Dear all
I need to burn a flow gas of 100-1000 kg/h of 1,3 Butadiene. The upstream pressure of Vent pipe is 1-2 barg. I don’t know if I have to design an Incinerator , or a Flare! Any assistance? Do you guys have any documents?
Regards
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Posted 03 July 2016 - 07:06 AM
Dear all
I need to burn a flow gas of 100-1000 kg/h of 1,3 Butadiene. The upstream pressure of Vent pipe is 1-2 barg. I don’t know if I have to design an Incinerator , or a Flare! Any assistance? Do you guys have any documents?
Regards
Posted 03 July 2016 - 07:17 AM
Hi,
Why would you want to burn such component?!
Posted 03 July 2016 - 07:19 AM
Hi Naser,
In my plant , there are several Horizontal Storage Tanks of 1,3 Butadiene from which the Feed of Process is to be supplied. But during loading and unloading of these tanks , and even during popping up the tanks PSV’s , I have to burn the gas stream of this component.
What shall I do , If I don’t want to burn that?
Any recommendation?
Edited by process-man, 03 July 2016 - 07:24 AM.
Posted 03 July 2016 - 12:57 PM
You should add a condenser for routine operation. Sounds like this has been operating for some time. Don't ever burn anything if there is an alternative.
Bobby
Posted 03 July 2016 - 02:38 PM
Hi Naser,
In my plant , there are several Horizontal Storage Tanks of 1,3 Butadiene from which the Feed of Process is to be supplied. But during loading and unloading of these tanks , and even during popping up the tanks PSV’s , I have to burn the gas stream of this component.
What shall I do , If I don’t want to burn that?
Any recommendation?
Hi process-man,
I think 100-1000 kg/hr flow of 1,3 Butadiene is so high for which considering a VRU (vapor recovery unit) instead burning to be reasonable in economical and emission reduction standpoints...
Posted 03 July 2016 - 10:29 PM
http://www.ddbst.com...CP/VAP_C364.php
Normally Butadiene 1-3 should be stored under low temperature ( below 10C) to prevent pressure built up and release .
Check the data attached .
hope this helps.
Breizh
Edited by breizh, 03 July 2016 - 10:32 PM.
Posted 04 July 2016 - 12:20 AM
Edited by Dan Putt, 04 July 2016 - 08:06 AM.
Posted 04 July 2016 - 01:54 AM
To Fallah's point, assuming a 99% destruction efficiency in a flare, at the high end of your flow rate estimation, you would be emitting 22 lbs/hr of butadiene into the atmosphere. In the United States, a release of 10 lbs over a 24-hour period qualifies as a "reportable quantity," a significant release.
Can you please share a source or links?
Posted 04 July 2016 - 08:15 AM
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