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Evaporator Failure Caused by Corrosion and Flow

机译:腐蚀和流动引起的蒸发器失效

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This paper deals with three cases of boiler tube failure. 1). Flow assisted chelant corrosion was concepted as reason for inadmissible thinning of economizer tubes. There were discontinuous orange peel and extremely thin layer of iron oxides on those scalloped waterside. Some pearlite grains with iron leached off were found in surface vicinity under oxides layer. 2) Caustic gauging was recognized as damage mechanism of evaporator arch tube. The failure was localized in vicinity of protruding weld seam. It had character of ellipsoidal funnel with solid dense piece of iron and copper oxides inside and thin sodium contained deposit between the deposit and tube surface. The last was significantly etched under the deposit. 3) Quasi corrosion cracking was real cause for bent tube rupture by an axial crack. Neither internal attack nor significant structure degradation was observed in crack vicinity. The crack sides were strongly oxided and ash constituents penetrated into the crack. Nothing like said was found in neighborhood, hence the fault tube was "pre-cracked" before its service beginning, for instance due to inefficient heat treatment after bending.
机译:本文涉及三种锅炉管衰竭。 1)。流动辅助螯合剂腐蚀被概念为经济化管不允许稀释的原因。在扇形水域上有不连续的橙皮和极薄的氧化铁层。在氧化物层下的表面附近发现一些带铁浸出的珠光体晶粒。 2)腐蚀性计被认为是蒸发器拱管的损伤机理。故障在突出的焊缝附近定位。它具有椭圆形漏斗的特性,具有固体密集的铁和铜氧化物内部和薄钠在沉积物和管表面之间含有沉积物。最后在押金下有显着蚀刻。 3)准腐蚀裂纹是弯曲管破裂的真实原因,轴向裂纹破裂。在裂缝附近观察到内部攻击并不具有显着的结构降解。裂缝侧面是强氧化物,灰分成分渗透到裂缝中。在邻里发现没有像说的话,由于弯曲后的热处理效率低下,故障管是“预破裂”。

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