Corrosion rates of concretes made with different binders and exposed for 10 years in natural sea water

Author(s):  
C. Alonso
Keyword(s):  
CORROSION ◽  
1979 ◽  
Vol 35 (11) ◽  
pp. 505-509 ◽  
Author(s):  
BARRY C. SYRETT ◽  
DIGBY D. MACDONALD

Abstract This work was stimulated by reports that electrochemical methods for measuring the polarization resistance of copper, nickel, or copper-nickel alloys in aqueous systems may lead to appreciable errors in the estimates of the corrosion rate. In the present work, the polarization resistance (Rp) of two copper-nickel alloys (90:10 Cu:Ni and 70:30 Cu:Ni) was monitored as a function of time in flowing sea water that contained 0.045, 0.85, 6.6, or 26.3 mg/dm3 dissolved oxygen. Rp values were obtained using the linear polarization, potential step, and AC impedance techniques. The total weight loss during the test period was calculated from the area under the 1/Rp versus time curve and compared with the measured weight loss. The experimental data support the validity of electrochemical methods for measuring corrosion rates of copper-nickel alloys in sea water, provided that a sufficient number of Rp measurements are made during the first 24 hours, and provided that proper consideration is given to the capacitive elements of the metal/solution interfacial impedance. Previous reports that electrochemical measurements may lead to underestimates of the corrosion rates are thought to have resulted primarily from undetected (and very high) corrosion rates at short exposure times. Reported overestimates of the corrosion rates are thought to have resulted from the use of a potential sweep rate that was too high (linear polarization technique), a time for current decay that was too short (potential step technique), or excitation frequencies that were insufficiently low (AC impedance technique).


CORROSION ◽  
1979 ◽  
Vol 35 (1) ◽  
pp. 23-33 ◽  
Author(s):  
JEFF PERKINS ◽  
K. J. GRAHAM ◽  
G. A. STORM ◽  
G. LEUMER ◽  
R. P. SCHACK

Abstract A unique “circling-foil” apparatus has been developed to study velocity effects on corrosion processes, and has been used initially to expose single metals and galvanic couples of some common marine structural materials in synthetic sea water electrolyte under controlled hydrodynamic conditions at relative velocities up to 3 m/s. The samples are deployed by mounting in a sample holder with a standard foil profile, which circles in a tank, with a turbulence trip wire at the leading edge of the foil. This scheme allows prediction and measurement of the fluid flow structure over the corrosion samples. Direct determinations of turbulence intensity and boundary layer thickness were made at various velocities, enabling correlations of hydrodynamic parameters with electrochemical data and other measures of corrosion behavior. The effects of velocity and potential distribution on average corrosion rates, and on the mode and distribution of corrosive attack and corrosion products, have been studied.


2018 ◽  
Vol 2018 ◽  
pp. 1-15 ◽  
Author(s):  
Aisha H. Al-Moubaraki ◽  
Hind H. Al-Rushud

Corrosion behavior of Al 7075, Al 2024, and Al 6061 in the Red Sea water was studied using weight loss (WL) measurements and potentiodynamic polarization (PDP) technique. The corrosion patterns and corrosion products formed on Al alloys were characterized using optical photography (OP), scanning electron microscopy (SEM), and energy-dispersive spectroscopy (EDS). The results showed that WL data were consistent with bimodal model rather than the power law function and the corrosion rates exhibit a continuous decrease with exposure time. The increasing order of the Red Sea corrosivity on the studied Al alloys can be given as follows: Al 6061 < Al 2024 < Al 7075. The results of temperature effect revealed that an increase in temperature resulted in an increase in both anodic and cathodic current density and a decrease in corrosion potential. Al 7075 was less influenced by temperature than the other alloys. Pitting corrosion was the predominant corrosion pattern detected on all Al alloy surfaces after prolonged immersion in the Red Sea water. The appearance of S peak in EDS spectra of Al 7075 after corrosion gives an indication of the contribution of bacteria in the corrosion process.


CORROSION ◽  
1966 ◽  
Vol 22 (1) ◽  
pp. 16-20 ◽  
Author(s):  
YU. M. KOROVIN ◽  
I B. ULANOVSKII

Abstract Using Russian steels of 13 Cr and 18–9 analyses in general experiments are conducted varying pH and oxygen concentrations in sea water to determine the relative effect of these variables on corrosion rates in crevices. Effect of oxygen concentrations in the range 1–9 mg/1 and pH 8.3 to 2.3 are reported. Changes in pH were found to strongly and changes in oxygen concentration weakly influence the corrosion rate. Authors postulate that anodic passivity is effected after application of tenths of a milliampere per square centimeter whereas when the pH in the anodic space is lowered, critical current density required for passivation increases 40–50 fold. Heat treatment of the steel does not influence electrode potentials when solution pH is lowered.


CORROSION ◽  
1974 ◽  
Vol 30 (2) ◽  
pp. 53-59 ◽  
Author(s):  
R. A. BONEWITZ

Abstract Aluminum alloys 3003, 3004, and 5050 were evaluated for desalination applications by means of their anodic polarization curves determined in 1X synthetic sea water at 25 C (77 F) to 150 C (302 F). Pitting performance was established from the relative values of the corrosion potential and the breakdown and protection potentials, and general corrosion rates were calculated from corrosion currents determined by the slop-intercept method. Pitting is not anticipated for 3003 and 3004 alloys at temperatures to 150 C and for 5050 alloy to 125 C (257 F). General corrosion rates for these alloys were less than 1 mpy.


2012 ◽  
Vol 591-593 ◽  
pp. 1030-1033
Author(s):  
Yan Gang Wang ◽  
Xing Hua Tong ◽  
Yong Jiang ◽  
Yong Liu ◽  
Lin Sen Zhu

The corrosion characteristics of various steels used by ocean wave energy equipment in sea water are investigated by electrochemical tests in this paper. The electrochemical experiments are carried out to research the corrosion rules of Q235, 20# steel, 16Mn and X42 through contrast experiments. Polarization curves and electrochemical impedance spectroscopy (EIS) are got by electrochemical workstation. Corrosion rates and corrosion potentials are analyzed from the polarization curves, and corrosion rules are founded. In addition, EIS is analyzed, and the analysis results are consistent with the results of polarization curves.


CORROSION ◽  
1979 ◽  
Vol 35 (9) ◽  
pp. 409-422 ◽  
Author(s):  
B. C. SYRETT ◽  
D. D. MACDONALD ◽  
S. S. WING

Abstract The corrosion rates of copper alloys 706 (90:10 Cu:Ni) and 715 (70:30 Cu:Ni) were measured, using rotating cylinder specimens in sea water that contained oxygen, sulfide, sulfur, and polysulfide, either singly or in combination. In addition a control test was performed using unpolluted deaerated sea water. Corrosion rates were monitored for over 24 hours, using linear polarization and potential step techniques. The work has shown that copper-nickel alloys can corrode quite rapidly in deaerated sea water if these normally “passive” alloys are made active by the presence of sulfide, or if sulfur is available as an oxidant.


2017 ◽  
Vol 728 ◽  
pp. 123-128
Author(s):  
Pornsak Srisungsitthisunti ◽  
Siriporn Daopiset ◽  
Noparat Kanjanaprayut

Crevice corrosions of duplex stainless steels were investigated under the aggressive condition of sea water pumps in offshore petroleum platforms. The study aims to compare crevice corrosion behavior of three grades of duplex stainless steels, UNS S32101 (2101), UNS S31803 (2205) and UNS S32750, in seawater with 200 ppm of hypochlorite. Duplex steels were compared with a widely used austenitic steel UNS S31603 (316). Specimens were tested under synthetic sea water prepared at pH4, pH6 and pH8 by the cyclic potentiodynamics polarization technique and the potentiostatic technique. The results show that the duplex stainless steels had higher corrosion resistance compared with the 316. The released charges and the corrosion rates of the 2101 and the 2205 were similar, but much lower than those of the 2507especially after 3 months period.


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