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采用模拟闭塞电池法和模拟闭塞区溶液法,测定了0Cr18Ni9 奥氏体不锈钢(304 SS)在0.5 mol·L-1 NaCl(pH=7)以及A3钢在0.01 mol·L-1 NaCl(pH=12)两种体系,孔蚀的不同阶段孔内外间电流的换向电位ET.结果表明,E T值随闭塞区溶液组成的变化而变化,但存在一个范围.将304不锈钢的ET值与用 孔蚀滞后环法在不同扫描速度,不同回扫电流时所测得的孔蚀保护电位EP值作比较, 发现EP值范围处于ET值范围之内.ET值可以为孔蚀阴极保护电位参数的 确定提供依据.

Two methodssimulated occluded cell and simulated occluded solutionhave been developed to determine the protection potential aga inst pitting of A3 steel and 0Cr18Ni9 stainless steel.They are based on the theo ry that the pitting protection potential(EP) is actually the transition po tential of the direction of current between the occluded cell and the external s urface(ET).The ET of 304 SS in 0.5 mol·L-1 NaCl solution is in the range of 220 mV to 440 mV(SCE), the ET of A3 steel in 0.01 mol ·L-1 NaCl solution(pH=12) is in the range of 390~670 mV, the lowest of which can be considered as cathode protection potential(EP).The E P of 304 SS determined with “cyclic” potentiodynamic polarization method is included in the ET with above methods.As for electrochemical protection ag ainst pitting, if the potential of the external surface is controlled below the EP,the activepassive transition will occur inside the occluded cell, so the pitting will be stifled.

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