Hello all forgive me for taking up your time but I'm struggling to move forward with a UG design project pertaining to the purification of H2 and in particular final drying stage to remove excess moisture prior to storage. Any help would be greatly appreciated.
The aim is to prepare H2 of purity in excess of 99.999% through a gas drying operation. The overall project is to assess the feasibility of using renewables (onshore wind turbines) to generate enough H2 to power a small community via combustion in fuel cells. The stream entering the drying unit is composed of 580 kg/h of H2 and 65 kg/h H2O at approx 80 C and 30 bar.
I have considered many different strategies such as PSA, TSA with the main drawback of loss of H2 during the purging of the regenerated column. In addition I assume condensing of the stream is a pre-requisite to reduce the around of H2O passing through the column to prevent quick saturation.
I've looked at condensing the stream by exploiting the Joule-Thompson effect, expanding the gas to allow cooling and thereby condensation of the water but reaching the required H2 purity seems implausible.
Are there any other technologies that you would recommend, taking into account the operating conditions specified above?
Once again, any help would be greatly appreciated.
D