Corrosion failure of Zn–Al detonator housing

Some batches of detonator housings made up of Chromium plated Zn–Al alloy were found in an extensively cracked condition after few months of storage at room temperature. An analysis of the failure showed that the cracks were due to intergranular corrosion facilitated by segregation of lead at the grain boundaries. Improper chromium plating further aggravated the corrosion problem. This failure case emphasises the need for strict control of chemical composition for components made from Zn–Al alloy and the process of Cr plating of the components.     

劣化环丁砜再生技术的工业应用

为解决国内外环丁砜抽提芳烃工艺中环丁砜的劣化问题，在不添加单乙醇胺的前提下，采用阴离子交换树脂处理劣化的环丁砜，可使系统的pH值从3．4升到5．5左右，离子交换树脂需30d左右再生一次，降低了设备的腐蚀，减少了装置的堵塞，使系统运行稳定，取得了可观的社会效益和经济效益。     

2RE69/Zr702双金属管氨汽提塔关键部件的设计与制造

介绍了2RE69／Zr702双金属管的特殊结构、优良耐蚀性能，与管板的连接接头型式及焊接工艺、管头及液体分布器加工、装配和试验。     

制盐设备用不锈钢及复合板的选材

OOCr18Ni5Mo3Si2(以下简称18－5）属铁素体（α）－奥氏体（γ）双相不锈钢，具有良好的耐Cl^-点蚀和应力腐蚀性能，18－5不锈钢复合板因其兼备优良的使用性能和较低的制造成本，在制盐领域不锈钢材料中，是理想的选择。本就OOCr18Ni5Mo3Si2双相不锈钢及复合板的性能、特点以及在制盐领域的成功事例作一介绍。     

成品油储罐内的腐蚀及防护

对成品油储罐内各部位腐蚀情况进行了介绍，说明了产生腐蚀的原因和腐蚀机理。介绍了油罐内防护技术，采用节点加固，降低边缘应力，可减缓油罐金属腐蚀速度；对选用油罐内防腐涂料的原则进行了阐述。     

牙哈采油树腐蚀检查分析及对策

介绍塔里木牙哈凝析气田高温高压井口采油树腐蚀的现象，腐蚀机理及采取的措施，对其他油田采油树腐蚀的防治起到指导借鉴作用。     

盐和水蒸气协同作用下TiAl合金腐蚀性能研究及其防护

研究了在700℃盐和水蒸气协同作用下TiAlNb合金的腐蚀行为以及溅射涂层对TiAlNb合金的防护作用。结果表明，在盐和水蒸气协同作用下，溅射TiAlCrAg涂层对TiAlNb合金具有一定的保护作用。盐和水蒸气协同作用加速了合金以及涂层的腐蚀。挥发性气体氯化物对α2相的循环作用是TiALNb合金腐蚀的主要原因。涂层中较少的α2相以及Laves相中较高的Cr含量是腐蚀有所减缓的主要原因。     

铸造高性能合金的显微组织及耐腐蚀行为

对铸造高性能合金Lewmet55进行了化学成分设计，确定了该合金中镍、铬、钼、铜和硅的含量。采用金相显微镜和X射线衍射相结合的方法，分析了该合金的显微组织，并采用多种腐蚀试验方法研究其耐腐蚀行为。着重研究了不同热处理制度对铸造高性能合金的均匀腐蚀、晶问腐蚀、点蚀和电化学腐蚀性能的影响。试验结果表明，Lewment55合金经1250℃×1．5h水冷固溶处理后，在高温浓硫酸介质中具有良好的耐蚀性，以及较好的抗晶间腐蚀、点蚀和电化学腐蚀性能。     

Theoretical and experimental evaluation of the limit state of transit gas pipelines having corrosion defects

The limit carrying capacity of gas pipelines having corrosion defects were evaluated by means of an improved FEM analysis, together with the ANSI/ASME defect judgement and an experimental verification. When compared with our past presentation at the proceedings of the CAPE'93 Colloquium (dealing with reproduced defects), this paper evaluates the remaining lifetime of a pipeline having natural faults. The new improved analysis includes geometrical nonlinearities leading to a modification of limit state parameters and thus matching better with actuality. This presented work was initiated by the firm of Trans-Gas in Prague after having had a pipeline inspected proving some parts of it as being heavily corroded. The task in hand was to determine the remaining pipeline lifetime with the view to at least a two-year period.     

Application of substituted N-arylpyrroles in the corrosion protection of aluminium in hydrochloric acid

The inhibiting action of N-arylpyrroles on aluminium in 0.17 mol dm^–3 hydrochloric acid solution, in the temperature range 20–60 °C, was studied using potentiodynamic and electrochemical impedence spectroscopy techniques. The inhibiting efficiency of both investigated compounds 1-(2-fluorophenyl)-2,5-dimethylpyrrole (compound A) and 1-(2-fluorophenyl)-2,5-dimethylpyrrole-3-carbaldehyde (compound B) slightly increases with increasing temperature of the corrosive solution. Inhibitor adsorption on the elecrode surface decreases the apparent activation energy of the hydrogen evolution reaction. Compound A follows the Temkin adsorption isotherm, while its carbaldehyde derivative follows the Langmuir isotherm. The results of the apparent energy of activation and the standard free energy of adsorption point to stronger chemisorption of the compound A. However, due to additional condensation of molecules with carbaldehyde groups on the electrode surface, the carbaldehyde derivative exhibits even better inhibiting efficiency than compound A. The kinetic corrosion parameters, analysed in terms of the impedance data, show a satisfactory agreement with those obtained by the potentiodynamic method.