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the pipeline is recieving a constant dosing rate of Corrosion inhibitor , the production team are requiring to reduce the flow pressure , is there any necessity to change the CI dosing rate ?

Can someone explain this method what is the principle ?

Can someone explain the principle of this method ? when and how shall we use it ?

The crude oil storage tank suffer from external corrosion ( heavy corrosion and even a holes ) in the chime plate, some portion suffer from distortion ( until the toe of the shell to bottom weld ) the internal annular plate is not corrded since it was repaired by an internal annular plate...