Limiting flow, Pressure loss (si units), Pressure loss formulas for promass f, m, e – FMC Corporation - Talstar 80 Benutzerhandbuch

Seite 101: Pressure loss formulas for promass h, i, s, p

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Proline Promass 80 PROFIBUS PA

Technical data

101

Limiting flow

See the "Measuring range" section

→ Page 88 ff.

Select nominal diameter by optimizing between required flow range and permissible pressure loss.
See the "Measuring range" section for a list of max. possible full scale values.
• The minimum recommended full scale value is approx. 1/20 of the max. full scale value.
• In most applications, 20 to 50% of the maximum full scale value can be considered ideal.
• Select a lower full scale value for abrasive substances such as liquids with entrained solids (flow

velocity < 1 m/s (3 ft/s)).

• For gas measurement the following rules apply:

– Flow velocity in the measuring tubes should not be more than half the sonic velocity

(0.5 Mach).

– The maximum mass flow depends on the density of the gas: formula

→ Page 91

Pressure loss (SI units)

Pressure loss depends on the properties of the fluid and on its flow. The following formulas can be
used to approximately calculate the pressure loss:

Pressure loss formulas for Promass F, M, E

Pressure loss formulas for Promass H, I, S, P

Reynolds number

a0004623

Re

≥ 2300 *

a0004626

Re < 2300

a0004628

Δp = pressure loss [mbar]
ν = kinematic viscosity [m2/s]
g = mass flow [kg/s]

ρ = fluid density [kg/m3]
d = inside diameter of measuring tubes [m]
K to K2 = constants (depending on nominal diameter)

* To compute the pressure loss for gases, always use the formula for Re

≥ 2300.

Reynolds number

a0003381

Re

≥ 2300 *

a0004631

Re < 2300

a0004633

Δp = pressure loss [mbar]
ν = kinematic viscosity [m2/s]
g = mass flow [kg/s]

ρ = fluid density [kg/m3]
d = inside diameter of measuring tubes [m]
K to K3 = constants (depending on nominal diameter)

* To compute the pressure loss for gases, always use the formula for Re

≥ 2300.

Re =

2 ·

g

p

n r

· d · ·

D

r

p = K ·

·

·

0.25

1.85

–0.86

g

n

Dp = K1 · · +

g

n

K2 ·

·

0.25

2

g

n

r

Re = p

n r

· d · ·

4 ·

g

D

n

r

p = K ·

·

·

0.25

1.75

–0.75

g

K3 ·

g

2

r

+

Dp = K1 · ·

g

n

K3 ·

g

2

r

+

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