1. P1
Ø:
6
in
L:
1
m
Flow:
70.67
m³/h
Vel:
1.053
m/s
HL:
7.061E-03
m
DP02
Ø: 4 in
L: 60 m
Flow: 70.67 m³/h
Vel: 2.39 m/s
HL: 3.117 m
DP1
Ø: 2 in
L: 0.6 m
Flow: 70.67 m³/h
Vel: 9.068 m/s
HL: 1.703 m
DP3
Ø:
2
in
L:
0.6
m
Flow:
70.67
m³/h
Vel:
9.068
m/s
HL:
1.703
m
P02
Ø:
4
in
L:
73
m
Flow:
70.67
m³/h
Vel:
2.39
m/s
HL:
3.792
m
DP4
Ø: 2 in
L: 0.6 m
Flow: 70.67 m³/h
Vel: 9.068 m/s
HL: 1.703 m
P01
TH:
51.33
m
P
Total:
0.5008
bar
g
AMBIENTE
El: 3 m
Set P: 0 bar g
Level: 0 m
POZO
El: -70 m
Set P: 0 bar g
Level: 37 m
CV2
dP Total: 0.2964 bar
Choked Flow: 160.9 m³/h
Curve dP Device 1
dP Total: 0.0265 bar
P Total: 1.324 bar g
02 prueba de pozo.pipe
bar
Lineup:
m Power:
<Design Case>
bar a
Program Version:
Maximum Iterations:
File Name:
Velocity:
Drawn by:
Density:
in
Flow rate:
cP
Company:
Calculation Method:
Elevation:
kg/m³
m³/h
0.01
16.1.44900
Project Information
Viscosity:
2100
0.9793
m/s
m
Thursday, December 09, 2021 06:16 PM
PIPE-FLO Professional
Print Date:
Temperature:
Size:
Project:
Laminar Cutoff Re:
Atmospheric Pressure:
Pressure:
°C
Units
100 hp
Hazen-Williams
Percent Tolerance:
Length:
h*ft²°F/BTU
BTU/h
Thermal Capacitance:
Thermal Insulance:
Heat Transfer Coefficient:
BTU/lb°F
Specific Heat Capacity:
Area: ft²
BTU/h°F
Heat Transfer Rate:
BTU/h*ft²°F
Allowable Deviation: 1 %
%
