Research Article |
Corresponding author: O. Ashraf ( osama.ashraf@edu.asu.edu.eg ) Academic editor: Maria Shchurovskaya
© 2024 O. Ashraf, Alaa Hamdy El-Kholy, Tarek Elzayat, Ayman M. Abdalla, A. H. Ashry.
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:
Ashraf O, El-Kholy AH, Elzayat T, Abdalla AM, Ashry AH (2024) Neutronic evaluation of VVER fuel assembly with chemical spectral shift regulation. Nuclear Energy and Technology 10(3): 153-160. https://doi.org/10.3897/nucet.10.125815
|
The performance of the spectral shift control (SSC) method is evaluated and compared to the conventional poison method in the VVER-1000 fuel assembly design. The SSC method can be implemented by gradually adjusting the ratio of heavy water to light water moderator (D2O/H2O) during the fuel cycle. In this study, the efficiency of using the SSC design with or without a thermal absorber (gadolinium) is investigated. We apply the SSC with both 12 burnable absorber rods containing 4.0 wt.% Gd2O3 (Case 1) and without Gd2O3 (Case 2). The neutronic calculations indicate that the discharge burnup is enhanced by 60% and the conversion ratio (CR) is increased by 64.4% at the beginning of the cycle (BOC) compared to the benchmark data. The breeding of Pu239 and Pu241 is extended to 33.7% and 29.5%, respectively, for the SSC design case (2), and better utilization of U-235 and U-238 has been achieved compared to BM.
Chemical spectral shift regulation, Neutronics, fuel cycle, VVER, SERPENT-2
During the last decades, there have been numerous efforts to extend the operational cycle of pressurized water reactors (PWRs) from months to years (
In the concept of the SSC, the neutron spectrum shifts from intermediate at the beginning of the cycle (BOC) to thermal at the end of the cycle (EOC). With a resonance spectrum during the early stage of operation, neutrons can be captured in fertile materials such as U238, increasing the converted fissile plutonium (
The SSC methods can be categorized into two groups:
The chemical method was initially introduced by Mars and Gans in 1961, involving the utilization of a mixture of light and heavy water (
The mechanical method varies depending on the type of reactor. In PWRs, achieving high burnup and CR can be accomplished by using fertile rods (
The main objective of the current paper is to assess the neutronic characteristics of the VVER-1000 LEU fuel assembly (FA) employing chemical spectral shift regulation. This study investigates the impact of varying the ratio between heavy water and light water on the VVER-1000 FA described in the OECD computational benchmark (
In the previous study (
According to the Monte Carlo simulation, the following parameters were studied: the variation of infinite multiplication factor (k∞), conversion ratio (CR) versus burnup, and the evolution of the isotopic composition of the fuel assembly (235U, 236U, 238U, 239Pu, 240Pu, 241Pu, and 242Pu), the accumulation of fission product poisons (135Xe and 149Sm) and burnout of burnable absorbers (155Gd and 157Gd). The obtained results were compared and analyzed according to the corresponding benchmark mean values (BM) (
In the present work, the VVER-1000 FA is presented from the VVER-1000 LEU and MOX Assembly Computational Benchmark (
Material type | Isotopic content, (atoms/barn.cm) | material type | Isotopic content, (atoms/barn.cm) | ||
---|---|---|---|---|---|
Fuel cell: 3.7 wt.% U235 | U 235 U238 O16 | 8.6264E-4 2.2169E-2 4.6063E-2 | Fuel gadolinium cell: 3.6 wt.% U235 with 4 wt.% Gd2O3 | U 235 U238 O16 Gd152 Gd154 Gd155 Gd156 Gd157 Gd158 Gd160 | 7.2875E-4 1.9268E-2 4.1854E-2 2.5159E-6 2.7303E-5 1.8541E-4 2.5602E-4 1.9480E-4 3.0715E-4 2.6706E-4 |
The clad material: Zirconium alloy | Zr Nb Hf | 4.259E-2 4.225E-4 6.597E-6 | |||
Moderator, 0.6 g/kg of boron | H O16 B10 B11 | 4.843E-2 2.422E-2 4.794E-6 1.942E-5 |
The Serpent-2 Monte Carlo code version 2.1.31 (
At the BOC, the D2O/H2O ratio starts at 65% in the case of the presence of 12 burnable absorber pins with 4.0 wt.% Gd2O3 (case 1), and with 73% in the case without using any burnable absorber (case 2). This ratio decreases with equal decrements of 5% in all cases over the operational cycle until it reaches a concentration of 0% at the EOC. The startup ratio of D2O/H2O (i.e., 65% and 73%) has been adopted to ensure acceptable initial excess reactivity. The Serpent-2 code cannot automatically apply the critical density iteration of D2O during burnup. Therefore, the D2O concentration is manually adjusted during the simulation through 14 different molecular ratios of D2O/H2O distributed over the operating cycle as follows: at the BOC, the molecular ratio of D2O/H2O is started with a high value until the model could not further maintain criticality conditions (i.e., k∞>1). Subsequently, as the fuel cycle proceeds, the subsequent values gradually decrease until reaching 0% D2O and 100% H2O at the EOC. The results obtained by Serpent-2 are compared with the benchmark mean values as a reference case, with corresponding statistical errors of ±64% and ±19 pcm for CR and k∞, respectively.
The influence of the chemical spectral shift control (SSC) method on the fuel utilization and the cycle length of the VVER-1000 FA has been demonstrated by determining the time evolution of the following parameters: k∞, CR, U235, U238, Pu239, Pu240, Pu241, Pu242, Xe135, Sm149. The simulation was performed by Serpent-2 for two cases: case (1) (D2O/H2O + 4.0 wt.% Gd2O3) and case (2) (D2O/H2O).
Fig.
Fig.
Fig.
Figs
As shown in Figs
According to Figs
Figs
Fig.
We conducted a comparison between two dilution process models relative to the benchmark model (BM). Table
Comparison of neutronic parameters and assembly average isotopic composition for different dilution processes
Neutronic parameters | Previous work ( |
Current work | |
---|---|---|---|
The dilution process | |||
10%, 13%, 15%, and 19% | 5% | ||
k ∞ | Shows rapid and large fluctuations (the maximum fluctuation in k∞ < 7%) | Shows rapid and small fluctuations (the maximum fluctuation in k∞ < 2.9%) | |
CR | Shows rapid and large fluctuations (the maximum fluctuation in CR < 14%) | Shows rapid and small fluctuations (the maximum fluctuation in CR < 6%) | |
Assembly average isotopic composition | U 235 | The inventory increases by 32% compared with BM at EOC. | The inventory increases by 31% compared with BM at EOC. |
U 238 | The inventory decreases by 0.45% compared with BM at EOC. | The inventory decreases by 0.62% compared with BM at EOC. | |
Pu 239 and Pu241 | The inventory increases by 39% and 28%, respectively, compared with BM at EOC. | The inventory increases by 33.7% and 29.5%, respectively, compared with BM at EOC. | |
Pu 240 and Pu242 | The inventory increases by 18% and 3%, respectively, compared with BM at EOC. | The inventory increases by 25.7% and 3.3%, respectively, compared with BM at EOC. | |
Xe 135 and Sm149 | The inventory increases by 51% and 66%, respectively, compared with BM at EOC. | The inventory increases by 24.7% and 21.9%, respectively, compared with BM at EOC. |
Based on the preceding analysis, it is evident that the SSC design offers several advantages, including enhanced conversion ratio throughout the operational cycle, improved fuel utilization, and a prolonged reactor life cycle.
It was observed that for both cases of the SSC method, there is a 60% improvement in the fuel discharge burnup compared to the benchmark reference model. Moreover, the existence of gadolinium in the first case of the SSC method would result in a reduction of D2O quantity by 12% at the BOC and by 100% at the EOC relative to the second case, without affecting the achieved discharge burnup. This, in turn, could potentially reduce the capital cost of implementing the SSC method.
Smoothly reducing the (D2O/H2O) ratio by 5% results in an enhancement in the variation of k∞during burnup and in the conversion ratio values, besides better utilization of the fuel source to breed more fissile material. Furthermore, significant improvements can be achieved by decreasing it by 1% or lower throughout the process.
Comparing case (2) to case (1), several improvements are notable, including enhanced conversion ratio, increased breeding of plutonium isotopes, better utilization of U238, and reduced use of enriched U.
However, there are also drawbacks to consider. The equilibrium condition of Xe135 and Sm149 has not been achieved. It is important to highlight that in the SSC design, the significant contribution of Pu239 and Pu241 to power generation will reduce the values of the main kinetic parameters. These continuous physical changes in the reactor parameters during the operating cycle emphasize the necessity of conducting a precise safety analysis for this type of reactivity control.