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Rupture Disk Sizing

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Rupture Disk Sizing

Based on: API RP 520 Part 1 - Sizing and Selection of Pressure-Relieving Devices in Refineries, 2000 ed.

I. DESIGN DATA

Fluid service : Production steam


Unit service : Steam oulet from separator
Max. flow rate W = 638,231.70 lb/hr = 289.50 t/hr
Max. (design) temperature T = 415.40 oF = 213.00 oC
Max. pressure (MAWP)/setting pressure P = 295.88 psia = 20.40 bara
Back pressure PB = 14.50 psia = 1.00 bara
Relieving pressure = (1.1 x MAWP) + PB P1 = 355.92 psig = 24.54 barg

II. CALCULATION

Rupture disk sizing for steam service (US customary units)


calculated in accordance with equation below :

W , Eq. 01 (see para. 3.7.1)


A = 51.5 x P1 x KD KB KC KN KSH

where,
A = required effective discharge area, in2
W = required flow rate, lb/hr
P1 = upstream relieving pressure, psia.
This is the set pressure + the allowable overpressure plus the atmospheric pressure.
KD = effective coefficient of discharge (0.62 for Rupture Disc Devices).
KB = capacity correction factor due to back pressure (1 for conventional valves)
KC = combination correction factor for installations with a rupture disk upstream of the pressure relief valve (negligible)
KN = correction factor for Napier equation
= 1.0 where P1 ≤ 1500 psia
0.1906 P1 - 1000
=
0.2292 P1 -1061
KSH = superheat steam correction factor (1 for saturated steam at any pressure)
Minimum discharge area A = 56.16 in.2 = 36,231.93 mm2

Min. inlet diameter (ID) of rupture didk D= 8.46 in. = 207.17 mm


Min. inlet diameter (ID) of rupture didk (selected) D= 10.00 in. = 245.00 mm

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