tablas

Tabla de Cons.y Caída de Pres.

Fórmula Dr. Poole
Caída de Presión
2.S.L.Q²
H=
D5

H= Pérdida de carga en Milímetros de Columna de Agua
S= Densidad del Gas (Natural 0,65)
L= Longitud deCañería
Q= Caudal en m³
D= Diámetro (en Cm)

Caida de presión por metro Lineal
Densidad

0.65

Metros
Comsumo
en m³/h
0.25
0.50
1.00
1.25
1.50
1.75
2.00
2.25
2.50
2.75
3.00
3.253.50
3.75
4.00
4.25
4.50
4.75
5.00
5.25
5.50
5.75
6.00
6.25
6.50
6.75
7.00
7.25
7.50
7.75
8.00
8.25
8.50
8.75
9.00
9.25
9.50
9.75
10.00
10.50
11.00
11.50
12.00
12.5013.00
13.50
14.00
14.50
15.00
15.50
16.00
16.50
17.00
17.50
18.00
18.50
19.00
19.50
20.00
20.50
21.00
21.50
22.00
22.50
23.00
23.50
24.00
24.50
25.00
25.50
26.00
26.50
27.0027.50
28.00
28.50
29.00
29.50
30.00

1
0.013
0.0219
0.0875
0.3501
0.5471
0.7878
1.0723
1.4005
1.7725
2.1883
2.6478
3.1512
3.6982
4.2891
4.9237
5.6020
6.3242
7.0901
7.89988.7532
9.6504
10.5914
11.5761
12.6046
13.6769
14.7929
15.9527
17.1563
18.4036
19.6947
21.0296
22.4082
23.8306
25.2967
26.8067
28.3604
29.9578
31.5990
33.2840
35.0128
38.6016
42.365546.3044
50.4184
54.7075
59.1716
63.8108
68.6250
73.6144
78.7788
84.1182
89.6327
95.3223
101.1869
107.2266
113.4414
119.8312
126.3961
133.1361
140.0511
147.1412
154.4064
161.8466169.4619
177.2522
185.2176
193.3581
201.6736
210.1642
218.8299
227.6706
236.6864
245.8772
255.2432
264.7841
274.5002
284.3913
294.4575
304.6987
315.1150

0.019
0.0033
0.01310.0525
0.0820
0.1181
0.1608
0.2100
0.2658
0.3281
0.3970
0.4725
0.5546
0.6431
0.7383
0.8400
0.9483
1.0632
1.1846
1.3125
1.4471
1.5882
1.7358
1.8901
2.0509
2.2182
2.3921
2.57262.7596
2.9532
3.1534
3.3601
3.5734
3.7933
4.0197
4.2527
4.4922
4.7383
4.9910
5.2502
5.7883
6.3527
6.9434
7.5603
8.2034
8.8728
9.5685
10.2904
11.0385
11.8129
12.6136
13.4405...