Blowdown Calc Formulae

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Sizing Calculations The sizing that can be done for a blowdown valve usually involves calculating either: The total time required to blowdown a fixed volume of gas from one pressure to another Calculating the valve flow coefficient (Cg) in order to blowdown a given volume in a fixed period Both of the calculations use the same formula it is just rearranged to solve for the required variable. The formulae are as follows: Calculations A. Critical Flow (P f > Pc) _____ C g = (93V/t) (G-TZ ) Ln (P i /P f ) V = actual enclosed volume of piping or vessel (ft 3 ) t = time to blowdown (min) G = specific gravity T = temperature degrees R (°F + 460) Z = compressibility factor P i = initial pressure (psia) P f = final pressure of enclosed volume Pc = pressure below which letdown to flare system is not sonic B. Subcritical Flow (P f < Pc) If P f < P c , the following equation for subcritical flow must be used in addition to the one above: __ _ __ C g = (3.133VC 1 ÷ t) (G-TZ ) Ln [(P c + P c - P a ) ÷ (P f + P f - P a )] V = actual volume (ft 3 ) t = time to blowdown (min) G = specific gravity T = temperature degrees R (°F + 460) P i = initial pressure (psia) P f = final pressure (psia) of enclosed volume P c = critical pressure (psia) P a = atmospheric pressure C 1 = valve Cg/Cv Critical pressure can be calculated by: Pc = P a / (1-(C1 / 59.64) 2 P a = atmospheric pressure C 1 = valve Cg/Cv

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Blowdown Calculations

Transcript of Blowdown Calc Formulae

Page 1: Blowdown Calc Formulae

Sizing Calculations The sizing that can be done for a blowdown valve usually involves calculating either:

• The total time required to blowdown a fixed volume of gas from one pressure to another

• Calculating the valve flow coefficient (Cg) in order to blowdown a given volume in a fixed period

Both of the calculations use the same formula it is just rearranged to solve for the required variable. The formulae are as follows:

Calculations A. Critical Flow (Pf > Pc)

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Cg ==== (93V/t) (√√√√G-TZ ) Ln (Pi/Pf)

V = actual enclosed volume of piping or vessel (ft3)

t = time to blowdown (min) G = specific gravity T = temperature degrees R (°F + 460) Z = compressibility factor Pi = initial pressure (psia)

Pf = final pressure of enclosed volume

Pc = pressure below which letdown to flare system is not sonic B. Subcritical Flow (Pf < Pc)

If Pf < Pc, the following equation for subcritical flow must be used in addition to the one above:

__ _ __

Cg ==== (3.133VC1 ÷÷÷÷ t) (√√√√G-TZ ) Ln [(√√√√Pc + √√√√Pc - Pa) ÷÷÷÷ (√√√√Pf + √√√√Pf - Pa)]

V = actual volume (ft3)

t = time to blowdown (min) G = specific gravity T = temperature degrees R (°F + 460) Pi = initial pressure (psia)

Pf = final pressure (psia) of enclosed volume

Pc = critical pressure (psia)

Pa = atmospheric pressure

C1 = valve Cg/Cv

Critical pressure can be calculated by:

Pc = Pa / (1-(C1 / 59.64)2

Pa = atmospheric pressure

C1 = valve Cg/Cv