i HAVE A CO2 STREAM IN PIPELINE!
HOWEVER I HAVE SOME 3000ppm of H2O inside of the stream!
iN MY CONDITIONS I MUST USE INSIDE INHIBITOR!
I would like to know how to calculate VOLUME OF THE INHIBITOR (wichever) WHICH I NEED TO USE AS A REZISTENT TO CORROSION!
THANK YOU EVERYBODY 100 OF TIMES!
HOWEVER I HAVE SOME 3000ppm of H2O inside of the stream!
iN MY CONDITIONS I MUST USE INSIDE INHIBITOR!
I would like to know how to calculate VOLUME OF THE INHIBITOR (wichever) WHICH I NEED TO USE AS A REZISTENT TO CORROSION!
THANK YOU EVERYBODY 100 OF TIMES!