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how much do transport processes contribute to electrochemical kinetics measurements? |
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transport processes are based on __ |
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hydrodynamics is described with what type of mathematics? |
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in eqn 7.1, Ji = -Di*grad(ci) - [zi*F/(R*T)]Di*ci*grad(phi) + ci*v
the first term represents __ |
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in eqn 7.1, Ji = -Di*grad(ci) - [zi*F/(R*T)]Di*ci*grad(phi) + ci*v
the second term represents __ |
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in eqn 7.1, Ji = -Di*grad(ci) - [zi*F/(R*T)]Di*ci*grad(phi) + ci*v
the third term represents __ |
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define potentiostatic regime |
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current-time dependence at constant potential |
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current measurements in the potentiostatic regime can be used to find what 3 things? |
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diffusion layer thickness time dependence of diffusion layer thickness
diffusion coeff. of electrochemically active species |
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define galvanostatic regime |
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current-time dependence at constant current |
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two key equations for transport processes in electrochem. systems are the __ and __ |
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flux vector eqn
molar conc. vs time eqn |
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in order to set up a constant potential so that current density vs. time can be measured, what is needed? |
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a 3-electrode system and a potentiostat |
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under a galvanostatic regime and when the charge-transfer reaction is fast, the conc. gradient at the electrode surface is __ |
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time to achieve 0 concentration at the electrode surface |
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list 2 ways that galvanostatic measurements can be used |
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1. to define the diffusion coeff. if bulk concentration is known
2. as an analytical tool to measure concentration of the electrochemically active species if the diffusion coeff. is known |
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galvanostatic measurements can be used to define the diffusion coeff. if... |
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bulk concentration is known |
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galvanostatic measurements can be used as an analytical tool to measure concentration of the electrochemically active species if... |
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the diffusion coeff. is known |
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name 2 ways electrochemical processes can be influenced |
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by mass transport due to diffusion
by convection |
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in eqn 7.7, (∂ci/∂t) = -Di*Lap^2*ci - v*grad(ci)
the first term represents __ |
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in eqn 7.7, (∂ci/∂t) = -Di*Lap^2*ci - v*grad(ci)
the second term represents __ |
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for eqn 7.7, (∂ci/∂t) = -Di*Lap^2*ci - v*grad(ci)
it is assumed that when convection in the electrochemical cell is changed, the Nernst diffusion layer is changed or unchanged? |
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cell current depends on hydrodynamics because... |
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when convection in the electrochemical cell is changed, the Nernst diffusion layer is also changed |
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as the intensity of mixing increases, the length of the diffusion layer |
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decreases (more intensive mixing = smaller diffusion layer) |
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Prandtl layer thickness pertains to velocity of solution or to concentration of the electrochemically active species? |
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Nernst diffusion layer thickness pertains to velocity of solution or to concentration of the electrochemically active species? |
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concentration of the electrochemically active species |
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at the distance below the Prandtl layer thickness, what happens to velocity of the solution? |
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velocity begins to drop, reaching zero at the electrode surface |
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at the distance below the Nernst diffusion layer thickness, what happens to concentration of the electrochemically active species? |
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concentration begins to drop, reaching zero at the electrode surface |
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which typically represents a greater distance from the electrode surface, Prandtl layer thickness or Nernst diffusion layer thickness? |
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which typically drops faster when approaching the electrode surface, velocity of the solution or the concentration of the electrochemically active species? |
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concentration of the electrochemically active species |
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when solution current is parallel to the electrode surface and perpendicular to the diffusion direction... |
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1. Nernst diffusion layer thickness is changing with the length of the electrode
2. the electrode is not equally accessible in the direction of the solution flow |
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for most systems, if there is mixing of the solution, the Nerst diffusion layer thickness is __ |
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one of the systems where the Nerst diffusion layer thickness is precisely defined is __ |
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what is the main feature of the RDE? |
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it is equally accessible at all points on the electrode surface |
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for the RDE, Nernst diffusion layer thickness depends on what 3 things? |
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1. diffusion coeff. of the electrochemically active species
2. viscosity and density of the solution 3. rotation rate of the RDE |
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for the RDE, the limiting current density can be calculated if... |
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the bulk concentration of the electrochemically active species is known |
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for the RDE, as angular velocity (and hence the rotation rate) of the electrode increases, limiting current density __ |
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increases
(high ang. velocity = high jlim) |
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for the RDE, if you plot limiting current vs. the square root of angular velocity, the shape of the line is __ |
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a straight line that goes through the origin |
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for the RDE, calculating the limiting current density at infinite angular velocity is possible or impossible? |
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for the RDE, when angular velocity is infinite, the Nernst diffusion layer thickness equals __ |
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at high overpotentials, the limiting current... |
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is entirely determined by transport processes and is therefore independent of potential |
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what kind of cell should be used with the RDE? |
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to get high quality data, the RDE should be __ |
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to study the electrochemical kinetics of a redox reaction, out of what material should the RDE ideally be made? |
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platinum
(other materials *can* be used if clean and polished, but Pt is best) |
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for the RDE, the current density at infinite angular velocity can be used with what equation to calculate exchange current density and symmetry coefficients for the RDE electrochemical reaction? |
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