Dear all,
We had surplus impure steam ( generated from effluent after evaporation) at 2.2 kg/cm2 g and this cant used anywhere in my process due to impurities. We would like to use this thermal energy in a different route.
We are planning to circulate DM water at shell side and tube side impure steam.So, Phase changes will occur and DM water becomes Pure steam and impure steam becomes as condensate.
How to calculate theoretically whether the above changes will occur or not.
Plz suggest for the above problem.
Regards
Talasila