Cheers for all the advice on my PSV problem - it all makes a lot of good sense. One further question though - 121202 - you mention that you doubt if the TEG/water mix will vapourise at 40 bara before the vessel fails. I've used HYSYS 3.1 to predict the bubble/dew points of the TEG/water mix and...
I am attempting to size a relief valve for fire case vapour generation on a glycol contactor used for removing water from hydrocarbon gas in a compression train.
The principal problem lies with determination of the latent heat of the fluids in the base of the vessel - which are a mixture of...