Yes my friends, I am agree with your suggestions, but I have calculated the quantity of anodes that the system requires and it seems to me that they are few for the length of the pipeline.
The pipeline is 12 km length, (12").
# of anodes: 8 (Ti MMO)
Coating efficiency=90%
Thanks for your prior answers, but I need to be clear respect to the following:
Which criteria is applicable to place one or more anode beds and where they must be located?
Hi,
I am designing a CP for a gas pipeline. I will use impressed current to do this. My questions are:
Where is the best location for the bed of anodes? What is the best distance between de pipeline and the anodes?
Could somebody suggest me any reference?
I will appreciate a lot your help
Thanks dlms;
I am really designing the internal and external corrosion protection of the tanks. But I am not clear about the arrangement of the anodes into the tank, for the oil tank and salt water tank. The anodes for each case must be different?
Hi,
I'm trying to design an internal Cathodic protection system for oil and salt water storage tanks. I am not sure about how can I choose the adequate anodes. Please if somebody knows a specific case to solve my doubts I'd appeciate your answer. A web page related can be adviced.
Thanks...