Mr. Montemayor,
I am sorry to cut in...
Thanks for differentiating....
My question here is there are installations where blowdown system was used and was replaced by flare at later stage. Is this change manly due to envirnoment point of view or are there some other technical issues involved.
I hasd the opportunity to see BP Texas refinery incident investigation on NATIONAL GEOGRAPHIC...there was a statement given that BP was using blowdown system and it was recommnded to be replaced by Flare system.This proposal was later dropped due to highy budgetry cost....
Also one supplementry question,
Do we have a stack in the blowdown system, if yes what is the purpose..
Thanks
binzee,
Blowdown system and flare system are totally different from operation, objective, function, limitation, etc although they are connected and have some degree of interaction between each and other. Please get a copy of API STD 521. There is explantion in it. For Blowdown, please look for "depressuring".
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My question here is there are installations where blowdown system was used and was replaced by flare at later stage. Is this change manly due to envirnoment point of view or are there some other technical issues involved.
Do you mind to elaborate a bit more about the "blowdown system" ? It is a vent system where release of gas from plant collected in a header and discharge to atmosphere without firing ?
Venting hydrocarbon without flaring may have at least the following impact :
i) Environment - From green house effect measurement, One mole of C1 equivalent to about 20 mole of CO2. Flaring one mole of C1 generate one mole of CO2
ii) Safety - Direct discharge hydrocarbon to atmosphere generate gas cloud. It is a big hazard once it get ignited e.g.lightning.
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Do we have a stack in the blowdown system, if yes what is the purpose..
I presumed your "Blowdowns system" is venting system...
To answer your qeustion, yes or no subject to dispersion of the vented components.
With direct venting, you have to ensure vented material is properly dispersed and the concentration of the component at the interested point (e.g. man reach area) and explosive limit (LEL) below the limit. One way to achieve this is to elevate the venting point by means of vent stack.
Hope this helps.