In-vesselでの燃料溶融

In-vesselでの燃料溶融

a. Early phase

一般に、炉心現象の初期段階では、燃料温度の急激な上昇が起こり、炉心材料のリロケーションが開始します。 初期段階での燃料劣化を説明するために、以下の2つの液相化進展挙動が特に重要です。

1）燃料ペレット-ジルカロイ被覆管界面の液相化進展挙動

2）燃料集合体部材の液化進展挙動

燃料ペレット-ジルカロイ被覆管界面の液相化進展挙動

図x1：UO₂燃料ペレットとZry被覆管の溶融進展の模式図

図X1に、温度上昇に伴うUO2燃料とジルカロイ被覆管(Zry)との界面近傍での相転移の概略図を示す[5]。左側は燃料ペレット、中央から右側はZry被覆管を示している。通常運転時では、冷却水が被覆管のすぐ外側を流れており、被覆管温度はおよそ300℃となる。被覆管外周部は冷却水との相互作用によりZrO2層が形成される（その厚さは操作条件や照射時間によるが、約20μm程度となる[１]）。 ZrO2層は酸素の拡散を防ぐ保護膜として機能するため、通常運転時にはα-Zr(O)相はほとんど形成されないと考えられている。

事故が発生すると、液状化は次の3つの段階に分けることができます。

酸素の拡散が支配的な温度範囲(約1800℃以下)

炉心への冷却水の供給が不足すると、冷却水の水位が低下し、炉心・燃料が水蒸気中に漏出する。これにより、燃料温度が上昇する。

温度が上昇すると、被覆管外周部では水蒸気酸化（水蒸気/Zr反応）により酸化物の二重層構造（ZrO2外層とα-Zr（O）内層）が形成され、約1200℃を超えると、水蒸気/Zry反応が急速に進み、温度の急上昇が起こる（毎秒8℃以上）。被覆管の中央にはβ相が残留する。UO2燃料t/Zry界面では、酸素とウランがペレットからジルカロイ側に、Zrが燃料側に拡散を開始する。しかしながら、比較的低い温度（約1800℃以下）では酸素の拡散が支配的と考えられ、UとZrの拡散は界面近傍に限定される。 酸素ポテンシャルが低下したUO2/Zry界面の非常に狭い領域（おそらくα-Zr（O）領域側）において、UO2とZrの間の酸化還元相互作用によって少量の液体が形成される可能性がある。その先に燃料からZryへの酸素拡散によるα-Zr(O)相が形成される。

（Hofmannの図にリンク）

水蒸気/Zr反応：　Zr + 2H₂O → ZrO₂ + 2H₂ (ΔH=-586 kJ/mol)

液相化が急速に進展する温度温度(約1800℃～2200℃)

約1800～2200℃の範囲では、複雑な反応が起こるが、全体的な傾向としては、U、Zr、Oの相互拡散が顕著になり界面反応が促進され、β-Zr相からα-Zr(O)相への変態およびU-Zr-Oメルト相の急速な拡大が生じる。このような相形成は、管束(バンドル)劣化試験でHofmannによって観察されています[7、8]。

熱力学的評価によると、被覆管の中央領域に残っているα-Zr（O）とβ-Zrは、1900〜2100°Cの温度範囲でU-Zr-Oメルト相として完全に液化すると考えられる (β相(酸素固溶飽和)の液化温度：約1950℃、α-Zr(O)相の液化温度：約2100℃、しかしながら、液化温度は 局所酸素含有量に依存する）。U-Zr-Oメルト相は、内側に残留するUO₂と外側に残留するZrO₂を溶融して成長するが、温度によってそれらの溶解度に制限がある。

約2200℃までには、中央領域が完全に液化すると仮定すると、燃料棒は大きく3つの領域、すなわち、UO₂/U-Zr-Oメルト/ZrO₂の構造が形成されると考えられている。

溶融した燃料の下方へのリロケーション(約2200℃以上)

Phebus-FPT試験等の模擬試験での観測結果に基づき、約2200℃でU-Zr-Oメルトが燃料棒の外周から噴出し、炉心下方向にリロケーション開始すると考えられている。シビアアクシデント解析コード（MAAP、MELCOR、ASTEC、SAMPSONなど）では、この温度が燃料溶融温度としてモデル化されている。また、ASTECコード等では、溶融物がZrO₂膜を破って下方にリロケーションするか、あるいは、ZrO₂膜の内側に維持されたまま、機械的に崩落するかについて、閾条件があるとされている。約2200℃に到達した際の外周のZrO₂膜が約200～250μmより厚い場合、U-Zr-Oメルトはこれを破ることができず、燃料棒内部で保持され、なんらかの衝撃により、機械的に崩落すると考えられている。

参考文献：Phebusの論文。これ？PFT 0 - 5全部ある or 持ってる人いる？

燃料溶融進展にともなう溶融物の平均組成の変化

Figure 2: Variation in the local composition of the fuel rod with increasing temperature. A’ represents the initial internal oxidation (a-Zry formation) at the initial temperature excursion and A represents the onset of major oxidation/liquefaction reactions.

SA分析コードでは、一般に、α-Zr（O）とUO2の間のいわゆる「共晶」液状化モデルが実装されます。ただし、このモデルはSA分析用に指定された一種の簡略化されたモデルであるため、このモデルでは燃料棒の液化メカニズムを正確に説明できませんでした。基本的に、初期段階での燃料棒の液化の進行は、U-Zr-O三元状態図を使用して認識できます[8]。図2は、温度の上昇に伴う燃料棒の局所組成の変化を模式的に示しています。通常の操作では、平均組成はUO2-Zr線（通常はBWR燃料中のZrが豊富）の間のどこかにプロットされ、外面でのZrベース合金の酸化によってUO2-ZrO2線に向かって徐々にふるいにかけられます（A ⇒B⇒C⇒D）事故が進むにつれて。このモデルは、初期段階で燃料棒で起こっている化学反応が、UO2-ZrO2-Zr三元領域の相安定性に基づいて熱力学的に議論できることを示しています。この特定の地域では、蛍石（FCC）、面心正方晶（TET）、単斜晶、HCP、BCC、および液体の熱力学的データが必要です。 FCC、TET、および単斜晶相は本質的に酸化性固溶体であり、一方、HCPおよびBCC相は金属固溶体（合金）です。液相には、より複雑な熱力学的記述が必要です。比較的低温では、U-Zr-O溶融物が液体の主要な成分です（いわゆる「金属」溶融物）。金属溶融物の組成範囲は、温度の上昇とともに徐々に拡大しています。次に、高温（約2550°C以上）では、金属溶融物（U-Zr-O）と酸化溶融物（UO2-ZrO2）が互いに溶解する可能性があります。これには、U-Zr-Oシステムの液体の複雑な熱力学モデルが必要です。また、中間温度領域で形成される混和性ギャップには、より複雑な熱力学モデルが必要です。

亜化学量論のU-Zr-Oメルトが形成される。

燃料集合体部材の溶融

Figure 3(a) Schematic image of a horizontal cross section of a prototypic BWR Fuel assembly. The red square shows the section illustrated in Fig. 3(b).

図3(a)に燃料棒、制御ブレードおよびチャネルボックスで構成される典型的なBWR燃料集合体の水平断面図を示す[9]。燃料集合体は、Zr基合金製のチャネルボックスに囲まれており、BWRの場合、Zrの量はPWRの量よりも多い(約2倍の量)ことに注意する必要がある。さらに、重要な特徴は、制御ブレードがチャネルボックスの外側に配置され、燃料棒から離れていることである。

図３(b)に制御ブレードとチャネルボックスの溶融進展の概略図を示す。相互作用の主なコンポーネントは、（1）B4C吸収材とステンレス鋼（SS-304）被覆管からなる制御棒、（2）SS-316で作られたブレードシース、および（3）Zry-4チャネルボックスである。温度の上昇に伴い、以下の(a)-(d)の反応が生じると考えられる：

(a)制御棒ブレード内のB4Cとステンレス（SS）間の相互作用

(b) チャネルボックスの表面の酸化、

(c) B4C－SSメルトとZry-4チャネルボックス間の相互作用

(d) B4C-SS-Zrメルトと残留B4Cの水蒸気酸化反応

Figure 3(b) Schematic image of liquefaction progression at the interface between the control blade and the channel box.

Reaction (a) (B4C-SS system):

So-called ‘eutectic’ melting between B4C and SS could occur at approximately 1200 °C. The Fe-B-C ternary phase diagram indicates that the most of SS cladding (major component: Fe) and a small amount of B4C are liquefied by the ‘eutectic’ formation. Hence, a significant amount of B4C is able to remain in the B4C-SS melt [10]. For more detailed understanding of the ‘eutectic’ melting, one needs to evaluate selective Fe-C reactions as opposed Fe-B reactions in the Fe-B-C melt and the local precipitation of Cr-boride [11, 12]. Table 16 shows the current assessed status of the ternary sub-systems of the B4C-SS systems. (‘⭕’ means the full assessment and ‘-’ means that its system has not been assessed yet.) The most important sub-system for this particular interaction is clearly Fe-B-C, because Fe is a dominant component of SS, which is already stored in both of TAF-ID and NUCLEA. Also, Fe-Ni-Cr system is already stored in the both databases. By using these databases, the ‘simplified’ evaluation of the ‘eutectic’ melting between B4C and SS could be carried out. However, the databases are still insufficient for the other subsystems especially including Cr, B and C. Cr could selectively react with B and C during solidification of the melt. This reaction appears to be important for the characterization of metallic debris [13]. Table 16: Current assessed status of ternary sub-systems regarding the liquefaction of the BWR control rod, which stored in TAF-ID and NUCLEA

Reaction (b) (Zr-O system):

As for the thermodynamic understanding of the oxidation of the channel box, one needs the Zr-O binary database which is already stored in the both databases.

Reaction (c) (B4C-SS-Zr-O system):

After the control blade melt (SS-B4C melt) makes contact with the Zry channel box, there is an interaction between the SS-B4C melt and the partially oxidized Zr. Several chemical reactions could simultaneously progress and hence the overall phenomena are very complicated. A kinetic model is definitely necessary for the detailed understanding. Thermodynamic database could identify the tendency (driving force) or threshold condition for the reaction. The interaction’s progress depends on the thickness of the Zry surface oxide of the channel box. If the oxide film is not sufficiently protective in a non-oxidizing atmosphere, the interaction between SS-B4C melt and Zr can occur upon contact. As a result, B and C are transported to the Zry via liquid and could cause a sudden change of the system toward its equilibrium state, in which Zr-boride or Zr-carbide could precipitate in the melt. This is predicted to be an exothermic reaction. Table 17 shows the ternary subsystems regarding the liquefaction between the non-oxidized Zircaloy channel box and the SS-B4C melt (in addition to Table 16). The dominant subsystem for this particular interaction could be Fe-Zr-X (X: Ni,Cr,B,C). The database is still insufficient for developing the mechanistic model. Also, considering the solidification path of the metallic debris, one needs to improve Zr-B-X and Zr-C-X databases.

Table 17: Current assessed status of ternary subsystems regarding the interaction between SS-B4C and non-oxidizing Zr (in addition to Table 16) On the other hand, in the case of a thick oxide film on the Zry channel box. This interaction (SS-B4C and Zr) does not significantly occur and only SS-B4C melt relocates to the lower part (the channel box could maintain its original configuration during the absorber rod melting). Then, after melting of the Zr-channel box interior at higher temperatures, one needs to evaluate the dissolution of ZrO2 in the metallic melt which could be extremely important to the metallic debris characteristics. Table 18 shows the ternary sub-systems with oxygen. Both databases can roughly evaluate the effects of oxidation. However, the formation of ternary compounds could not be sufficiently evaluated using these databases. Also, TAF-ID does not store any databases on the stable compounds of B-oxide in the melt. Reaction (d) (B4C-SS-Zr-O system): The steam oxidation of the SS-B4C-Zr melt is extremely important for the characteristics of the metallic debris. Also, the formation of B2O3 could accelerate the liquefaction of the fuel rod, because the melting temperature range of B2O3 is ~ 450-465 °C and it could allow the easy contact/wetting with the fuel rod. Moreover, volatilization of B is extremely accelerated by the steam oxidation and gaseous boron oxides could influence the chemical stability of volatile FP, such as Cs and I [10, 14-15]. The improvement of B-related database is highly recommended.

On the other hand, in the case of a thick oxide film on the Zry channel box. This interaction (SS-B₄C and Zr) does not significantly occur and only SS-B₄C melt relocates to the lower part (the channel box could maintain its original configuration during the absorber rod melting). Then, after melting of the Zr-channel box interior at higher temperatures, one needs to evaluate the dissolution of ZrO2 in the metallic melt which could be extremely important to the metallic debris characteristics.

Table 18 shows the ternary sub-systems with oxygen. Both databases can roughly evaluate the effects of oxidation. However, the formation of ternary compounds could not be sufficiently evaluated using these databases. Also, TAF-ID does not store any databases on the stable compounds of B-oxide in the melt.

Reaction (d) (B₄C-SS-Zr-O system):

The steam oxidation of the SS-B₄C-Zr melt is extremely important for the characteristics of the metallic debris. Also, the formation of B₂O₃ could accelerate the liquefaction of the fuel rod, because the melting temperature range of B₂O₃ is ~ 450-465 °C and it could allow the easy contact/wetting with the fuel rod. Moreover, volatilization of B is extremely accelerated by the steam oxidation and gaseous boron oxides could influence the chemical stability of volatile FP, such as Cs and I [10, 14-15]. The improvement of B-related database is highly recommended.

b. Transient and late phases

Figure 4 Schematic image of the five stages (b1-b5) in the transient and late phases of in-vessel phenomena.

Figures 4 (b1)-(b5) indicate the schematic image of the prototypic five stages for the transient and late phases:

(b1) Start significant relocation of the fuel melt,

(b2) Blockage of steam flow at lower part of the core by the relocated debris,

(b3) Formation of corium pool,

(b4) Secondary relocation of corium melt to the lower plenum,

(b5) Liquefaction and stratification of oxidic and metallic melt in the lower plenum.

(b1) Start significant relocation of the fuel melt:

The leading relocation mainly of the metal components (such as the control rod blades and channel box) begins and then the partial blockage of the coolant flow path occurs by the relocated melt. After that, the relocation to the lower head of the U-Zr-O melt occurs. It is not sufficient to understand precisely these complicated reactions only by the thermodynamic approach because each reaction is accompanied by the rapid temperature changes. However, the reaction trends according to the accident scenarios could be evaluated by the thermodynamic databases. In the FDNPS accident, the different progression from the typical accident scenarios could occur (see chapter 4.6). The improvement/enlargement of the thermodynamic databases is expected to show some of the reasons of these deviations. Especially, it is important to improve the accuracy of the high temperature database of U-Zr-O system because the initial U-Zr-O melt is generally oxidized but the composition of the melt becomes more complex during the relocation stage.

(b2) Blockage of steam flow at lower part of the core by the relocated debris:

The blockage of the lower part of the core occurs by the collapsed oxide and metal debris. However, the BWR drainage scenario could occur in case of the insufficient blockage [16]. It is necessary to enhance accuracy of the U-Zr-Fe-O system data because the degree of blockage depends on the degree of oxidation of debris and the dissolution of the oxidized structural materials by the oxidic melt. As shown in chapter 4.5, the reaction between the U-Zr-O melt and Fe-oxide could proceed rapidly with local heat generation according to the thermodynamic analysis. This process could enhance the drainage scenario.

(b3) Formation of corium pool:

The melted and collapsed fuel is once cooled and re-solidified by the inhibition of the steam oxidation of Zr. After that, the temperature rises again by the decay heat, and this leads to the corium pool formation with a crust. The main components of corium are UO₂-ZrO₂ due to the oxidation progression of Zr. (However, in the case of the unit-2 of FDNPS, in which fuel melt could progress under the steam-served condition, the phase separation of oxidic and metallic melts could occur.) Therefore, the important system in this stage is also the U-Zr-O system.

(b4) Secondary relocation of corium melt to the lower plenum:

The corium pool is insulated by the surrounding crust layer and then it gradually expands. When the crust cannot support the corium weight with the corium extenuation, then the liquid corium can have secondary relocations to the lower plenum in a short period, either as rivulets or larger masses. The important database for this particular stage is U-Zr-Fe-O. However, the Fe-related databases are insufficient. The improvement is necessary. Besides, if the blockage by the crust layer is incomplete, it could lead to, not the corium pool growth, but the drainage scenario [16].

(b5) liquefaction and stratification of oxidic and metallic melt in the lower plenum:

In a typical accident scenario, the debris, which has fallen into the lower plenum and has cooled and solidified again on the lower plenum. Subsequent reheating and melting, could cause a stratification of the oxide and metal layers. In this scenario, the oxide melt is composed mainly of UO₂-ZrO₂-FeO, and mixed with the easily oxidized FP and presumably boron oxide. Metallic melts are mainly composed of SS-Zr-U, and mixed with metallic FP and B compounds. In some cases, the metal layer might be separated into heavy metal (U-Zr-rich) and light metal (Fe-rich) layers, according to MASCA results [17].

In such a multi-component system, it is difficult to evaluate its properties only by experiments, and conversely, it is effective to roughly evaluate the chemical state by the thermodynamic database [18]. Therefore, the accumulation of the experimental data and the improvement of thermodynamic databases and their joint evaluation for the multi-component system is continuously necessary.

Consequently, the base thermodynamic system for investigating these sequential reactions is U-Zr-SS-B₄C-O. By considering the metallic corium and the oxidic corium separately, metallic corium can be evaluated by mainly Fe-Zr-X (X means U, Cr, Ni, B or C), and basically, it is important to enlarge the thermodynamic data already shown in the early phase section. On the other hand, the oxidic corium consists of mainly U-O-X and Zr-O-X (X means Fe, Cr, Ni, B or C). Table 19 shows the currently assessed status of U-O-X (see Table 18 as for the Zr-O-Fe system). The important systems are U-O-Zr, U-O-Fe and Zr-O-Fe. In the future, the enlargement of the U-Zr-Fe-O system will be an important issue for performing FDNPS debris analysis.

In-vessel debrisの凝固

In-vessel debrisの凝固説明文追記

二酸化物コリウムの凝固とU-Zr-Oの凝固が異なることの説明

In-Vessel debrisの凝固に関する熱力学解析 （凝固パス逆問題解析）

U-Zr-O系デブリの凝固パス解析１）亜量論U-Zr-Oメルトからの凝固

図５に

最高到達温度　約1900℃～約2550℃ 説明文追記 〇〇組成の液相が 急冷：〇相と〇相が検出される可能性 徐冷：〇相と〇相が検出される可能性

Case-2：UO2-ZrO2コリウムからの凝固

最高到達温度　約2550℃～ 説明文追記 〇〇組成の液相が 急冷：〇相と〇相が検出される可能性 徐冷：〇相と〇相が検出される可能性

• Example.jpg

  キャプション1

• Example.jpg

  キャプション2

Case-3：金属メルトからの凝固（現在解析中）

3-1) SS-B4C 最高到達 〇〇組成の液相が 急冷：〇相と〇相が検出される可能性 徐冷：〇相と〇相が検出される可能性

3-2) SS-B4C-Zr 〇〇組成の液相が 急冷：〇相と〇相が検出される可能性 徐冷：〇相と〇相が検出される可能性

• 凝固パス逆問題解析

実デブリサンプル中に同定された相により、デブリ最高到達温度、冷却状態（徐冷、急冷）および組成を評価することができる。 参考リンク