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Quantitative Approach for Determining the Critical Volume Fraction for the Transition from Internal to External Oxidation

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Abstract

A theoretical approach is presented to calculate the critical volume fraction f * v for the transition from internal to external oxidation. The focus was on the evolution of internal-oxide volume fraction during the initial stage of oxidation. An equation to calculate f * v was developed by considering an effective diffusion coefficient of oxygen in the alloy (D eff O ) which takes into account the evolving blocking effect by forming internal oxide precipitates. Based on this physical process, three types of oxidation behavior can result, depending on the properties of the alloy and exposure atmosphere. Further discussions on the remaining discrepancy between predicted and experimentally-determined f * v values are provided for refinement on the theoretical prediction of this parameter.

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Notes

  1. Wagner and other treatment have used other notations for this critical volume fraction but they are physically the same.

References

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Acknowledgments

This work was funded by the Cross-Cutting Technologies Program at the National Energy Technology Laboratory, managed by Susan Maley (Technology Manager) and Charles Miller (Technical Monitor). The Research was executed through NETL Office of Research and Development’s Innovative Process Technologies (IPT) Field Work Proposal. This work was financially supported at the University of Pittsburgh by NETL through the RES Contract No. DE-FE00400.

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This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United States Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof.

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Correspondence to Wei Zhao.

Appendices

Appendix 1

Determining volume fraction (f v ) from mole fraction (N BOv )

$$\begin{gathered} f_{v}^{'} = \frac{{V_{{BO_{\upsilon } }} }}{{V_{{BO_{\upsilon } }} + V_{matrix} }}\;where\;V_{i} \;is\;volume\;of\;i \hfill \\ = \frac{{n_{{BO_{\upsilon } }} V_{m}^{oxide} }}{{n_{{BO_{\upsilon } }} V_{m}^{oxide} + (n_{total} - n_{{BO_{\upsilon } }} )V_{m}^{alloy} }}\;where\;n_{i} \;is\;mole\;of\;i \hfill \\ = \frac{1}{{1 + \left( {\frac{{n_{total} }}{{n_{{BO_{\upsilon } }} }} - 1} \right)\frac{{V_{m}^{alloy} }}{{V_{m}^{{BO_{\upsilon } }} }}}}\;note\;that\;\frac{{n_{{BO_{v} }} }}{{n_{total} }} = N_{{BO_{v} '}} \hfill \\ = \frac{{V_{m}^{{BO_{\upsilon } }} /V_{m}^{alloy} }}{{V_{m}^{{BO_{\upsilon } }} /V_{m}^{alloy} + \left[ {\frac{{\pi N_{O}^{S} D_{O} }}{{\nu D_{B} (N_{B}^{0} )^{2} }}\frac{{1 - f_{v} }}{{2 + f_{v} }} - 1} \right]}} \hfill \\ = \frac{{V_{m}^{{BO_{\upsilon } }} /V_{m}^{alloy} }}{{V_{m}^{{BO_{\upsilon } }} /V_{m}^{alloy} + \left[ {Z\frac{{1 - f_{v} }}{{2 + f_{v} }} - 1} \right]}} \hfill \\ \end{gathered}$$

where V oxide m , V alloy m are molar volumes of BOν and alloy and \(Z \equiv \frac{{\pi N_{O}^{S} D_{O} }}{{vD_{B} \left( {N_{B}^{0} } \right)^{2} }}\)

Appendix 2

Mathematical derivation to determine f * v (after Leblond [6]).

Letting f v  = f v, the Eq. (12) becomes:

$$f_{v} = \frac{{V_{m}^{oxide} /V_{m}^{alloy} }}{{V_{m}^{oxide} /V_{m}^{alloy} + \left[ {Z\frac{{1 - f_{v} }}{{2{ + }f_{v} }} - 1} \right]}}$$

This can be converted to a quadratic equation:

$$\left( {R - Z - 1} \right) \cdot f_{v}^{2} + \left( {R + Z - 2} \right)f_{v} - 2R = 0$$
(15)

where R = V oxide m /V alloy m .

For the critical transition point, the quadratic equation has a unique solution, which means the discriminant is zero:

$$\varDelta = \left( {R + Z - 2} \right)^{2} + 8R\left( {R - Z - 1} \right) = 0$$

From that, we can determine Z as a function of R:

$$Z_{1} = 3R + 2 + 2\sqrt {6R}\; {\text{or}}\; Z_{2} = 3R + 2 - 2\sqrt {6R}$$

When the quadratic Eq. (15) has a double solution, this solution is

$$f_{v} = - \frac{R + Z - 2}{{2\left( {R - Z - 1} \right)}}$$
(16)

Substituting Z 1 into the Eq. (16), it is found that f v is negative, which is not realistic for a volume fraction.

Therefore, the only solute is obtained by substituting Z 2 into Eq. (16), which is:

$$\begin{gathered} f_{v}^{*} = \frac{{2\sqrt {V_{m}^{oxide} /V_{m}^{alloy} } }}{{\sqrt 6 + 2\sqrt {V_{m}^{oxide} /V_{m}^{alloy} } }} \hfill \\ \hfill \\ \end{gathered}$$

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Zhao, W., Kang, Y., Orozco, J.M.A. et al. Quantitative Approach for Determining the Critical Volume Fraction for the Transition from Internal to External Oxidation. Oxid Met 83, 187–201 (2015). https://doi.org/10.1007/s11085-014-9516-1

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