Dear TD2K
Last time I asked a question in this forum the help was overwhelming. I was really suprised. I didn't realize the seriousness of my question until I read the responses.
You're right and thanks for your concern. I am not qualified to do this calculation but it has been given to me...
Hello
I have been charged with calculating rupture disc sizes.
I do not have access to the entire standard but I do have a formula.
A = [Q/(38*Kd*Kw*Kv)] * sqrt of [G/(P1-P2)]
A = Required discharge area
Kd = Effective coefficient of discharge
Kw = Correction for back pressure
P1 =...
My goodness. The response on this question has been overwhelming. I must apologise for the lack of information I have given to you all.
This was a problem my boss wanted me to do in a very crude manner. We were just wanting to know the many different scenarios that could result in flash/loss...
Thank you for your previous help.
Part 1
Is this equation correct?
Flash Ratio =
HL(into tank) - HL(of tank)
___________________________
HV(of tank) - HL(of tank)
HL = Enthalpy of sat.liquid
HV = Enthalpy of sat.vapor
into tank = flow of...
Hello, Quark. Who ever you are. Thanks alot.
I have just recently started my job as a chemical engineer. thing is I don't have any background. I majored in chemistry in university. I guess this was a an easy problem to solve.
This forum will be a big help to me.
I learn new things...
How does one go about doing this?
If I have a 1" pipe that is 50 meters long made out of stainless steel.
Its at ambient temp. Then you flow liquid O2 at -186 C through it. If it takes about 30 minutes to bring the pipe from ambient to operation temp of -186C. How do I calculate the...
