calculo de caudal y perdidas hunter y nec 11 xls

7/23/2019 Calculo de Caudal y Perdidas Hunter y NEC 11 Xls

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M

TIPO DE APARATO SANITARIO CANTIDAD

[l/s] [l/s]

Inodoro con Fluxmetro 2.00 1.25 1.60

Inodoro con Tanque 0.00 0.10 0.20

Urinario con Fluxmetro 0.00 0.50 0.90

Urinario con Llave 0.00 0.15 0.90

Lavamanos 2.00 0.10 0.15

Fregadero de ocina 0.00 0.20 0.20

!uc"a 0.00 0.20 0.20

Llave de #anguera 0.00 0.20 0.20

TOTAL APARATOS SANITARIOS 4.00 CAUDAL BRUTO [l/s]

MTODO DE APORTES

SELECCIN DE MTODO METODO 1

DESCRIPCIN UNIDADES VALOR

audal $ruto %l&s' 2.(0

Factor de Uso %)dimensional' 1.00

oe* de +imultaneidad ,+ %-' 0.61

audal +imultneo %l&s' 1.6/

MTODO DE UNIDADES DE CARGA M

SELECCIN DE MTODO METODO 3

DESCRIPCIN UNIDADES VALOR DESCRIPCIN

Unidades de arga %+FU' 1/.00 Unidades de arga

U2/0 %l&s' 2.00 20U00

2/0U1000 %l&s' 0.00 00U900

3ara 4 !FU 2/0 con aaratos comunes 3ara 20 4 !FU

3ara 4 !FU 2/0 con aaratos *luxores

3ara 260 4 !FU 1000 con aaratos comunes 3ara 00 4 !F

3ara 260 4 !FU 1000 con aaratos *luxores

3ara !FU 900

CAUDAL UNITARIOSEGN NEC!11

CAUDAL UNITARIOSEGN IPC

CAUDAL TOTAL SEGNNEC!11

TOTAL UNIDADES DECARGA USO PRIVADO

SELECCIN DEMTODO

7c8060521(:;

7c80/6(95:;

7c8012(6/2:;


2/15

ODO DE APORTES MTODO

[l/s] [l/s] ["SFU] # [U.M.] ["SFU] # [U.M.]

2.50 6.00 10.00

0.00 0.00 .00 5.00

0.00 0.00 5.00 5.00

0.00 0.00 2.00 2.00

0.20 0.0 1.00 1.50

0.00 0.00 2.00 .00

0.00 0.00 2.00 /.00

0.00 0.00 1.00 1.00

$.%0 0.30 UNIDADES TOTALES ["SFU]

TODO DE UNIDADES DE CARGA EDIFICIOS

METODO 3

UNIDADES VALOR

%+FU' 1/.00

%l&s' 0.00

%l&s' 0.00

00 con aaratos *luxores

900 con aaratos *luxores

on aaratos comunes

CAUDAL TOTAL SEGN NEC!11METODO 1

CAUDAL TOTAL SEGN IPCMETODO $

UNIDADES DE CARGAUSO PRIVADO

UNIDADES DE CARGAUSO PBLICO

TOTAL UNIDADES DECARGA USO PRIVADO

!FU=>0/2601

!FU=>0/(?095

!FU=>065550?


3/15

E UNIDADES DE CARGA

["SFU] ["SFU]

12.00 20.00

0.00 0.00

0.00 0.00

0.00 0.00

2.00 .00

0.00 0.00

0.00 0.00

0.00 0.00

14.00 $3.00

TOTAL UNIDADES DE CARGAUSO PRIVADO

METODO 3

TOTAL UNIDADES DE CARGAUSO PBLICO

METODO 4


4/15

@AB) !C DLUL

,8 0.00002 m

7 ! ! )

Tramo U!H :L&s= :3ulg= :m=2 1/.00 2.00 2 5.0?00C02 2.0C0

2L# 0.(5 0.20 1&2 1.2(00C02 1.2(C0/12 .(5 0.26 1&2 1.2(00C02 1.2(C0/1F 2.00 0.20 1&2 1.2(00C02 1.2(C0/C1 5.(5 0./2 1&2 1.2(00C02 1.2(C0/

:m2=


5/15

3)E) TU$CEI)+ E)#IFI)!)+ 3AE CL #TA!A !C @UGTCE

Eugosidad )Jsoluta :TaJlas= 8 1/0

K e8,&! Ee f L Le "* B

:m&s= :m= :m= :m= :m= -0.9?6? .9/C0/ .?C0/ 0.02/ .6/00 0.(500 /.9 0.0? 2.2?-

1.5(?? 1.5(C0 1.5C0/ 0.0650 0.6000 0.5000 1.10 0.(15 /.?6-2.0525 1.5(C0 1.99C0/ 0.0650 2.0000 0.5000 2.50 2.(/( 0.00-1.5(?? 1.5(C0 1.5C0/ 0.0650 0.6000 0.5000 1.10 0.(15 0.00-.155 1.5(C0 .21C0/ 0.0650 10.0000 0.0600 10.06 2?.?/? 0.00-

"*8 0.0? @aMenB8 2.9-

LT


6/15

:m= :m= :m= :m=0.0000 0.0000 0.0?0 0.0?0

0.6000 2.0000 .15 .150.0000 0.0000 2.(/( 2.?00.6000 2.0000 .15 .150.0000 0.0000 2?.?/(? 1.6(?0

M @equios @T @Tacum.


7/15

DATOS DE ENTRADA

N& TRAMO MATERIAL ESPECIFICACIN

1.00 )/?G9 )cero InoxidaJle )cero InoxidaJle 16.91

$.00 G9G(6 )cero InoxidaJle )cero InoxidaJle 1.55

3.00 G(6G(6N )cero InoxidaJle )cero InoxidaJle /.?

4.00 G(6NG(6NN )cero InoxidaJle )cero InoxidaJle /.20

'.00 G(6NNG(0 )cero InoxidaJle )cero InoxidaJle .20

(.00 G(0G5( )cero InoxidaJle )cero InoxidaJle 6.0

%.00 G5(G66 )cero InoxidaJle )cero InoxidaJle 15.69

).00 G66G6? )cero InoxidaJle )cero InoxidaJle /.16

*.00 G6?G(1 )cero InoxidaJle )cero InoxidaJle /.10

10.00 G(1G/ )cero InoxidaJle )cero InoxidaJle .6?

11.00 G/G1? )cero InoxidaJle )cero InoxidaJle .(?

1$.00 G1?G6 )cero InoxidaJle )cero InoxidaJle 1//.5

13.00 G6G/2 )cero InoxidaJle )cero InoxidaJle /.00

14.00

1'.00

1(.00

1%.00

1).00

1*.00

$0.00

$1.00

$$.00

$3.00

$4.00

$'.00

$(.00

$%.00

$).00

$*.00

30.00

31.00

3$.00

33.0034.00

3'.00

3(.00

3%.00

3).00

3*.00

40.00

41.00

4$.00

43.0044.00

4'.00

LONGITUD[+]


8/15

4(.00

4%.00

4).00

4*.00

'0.00

RESUMEN DE RESULTADOS

DESCRIPCIN UNIDADES VALOR

3resin de onsumo %si' 10.00

3Ordidas #aPores %si' 2.06

3Ordidas #enores %si' 1.60

olumna de )gua %mca' 22.5?

arga Total %si' (5.95


9/15

0.20 100.00 0.50 1/.2?

0./1 100.00 0.(5 20.22

0./1 100.00 0.(5 20.22

0.(1 100.00 0.(5 20.22

0.(1 100.00 1.00 26.5?

1.09 100.00 1.00 26.5?

1.09 100.00 1.00 26.5?

.6/ 100.00 2.00 /6.20

/./ 100.00 2.00 /6.20

5.51 100.00 .00 ?5.10

6.2( 100.00 .00 ?5.10

6.2( 100.00 .00 ?5.10

6.2( 100.00 .00 ?5.10

CAUDAL SIMULT,NEO[l/s]

COEFICIENTE-AEN!"ILLIAMS

DI,METRO NOMINAL[]

DI,METRO INTERIOR[++]


10/15


11/15

DATOS DE SALIDA

1.60C0/ 1.2/9 0.200 6.966

.21C0/ 1.2(( 0./10 0.//

.21C0/ 1.2(( 0./10 1.25

.21C0/ 2.211 0.(10 .22

5.55C0/ 1.2?0 0.(10 0.66?

5.55C0/ 1.96/ 1.090 2.909

5.55C0/ 1.96/ 1.090 (.2//

1.6?C0 2.1(1 .6/0 1.21

1.6?C0 2.6/ /./0 1.(20

5.69C0 0.969 5.510 0.11?

5.69C0 1.102 6.2(0 0.15/

5.69C0 1.102 6.2(0 5.??9

5.69C0 1.102 6.2(0 0.16

,REA -IDR,ULICA[+$]

VELOCIDAD[+/s]

CAUDAL CALCULADO[l/s]

DIFERENCIAL DEPRESIN

[2s]


12/15


13/15

MATERIAL COEFICIENTE -AEN!"ILLIAMS

3K 150.00

oJre 10.00

Latn 10.00

@ierro Fundido 100.00

)sJesto emento 1/0.00

Ladrillo de +aneamiento 100.00oncreto 120.00

@ierro !uctil 1/0.00

FiJra 1/0.00

FiJra de Kidrio 150.00

@ierro HalvaniMado 120.00

Kidrio 10.00

3lomo 15.00

3lstico 1/0.00

3olietileno 150.00

3K 150.00)cero InoxidaJle 100.00


14/15

TIPO DE TUBERIA ESPECIFICACIN

3K EoscaJle 33 0.50 20.00

3K EoscaJle 33 0.(5 25.00

3K EoscaJle 33 1.00 2.00

3K EoscaJle 33 1.25 /0.00

3K EoscaJle 33 1.50 50.00

3K EoscaJle 33 2.00 6.00

3ALI3EA3ILCGA Termo*usin 0.50 20.00

3ALI3EA3ILCGA Termo*usin 0.(5 25.00


3ALI3EA3ILCGA Termo*usin 1.25 /0.00



)CEA )cero InoxidaJle 0.50 15.??

)CEA )cero InoxidaJle 0.(5 22.22

)CEA )cero InoxidaJle 1.00 2?.5?

)CEA )cero InoxidaJle 1.25 /.00

)CEA )cero InoxidaJle 1.50 /2.(0

)CEA )cero InoxidaJle 2.00 /?.60

)CEA )cero InoxidaJle 2.50 60.50

)CEA )cero InoxidaJle .00 ?9.10

)CEA )cero InoxidaJle /.00 11/.0

)CEA )cero InoxidaJle 6.00 16?.0

DI,METRO NOMINAL[]

DI,METRO NOMINAL[++]


15/15

./0 1.20 1.(C0/

.90 1(.20 2.2C0/

/.90 22.20 .?(C0/

5.(0 2?.60 6./2C0/

6.0 (./0 1.10C0

(.50 /?.00 1.?1C0

./0 1.20 1.(C0/

/.20 16.60 2.16C0/

5./0 21.20 .5C0/

6.(0 26.60 5.56C0/

?.0 ./0 ?.(6C0/

10.50 /2.00 1.9C0

0.?0 1/.2? 1.60C0/

1.00 20.22 .21C0/

1.00 26.5? 5.55C0/

1.20 1.60 (.?/C0/

1.20 /0.0 1.2?C0

1.20 /6.20 1.6?C0

1.50 5(.50 2.60C0

2.00 ?5.10 5.69C0

2.00 110.0 9.56C0

2.(0 162.90 2.0?C02

ESPESOR DE PARED[++]

DI,METRO INTERIOR[++]

,REA DE FLUO[+$]

calculo de caudal y perdidas hunter y nec 11 xls

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