Folks.
Is there any available spreadsheet for the calculation of the sulfur recovery in a SRU , i am asking this because different results has been used from engineering compared to operation
Folks;
I am designing in aspen flare analyzer the flare network.
when setting the parameters of the Blowdown valves, I am supposed to set the back pressure @the valve.
Any idea how to calculated it?
is it based on the Maximum pressure of the system?
Folks;
While running aspen flare analyser, I am getting this mesage: nhv calculation failed because phase properties are not saved!
any thoughts to resolve?
Folks;
our current design on site we have a chemical injection pump operating at high pressure.
we are intend to add a second train operating at low pressure, same pumps will be used.
on this low P, a PVC (with PIT) is being presented in the design, OPs team has challenged the design , under...
Folks;
in the design of a plant, the compressor in equipped with suction scubber,at LL liquid level the ESD will close, however there is no liquid in the suction in normal operation.
how to fix this?
thx
Folks;
our engineering companie is proposing 2x 50% compressors configuration.
one is electrically driven and the second is through gas engine working in parallel.
from technical perspective anyone has an experience with this configuration and especially any expected drawbacks, potential...
Floks,
Our plant is designed with electrical and back up diesel pump.
According to NFPA 20 should we Connect the electrical one to UPS in addition to a national grid (reliable source) or only to the latest one (no need to UPS connection)
Regards
Folks
We have in our Plant two storage vessel of LPG.
one is filled and the other is a back up
from safety perspective is there any recommendation to avoid to have the second one is filled to avoid potential leaks,etc or is it safe to have both of them filled.
these two vessels are above...
folks;
is there any std, code, best practice which specify the fire extuiguishing selection of pool fire and jet fire.
as far as i know, the pool fire is supressed through spray water-foam system according to NFPA16
folks,
in NFPA is there any requirement for the minimum pressure inside the Fire water ring?
some companies specify 10 barg as operating P, but is it by std or norm?
folks;
is there any requirement to implement the interstage cooler of compressors based on discharge temperature?
according to the some reading, when exceeding 150 Deg we need intersatge one.
any reference to API, ASME??