<p>Hydrogen–oxygen torch igniters are widely used to promote ignition and flame holding during high-speed propulsion. However, the coupled internal reaction flow and solid heat conduction processes that govern their thermal limits remain insufficiently quantified. We developed a conjugate framework that couples a one-dimensional plug-flow reactor for gas-phase H<InlineEquation ID="IEq1"> <EquationSource Format="TEX">\(_2\)</EquationSource> <EquationSource Format="MATHML"><math> <mmultiscripts> <mrow /> <mn>2</mn> <mrow /> </mmultiscripts> </math></EquationSource> </InlineEquation>/O<InlineEquation ID="IEq2"> <EquationSource Format="TEX">\(_2\)</EquationSource> <EquationSource Format="MATHML"><math> <mmultiscripts> <mrow /> <mn>2</mn> <mrow /> </mmultiscripts> </math></EquationSource> </InlineEquation> chemistry with an axisymmetric transient heat conduction model of a noncooled copper micro-rocket torch. The inner/outer wall boundary conditions account for gas-to-wall convection, external natural convection, and radiation. The solver was verified against the analytical solution for an infinitely long cylinder with convective cooling, yielding a small and decaying RMSE (<InlineEquation ID="IEq3"> <EquationSource Format="TEX">\(\sim 10^{-2}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mo>∼</mo> <msup> <mn>10</mn> <mrow> <mo>-</mo> <mn>2</mn> </mrow> </msup> </mrow> </math></EquationSource> </InlineEquation>–<InlineEquation ID="IEq4"> <EquationSource Format="TEX">\(10^{-3}\)</EquationSource> <EquationSource Format="MATHML"><math> <msup> <mn>10</mn> <mrow> <mo>-</mo> <mn>3</mn> </mrow> </msup> </math></EquationSource> </InlineEquation>), which supports the fidelity of temporal/spatial discretization and boundary implementation. Simulations at <InlineEquation ID="IEq5"> <EquationSource Format="TEX">\(\phi =1.14\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mi>ϕ</mi> <mo>=</mo> <mn>1.14</mn> </mrow> </math></EquationSource> </InlineEquation> show post-ignition chamber temperatures near <InlineEquation ID="IEq6"> <EquationSource Format="TEX">\(3100~\textrm{K}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mn>3100</mn> <mspace width="3.33333pt" /> <mtext>K</mtext> </mrow> </math></EquationSource> </InlineEquation> and near-exit temperatures that decrease with increasing internal heat-transfer coefficient <InlineEquation ID="IEq7"> <EquationSource Format="TEX">\(h_{\textrm{inner}}\)</EquationSource> <EquationSource Format="MATHML"><math> <msub> <mi>h</mi> <mtext>inner</mtext> </msub> </math></EquationSource> </InlineEquation> [50–500 W/(m<InlineEquation ID="IEq8"> <EquationSource Format="TEX">\(^2 \cdot\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mmultiscripts> <mrow /> <mrow /> <mn>2</mn> </mmultiscripts> <mo>·</mo> </mrow> </math></EquationSource> </InlineEquation> K)] from <InlineEquation ID="IEq9"> <EquationSource Format="TEX">\(\approx 3180\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mo>≈</mo> <mn>3180</mn> </mrow> </math></EquationSource> </InlineEquation> to <InlineEquation ID="IEq10"> <EquationSource Format="TEX">\(2930~\textrm{K}\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mn>2930</mn> <mspace width="3.33333pt" /> <mtext>K</mtext> </mrow> </math></EquationSource> </InlineEquation>. A comparison with the wall thermocouple data at 3 and 6&#xa0;cm from the tip indicates <InlineEquation ID="IEq11"> <EquationSource Format="TEX">\(h_{\textrm{inner}}\approx 100\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>h</mi> <mtext>inner</mtext> </msub> <mo>≈</mo> <mn>100</mn> </mrow> </math></EquationSource> </InlineEquation>–200 W/(m<InlineEquation ID="IEq12"> <EquationSource Format="TEX">\(^2 \cdot\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mmultiscripts> <mrow /> <mrow /> <mn>2</mn> </mmultiscripts> <mo>·</mo> </mrow> </math></EquationSource> </InlineEquation> K), which is consistent with the Nusselt-based estimates for nominally laminar flow (Re<InlineEquation ID="IEq13"> <EquationSource Format="TEX">\(_d\approx 1690\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mmultiscripts> <mrow /> <mi>d</mi> <mrow /> </mmultiscripts> <mo>≈</mo> <mn>1690</mn> </mrow> </math></EquationSource> </InlineEquation>). Despite strong internal heating, the torch temperature-rise rate remained <InlineEquation ID="IEq14"> <EquationSource Format="TEX">\(&lt;4\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mo>&lt;</mo> <mn>4</mn> </mrow> </math></EquationSource> </InlineEquation> K/s and diminished over time, implying thermal robustness for at least 15&#xa0;s of operation under the present conditions. The gas-phase radiation inside the chamber is negligible because of the small <InlineEquation ID="IEq15"> <EquationSource Format="TEX">\(p_{\mathrm {H_2O}}L\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <msub> <mi>p</mi> <mrow> <msub> <mi mathvariant="normal">H</mi> <mn>2</mn> </msub> <mi mathvariant="normal">O</mi> </mrow> </msub> <mi>L</mi> </mrow> </math></EquationSource> </InlineEquation>, whereas the external radiation becomes comparable to natural convection near <InlineEquation ID="IEq16"> <EquationSource Format="TEX">\(\sim 600\)</EquationSource> <EquationSource Format="MATHML"><math> <mrow> <mo>∼</mo> <mn>600</mn> </mrow> </math></EquationSource> </InlineEquation> K and must be included in the design. The framework enables quantitative assessment of gas–wall coupling and provides actionable guidance for selecting operating windows and material/thickness choices to balance ignition strength against structural heating in scramjet and liquid/hybrid-rocket torch igniters.</p>

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Coupled simulation of gas-phase combustion and solid heat conduction in a hydrogen–oxygen micro-rocket torch igniter

  • Shinichiro Ogawa,
  • Yuya Hirayama

摘要

Hydrogen–oxygen torch igniters are widely used to promote ignition and flame holding during high-speed propulsion. However, the coupled internal reaction flow and solid heat conduction processes that govern their thermal limits remain insufficiently quantified. We developed a conjugate framework that couples a one-dimensional plug-flow reactor for gas-phase H \(_2\) 2 /O \(_2\) 2 chemistry with an axisymmetric transient heat conduction model of a noncooled copper micro-rocket torch. The inner/outer wall boundary conditions account for gas-to-wall convection, external natural convection, and radiation. The solver was verified against the analytical solution for an infinitely long cylinder with convective cooling, yielding a small and decaying RMSE ( \(\sim 10^{-2}\) 10 - 2 \(10^{-3}\) 10 - 3 ), which supports the fidelity of temporal/spatial discretization and boundary implementation. Simulations at \(\phi =1.14\) ϕ = 1.14 show post-ignition chamber temperatures near \(3100~\textrm{K}\) 3100 K and near-exit temperatures that decrease with increasing internal heat-transfer coefficient \(h_{\textrm{inner}}\) h inner [50–500 W/(m \(^2 \cdot\) 2 · K)] from \(\approx 3180\) 3180 to \(2930~\textrm{K}\) 2930 K . A comparison with the wall thermocouple data at 3 and 6 cm from the tip indicates \(h_{\textrm{inner}}\approx 100\) h inner 100 –200 W/(m \(^2 \cdot\) 2 · K), which is consistent with the Nusselt-based estimates for nominally laminar flow (Re \(_d\approx 1690\) d 1690 ). Despite strong internal heating, the torch temperature-rise rate remained \(<4\) < 4 K/s and diminished over time, implying thermal robustness for at least 15 s of operation under the present conditions. The gas-phase radiation inside the chamber is negligible because of the small \(p_{\mathrm {H_2O}}L\) p H 2 O L , whereas the external radiation becomes comparable to natural convection near \(\sim 600\) 600 K and must be included in the design. The framework enables quantitative assessment of gas–wall coupling and provides actionable guidance for selecting operating windows and material/thickness choices to balance ignition strength against structural heating in scramjet and liquid/hybrid-rocket torch igniters.