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Gas Vessel Blow Down Conditions

blowdown depressurization

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#1 raman123

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Posted 22 November 2017 - 12:57 PM

Hello,

 

I am a junior engineer and am doing some blowdown and depressurization calculations. I am a bit confused regarding initial conditions for fire case blowdown. I assume that pressure should be the design pressure. Should we take the corresponding temperature from ideal gas law for initial temperature. The vessel is gas filled only. What should be assumption of starting temperature. 

 

RS



#2 fallah

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Posted 22 November 2017 - 02:19 PM

RS,

 

The depressurization in case of fire starts at the temperature reached by the system due to the fire heat input which is calculated by relevant simulator while performing the simulation.


#3 runsaep

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Posted 06 February 2019 - 07:33 AM

What reflections have the members of cold blowdown of an oil/gas 1.st Stg separator with starting temperature minimum ambient of - 7 deg C , what important  issues do you have to be aware of ? Amongst others, fluid temperatures, wall temperature ?



#4 runsaep

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Posted 02 March 2019 - 07:55 AM

A blowdown simulator uses PSV nozzle API 521 equations for the orifice. Is the calculation of minimum temperature inside vessel (gas/liquid/wall) more conservative with nozzle equation than with "pure" orifice equations ? Can you share your thoughts of that ?






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