We have a glycol dehydration unit to dry the wet gas by TEG. During the regeneration of TEG, we use natural gas as stripping gas to reach the purity of 99.9wt% of TEG. Note the process under temperature and pressure of 204C and atm.
We have a proposal to substitute the stripping gas with N2 gas.
Please could any one tell me if the N2 will adequate for that process or not ?