COMPARATIVE STUDY OF CORROSION RATE AND EQUIVALENT CIRCUIT MODEL FOR GALVANIZED STEEL IN CHLORIDE SOLUTION TO CARBONATE
Galvanized steel is a regular carbon steel which has been coated with zinc to protect <br /> <br /> steel from corrosion. Zinc on galvanized steel provides protection to steel with two <br /> <br /> mechanisms, as barrier between steel and the environment, and as cathod...
Saved in:
Main Author: | |
---|---|
Format: | Final Project |
Language: | Indonesia |
Online Access: | https://digilib.itb.ac.id/gdl/view/30848 |
Tags: |
Add Tag
No Tags, Be the first to tag this record!
|
Institution: | Institut Teknologi Bandung |
Language: | Indonesia |
Summary: | Galvanized steel is a regular carbon steel which has been coated with zinc to protect <br />
<br />
steel from corrosion. Zinc on galvanized steel provides protection to steel with two <br />
<br />
mechanisms, as barrier between steel and the environment, and as cathodic <br />
<br />
protection in which zinc will be corroded first when there is imperfection at the <br />
<br />
coating as zinc is more galvanic relatively to steel. Galvanized steel application at <br />
<br />
outdoor environment will create a contact of galvanized steel with corrosive media <br />
<br />
such as rainwater. Rainwater can contain chloride and carbonate ion that can affect <br />
<br />
the corrrosion process on galvanized steel. This research will investigating the <br />
<br />
difference of corrosion process of galvanized steel in chloride and carbonate <br />
<br />
solution from the perspective of corrosion rate and equivalent circuit model. <br />
<br />
A series of electrochemical testing consist of potentiodynamic polarization and <br />
<br />
electrochemical impedance spectroscopy (EIS) were conducted with laboratory <br />
<br />
potentiostat and also immersion test to study the difference of galvanized steel <br />
<br />
corrosion in chloride and carbonate solution. Potentiodynamic test was conducted <br />
<br />
on galvanized steel sample that has been immersed for 15 days in chloride and <br />
<br />
carbonate solution with concentration each of 1 M, 0,5 M, and 0,3 M at room <br />
<br />
temperature. Corrosion potential, corrosion current density, and Tafel slope were <br />
<br />
determined with Tafel extrapolation method from polarization curved acquired <br />
<br />
from potentiodynamic test. Immersion test was also conducted at solution <br />
<br />
concentration of 1 M to calculate corrosion rate that will be compared to corrosion <br />
<br />
rate from Tafel extrapolation. To determine the equivalent circuit model, EIS was <br />
<br />
conducted at day 1, 2, 3, 7, 11, and 15 of immersed sample. <br />
<br />
Highest corrosion rate in chloride solution was 0,22 mm/year at 1 M concentration, <br />
<br />
whereas in carbonate solution was 0,03 mm/year at 0,3 M. Equivalent circuit model <br />
<br />
suitable for galvanized steel corrosion in 1 M chloride solution indicates the <br />
<br />
presence of diffusion process on day 3 to 15. At concentration of 0,5 M, the <br />
<br />
corresponding model indicates no interface diffusion process, and at concentration <br />
<br />
of 0,3 M diffusion occured since day 1 of immersion. On the other hand, in <br />
<br />
carbonate solution of 1 M, the model indicates the presence of oxide layer which <br />
<br />
dissolved on day 11. For concentration of 0,5 M, diffusion process occured on 2 <br />
<br />
days of immersion, with the presence of oxide layer until day 15. At concentration <br />
<br />
of 0,3 M, the model indicates the presence of oxide layer and no diffusion process <br />
<br />
occured. |
---|