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Series: ASM Handbook Archive
Volume: 10
Publisher: ASM International
Published: 01 January 1986
DOI: 10.31399/asm.hb.v10.a0001744
EISBN: 978-1-62708-178-8
... Abstract Controlled-potential coulometry is a highly precise and accurate method primarily used for major constituent analysis of analyte substances such as alloys, compounds, nonmetallic materials and organic compounds. This article illustrates the apparatus required for controlled-potential...
Abstract
Controlled-potential coulometry is a highly precise and accurate method primarily used for major constituent analysis of analyte substances such as alloys, compounds, nonmetallic materials and organic compounds. This article illustrates the apparatus required for controlled-potential coulometry, and provides information on its techniques and applications. It contains a table that lists the metals for which accurate methods have been developed and the basic electrochemistry of the procedures. The article explains that gold and uranium are the elements that are determined frequently in various sample types.
Series: ASM Handbook
Volume: 13A
Publisher: ASM International
Published: 01 January 2003
DOI: 10.31399/asm.hb.v13a.a0003592
EISBN: 978-1-62708-182-5
... Abstract Electrode potential is a key parameter in the thermodynamic and kinetic processes that drive aqueous corrosion. This article discusses the complexities associated with measuring electrode potential and explains where and how to use reference electrodes to improve measurement accuracy...
Abstract
Electrode potential is a key parameter in the thermodynamic and kinetic processes that drive aqueous corrosion. This article discusses the complexities associated with measuring electrode potential and explains where and how to use reference electrodes to improve measurement accuracy. It describes a three-electrode approach that compensates for measurement error stemming from nonequilibrium conditions. It also examines electrode materials and behaviors and offers insights on selection and operating conditions.
Series: ASM Handbook
Volume: 13A
Publisher: ASM International
Published: 01 January 2003
DOI: 10.31399/asm.hb.v13a.a0003580
EISBN: 978-1-62708-182-5
... Abstract A potential pH diagram is a graphical representation of the relations, derived from the Nernst equation, between the pH and the equilibrium potentials (E) of the most probable electrochemical reactions occurring in a solution containing a specific element. This article describes three...
Abstract
A potential pH diagram is a graphical representation of the relations, derived from the Nernst equation, between the pH and the equilibrium potentials (E) of the most probable electrochemical reactions occurring in a solution containing a specific element. This article describes three types of reactions for calculation and construction of E-pH diagrams: electrochemical reactions of pure charge (electron) transfer; reactions involving both electron and solvated proton transfer; and acid-base reactions of pure solvated proton transfer. It illustrates the practical use of E-pH diagrams for temperature aqueous solutions and adsorbed species and in prediction of corrosion of nickel and copper.
Series: ASM Handbook
Volume: 24A
Publisher: ASM International
Published: 30 June 2023
DOI: 10.31399/asm.hb.v24A.a0006991
EISBN: 978-1-62708-439-0
... Abstract To improve the performance of additive manufacturing (AM) systems, a critical need exists for collaborative generation, acquisition, curation, and analysis of digital AM data across the product life cycle. This article discusses the history, development, and potential benefits...
Abstract
To improve the performance of additive manufacturing (AM) systems, a critical need exists for collaborative generation, acquisition, curation, and analysis of digital AM data across the product life cycle. This article discusses the history, development, and potential benefits of the AM Common Data Dictionary (AM-CDD), along with future directions.
Series: ASM Handbook
Volume: 13A
Publisher: ASM International
Published: 01 January 2003
DOI: 10.31399/asm.hb.v13a.a0003579
EISBN: 978-1-62708-182-5
... Abstract The electrode potential is one of the most important parameters in the thermodynamics and kinetics of corrosion. This article discusses the fundamentals of electrode potentials and illustrates the thermodynamics of chemical equilibria by using the hydrogen potential scale...
Abstract
The electrode potential is one of the most important parameters in the thermodynamics and kinetics of corrosion. This article discusses the fundamentals of electrode potentials and illustrates the thermodynamics of chemical equilibria by using the hydrogen potential scale and the Nernst equation. It describes galvanic cell reactions and corrosion reactions in an aqueous solution in an electrochemical cell. The article explores the most common cathodic reactions encountered in metallic corrosion in aqueous systems. The reactions included are proton reduction, water reduction, reduction of dissolved oxygen, metal ion reduction, and metal deposition. The article also presents the standard equilibrium potentials measured at 25 deg C relative to a standard hydrogen electrode for various metal-ion electrodes in a tabular form.
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Published: 30 September 2015
Fig. 2 Potential of 1 and 10 –3 molar metal solutions and hydrogen potential at varying pH at 25 °C (75 °F). Source: Ref 2
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Published: 01 January 2006
Fig. 23 Map of potential variations. (a) Low potential variation with relatively negative potentials indicates very low oxygen availability and little corrosion. (b) Abrupt variation in potential indicates corrosion activity.
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in Potential Measurements with Reference Electrodes
> Corrosion: Fundamentals, Testing, and Protection
Published: 01 January 2003
Fig. 5 The potential decay at current interruption. IR is the potential drop due to the electrolyte ohmic resistance.
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in Methods for Determining Aqueous Corrosion Reaction Rates
> Corrosion: Fundamentals, Testing, and Protection
Published: 01 January 2003
Fig. 1 Application of mixed-potential theory showing the electrochemical potential-current relationship for a corroding system consisting of a single charge-transfer-controlled cathodic reaction and charge-transfer-controlled anodic electrochemical reaction. β c and β a are Tafel slopes
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in Methods for Determining Aqueous Corrosion Reaction Rates
> Corrosion: Fundamentals, Testing, and Protection
Published: 01 January 2003
Fig. 2 Application of mixed-potential theory showing the electrochemical potential-current relationship for a corroding system consisting of a mass-transport-controlled cathodic reaction and a charge-transfer-controlled anodic reaction. As the fluid velocity increases from 1 to 4
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in Introduction to Corrosion for Constructive Purposes
> Corrosion: Fundamentals, Testing, and Protection
Published: 01 January 2003
Fig. 3 Potential versus log current plot relating overpotential to potential scale for anodic and cathodic reactions. M is a metal, and n is a positive integer.
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Published: 01 January 2003
Fig. 9 Effects of applied potential and corrosion potential on the pitting- and crevice-corrosion initiation time for alloy 825 in 1000 ppm Cl − at 95 °C (203 °F). Note that at and below the repassivation potential, E rp no initiation occurs out to at least three years. Source: Ref 39
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Published: 01 January 1986
Fig. 6 Fundamentals of cyclic voltammetry. (a) Symmetrical saw-tooth potential-time variation used in cyclic voltammetry. (b) Corresponding cyclic voltammogram expected for a near-reversible system. The greater the separation between the peaks for forward and reverse scans, the more
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Published: 01 January 1986
Fig. 3 Classical cell types. (a) Constant current (top) and controlled potential (bottom) cells. (b) Cell for constant current electrolysis with mercury cathode. Source: Ref 10
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Published: 01 January 1986
Fig. 4 Automatic potentiostat for controlled-potential analysis. The cell emf may be varied automatically using this type of device. Source: Ref 11
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Published: 01 January 1986
Fig. 2 Completeness of reaction as a function of potential for the reversible reduction of a metal ion species to another soluble species. E is the control potential required for 99.9% conversion of M(m) to M(m−n).
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Published: 01 January 1986
Fig. 7 Potential energy of an outer electron in an image gas atom near the sample surface in the presence of a high field.
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Published: 01 January 1986
Fig. 8 Potential-energy diagram illustrating field evaporation.
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Published: 01 January 1987
Fig. 52 Effect of electrochemical potential on the stress-corrosion fracture path in a cold-worked AISI C-1018 low-carbon steel with a 0.2% offset yield strength of 63 MPa (9 ksi). The steel was tested in a 92- °C (198- °F) aqueous 33% sodium hydroxide solution. At a potential of E = −0.76 V
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