<p>Thermodynamic models are employed to describe the equilibrium between nonstoichiometric carbonitride and the Fe-based solid solution. The solubility of fcc Ti and fcc V in the Fe-based solid solution was developed separately. Values for four thermodynamic interaction parameters of the nonstoichiometric carbonitride were determined using equilibrium equations, by comparing the calculated results with previously published experimental data. Specific solubility product expressions for <InlineEquation ID="IEq1"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq1.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="56" /> </InlineMediaObject> <EquationSource Format="TEX">\({\text{TiC}}_{x}{\text{N}}_{y}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mtext>TiC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> </math></EquationSource> </InlineEquation> and <InlineEquation ID="IEq2"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq2.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="51" /> </InlineMediaObject> <EquationSource Format="TEX">\({\text{VC}}_{x}{\text{N}}_{y}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mtext>VC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> </math></EquationSource> </InlineEquation> in austenite (containing Mn, Ni, Cr, and Mo as solid solution elements) and ferrite (containing Mn and Ni as solid solution elements) were then developed. The calculated results in this study show good agreement with both calculated results from ThermoCalc and experimental data from earlier references, demonstrating their reliability. The developed solubility products of <InlineEquation ID="IEq3"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq1.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="56" /> </InlineMediaObject> <EquationSource Format="TEX">\({\text{TiC}}_{x}{\text{N}}_{y}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mtext>TiC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> </math></EquationSource> </InlineEquation> and <InlineEquation ID="IEq4"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq2.gif" Format="GIF" Height="19" Rendition="HTML" Resolution="72" Type="Linedraw" Width="51" /> </InlineMediaObject> <EquationSource Format="TEX">\({\text{VC}}_{x}{\text{N}}_{y}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mtext>VC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> </math></EquationSource> </InlineEquation> are as follows (solubility products of <InlineEquation ID="IEq5"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq5.gif" Format="GIF" Height="14" Rendition="HTML" Resolution="72" Type="Linedraw" Width="30" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{TiC}\)</EquationSource> <EquationSource Format="MATHML"><math> <mtext>TiC</mtext> </math></EquationSource> </InlineEquation>, <InlineEquation ID="IEq6"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq6.gif" Format="GIF" Height="14" Rendition="HTML" Resolution="72" Type="Linedraw" Width="30" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{TiN}\)</EquationSource> <EquationSource Format="MATHML"><math> <mtext>TiN</mtext> </math></EquationSource> </InlineEquation>, <InlineEquation ID="IEq7"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq7.gif" Format="GIF" Height="14" Rendition="HTML" Resolution="72" Type="Linedraw" Width="25" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{VC}\)</EquationSource> <EquationSource Format="MATHML"><math> <mtext>VC</mtext> </math></EquationSource> </InlineEquation>, and <InlineEquation ID="IEq8"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq8.gif" Format="GIF" Height="14" Rendition="HTML" Resolution="72" Type="Linedraw" Width="26" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{VN}\)</EquationSource> <EquationSource Format="MATHML"><math> <mtext>VN</mtext> </math></EquationSource> </InlineEquation> can be referenced from our previous work).</p><p><InlineEquation ID="IEq9"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq9.gif" Format="GIF" Height="23" Rendition="HTML" Resolution="72" Type="Linedraw" Width="1165" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{log}{^{\alpha /\upgamma }K}_{{\text{TiC}}_{ x}{\text{N}}_{y}}=x\text{log}{^{\alpha /\upgamma }K}_{\text{TiC}}+y\text{log}{^{\alpha /\upgamma }K}_{\text{TiN}}+\left(1-x-y\right)\text{log}{^{\alpha /\upgamma }K}_{\text{Ti}}+x\text{log}x+y\text{log}y+\left(1-x-y\right)\text{log}\left(1-x-y\right)+xy\frac{121}{T}-x\left(1-x-y\right)\frac{4709}{T}-y\left(1-x-y\right)\frac{2093}{T},\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mrow> <msub> <mtext>TiC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> <mrow /> </mmultiscripts> <mo>=</mo> <mi>x</mi> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>TiC</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mi>y</mi> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>TiN</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>Ti</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mi>x</mi> <mtext>log</mtext> <mi>x</mi> <mo>+</mo> <mi>y</mi> <mtext>log</mtext> <mi>y</mi> <mo>+</mo> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mtext>log</mtext> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mo>+</mo> <mi>x</mi> <mi>y</mi> <mfrac> <mn>121</mn> <mi>T</mi> </mfrac> <mo>-</mo> <mi>x</mi> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mfrac> <mn>4709</mn> <mi>T</mi> </mfrac> <mo>-</mo> <mi>y</mi> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mfrac> <mn>2093</mn> <mi>T</mi> </mfrac> <mo>,</mo> </mrow> </math></EquationSource> </InlineEquation></p><p><InlineEquation ID="IEq10"> <InlineMediaObject> <ImageObject Color="BlackWhite" FileRef="11663_2025_3621_Article_IEq10.gif" Format="GIF" Height="23" Rendition="HTML" Resolution="72" Type="Linedraw" Width="1140" /> </InlineMediaObject> <EquationSource Format="TEX">\(\text{log}{^{\alpha /\upgamma }K}_{{\text{VC}}_{ x}{\text{N}}_{y}}=x\text{log}{^{\alpha /\upgamma }K}_{\text{VC}}+y\text{log}{^{\alpha /\upgamma }K}_{\text{VN}}+\left(1-x-y\right)\text{log}{^{\alpha /\upgamma }K}_{\text{V}}+x\text{log}x+y\text{log}y+\left(1-x-y\right)\text{log}\left(1-x-y\right)+xy\frac{13}{T}-x\left(1-x-y\right)\frac{3663}{T}-y\left(1-x-y\right)\frac{2093}{T}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mrow> <msub> <mtext>VC</mtext> <mi>x</mi> </msub> <msub> <mtext>N</mtext> <mi>y</mi> </msub> </mrow> <mrow /> </mmultiscripts> <mo>=</mo> <mi>x</mi> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>VC</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mi>y</mi> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>VN</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mtext>log</mtext> <mmultiscripts> <mrow> <mmultiscripts> <mrow /> <mrow /> <mrow> <mi>α</mi> <mo stretchy="false">/</mo> <mi mathvariant="normal">γ</mi> </mrow> </mmultiscripts> <mi>K</mi> </mrow> <mtext>V</mtext> <mrow /> </mmultiscripts> <mo>+</mo> <mi>x</mi> <mtext>log</mtext> <mi>x</mi> <mo>+</mo> <mi>y</mi> <mtext>log</mtext> <mi>y</mi> <mo>+</mo> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mtext>log</mtext> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mo>+</mo> <mi>x</mi> <mi>y</mi> <mfrac> <mn>13</mn> <mi>T</mi> </mfrac> <mo>-</mo> <mi>x</mi> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mfrac> <mn>3663</mn> <mi>T</mi> </mfrac> <mo>-</mo> <mi>y</mi> <mfenced close=")" open="("> <mn>1</mn> <mo>-</mo> <mi>x</mi> <mo>-</mo> <mi>y</mi> </mfenced> <mfrac> <mn>2093</mn> <mi>T</mi> </mfrac> </mrow> </math></EquationSource> </InlineEquation>.</p>

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Solubility Products of Nonstoichiometric Titanium Carbonitride and Vanadium Carbonitride in Steels: Thermodynamic Calculations

  • Li Sun,
  • Deng-Bang Gao,
  • Hai-Tao Jian,
  • Xuan-Wei Lei,
  • Min Liu,
  • Chao-Bin Lai

摘要

Thermodynamic models are employed to describe the equilibrium between nonstoichiometric carbonitride and the Fe-based solid solution. The solubility of fcc Ti and fcc V in the Fe-based solid solution was developed separately. Values for four thermodynamic interaction parameters of the nonstoichiometric carbonitride were determined using equilibrium equations, by comparing the calculated results with previously published experimental data. Specific solubility product expressions for \({\text{TiC}}_{x}{\text{N}}_{y}\) TiC x N y and \({\text{VC}}_{x}{\text{N}}_{y}\) VC x N y in austenite (containing Mn, Ni, Cr, and Mo as solid solution elements) and ferrite (containing Mn and Ni as solid solution elements) were then developed. The calculated results in this study show good agreement with both calculated results from ThermoCalc and experimental data from earlier references, demonstrating their reliability. The developed solubility products of \({\text{TiC}}_{x}{\text{N}}_{y}\) TiC x N y and \({\text{VC}}_{x}{\text{N}}_{y}\) VC x N y are as follows (solubility products of \(\text{TiC}\) TiC , \(\text{TiN}\) TiN , \(\text{VC}\) VC , and \(\text{VN}\) VN can be referenced from our previous work).

\(\text{log}{^{\alpha /\upgamma }K}_{{\text{TiC}}_{ x}{\text{N}}_{y}}=x\text{log}{^{\alpha /\upgamma }K}_{\text{TiC}}+y\text{log}{^{\alpha /\upgamma }K}_{\text{TiN}}+\left(1-x-y\right)\text{log}{^{\alpha /\upgamma }K}_{\text{Ti}}+x\text{log}x+y\text{log}y+\left(1-x-y\right)\text{log}\left(1-x-y\right)+xy\frac{121}{T}-x\left(1-x-y\right)\frac{4709}{T}-y\left(1-x-y\right)\frac{2093}{T},\) log α / γ K TiC x N y = x log α / γ K TiC + y log α / γ K TiN + 1 - x - y log α / γ K Ti + x log x + y log y + 1 - x - y log 1 - x - y + x y 121 T - x 1 - x - y 4709 T - y 1 - x - y 2093 T ,

\(\text{log}{^{\alpha /\upgamma }K}_{{\text{VC}}_{ x}{\text{N}}_{y}}=x\text{log}{^{\alpha /\upgamma }K}_{\text{VC}}+y\text{log}{^{\alpha /\upgamma }K}_{\text{VN}}+\left(1-x-y\right)\text{log}{^{\alpha /\upgamma }K}_{\text{V}}+x\text{log}x+y\text{log}y+\left(1-x-y\right)\text{log}\left(1-x-y\right)+xy\frac{13}{T}-x\left(1-x-y\right)\frac{3663}{T}-y\left(1-x-y\right)\frac{2093}{T}\) log α / γ K VC x N y = x log α / γ K VC + y log α / γ K VN + 1 - x - y log α / γ K V + x log x + y log y + 1 - x - y log 1 - x - y + x y 13 T - x 1 - x - y 3663 T - y 1 - x - y 2093 T .