1. Introduction

6. NOMENCLATURE

d1

Diameter 1 = 50 mm = 0.05 m

d2

Diameter 2 = 32 mm = 0.032 m

Ef

Energy due to friction (µ).

G

Volumetric flow (m3/s).

g

Gravity (m/s2).

H

Height (m).

hF

Losses load.

m

Mass flow (kg/s).

P

Pressure (Pa).

P1

Pressure point 1 (bar).

P2

Pressure point 2 (bar).

S

Section perpendicular to the passage of fluid (cm).

u1

Linear velocity of the fluid at point 1 (m/s).

u2

Linear velocity of the fluid at point 2 (m/s).

Wmec

Mechanical energy.

ω

Angular velocity (rpm).

z

Height between the two manometers = 0.25 m.

ρ

Density of the fluid (kg/m3).

2. Theoretical foundations
3. Presentació de la planta
4. Experimental procedure
5. Test
6. Nomenclature
7. References

© UPC. Universitat Politécnica de Catalunya. EPSEM