A Corrosion Test Method for Redox Buffer Molten Salt System
A corrosion test, molten salt technology, applied in the direction of measuring devices, electrochemical variables of materials, instruments, etc., can solve the problems that are not suitable for corrosion evaluation of molten salt systems containing redox buffer ions
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Embodiment 1
[0160] Test 316L stainless steel (316LSS) containing 1000ppmCrF 3 and 600ppmCrF 2 Corrosion rate in FLiNaK molten salt. The test temperature is 600°C, the 316L stainless steel wire to be tested has a diameter of 1 mm, and is immersed in molten salt for 3 cm. The comparative inert metal electrode is a silver wire with a diameter of 1mm, immersed in molten salt for 3cm. Using the metal wire and the silver wire to be tested as the working electrodes respectively, at a scan speed of 0.5mV / s, scan 0.15V from the open circuit potential to the positive and negative directions to obtain two sets of anode and cathode polarization curves, as Figure 5 shown. Since the molten salt system contains CrF 2 / CrF 3 For buffer ion pairs, the classic Tafel extrapolation method is not applicable, and the method of the present invention is required to be tested. That is, in the anode strong polarization region (ΔE is about 0.13 ~ 0.15V), the polarization current obtained on the 316L stainles...
Embodiment 2
[0162] Test 304 stainless steel (304SS) containing 1000ppmCrF 3 and 800ppmCrF 2 Corrosion rate in FLiNaK molten salt. The test temperature is 600°C, the 304 stainless steel wire to be tested has a diameter of 1 mm, and is immersed in molten salt for 3 cm. The comparative inert metal electrode is a silver wire with a diameter of 1mm, immersed in molten salt for 3cm. Using the metal wire and the silver wire to be tested as the working electrodes respectively, at a scan speed of 0.5mV / s, scan 0.15V from the open circuit potential to the positive and negative directions to obtain two sets of anode and cathode polarization curves, as Figure 6 shown. Adopt the processing method similar to embodiment 1, obtain new lgi~ΔE curve, carry out linear fitting to this curve, the equation of the straight line that obtains is: y=11.69x-4.165 (R 2 =0.999), the corrosion current density of 304 stainless steel in the redox buffer molten salt system calculated from the intercept with the long...
Embodiment 3
[0164] Test Hastelloy C276 alloy containing 1000ppmCrF 3 and 800ppmCrF 2 Corrosion rate in FLiNaK molten salt. The test temperature is 600°C, the Hastelloy C276 metal wire to be tested has a diameter of 1 mm, and is immersed in molten salt for 3 cm. The comparative inert metal electrode is a silver wire with a diameter of 1mm, immersed in molten salt for 3cm. Using the metal wire and the silver wire to be tested as the working electrodes respectively, at a scan speed of 0.5mV / s, scan 0.15V from the open circuit potential to the positive and negative directions to obtain two sets of anode and cathode polarization curves, as Figure 7 shown. Adopt the processing method similar to embodiment 1, obtain new lgi~ΔE curve, carry out linear fitting to this curve, the equation of the straight line obtained is: y=3.142x-4.515, from the Hastelloy C276 that obtains with the vertical axis intercept calculation The corrosion current density of the alloy in the redox buffer molten salt s...
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