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CHARACTERISATION OF IRON OXIDE DEPOSITS ON NICKEL-BASED ALLOY TUBES

机译:镍基合金管上氧化铁沉积的表征

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摘要

In nuclear pressurised water reactors (PWRs), steam generators (SGs) which are composed of thousands of tubes are used as heat exchangers between the primary (inside the tubes) and secondary (outside the tubes) circuits. On the SG secondary side, a fouling phenomenon occurs due to the deposition of corrosion products (mainly composed of iron oxides) at the surface of the tubes. In the long term, this effect could degrade thermal performances and may enhance risks of SG tube cracking. Several studies have been made on the characterisation of these deposits [1], on their formation mechanisms [2], and on their impact on the thermal transfer [3-5]. However, the relation between the deposit morphology and composition, the fouling mechanisms and their effect on the heat transfer efficiency in SG needs further investigations. The aim of this study is to get a detailed characterisation of the morphology, chemistry and crystallography of the deposits formed at the surface of SG tubes. Since PWR SG tube extraction is very difficult, experimental loops have been used to form fouling deposits on Ni-Cr based alloy (Inconel 600) tubes using representative secondary side thermodynamic conditions. As in a SG, two types of deposit conditions are considered: monophasic liquid and biphasic liquid-steam. In the present work, focus was made on morphological multi-scale characterisations. The observation of the surface of various sections of tubes using a FEI Nova NanoSEM 450 SEM and chemical analyses using a Bruker SDD EDS revealed that the deposits consist of geometrically-shaped crystallites containing Fe and O (Fig. 1) and allowed coverage estimations of about 82 %. Those observations were completed with u-Raman mappings to determine the molecular species present in the deposit. Deposit thickness measurements of various sections of tubes were also made from SEM observations in cross-sections to get statistical results giving a mean thickness of 0.97 ± 0.44 nm. As deposits are brittle and sensitive to oxidation, a water-free methodology has been developed for the metallographic preparation of samples, from cutting to polishing step including nickel-plating and cold resin-coating. Then, 3D electron tomography using a FEI Helios 660 dual column scanning electron microscope associated with a focussed ion beam (SEM/FIB) was used to get 3D reconstructions of the deposits over cubic micrometre volumes (Fig. 2). These reconstructions allowed the quantification of porosity, thickness distribution and coverage rate at the local scale.
机译:在核压水堆(PWR)中,由数千个管道组成的蒸汽发生器(SGs)用作一次(管道内部)和二次(管道外部)回路之间的热交换器。在SG二次侧,由于腐蚀产物(主要由氧化铁组成)在管子表面的沉积而产生结垢现象。从长远来看,这种影响可能会降低热性能,并可能增加SG管破裂的风险。已经对这些沉积物的特征[1],其形成机理[2]及其对热传递的影响[3​​-5]进行了多项研究。然而,SG的沉积物形态与组成,结垢机理及其对传热效率的影响之间的关系需要进一步研究。这项研究的目的是对SG管表面形成的沉积物的形态,化学和晶体学进行详细的表征。由于PWR SG管的提取非常困难,因此已使用代表性的二次侧热力学条件使用实验回路在Ni-Cr基合金(Inconel 600)管上形成结垢沉积物。与SG中一样,考虑了两种沉积条件:单相液体蒸汽和双相液体蒸汽。在当前的工作中,重点放在形态学多尺度表征上。使用FEI Nova NanoSEM 450 SEM观察管的各个部分的表面,并使用Bruker SDD EDS进行化学分析,结果表明该沉积物由含有Fe和O的几何形状的微晶组成(图1),并且覆盖率估计约为82%。这些观察结果通过u-Raman映射完成,以确定沉积物中存在的分子种类。还通过横截面的SEM观察对试管各部分的沉积物厚度进行了测量,以获得统计结果,得出平均厚度为0.97±0.44 nm。由于沉积物易碎且对氧化敏感,因此开发了一种无水方法用于样品的金相制备,从切割到抛光步骤(包括镀镍和冷树脂涂层)。然后,使用FEI Helios 660双柱扫描电子显微镜和聚焦离子束(SEM / FIB)进行3D电子断层扫描,以在立方微米的体积上对沉积物进行3D重建(图2)。这些重建可以量化孔隙度,厚度分布和局部覆盖率。

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    Chimie ParisTech, PSL Research University, CNRS, Institut de Recherche de Chimie Paris (IRCP) FR-75005 Paris, France,MINES ParisTech, PSL Research University, Centre des Materiaux, CNRS UMR 7633 P.O. Box 87, FR-91003 Evry Cedex, France;

    MINES ParisTech, PSL Research University, Centre des Materiaux, CNRS UMR 7633 P.O. Box 87, FR-91003 Evry Cedex, France;

    MINES ParisTech, PSL Research University, Centre des Materiaux, CNRS UMR 7633 P.O. Box 87, FR-91003 Evry Cedex, France;

    Chimie ParisTech, PSL Research University, CNRS, Institut de Recherche de Chimie Paris (IRCP) FR-75005 Paris, France;

    EDF RD/Chemistry and Corrosion Group Avenue des Renardieres, FR-77818 Moret-sur-Loing Cedex, France;

    EDF RD/Chemistry and Corrosion Group Avenue des Renardieres, FR-77818 Moret-sur-Loing Cedex, France;

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