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Impact of electrolyte contamination on surface finishing and pitting corrosion of electropolished 304 stainless steel

机译:电解质污染对电解研制304不锈钢表面整理和蚀腐蚀的影响

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The aim of the process of electropolishing (EP) stainless steel based on anodic dissolution of themetal surface is to enhance corrosion resistance and to improve the aesthetical properties of thesurface of the polished element. Due to economic reasons, EP processes are conducted at thetemperature of 30-70˚C while preserving the sustainability of the bath. In industrial conditions, thebaths usually consist of: concentrated solutions of H_3PO_4 and H_2SO_4 acids and organic additives.Sulphuric(VI) acid ensures an adequate conductivity of the bath, while phosphoric(V) acid is mainlyresponsible for the polishing of metal surface. During the EP process, the electrolytic bath isenriched with metal (iron, chromium and nickel) ions that originate from the dissolution of theanode. If the electrolyte has been used for a long time, this may result in increased roughness anddeteriorated gloss of electropolished surfaces. Monitoring the changes in the composition ofprocessing baths during electropolishing of austenitic stainless steel on an industrial scale allowsus to determine the conditions for the EP process. This, in turn, enables to obtain the best qualityproducts while at the same time minimising the costs of bath replacement and disposal taking intoaccount the environmental impact by mobile speciation of heavy metals.The paper presents the results of laboratory tests considering the influence of long-termcontamination of a bath that contains a mixture of H_3PO_4 and H_2SO_4 on surface finishing andpitting corrosion of electropolished 304 stainless steel. Potentiodynamic measurements werecarried out using the Solartron SI 1287 Electronic Interface towards a Saturated Calomel Electrode.The pitting corrosion resistance tests of steel in a 0.5M solution of sodium chloride demonstratedthat, although the electrolyte was strongly contaminated with iron, chromium and nickel ions,electropolishing (process parameters 8 A/dm~2, 15 min, 55°C) did not reduce the pitting potential,although the roughness and gloss of the samples were significantly lowered. After the EP processin electrolyte that was not contaminated with metal ions samples were characterised by roughnessRa=0.11 μm and gloss 955 GU. On the other hand, in samples that had been electropolished inelectrolyte contaminated with iron (over 6% by mass), chromium (less than 2%), and nickel ions(less than 1%) these values were, respectively, Ra=0.29 μm and 200 GU. The study also presentsresults of tests related to the removal of nickel and chromium compounds from used industrialbaths.
机译:基于阳极溶解的电解(EP)不锈钢过程的目的 金属表面是提高耐腐蚀性,提高耐腐蚀性 抛光元件的表面。由于经济原因,EP流程进行了 温度为30-70˚C,同时保持浴缸的可持续性。在工业条件下 浴缸通常包括:H_3PO_4和H_2SO_4酸和有机添加剂的浓缩溶液。 硫(VI)酸确保了浴的足够电导率,而磷(V)酸主要是 负责金属表面的抛光。在EP过程中,电解浴是 富含金属(铁,铬和镍)离子,源自溶解 阳极。如果电解质已经使用了很长时间,这可能导致粗糙度增加和 电力研磨表面劣化。监测组成的变化 在工业规模允许的奥氏体不锈钢电极抛光过程中加工浴 我们确定EP流程的条件。反过来,这使得能够获得最佳质量 产品同时最大限度地减少浴室更换和处置的成本 考虑到重金属的移动形态的环境影响。 本文介绍了实验室测试的结果,考虑到长期的影响 含有H_3PO_4和H_2SO_4的浴含有表面精加工的浴的污染物 电抛光304不锈钢的蚀腐蚀。电位动力学测量是 使用Solartron Si 1287电子界面朝向饱和的Calomel电极进行。 氯化钠0.5M溶液中钢的点蚀耐腐蚀试验 即,虽然电解质被铁,铬和镍离子强烈污染,但 电抛光(工艺参数8 A / DM〜2,15分钟,55°C)没有减少蚀势, 虽然样品的粗糙度和光泽度显着降低。在EP过程之后 在没有金属离子样品的电解质中,以粗糙度为样本的特征 Ra =0.11μm和光泽955 u。另一方面,在已经电力研入的样品中 用铁(超过6质量%),铬(小于2%)和镍离子污染电解质 (小于1%),这些值分别是ra =0.29μm和200 ug。这项研究也提出了 与二手工业中除去镍和铬化合物有关的试验结果 浴。

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