Art,
thank you for your reply , i will explain to you what i have and what i want to do:
- from hysys simulation : i have as mass flow from overhead vapor outlet of teg stripper :
5 kg/hr Nitrogen
34.9835 kg/hr H2O
0.1235 kg/hr TEG
2.8628 kg/hr Benzene
9.7107 kg/hr Toluene
0.5611 kg/hr Ethel Benzene
7.9014 kg/hr p-Xylene
- i want to condensate the BTEX from this flow by using the technique as descriped in the link above .
so any information can help me for design and if exit a software for design and simulation for the BTEX unit, so if you can contact KIWI I will be thankful ?