2017
DOI: 10.2298/jmmb170425015p
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Electrochemical corrosion of Al-Pd alloys in HCl and NaOH solutions

Abstract: The corrosion performance of as-solidified Al-Pd alloys in HCl and NaOH aqueous solutions is investigated in this work. Four different alloys (Al 88 Pd 12 , Al 77 Pd 23 , Al 72 Pd 28 and Al 67 Pd 33 , element concentrations are given in at.%) were prepared from high purity Al and Pd lumps by arc-melting in Ar. Subsequently, the alloy microstructure and phase occurrence were investigated by a combination of scanning electron microscopy and room-temperature powder X-ray diffraction. The assolidified Al-Pd alloys… Show more

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Cited by 11 publications
(13 citation statements)
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“…In addition, due to changes in pH and Cl − ion concentration in the corrosion solution [3,4], the i corr of the siloxane sealing PEO coating increased, and the E corr and R p decreased, as the concentration of the solution increased. The reason for this change is that the corrosion solution passed through the micro defects of the siloxane layer, causing the layer to crack.…”
Section: Potentiodynamic Polarization Analysismentioning
confidence: 99%
See 1 more Smart Citation
“…In addition, due to changes in pH and Cl − ion concentration in the corrosion solution [3,4], the i corr of the siloxane sealing PEO coating increased, and the E corr and R p decreased, as the concentration of the solution increased. The reason for this change is that the corrosion solution passed through the micro defects of the siloxane layer, causing the layer to crack.…”
Section: Potentiodynamic Polarization Analysismentioning
confidence: 99%
“…Aluminum alloys are widely used in many engineering applications due to their superior performance. But in corrosive environments such as humid, acidic, and alkaline environments, aluminum alloys are prone to corrosion [1][2][3][4]. To protect or mitigate corrosion processes, protective coatings are typically applied to metal surfaces.…”
Section: Introductionmentioning
confidence: 99%
“…Each layer is considered as a uniform material with the thermal conductivities of λ 1 , λ 2 and λ 3 , respectively. Then, the total thermal resistance of the three-layer cylindrical walls is (12) (5) Heat transfer of the BFG pipelines (a) for single-phase heat transfer section The convective heat transfer from the BFG to the inner wall of the pipelines is (13) where l 1 is the length of the single-phase section [m], T and t 1 are the mean temperature of BFG and the inner wall of the single-phase section [K], respectively.…”
Section: Heat Transfer Modelmentioning
confidence: 99%
“…The conductive heat transfer through the threelayer cylindrical walls is (14) The convective heat transfer from the outer of the pipelines to the surroundings is (15) For simplicity, the whole heat transfer process is considered as a steady-state process, then (16) From Eqs. (13) to (16), the heat transfer is written as (17) (b) for condensation heat transfer section The convective heat transfer from the BFG to the inner wall of the pipeline is (18) where l 1 is the length of the condensation section [m], and the superscript ′ represents the parameter at the condensation heat transfer section. The conductive heat transfer through the threelayer cylindrical walls is (19) The convective heat transfer from the outer of the pipelines to the surroundings is (20) Also, (21) From Eqs.…”
Section: Heat Transfer Modelmentioning
confidence: 99%
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