Modeling Relief Valve (Pressure Safety Valve) Thrust force

Start-Prof can estimate the support loads and stresses caused by relief valve discharge by an equivalent static method.

The relief valve discharge thrust load acts on elbow 28. In Start-Prof it should be applied at the end of the elbow in node 29.

Download this piping model file. See how to open the piping model file

There’s two methods to estimate the dynamic equivalent thrust force F:

  • ASME B31.1 method
  • Direct calculation of V1 и P1 by special software like Hydrosystem

ASME B31.1 Method

Equivalent dynamic thrust force can be estimated by the equation:
F = DLF ∙ F1
where
DLF – dynamic load factor, depending on the first natural period of piping. If the period is unknown the DLF=2.0.

F1 – static reaction force, kgf. May be computed by the following equation:

where
W – mass flow rate (relieving capacity stamped on the valve by 1.11), kg/sec
gc=9.81 m/sec² – gravitational constant,
Pa – atmospheric pressure, kgf/sm²
A1 – exit flow area, sm²  A1=p(D-2t)²/4
V1 – exit velocity (node  36), m/sec

P1 – static pressure, kgf/sm²

h0 – stagnation enthalpy at the safety valve inletMJ/kg
J = 101970.408 m*kgf/MJ
a, b – constants according to the table below

Steam Condition a, MJ/kg b
Wet steam

<90% quality

0.6769 11
Saturated steam

≥90%  quality

1.05 kgf/sm² ≤ P1 ≤ 70.31 kgf/sm²

1.9143 4.33
Superheated steam

≥90%  quality

0.07 kgf/sm² ≤ P1 ≤ 140.61 kgf/sm²

1.93291 4.33

Example

Example project file: ReliefValve.ctp. See how to open the piping model file

Input data:

  • Diameter of discharge pipe: 21.9 sm

  • Wall thickness of discharge pipe: 1.6 sm

  • product: Saturated steam

  • relief valve relieving capacity: 48 kg/sec

  • Steam pressure: 64 kgf/sm²

  • Steam temperature: 538°C

Calculation:

A1=p(D-2t)²/4 = 3.14159(21.9-2∙1.6)²/4 = 274.65 sm²
a = 1,9143 MJ/kg
b = 4.33
W = 48∙1.11 = 53.28 kg/sec
stagnation enthalpy for steam at 70 kgf/sm² and 538°C h0 =  3,506 MJ/kg
P1=53.28/274.65*(4.33-1)/4.33*(2*(3.506-1.9143)*101970.408/(2*4.33-1)/9.81)^0.5 = 9.8 kgf/sm²
V(2*9.81*101970.408*(3.506-1.9143)/(2*4.33-1))^0.5 = 644.77 m/sec
F1 = 53.28*644.77/9.81 + (9.8-1)*274.65 = 5919 kgf
F = DLF ∙ F1 = 2*5919 = 11838 kgf

Create additional occasional force loading 1.1 in operation mode editor:

If we have more relief valves, then we should add more additional modes (1.2, 1.3, etc.) if it’s open not simultaneously.

Apply dynamic thrust force at node 29 for mode 1.1:

Support loads due to relief valve thrust load:

Stresses due to relief valve thrust load:

READ  Difference between Primary loads and Secondary loads in a Piping System

Alex Matveev

Alex Matveev is the head of the PASS/START-PROF pipe stress analysis software development team, which is developed since 1965. Also, He offers technical support and training for users of their software that number already 3000+, industry standard in several countries for 50+ years.

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