Corresponding author: Yury G. Cherednichenko ( cheryug@ippe.ru ) Academic editor: Boris Balakin
© 2020 Yury G. Cherednichenko, Oleg E. Levin.
This is an open access article distributed under the terms of the Creative Commons Attribution License (CC BY 4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.
Citation:
Cherednichenko YG, Levin OE (2020) On the control of coolant parameters in long-life facilities. Nuclear Energy and Technology 6(3): 137-141. https://doi.org/10.3897/nucet.6.57734
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When nuclear power plants with heavy coolants are brought to operating mode as well as during their operation, it is necessary to control and maintain the oxygen content in the coolant within the specified limits. As a rule, the oxygen content in metal melts is controlled by sensors based on solid oxygen-ionic electrolytes. The article presents an analysis of the methodological aspects of dissolved oxygen control in non-isothermal circulating loops with metal coolants, using such sensors. It is shown that in the presence of dissolved loop wall materials and suspensions of their various oxides in the coolant, control over the values of the oxygen activity and concentration calculated for a pure coolant is in general unjustified. The authors present the experimental results of the distribution of oxidation potentials along the loop depending on the coolant temperature, obtained during long-term tests of cladding samples in a lead melt in two circulation facilities – SM2-M and TsU1-M – which differ in principal methods for maintaining specified oxygen conditions. In the low temperature region, the experimental values of the oxidation potential in both facilities are lower than those calculated for pure lead, which leads to a difference by two or more times of the calculated oxygen concentrations for the regions of the loop with Тmin and Тmax, i.e., the so-called oxygen ‘non-isoconcentration’ is observed along the loop. In deoxidation mode during hydrogen ejection into the coolant, the oxidation potential in the loop changes in a complex way, and it makes no sense to talk about the oxygen concentration. It is concluded that in long-life facilities, the coolant parameters for oxygen must be controlled not by the calculated oxygen activity or concentration but by the oxidation potential in the maximum temperature region. To obtain the correct values of the oxidation potential, measurements should be carried out in temperature-stable modes of throughout the facility.
Control, oxygen, heavy coolant, circulation loop, oxygen-ionic electrolyte, oxidation potential
In nuclear power plants with heavy coolants, it is necessary to continuously maintain optimal conditions for the formation of oxide protective films on all surfaces exposed to the melt (i.e., to create conditions for the continuous passivation of loop materials with dissolved oxygen from the coolant). For this, it is required to control the coolant deoxidation and makeup with oxygen during the start-up passivation of materials and operation of the nuclear power plant.
The dissolved oxygen concentration in the melt is controlled by the EMF method using electrochemical cells based on solid electrolytes (
The EMF of the electrochemical cell, Е, is determined by the difference between the oxidation potentials (Gibbs energies) in the reference electrode, ΔGref, and in the melt (coolant), ΔGcool:
Е = (ΔGref – ΔGcool) / (2×F), (1)
where F = 9.648456×104 C/mol is the Faraday constant; ΔG is the oxidation potential, J/g-at.O.
The oxidation potential of the melt, ΔGcool, with any content of impurities is written as
ΔGcool = ΔG0cool + RT × ln ao, (2)
where R = 8.31441 J/(mol×K) is the universal gas constant; Т is the temperature, K; ΔG0cool is the melt oxidation potential in the oxygen saturation state, (J/g-at.O); ao = СО/СОS is the oxygen activity in the melt; CО is the dissolved oxygen concentration in the melt; СОS is the dissolved oxygen concentration in saturation mode.
In the reference electrode ao = 1(the melt is in the oxygen saturation state) and ΔGref = ΔG0ref is a known function. Then the oxidtion potential of any coolant, ΔGcool, with any impurity content at any point in the loop is written as
ΔGcool ≡ΔG0ref – 2F × Е (V). (3)
When analyzing the state of the coolant in physical chemistry, it is customary to deal with the Gibbs free energy (ΔG) or, in other words, with the oxidation potential of the melt.
In practice, reactor physicists operate with the parameter of the impurity concentration in the coolant. To visualize the real deviations of activity from ideal conditions, the well-known a-С-Т-Е diagram is used (
In circulation facilities, as in reactor plants, there is a constant supply of metallic impurities (iron, chromium, etc.) from the walls of the loop, which causes the coolant deoxidation. To compensate for deoxidation, additional sources of dissolved oxygen to liquid metal are used (
Over time, a finely dispersed solid phase based on iron oxides (Fe3O4, PbO×5Fe2O3 etc.) is formed in the coolant of the loop. It controls the coolant oxidation potential in the entire nonisothermal circulation loop (
Since the formation and decomposition of these oxides due to temperature changes occurs slowly (with a long delay time), a composition with a constant content of oxides and dissolved oxygen and iron throughout the loop is formed in the circulating coolant. This is indicated by the absence of any noticeable hysteresis of the EMF sensors when the coolant moves from the cooler to the maximum temperature (Тmax) region and vice versa in the circulation facilities during their life tests.
Impurities can significantly affect both the composition of the oxides in the coolant (i.e., the ΔG0 value of the coolant (
According to the form, the temperature dependences for ΔG0 and СОS for a real coolant with impurities will look the same as these dependences do for a pure coolant, but the coefficients included in them will be different. Therefore, in the case of a linear temperature dependence ΔGcool (Т) and, consequently, the EMF Е (Т) in the circuit, СО = const is always observed. However, for calculating the true values of the oxygen activity and concentration (especially in reactor plants), it is necessary to have the ΔG0 and СОS dependences for a real coolant with impurities, which is hardly feasible or at least difficult in practice.
Therefore, in general terms of the physics of the process, to control the deoxidation and passivation of materials and the coolant makeup with oxygen both at the start-up stage and during operation of the plants, it is necessary to control not the oxygen activity and concentration (due to the uncertainty of ΔG0 и СОS in the coolant), but the difference between the oxidation potentials of the coolant, ΔGcool, and oxide, ΔG0(Fe3O4):
δΔG = ΔGcool – ΔG0(Fe3O4) > 0, (4)
where ΔG0(Fe3O4) is the oxidation potential of Fe3O4, which forms a protective film on the inner surfaces of the loop.
This condition must be met for any impurities in the coolant.
In fact, it is necessary to control, at the maximum temperature, Тmax, in the loop, the EMF Е value of the oxygen activity sensor (OAS) in the coolant relative to the calculated EMF Е (Fe3O4), at which the depassivation of the films begins (Figs
Е = Е (Fe3O4)(Тmax) – δЕ (Тmax). (5)
Permissible (minimum and maximum) values of δΔGP b(Тmax), δЕ (Тmax) should be obtained on the basis of preliminary resource tests of materials in the circulation facilities. In the case of small deviations of the true oxidation potential values of the real coolant, ΔGcool, from ΔG of the coolant without impurities, the mode on the resource can be controlled by the oxygen activity or concentration from the known а-С-Т-Е diagram, after preliminary evaluations of the permissible oxygen “non-isoconcentration” along the loop.
To illustrate the foregoing, Fig.
For the SM-2 and TsU-1M facilities, there was a fundamental difference in the methods for maintaining test conditions. In the SM-2 facility, a slow constant increase in the EMF of all the OASs was observed on the resource, which is equivalent to a decrease in the coolant oxidation potential, a decrease in the concentration of oxygen dissolved in the coolant, most likely due to its binding by iron diffusing through the protective films. To maintain the oxygen concentration in the range of the set values, gaseous oxygen was periodically metered into the gas cavity of the centrifugal pump to the melt surface. On the contrary, in the TsU-1M facility, the resource showed a constant decrease in the EMF of all the OASs, which is equivalent to an increase in the coolant oxidation potential and an increase in the concentration of oxygen dissolved in the coolant, most likely due to the decomposition of various solid oxide impurities when they are in a significant amount in the facility. To maintain the oxygen concentration in the range of permissible values, an argon-hydrogen mixture was periodically metered into the gas cavity of the centrifugal pump to the melt surface. In other words, the SM-2M facility was conditionally “clean” and the TsU-1M facility was conditionally “dirty”, which is confirmed by the fact that there is a significantly larger amount of slag in the melt when the coolant is drained in TsU-1M than in SM-2.
In Figures
Even more unjustified is the control of the coolant by the oxygen activity or concentration during its hydrogen regeneration (deoxidation), especially when hydrogen is ejected directly into the loop. Figure
This will make it possible