Bombas
description
Transcript of Bombas
![Page 1: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/1.jpg)
Datoslongitud altura (m) 12
Area Transversal Tuberia (m2) 0.254Temperatura (º C) 25Densidad (kg/m3) 1000
Viscosidad (kg/m x s) 0.001Material Tuberia Acero
Longitud (m) 84.6Caudal (m3/seg) 0.006
Diametro (m) 0.254Velocidad (m/seg) 0.11
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.006
Perdida de carga (m) 0.006factor f 0.027
Longitud (m) 84.6Diametro (m) 0.254
Velocidad (m/seg) 0.012Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.423factor f 0.027
Longitud equivalente (m) 6456
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 2: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/2.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.012
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt 1391.0altura ultil 25.4
Peso especifico (kg/m2 x seg2) 9810.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 84.6
Velocidad (m/s) 0.0121coeficiente friccion (f) 0.027
Gravedad especifica (kg/m3) 1Caida de Presion (pa) 0.054
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 3: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/3.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 18 210 3780Valvula (4") Compuerta 16 90 1440
Codo (10") 27 18 486Codo (4") 48 7 336Cruz (10") 0Cruz (4") 0Tee (10") 16 18 288Tee (4") 18 7 126
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 6456
(10") 0.002(4") 0.004
RE 27940.0
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.012 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.006Perdida de Carga secundaria 0.423Perdida por estrechamiento 0.000
Perdida total 0.429
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 4: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/4.jpg)
∆Z Altura bombeo(m) 12∆P Presion mcnm (pa) 117720 6.17E-04∆P Veloidad (m/seg) 0.012 1.20E+01
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 9810.0
Altura util (m) 2.54E+01Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt 1636.46 W a CVRendimiento (%) 0.85 1636.46
Potencia Neta (J/seg) = watt 1391.00
Gravedad Especifica (kg/m3) 1 Densidad (kg/m3)Densidad Absoluta (kg/m3) 1000 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 5: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/5.jpg)
0.00227940.0
0.8235.1
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2× )𝑔+ _𝑃 2/ + _𝛾 ℎ 𝑇ℎ_ =∆ ×(∆ ^2)/(2× )+∆ /𝑢 𝑍 𝑉 𝑔 𝑃 𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 6: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/6.jpg)
2.23735
10009.8112
117720
![Page 7: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/7.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2× )𝑔+ _𝑃 2/ + _𝛾 ℎ 𝑇ℎ_ =∆ ×(∆ ^2)/(2× )+∆ /𝑢 𝑍 𝑉 𝑔 𝑃 𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 8: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/8.jpg)
![Page 9: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/9.jpg)
![Page 10: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/10.jpg)
![Page 11: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/11.jpg)
Datoslongitud altura (m) 0.84
Area Transversal Tuberia (m2) 0.254Temperatura (º C) 25Densidad (kg/m3) 1225
Viscosidad (kg/m x s) 0.017Material Tuberia Acero
Longitud (m) 21.356Caudal (m3/seg) 0.002
Diametro (m) 0.254Velocidad (m/seg) 0.03
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.002
Perdida de carga (m) 0.00factor f 0.4
Longitud (m) 21.356Diametro (m) 0.254
Velocidad (m/seg) 0.001Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.108factor f 0.4
Longitud equivalente (m) 1494
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 12: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/12.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.001
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt 57.0altura ultil 3.1
Peso especifico (kg/m2 x seg2) 12017.3Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 21.356
Velocidad (m/s) 0.0009coeficiente friccion (f) 0.4
Gravedad especifica (kg/m3) 1.225Caida de Presion (pa) 0.019
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 13: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/13.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 6 210 1260Valvula (4") Compuerta 90 0
Codo (10") 10 18 180Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 3 18 54Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1494
(10") 0.002(4") 0.004
RE 549.1
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.001 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.002Perdida de Carga secundaria 0.108Perdida por estrechamiento 0.000
Perdida total 0.109
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 14: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/14.jpg)
∆Z Altura bombeo(m) 0.84∆P Presion mcnm (pa) 10094.49 4.59E-05∆P Veloidad (m/seg) 0.001 8.40E-01
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 12017.3
Altura util (m) 3.12E+00Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt 67.05 W a CVRendimiento (%) 0.85 67.05
Potencia Neta (J/seg) = watt 56.99
Gravedad Especifica (kg/m3) 1.225 Densidad (kg/m3)Densidad Absoluta (kg/m3) 1225 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 15: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/15.jpg)
0.117549.1
0.4392.7
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 16: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/16.jpg)
0.09735
12259.810.84
10094.49
![Page 17: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/17.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 18: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/18.jpg)
![Page 19: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/19.jpg)
![Page 20: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/20.jpg)
![Page 21: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/21.jpg)
Datoslongitud altura (m) 2
Area Transversal Tuberia (m2) 0.051Temperatura (º C) 25Densidad (kg/m3) 1256
Viscosidad (kg/m x s) 0.001Material Tuberia Acero
Longitud (m) 8.54Caudal (m3/seg) 0.004
Diametro (m) 0.254Velocidad (m/seg) 0.08
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.004
Perdida de carga (m) 0.00factor f 0.027
Longitud (m) 8.54Diametro (m) 0.254
Velocidad (m/seg) 0.006Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.035factor f 0.027
Longitud equivalente (m) 1002
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 22: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/22.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.006
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt 271.7altura ultil 5.4
Peso especifico (kg/m2 x seg2) 12321.4Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 8.54
Velocidad (m/s) 0.0064coeficiente friccion (f) 0.027
Gravedad especifica (kg/m3) 1.256Caida de Presion (pa) 0.004
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 23: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/23.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 4 210 840Valvula (4") Compuerta 90 0
Codo (10") 7 18 126Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 2 18 36Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1002
(10") 0.002(4") 0.004
RE 25521.9
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.006 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.035Perdida por estrechamiento 0.000
Perdida total 0.035
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 24: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/24.jpg)
∆Z Altura bombeo(m) 2∆P Presion mcnm (pa) 24642.72 3.26E-04∆P Veloidad (m/seg) 0.006 2.00E+00
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 12321.4
Altura util (m) 5.44E+00Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt 319.64 W a CVRendimiento (%) 0.85 319.64
Potencia Neta (J/seg) = watt 271.69
Gravedad Especifica (kg/m3) 1.256 Densidad (kg/m3)Densidad Absoluta (kg/m3) 1256 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 25: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/25.jpg)
0.00325521.9
0.8115.1
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 26: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/26.jpg)
0.43735
12569.81
224642.72
![Page 27: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/27.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 28: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/28.jpg)
![Page 29: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/29.jpg)
![Page 30: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/30.jpg)
![Page 31: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/31.jpg)
Datoslongitud altura (m) 2
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.002
Diametro (m) 0.254Velocidad (m/seg) 0.04
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.002
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.002Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 1056
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 32: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/32.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.002
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0.0016coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 33: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/33.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 4 210 840Valvula (4") Compuerta 90 0
Codo (10") 10 18 180Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 2 18 36Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1056
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.002 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 34: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/34.jpg)
∆Z Altura bombeo(m) 2∆P Presion mcnm (pa) 0 8.15E-05∆P Veloidad (m/seg) 0.002 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 35: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/35.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 36: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/36.jpg)
#DIV/0!735
09.81
20
![Page 37: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/37.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 38: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/38.jpg)
![Page 39: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/39.jpg)
![Page 40: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/40.jpg)
![Page 41: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/41.jpg)
Datoslongitud altura (m) 2
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.002
Diametro (m) 0.254Velocidad (m/seg) 0.04
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.002
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.002Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 1056
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 42: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/42.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.002
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0.0016coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 43: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/43.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 4 210 840Valvula (4") Compuerta 90 0
Codo (10") 10 18 180Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 2 18 36Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1056
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.002 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 44: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/44.jpg)
∆Z Altura bombeo(m) 2∆P Presion mcnm (pa) 0 8.15E-05∆P Veloidad (m/seg) 0.002 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 45: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/45.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 46: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/46.jpg)
#DIV/0!735
09.81
20
![Page 47: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/47.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 48: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/48.jpg)
![Page 49: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/49.jpg)
![Page 50: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/50.jpg)
![Page 51: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/51.jpg)
Datoslongitud altura (m) 2
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.002
Diametro (m) 0.254Velocidad (m/seg) 0.04
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.002
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.002Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 1056
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 52: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/52.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.002
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0.0016coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 53: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/53.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 4 210 840Valvula (4") Compuerta 90 0
Codo (10") 10 18 180Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 2 18 36Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1056
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.002 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 54: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/54.jpg)
∆Z Altura bombeo(m) 2∆P Presion mcnm (pa) 0 8.15E-05∆P Veloidad (m/seg) 0.002 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 55: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/55.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 56: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/56.jpg)
#DIV/0!735
09.81
20
![Page 57: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/57.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 58: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/58.jpg)
![Page 59: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/59.jpg)
![Page 60: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/60.jpg)
![Page 61: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/61.jpg)
Datoslongitud altura (m) 2
Area Transversal Tuberia (m2) 0.051Temperatura (º C) 50Densidad (kg/m3) 1002
Viscosidad (kg/m x s) 0.002Material Tuberia Acero
Longitud (m) 36.25Caudal (m3/seg) 0.003
Diametro (m) 0.254Velocidad (m/seg) 0.06
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.003
Perdida de carga (m) 0.00factor f 0.034
Longitud (m) 36.25Diametro (m) 0.254
Velocidad (m/seg) 0.004Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.031factor f 0.034
Longitud equivalente (m) 1248
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 62: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/62.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.004
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt 162.6altura ultil 5.4
Peso especifico (kg/m2 x seg2) 9829.6Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 36.25
Velocidad (m/s) 0.0036coeficiente friccion (f) 0.034
Gravedad especifica (kg/m3) 1.002Caida de Presion (pa) 0.009
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 63: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/63.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 5 210 1050Valvula (4") Compuerta 90 0
Codo (10") 9 18 162Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 2 18 36Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 1248
(10") 0.002(4") 0.004
RE 7635.2
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.004 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.001Perdida de Carga secundaria 0.031Perdida por estrechamiento 0.000
Perdida total 0.032
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 64: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/64.jpg)
∆Z Altura bombeo(m) 2∆P Presion mcnm (pa) 19659.24 1.83E-04∆P Veloidad (m/seg) 0.004 2.00E+00
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 9829.6
Altura util (m) 5.44E+00Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt 191.25 W a CVRendimiento (%) 0.85 191.25
Potencia Neta (J/seg) = watt 162.57
Gravedad Especifica (kg/m3) 1.002 Densidad (kg/m3)Densidad Absoluta (kg/m3) 1002 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 65: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/65.jpg)
0.0087635.2
0.6694.2
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 66: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/66.jpg)
0.26735
10029.81
219659.24
![Page 67: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/67.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 68: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/68.jpg)
![Page 69: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/69.jpg)
![Page 70: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/70.jpg)
![Page 71: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/71.jpg)
Datoslongitud altura (m)
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.000
Diametro (m) 0.254Velocidad (m/seg)
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.000
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.000Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 0
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 72: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/72.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.000
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 73: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/73.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 210 0Valvula (4") Compuerta 90 0
Codo (10") 18 0Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 18 0Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 0
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.000 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 74: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/74.jpg)
∆Z Altura bombeo(m) 0∆P Presion mcnm (pa) 0 0.00E+00∆P Veloidad (m/seg) 0.000 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 75: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/75.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 76: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/76.jpg)
#DIV/0!735
09.81
00
![Page 77: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/77.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 78: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/78.jpg)
![Page 79: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/79.jpg)
![Page 80: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/80.jpg)
![Page 81: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/81.jpg)
Datoslongitud altura (m)
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.000
Diametro (m) 0.254Velocidad (m/seg)
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.000
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.000Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 0
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 82: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/82.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.000
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 83: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/83.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 210 0Valvula (4") Compuerta 90 0
Codo (10") 18 0Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 18 0Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 0
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.000 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 84: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/84.jpg)
∆Z Altura bombeo(m) 0∆P Presion mcnm (pa) 0 0.00E+00∆P Veloidad (m/seg) 0.000 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 85: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/85.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 86: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/86.jpg)
#DIV/0!735
09.81
00
![Page 87: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/87.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 88: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/88.jpg)
![Page 89: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/89.jpg)
![Page 90: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/90.jpg)
![Page 91: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/91.jpg)
Datoslongitud altura (m)
Area Transversal Tuberia (m2) 0.051Temperatura (º C)Densidad (kg/m3)
Viscosidad (kg/m x s)Material Tuberia Acero
Longitud (m)Caudal (m3/seg) 0.000
Diametro (m) 0.254Velocidad (m/seg)
pulg a m 0.25410 0.0254
Area Transversal Tuberia (m2) 0.0513.142 4
Caudal (m3/seg) 0.000
Perdida de carga (m) 0.00factor f
Longitud (m) 0Diametro (m) 0.254
Velocidad (m/seg) 0.000Gravedad (m/seg2) 19.62
Perdida de carga (m) 0.000factor f
Longitud equivalente (m) 0
𝐶𝑎𝑢𝑑𝑎𝑙 →𝑄=𝑣×𝐴 𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑝𝑟𝑖𝑚𝑎𝑟𝑖𝑎 →ℎ_𝐴=𝑓×(𝐿/𝐷)×(𝑉)^2/(2×𝑔) 𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑑𝑒 𝐶𝑎𝑟𝑔𝑎 𝑎𝑐𝑐𝑒𝑠𝑜𝑟𝑖𝑜𝑠→ℎ_𝑐=𝑓×((∑▒𝐿_𝑒𝑞 )/𝐷)×(𝑉)^2/(2×𝑔)𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
![Page 92: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/92.jpg)
Diametro (m) 0.254Velocidad (m/seg) 0.000
Gravedad (m/seg2) 19.62
Potencia neta (J/seg) = watt #DIV/0!altura ultil #DIV/0!
Peso especifico (kg/m2 x seg2) 0.0Caudal (m3/seg) 0.0
Diametro Tuberia (m) 0.508Longitud Tuberia (m) 0
Velocidad (m/s) 0coeficiente friccion (f) 0
Gravedad especifica (kg/m3) 0Caida de Presion (pa) 0.000
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑛𝑒𝑡𝑎→𝑃_𝑛=ℎ_𝐴×𝛾×𝑄
𝑃𝑜𝑡𝑒𝑛𝑐𝑖𝑎 𝑏𝑟𝑢𝑡𝑎→𝑃_𝑏=𝑝_𝑛/𝑅𝑒𝑛𝑑𝑖𝑚𝑖𝑒𝑛𝑡𝑜𝐶𝑎𝑖𝑑𝑎 𝑑𝑒 𝑝𝑟𝑒𝑠𝑖𝑜𝑛 ∆𝑝=(𝑆𝐺 × 𝑓 × 𝐿 × (𝑉)^2)/(2×𝑑)
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 93: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/93.jpg)
Accesorios Cantidad Leq (m) TotalValvula (10") Compuerta 210 0Valvula (4") Compuerta 90 0
Codo (10") 18 0Codo (4") 7 0Cruz (10") 0Cruz (4") 0Tee (10") 18 0Tee (4") 7 0
Reductor (10" a 4") 0Reductor (4" a 2") 0
Codo Especial 0Tee Especial 0
Suma (m) 0
(10") 0.002(4") 0.004
RE #DIV/0!
f64
Perdida estrechamiento (m) 0.0000Velocidad (m/seg) 0.000 f
Gravedad (m/seg2) 19.62 0.16Constante (K)
Perdida de Carga primaria 0.000Perdida de Carga secundaria 0.000Perdida por estrechamiento 0.000
Perdida total 0.000
𝑁` 𝑅𝑒𝑦𝑛𝑜𝑙𝑑𝑠 →𝑅𝐸=(𝑣×𝜌×𝐷)/𝜇𝑃𝑒𝑟𝑑𝑖𝑑𝑎 𝑒𝑠𝑡𝑟𝑒𝑐ℎ𝑎𝑚𝑖𝑒𝑛𝑡𝑜 →ℎ_𝐵=𝑘×(𝑣^2/(2×𝑔))
𝑆𝑢𝑚𝑎 𝑑𝑒 𝐴𝑙𝑡𝑢𝑟𝑎 𝑡𝑜𝑡𝑎𝑙𝑒𝑠→ℎ_𝑇=ℎ_𝐴+ℎ_𝐵+ℎ_𝑐
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
CALCULO BOMBAS CENTRIFUGA DE EMPRESA ACITROVEN.S.A
Rugosidad Relativa ACERO = 𝑒∕𝐷
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 94: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/94.jpg)
∆Z Altura bombeo(m) 0∆P Presion mcnm (pa) 0 0.00E+00∆P Veloidad (m/seg) 0.000 #DIV/0!
Gravedad 19.62Peso espcifico (kg/m2 x seg2) 0.0
Altura util (m) #DIV/0!Perdida total (m) 1.44
Potencia Bruta (J/seg) = watt #DIV/0! W a CVRendimiento (%) 0.85 #DIV/0!
Potencia Neta (J/seg) = watt #DIV/0!
Gravedad Especifica (kg/m3) 0 Densidad (kg/m3)Densidad Absoluta (kg/m3) 0 Gravedad (m/seg2)
Densidad referencia (kg/m3) 1000 Altura (m)Presion (pa)
𝑎𝑙𝑡𝑢𝑟𝑎 𝑢𝑡𝑖𝑙→ℎ_𝑢=∆𝑍+(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾+ℎ_𝑇
𝐺𝑟𝑎𝑣𝑒𝑑𝑎𝑑 𝑒𝑠𝑝𝑒𝑐𝑖𝑓𝑖𝑐𝑎 𝜌_𝑟=𝜌/𝜌_𝑢
![Page 95: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/95.jpg)
#DIV/0!#DIV/0!
#DIV/0!#DIV/0!
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
Rugosidad Relativa ACERO = 𝑒∕𝐷PERDIDA DE CARGA TOTAL METODOS DE LONGITUD EQUIVALENTES DE
ECUACION DARCY FLUJO LAMINAR
flujo laminar →𝑓=64/𝑅𝐸
Formula emperica →𝑓=0,16〖 〗𝑅𝐸 ^(−0,16)
![Page 96: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/96.jpg)
#DIV/0!735
09.81
00
![Page 97: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/97.jpg)
𝐸𝑐𝑢𝑎𝑐𝑖𝑜𝑛 𝑑𝑒 𝐵𝐸𝑅𝑀𝑂𝑈𝐼𝐿𝐿𝐼𝑍_1+ 〖𝑉 _1〗^2/(2×𝑔)+𝑃_1/𝛾+ℎ_𝐴=𝑍_2+〖𝑉 _2〗 ^2/(2×𝑔)+𝑃_2/𝛾+ℎ_𝑇ℎ_𝑢=∆𝑍×(∆𝑉^2)/(2×𝑔)+∆𝑃/𝛾
METODOS DE LONGITUD EQUIVALENTES DE
![Page 98: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/98.jpg)
![Page 99: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/99.jpg)
![Page 100: Bombas](https://reader036.fdocuments.mx/reader036/viewer/2022062420/563db921550346aa9a9a5068/html5/thumbnails/100.jpg)