100 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.287921 6.2879205 0.0252922 0.001 ### 55,358 5.6088 5.60887.083954 7.0839541 0.0199273 0.031788 ### 55,358 6.8191 6.81917.043941 7.0439407 0.0201543 0.0215053 ### 55,358 6.7046 6.70467.045909 7.0459086 0.0201431 0.0222461 ### 55,358 6.7148 6.71487.045812 7.0458118 0.0201436 0.0221785 ### 55,358 6.7139 6.7139
Tubería (5-6) Tubería (1-6)Caudal -0.032623 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.66459799 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.295599 6.2955992 0.0252305 0.001 ### 402,030 6.7956 6.79567.132348 7.1323483 0.0196578 0.0216544 ### 402,030 7.2212 7.2212
7.08705 7.0870499 0.0199099 0.019177 ### 402,030 7.2118 7.21187.089443 7.0894426 0.0198965 0.0192268 ### 402,030 7.212 7.2127.089316 7.0893161 0.0198972 0.0192257 ### 402,030 7.212 7.212
Tubería (4-5) Tubería (2-5)Caudal -0.036547 Longitud= 500 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.16332025 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.450931 6.4509305 0.0240301 0.001 ### 250,391 6.4623 6.46237.097241 7.0972412 0.0198528 0.0239454 ### 250,391 6.9498 6.94987.072951 7.072951 0.0199894 0.0207042 ### 250,391 6.9372 6.93727.073852 7.0738517 0.0199843 0.0207793 ### 250,391 6.9375 6.93757.073818 7.0738183 0.0199845 0.0207774 ### 250,391 6.9375 6.9375
Tubería (5-6) Tubería (1-6)Caudal -0.034254 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.69782188 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.32813 6.3281304 0.0249718 0.001 ### 411,058 6.8051 6.8051
7.147414 7.1474137 0.019575 0.0215942 ### 411,058 7.2243 7.22437.104377 7.104377 0.0198129 0.0191605 ### 411,058 7.2153 7.21537.106585 7.1065854 0.0198006 0.0192086 ### 411,058 7.2154 7.21547.106472 7.106472 0.0198012 0.0192076 ### 411,058 7.2154 7.2154
Tubería (4-5) Tubería (2-5)Caudal -0.033223 Longitud= 500 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.05752555 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.395449 6.3954487 0.0244488 0.001 ### 213,822 6.3856 6.38567.075252 7.0752516 0.0199764 0.0245241 ### 213,822 6.9238 6.92387.047898 7.0478978 0.0201317 0.0208599 ### 213,822 6.908 6.9087.048982 7.048982 0.0201255 0.0209552 ### 213,822 6.9085 6.90857.048939 7.048939 0.0201258 0.0209524 ### 213,822 6.9085 6.9085
Tubería (5-6) Tubería (1-6)Caudal -0.033844 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.68945629 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.320122 6.3201219 0.0250351 0.001 ### 408,785 6.8027 6.80277.143723 7.1437231 0.0195952 0.0216091 ### 408,785 7.2235 7.22357.100134 7.1001343 0.0198366 0.0191646 ### 408,785 7.2144 7.21447.102387 7.1023872 0.019824 0.0192132 ### 408,785 7.2146 7.21467.102271 7.1022706 0.0198247 0.0192121 ### 408,785 7.2146 7.2146
Tubería (4-5) Tubería (2-5)Caudal -0.03387 Longitud= 500 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.07811186 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.406808 6.4068077 0.0243622 0.001 ### 221,626 6.4035 6.4035
7.0798 7.0798001 0.0199507 0.0243873 ### 221,626 6.9299 6.92997.053088 7.053088 0.0201021 0.0208229 ### 221,626 6.915 6.9157.054133 7.0541327 0.0200961 0.0209132 ### 221,626 6.9154 6.9154
7.054092 7.0540919 0.0200964 0.0209106 ### 221,626 6.9154 6.9154
Tubería (5-6) Tubería (1-6)Caudal -0.033919 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.69098319 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.321593 6.3215925 0.0250234 0.001 ### 409,200 6.8031 6.80317.144402 7.1444017 0.0195915 0.0216064 ### 409,200 7.2237 7.22377.100915 7.1009145 0.0198322 0.0191639 ### 409,200 7.2146 7.21467.103159 7.1031592 0.0198197 0.0192123 ### 409,200 7.2148 7.21487.103043 7.1030432 0.0198203 0.0192113 ### 409,200 7.2148 7.2148
Tubería (4-5) Tubería (2-5)Caudal -0.033697 Longitud= 500 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.07261917 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.403805 6.4038052 0.0243851 0.001 ### 219,800 6.3994 6.3994
7.0786 7.0786001 0.0199575 0.0244186 ### 219,800 6.9285 6.92857.051719 7.0517191 0.0201099 0.0208314 ### 219,800 6.9134 6.91347.052774 7.0527742 0.0201039 0.0209228 ### 219,800 6.9138 6.91387.052733 7.0527328 0.0201041 0.0209202 ### 219,800 6.9138 6.9138
Tubería (5-6) Tubería (1-6)Caudal -0.033898 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.6905541 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.32118 6.3211796 0.0250267 0.001 ### 409,083 6.803 6.803
7.144211 7.1442112 0.0195926 0.0216072 ### 409,083 7.2236 7.22367.100696 7.1006955 0.0198334 0.0191641 ### 409,083 7.2145 7.21457.102943 7.1029425 0.0198209 0.0192126 ### 409,083 7.2147 7.21477.102826 7.1028263 0.0198215 0.0192115 ### 409,083 7.2147 7.2147
Tubería (4-5) Tubería (2-5)Caudal -0.033727 Longitud= 250 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.07357029 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin
1/f dato Ks/d RreynoldsCALCULADO asumido DATO CALCULADO
6.404327 6.4043266 0.0243811 0.001 ### 220,176 6.4003 6.40037.078809 7.0788086 0.0199563 0.0244121 ### 220,176 6.9288 6.92887.051957 7.051957 0.0201085 0.0208296 ### 220,176 6.9137 6.9137
7.05301 7.0530103 0.0201025 0.0209208 ### 220,176 6.9141 6.91417.052969 7.0529689 0.0201028 0.0209182 ### 220,176 6.9141 6.9141
Tubería (5-6) Tubería (1-6)Caudal -0.033901 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.69062414 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.321247 6.321247 0.0250262 0.001 ### 545,469 6.7623 6.76237.144242 7.1442423 0.0195924 0.0218683 ### 545,469 7.0418 7.04187.100731 7.1007313 0.0198332 0.0201669 ### 545,469 7.0381 7.03817.102978 7.1029779 0.0198207 0.0201881 ### 545,469 7.0381 7.03817.102862 7.1028618 0.0198214 0.0201878 ### 545,469 7.0381 7.0381
Tubería (4-5) Tubería (2-5)Caudal -0.033718 Longitud= 500 Caudal
Diámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.07328681 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.404171 6.4041713 0.0243823 0.001 ### 220,084 6.4001 6.40017.078746 7.0787465 0.0199566 0.0244137 ### 220,084 6.9288 6.92887.051886 7.0518861 0.020109 0.02083 ### 220,084 6.9136 6.9136
7.05294 7.0529399 0.0201029 0.0209213 ### 220,084 6.9141 6.91417.052899 7.0528986 0.0201032 0.0209187 ### 220,084 6.914 6.914
Tubería (5-6) Tubería (1-6)Caudal -0.032912 Longitud= 500 CaudalDiámetro 0.25 Viscosida= 1.15E-006 DiámetrVelocidad 0.67047974 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.301502 6.3015023 0.0251833 0.001 ### 403,628 6.7973 6.79737.135097 7.1350966 0.0196427 0.0216436 ### 403,628 7.2218 7.22187.090212 7.0902124 0.0198921 0.019174 ### 403,628 7.2125 7.21257.092571 7.0925709 0.0198789 0.0192235 ### 403,628 7.2127 7.21277.092447 7.0924468 0.0198796 0.0192225 ### 403,628 7.2127 7.2127
Tubería (4-5) Tubería (2-5)Caudal -0.03372 Longitud= 500 CaudalDiámetro 0.2 Viscosida= 1.15E-006 DiámetrVelocidad 1.07332967 Ks 0.000150 Velocida
Denomin denomina G(f) f Número deDenomindenomin1/f dato Ks/d Rreynolds
CALCULADO asumido DATO CALCULADO6.404195 6.4041947 0.0243821 0.001 ### 227,393 6.4162 6.41627.078756 7.0787559 0.0199566 0.0242912 ### 227,393 6.9343 6.93437.051897 7.0518969 0.0201089 0.020797 ### 227,393 6.9198 6.91987.052951 7.0529506 0.0201029 0.0208839 ### 227,393 6.9202 6.92027.052909 7.0529092 0.0201031 0.0208815 ### 227,393 6.9202 6.9202
-0.080.2
2.5464731G(f)1/f
0.0203780.0177080.0177750.0177740.017774
-0.010.2
0.3183091G(f)1/f
0.0317880.0215050.0222460.0221780.022185
-0.072620.2
2.3116709G(f)1/f
0.0216540.0191770.0192270.0192260.019226
-0.0340.15
1.9196681G(f)1/f
0.0239450.0207040.0207790.0207770.020777
-0.074250.2
2.3635833G(f)1/f
0.0215940.0191610.0192090.0192080.019208
-0.0290.15
1.6393001G(f)1/f
0.0245240.02086
0.0209550.0209520.020952
-0.073840.2
2.350512G(f)1/f
0.0216090.0191650.0192130.0192120.019212
-0.0300.15
1.6991357G(f)1/f
0.0243870.0208230.0209130.020911
0.020911
-0.073920.2
2.3528978G(f)1/f
0.0216060.0191640.0192120.0192110.019211
-0.0300.15
1.6851295G(f)1/f
0.024419
0.0208310.020923
0.020920.02092
-0.07390.2
2.3522273G(f)1/f
0.0216070.0191640.0192130.0192120.019212
-0.0300.15
1.6880123G(f)
1/f
0.0244120.02083
0.0209210.0209180.020918
-0.07390.15
4.1819321G(f)1/f
0.0218680.0201670.0201880.0201880.020188
-0.030
0.151.6873138
G(f)1/f
0.0244140.02083
0.0209210.0209190.020919
-0.072910.2
2.3208612G(f)1/f
0.0216440.0191740.0192240.0192220.019222