DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°12-PLANTA DE TRATAMIENTO PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s PT 3352 CODO 0.8

Qmacachacra 1.0 l/s Qmd=Qm*Cvd RV 3345 UNION 1.0Qantarumi 0.6 l/s cvd= 1.3 ∆H 7 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 3.30Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 60 m 2 0.0508 7 2.5 3.016 5.470 0.003 0.010 1 1.530Ks 0.0000015 m 2.5 0.0635 7 2.5 3.016 5.470 0.003 0.010 1 1.530d 0.0508 m C-7,5 3 0.0762 5.470 2.5 2.632 5.835 0.003 0.008 1 1.165PERDIDAS POR ACCESORIOS 4 0.1016 5.835 2.5 2.728 5.749 0.003 0.009 1 1.251

Km 3.30 6 0.1524 5.749 2.5 2.705 5.769 0.003 0.009 1 1.231CARACTERISTICAS DEL FLUIDO 8 0.2032 5.769 2.5 2.711 5.764 0.003 0.009 1 1.236ρ 998.2 Kg/m3 10 0.254 5.764 2.5 2.709 5.765 0.003 0.009 1 1.235μ 0.001005 Pa.s 12 0.3048 5.765 2.5 2.710 5.765 0.003 0.009 1 1.235ν 0.000001007 m2/seg 14 0.3556 5.765 2.5 2.710 5.765 0.003 0.009 1 1.235CARACTERIATICAS DEL FLUJO 18 0.4572 5.765 2.5 2.710 5.765 0.003 0.009 1 1.235

Qd 0.005 m3/seg 24 0.6096 5.765 2.5 2.710 5.765 0.003 0.009 1 1.235CARACTERISTICAS TOPOGRAFICAS 30 0.762 5.765 2.5 2.710 5.765 0.003 0.009 1 1.235

H 7 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.009 m3/s 0.040g 9.81 m/seg2 60 1.524 V 2.710 m/s

otros 72 1.8288 hf 1.235 mE 0.001 hm 5.765 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°12-PLANTA DE TRATAMIENTO PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR12 3362 CODO 0.8

Qmacachacra 1.0 l/s Qmd=Qm*Cvd PT 3352 UNION 2.0Qantarumi 0.6 l/s cvd= 1.3 ∆H 10 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 4.30Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 120 m 2 0.0508 10 2.5 2.504 8.625 0.003 0.008 1 1.375Ks 0.0000015 m 2.5 0.0635 10 2.5 2.504 8.625 0.003 0.008 1 1.375d 0.0508 m C-7,5 3 0.0762 8.625 2.5 2.308 8.833 0.003 0.007 1 1.167PERDIDAS POR ACCESORIOS 4 0.1016 8.833 2.5 2.338 8.802 0.003 0.007 1 1.198

Km 4.30 6 0.1524 8.802 2.5 2.334 8.806 0.003 0.007 1 1.194CARACTERISTICAS DEL FLUIDO 8 0.2032 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194ρ 998.2 Kg/m3 10 0.254 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194μ 0.001005 Pa.s 12 0.3048 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194ν 0.000001007 m2/seg 14 0.3556 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194CARACTERIATICAS DEL FLUJO 18 0.4572 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194

Qd 0.005 m3/seg 24 0.6096 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194CARACTERISTICAS TOPOGRAFICAS 30 0.762 8.806 2.5 2.334 8.806 0.003 0.007 1 1.194

H 10 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.007 m3/sg 9.81 m/seg2 60 1.524 V 2.334 m/s

otros 72 1.8288 hf 1.194 mE 0.001 hm 8.806 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°11-CAMARA ROMPE PRESION N°12 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR11 3394 CODO 2

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR12 3362 UNION 9.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 32 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 12.83Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 560 m 2 0.0508 32 2.5 2.032 29.299 0.003 0.006 1 2.701Ks 0.0000015 m 2.5 0.0635 32 2.5 2.032 29.299 0.003 0.006 1 2.701d 0.0508 m C-7,5 3 0.0762 29.299 2.5 1.935 29.551 0.003 0.006 1 2.449PERDIDAS POR ACCESORIOS 4 0.1016 29.551 2.5 1.944 29.527 0.003 0.006 1 2.473

Km 12.83 6 0.1524 29.527 2.5 1.943 29.529 0.003 0.006 1 2.471CARACTERISTICAS DEL FLUIDO 8 0.2032 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471ρ 998.2 Kg/m3 10 0.254 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471μ 0.001005 Pa.s 12 0.3048 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471ν 0.000001007 m2/seg 14 0.3556 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471CARACTERIATICAS DEL FLUJO 18 0.4572 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471

Qd 0.005 m3/seg 24 0.6096 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471CARACTERISTICAS TOPOGRAFICAS 30 0.762 29.529 2.5 1.944 29.529 0.003 0.006 1 2.471

H 32 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.006 m3/sg 9.81 m/seg2 60 1.524 V 1.944 m/s

otros 72 1.8288 hf 2.471 mE 0.001 hm 29.529 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°10-CAMARA ROMPE PRESION N°11 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR10 3444 CODO 1

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR11 3394 UNION 3.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 5.83Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 200 m 2 0.0508 50 2 3.961 45.334 0.002 0.008 1 4.666Ks 0.0000015 m 2.5 0.0635 50 2 3.961 45.334 0.002 0.008 1 4.666d 0.0508 m C-7,5 3 0.0762 45.334 2 3.753 45.812 0.002 0.008 1 4.188PERDIDAS POR ACCESORIOS 4 0.1016 45.812 2 3.775 45.763 0.002 0.008 1 4.237

Km 5.83 6 0.1524 45.763 2 3.773 45.768 0.002 0.008 1 4.232CARACTERISTICAS DEL FLUIDO 8 0.2032 45.768 2 3.773 45.767 0.002 0.008 1 4.233ρ 998.2 Kg/m3 10 0.254 45.767 2 3.773 45.768 0.002 0.008 1 4.232μ 0.001005 Pa.s 12 0.3048 45.768 2 3.773 45.768 0.002 0.008 1 4.232ν 0.000001007 m2/seg 14 0.3556 45.768 2 3.773 45.768 0.002 0.008 1 4.232CARACTERIATICAS DEL FLUJO 18 0.4572 45.768 2 3.773 45.768 0.002 0.008 1 4.232

Qd 0.005 m3/seg 24 0.6096 45.768 2 3.773 45.768 0.002 0.008 1 4.232CARACTERISTICAS TOPOGRAFICAS 30 0.762 45.768 2 3.773 45.768 0.002 0.008 1 4.232

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.008 m3/sg 9.81 m/seg2 60 1.524 V 3.773 m/s

otros 72 1.8288 hf 4.232 mE 0.001 hm 45.768 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°9-CAMARA ROMPE PRESION N°10 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR9 3494 CODO 1.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR10 3444 UNION 7.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 10.33Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 440 m 2 0.0508 50 2.5 2.973 45.346 0.003 0.009 1 4.654Ks 0.0000015 m 2.5 0.0635 50 2.5 2.973 45.346 0.003 0.009 1 4.654d 0.0508 m C-7,5 3 0.0762 45.346 2.5 2.817 45.822 0.003 0.009 1 4.178PERDIDAS POR ACCESORIOS 4 0.1016 45.822 2.5 2.833 45.774 0.003 0.009 1 4.226

Km 10.33 6 0.1524 45.774 2.5 2.831 45.779 0.003 0.009 1 4.221CARACTERISTICAS DEL FLUIDO 8 0.2032 45.779 2.5 2.831 45.778 0.003 0.009 1 4.222ρ 998.2 Kg/m3 10 0.254 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222μ 0.001005 Pa.s 12 0.3048 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222ν 0.000001007 m2/seg 14 0.3556 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222CARACTERIATICAS DEL FLUJO 18 0.4572 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222

Qd 0.005 m3/seg 24 0.6096 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222CARACTERISTICAS TOPOGRAFICAS 30 0.762 45.778 2.5 2.831 45.778 0.003 0.009 1 4.222

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.009 m3/sg 9.81 m/seg2 60 1.524 V 2.831 m/s

otros 72 1.8288 hf 4.222 mE 0.001 hm 45.778 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°8-CAMARA ROMPE PRESION N°9 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR8 3544 CODO 0.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR9 3494 UNION 4.7Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 6.67Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 280 m 2 0.0508 50 2 3.291 46.321 0.002 0.007 1 3.679Ks 0.0000015 m 2.5 0.0635 50 2 3.291 46.321 0.002 0.007 1 3.679d 0.0508 m C-7,5 3 0.0762 46.321 2 3.155 46.619 0.002 0.006 1 3.381PERDIDAS POR ACCESORIOS 4 0.1016 46.619 2 3.166 46.595 0.002 0.006 1 3.405

Km 6.67 6 0.1524 46.595 2 3.165 46.597 0.002 0.006 1 3.403CARACTERISTICAS DEL FLUIDO 8 0.2032 46.597 2 3.165 46.596 0.002 0.006 1 3.404ρ 998.2 Kg/m3 10 0.254 46.596 2 3.165 46.596 0.002 0.006 1 3.404μ 0.001005 Pa.s 12 0.3048 46.596 2 3.165 46.596 0.002 0.006 1 3.404ν 0.000001007 m2/seg 14 0.3556 46.596 2 3.165 46.596 0.002 0.006 1 3.404CARACTERIATICAS DEL FLUJO 18 0.4572 46.596 2 3.165 46.596 0.002 0.006 1 3.404

Qd 0.005 m3/seg 24 0.6096 46.596 2 3.165 46.596 0.002 0.006 1 3.404CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.596 2 3.165 46.596 0.002 0.006 1 3.404

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.006 m3/sg 9.81 m/seg2 60 1.524 V 3.165 m/s

otros 72 1.8288 hf 3.404 mE 0.001 hm 46.596 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°7-CAMARA ROMPE PRESION N°8 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR7 3594 CODO 0.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR8 3544 UNION 5.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 7.33Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 320 m 2 0.0508 50 2 3.057 46.508 0.002 0.006 1 3.492Ks 0.0000015 m 2.5 0.0635 50 2 3.057 46.508 0.002 0.006 1 3.492d 0.0508 m C-7,5 3 0.0762 46.508 2 2.937 46.777 0.002 0.006 1 3.223PERDIDAS POR ACCESORIOS 4 0.1016 46.777 2 2.946 46.756 0.002 0.006 1 3.244

Km 7.33 6 0.1524 46.756 2 2.945 46.758 0.002 0.006 1 3.242CARACTERISTICAS DEL FLUIDO 8 0.2032 46.758 2 2.945 46.758 0.002 0.006 1 3.242ρ 998.2 Kg/m3 10 0.254 46.758 2 2.945 46.758 0.002 0.006 1 3.242μ 0.001005 Pa.s 12 0.3048 46.758 2 2.945 46.758 0.002 0.006 1 3.242ν 0.000001007 m2/seg 14 0.3556 46.758 2 2.945 46.758 0.002 0.006 1 3.242CARACTERIATICAS DEL FLUJO 18 0.4572 46.758 2 2.945 46.758 0.002 0.006 1 3.242

Qd 0.005 m3/seg 24 0.6096 46.758 2 2.945 46.758 0.002 0.006 1 3.242CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.758 2 2.945 46.758 0.002 0.006 1 3.242

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.006 m3/sg 9.81 m/seg2 60 1.524 V 2.945 m/s

otros 72 1.8288 hf 3.242 mE 0.001 hm 46.758 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°6-CAMARA ROMPE PRESION N°7 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR6 3644 (1)CODO 0.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR7 3594 UNION 4.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 6.33Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 260 m 2 0.0508 50 2 3.428 46.207 0.002 0.007 1 3.793Ks 0.0000015 m 2.5 0.0635 50 2 3.428 46.207 0.002 0.007 1 3.793d 0.0508 m C-7,5 3 0.0762 46.207 2 3.282 46.523 0.002 0.007 1 3.477PERDIDAS POR ACCESORIOS 4 0.1016 46.523 2 3.294 46.497 0.002 0.007 1 3.503

Km 6.33 6 0.1524 46.497 2 3.293 46.499 0.002 0.007 1 3.501CARACTERISTICAS DEL FLUIDO 8 0.2032 46.499 2 3.293 46.499 0.002 0.007 1 3.501ρ 998.2 Kg/m3 10 0.254 46.499 2 3.293 46.499 0.002 0.007 1 3.501μ 0.001005 Pa.s 12 0.3048 46.499 2 3.293 46.499 0.002 0.007 1 3.501ν 0.000001007 m2/seg 14 0.3556 46.499 2 3.293 46.499 0.002 0.007 1 3.501CARACTERIATICAS DEL FLUJO 18 0.4572 46.499 2 3.293 46.499 0.002 0.007 1 3.501

Qd 0.005 m3/seg 24 0.6096 46.499 2 3.293 46.499 0.002 0.007 1 3.501CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.499 2 3.293 46.499 0.002 0.007 1 3.501

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.007 m3/sg 9.81 m/seg2 60 1.524 V 3.293 m/s

otros 72 1.8288 hf 3.501 mE 0.001 hm 46.499 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°5-CAMARA ROMPE PRESION N°6 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR5 3694 (1)CODO 0.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR6 3644 UNION 4.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 6.33Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 260 m 2 0.0508 50 2 3.428 46.207 0.002 0.007 1 3.793Ks 0.0000015 m 2.5 0.0635 50 2 3.428 46.207 0.002 0.007 1 3.793d 0.0508 m C-7,5 3 0.0762 46.207 2 3.282 46.523 0.002 0.007 1 3.477PERDIDAS POR ACCESORIOS 4 0.1016 46.523 2 3.294 46.497 0.002 0.007 1 3.503

Km 6.33 6 0.1524 46.497 2 3.293 46.499 0.002 0.007 1 3.501CARACTERISTICAS DEL FLUIDO 8 0.2032 46.499 2 3.293 46.499 0.002 0.007 1 3.501ρ 998.2 Kg/m3 10 0.254 46.499 2 3.293 46.499 0.002 0.007 1 3.501μ 0.001005 Pa.s 12 0.3048 46.499 2 3.293 46.499 0.002 0.007 1 3.501ν 0.000001007 m2/seg 14 0.3556 46.499 2 3.293 46.499 0.002 0.007 1 3.501CARACTERIATICAS DEL FLUJO 18 0.4572 46.499 2 3.293 46.499 0.002 0.007 1 3.501

Qd 0.005 m3/seg 24 0.6096 46.499 2 3.293 46.499 0.002 0.007 1 3.501CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.499 2 3.293 46.499 0.002 0.007 1 3.501

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.007 m3/sg 9.81 m/seg2 60 1.524 V 3.293 m/s

otros 72 1.8288 hf 3.501 mE 0.001 hm 46.499 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°4-CAMARA ROMPE PRESION N°5 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR4 3744 CODO 3

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR5 3694 UNION 6.7Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 11.17Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 400 m 2 0.0508 50 2 2.702 45.846 0.002 0.005 1 4.154Ks 0.0000015 m 2.5 0.0635 50 2 2.702 45.846 0.002 0.005 1 4.154d 0.0508 m C-7,5 3 0.0762 45.846 2 2.575 46.227 0.002 0.005 1 3.773PERDIDAS POR ACCESORIOS 4 0.1016 46.227 2 2.587 46.192 0.002 0.005 1 3.808

Km 11.17 6 0.1524 46.192 2 2.586 46.195 0.002 0.005 1 3.805CARACTERISTICAS DEL FLUIDO 8 0.2032 46.195 2 2.586 46.195 0.002 0.005 1 3.805ρ 998.2 Kg/m3 10 0.254 46.195 2 2.586 46.195 0.002 0.005 1 3.805μ 0.001005 Pa.s 12 0.3048 46.195 2 2.586 46.195 0.002 0.005 1 3.805ν 0.000001007 m2/seg 14 0.3556 46.195 2 2.586 46.195 0.002 0.005 1 3.805CARACTERIATICAS DEL FLUJO 18 0.4572 46.195 2 2.586 46.195 0.002 0.005 1 3.805

Qd 0.005 m3/seg 24 0.6096 46.195 2 2.586 46.195 0.002 0.005 1 3.805CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.195 2 2.586 46.195 0.002 0.005 1 3.805

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.005 m3/sg 9.81 m/seg2 60 1.524 V 2.586 m/s

otros 72 1.8288 hf 3.805 mE 0.001 hm 46.195 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°3-CAMARA ROMPE PRESION N°4 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR3 3794 CODO 5.5

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR4 3744 UNION 17.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 24.33Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 1040 m 2 0.0508 50 2.5 1.846 45.772 0.003 0.006 1 4.228Ks 0.0000015 m 2.5 0.0635 50 2.5 1.846 45.772 0.003 0.006 1 4.228d 0.0508 m C-7,5 3 0.0762 45.772 2.5 1.758 46.167 0.003 0.006 1 3.833PERDIDAS POR ACCESORIOS 4 0.1016 46.167 2.5 1.766 46.131 0.003 0.006 1 3.869

Km 24.33 6 0.1524 46.131 2.5 1.766 46.134 0.003 0.006 1 3.866CARACTERISTICAS DEL FLUIDO 8 0.2032 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866ρ 998.2 Kg/m3 10 0.254 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866μ 0.001005 Pa.s 12 0.3048 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866ν 0.000001007 m2/seg 14 0.3556 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866CARACTERIATICAS DEL FLUJO 18 0.4572 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866

Qd 0.005 m3/seg 24 0.6096 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.134 2.5 1.766 46.134 0.003 0.006 1 3.866

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.006 m3/sg 9.81 m/seg2 60 1.524 V 1.766 m/s

otros 72 1.8288 hf 3.866 mE 0.001 hm 46.134 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°2-CAMARA ROMPE PRESION N°3 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR2 3844 CODO 8

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR3 3794 UNION 15.0Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 24.50Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 900 m 2 0.0508 50 2.5 2.001 45.002 0.003 0.006 1 4.998Ks 0.0000015 m 2.5 0.0635 50 2.5 2.001 45.002 0.003 0.006 1 4.998d 0.0508 m C-7,5 3 0.0762 45.002 2.5 1.887 45.553 0.003 0.006 1 4.447PERDIDAS POR ACCESORIOS 4 0.1016 45.553 2.5 1.900 45.493 0.003 0.006 1 4.507

Km 24.50 6 0.1524 45.493 2.5 1.898 45.499 0.003 0.006 1 4.501CARACTERISTICAS DEL FLUIDO 8 0.2032 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501ρ 998.2 Kg/m3 10 0.254 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501μ 0.001005 Pa.s 12 0.3048 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501ν 0.000001007 m2/seg 14 0.3556 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501CARACTERIATICAS DEL FLUJO 18 0.4572 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501

Qd 0.005 m3/seg 24 0.6096 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501CARACTERISTICAS TOPOGRAFICAS 30 0.762 45.499 2.5 1.899 45.499 0.003 0.006 1 4.501

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.006 m3/sg 9.81 m/seg2 60 1.524 V 1.899 m/s

otros 72 1.8288 hf 4.501 mE 0.001 hm 45.499 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAMARA ROMPE PRESION N°1-CAMARA ROMPE PRESION N°2 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s CR1 3894 CODO 2

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR2 3844 UNION 10.3Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 13.83Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 620 m 2 0.0508 50 2.5 2.459 45.735 0.003 0.008 1 4.265Ks 0.0000015 m 2.5 0.0635 50 2.5 2.459 45.735 0.003 0.008 1 4.265d 0.0508 m C-7,5 3 0.0762 45.735 2.5 2.341 46.136 0.003 0.007 1 3.864PERDIDAS POR ACCESORIOS 4 0.1016 46.136 2.5 2.352 46.098 0.003 0.007 1 3.902

Km 13.83 6 0.1524 46.098 2.5 2.351 46.102 0.003 0.007 1 3.898CARACTERISTICAS DEL FLUIDO 8 0.2032 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898ρ 998.2 Kg/m3 10 0.254 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898μ 0.001005 Pa.s 12 0.3048 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898ν 0.000001007 m2/seg 14 0.3556 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898CARACTERIATICAS DEL FLUJO 18 0.4572 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898

Qd 0.005 m3/seg 24 0.6096 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.102 2.5 2.351 46.102 0.003 0.007 1 3.898

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.007 m3/sg 9.81 m/seg2 60 1.524 V 2.351 m/s

otros 72 1.8288 hf 3.898 mE 0.001 hm 46.102 m

Q≥Qd

DISEÑO DE LA LINEA DE CONDUCCION CAPTACION -CAMARA ROMPE PRESION N°1 PERDIDAS LOCALES

Q nueva union 0.3 l/s ENTRADA 0.5Q cora cora 0.25 l/s COTA-CAP 3944 CODOS 1

Qmacachacra 1.0 l/s Qmd=Qm*Cvd CR1 3894 UNION 12.7Qantarumi 0.6 l/s cvd= 1.3 ∆H 50 SALIDA 1

Qvilla florida 1.2 l/s ∑Km 15.17Qmosoccllacta 0.2 l/s

Qm 2.55 l/sQmd 5 l/s DISEÑO DE TUBERIAS SIMPLES RESULTADOS

DATOS DIAMETROS H Ø v hf+1 A Q ∑hmCARACTERISTICAS DE LA TUBERIA Ø (PULG) m (m) (m) (m/s) (m) (m2) (m3/Seg) (si ó no) (m)

L 760 m 2 0.0508 50 2.5 2.197 46.268 0.003 0.007 1 3.732Ks 0.0000015 m 2.5 0.0635 50 2.5 2.197 46.268 0.003 0.007 1 3.732d 0.0508 m C-7,5 3 0.0762 46.268 2.5 2.105 46.575 0.003 0.007 1 3.425PERDIDAS POR ACCESORIOS 4 0.1016 46.575 2.5 2.113 46.550 0.003 0.007 1 3.450

Km 15.17 6 0.1524 46.550 2.5 2.112 46.552 0.003 0.007 1 3.448CARACTERISTICAS DEL FLUIDO 8 0.2032 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448ρ 998.2 Kg/m3 10 0.254 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448μ 0.001005 Pa.s 12 0.3048 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448ν 0.000001007 m2/seg 14 0.3556 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448CARACTERIATICAS DEL FLUJO 18 0.4572 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448

Qd 0.005 m3/seg 24 0.6096 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448CARACTERISTICAS TOPOGRAFICAS 30 0.762 46.552 2.5 2.112 46.552 0.003 0.007 1 3.448

H 50 m 36 0.9144Z 0 m 42 1.0668 resultados

GRAVEDAD 48 1.2192 Q 0.007 m3/sg 9.81 m/seg2 60 1.524 V 2.112 m/s

otros 72 1.8288 hf 3.448 mE 0.001 hm 46.552 m

Q≥Qd