1977
DOI: 10.2172/1107614
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CORROSION OF IRON-BASE ALLOYS VERSUS ALTERNATE MATERIALS IN GEOTHERMAL BRINES (Interim Report - Period Ending October 1977)

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Cited by 15 publications
(15 citation statements)
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“…In regard to the operation of a geothermal power plant, the steel grade API L80 shows better corrosion resistance at temperatures of 200 • C, which can be found nearby the bottom of the boreholes as shown in Figure 1, than those at 100 • C. This is because iron oxides are stable at 200 • C, leading to the formation of a protective scale [57]. However, the temperature in the reservoir might drop over the lifetime of the power plant [9], and, as a consequence, the entire system might be jeopardized.…”
Section: Discussionmentioning
confidence: 99%
“…In regard to the operation of a geothermal power plant, the steel grade API L80 shows better corrosion resistance at temperatures of 200 • C, which can be found nearby the bottom of the boreholes as shown in Figure 1, than those at 100 • C. This is because iron oxides are stable at 200 • C, leading to the formation of a protective scale [57]. However, the temperature in the reservoir might drop over the lifetime of the power plant [9], and, as a consequence, the entire system might be jeopardized.…”
Section: Discussionmentioning
confidence: 99%
“…Specific metals were eliminated because of poor corrosion resistance, high cost (e.g., precious metals), poor availability (e.g., rare earths), or inability to fabricate at temperatures compatible with waste cores, that is, below 1300°C (e.g., refractory metals). Zirconium is an exception and is a logical alternative to titanium because it has very similar corrosion Shannon 1977) and fabrication characteristics (Schwope 1961). However, titanium is generally more available and seems to be a somewhat better choice for corrosion resistance.…”
Section: Metalsmentioning
confidence: 99%
“…A typical corrosion 2+ reaction is: Fe + Fe + 2e. Two of the most important cathodic reactions required to complete and sustain the electrochemical corrosion process are: 2H+ + 2e-+ H2 (gas) and O 2 + 2H2 + 4e-+ 40H- (Shannon 1977). This shows that the acidity (pH) and the oxygen content of the brine are extremely important in controlling the corrosion of carbon steels.…”
Section: Redox Reactionsmentioning
confidence: 99%
“…Naturally, CO 2 will be readily available in a CAES operation. The average corrosion rates of 10 carbon steels in 1% NaCl brines are plotted against pH in Figure 39 (Shannon 1977). It has been observed that the effects of dissolved CO 2 become less serious at elevated temperatures, e.g., 423°K to 523°K.…”
Section: Liquid Water Environmentmentioning
confidence: 99%
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