The Q1D equations: Difference between revisions
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=== Governing Equations === | === Governing Equations === | ||
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In the following quasi-one-dimensional flow will be assumed. That means that the cross-section is allowed to vary smoothly but flow quantities varies in one direction only. The equations that are derived will thus describe one-dimensional flow in axisymmetric tubes. Let's assume flow in the <math>x</math>-direction, which means that all flow quantities and the cross-section area will vary with the axial coordinate <math>x</math>. | In the following quasi-one-dimensional flow will be assumed. That means that the cross-section is allowed to vary smoothly but flow quantities varies in one direction only. The equations that are derived will thus describe one-dimensional flow in axisymmetric tubes. Let's assume flow in the <math>x</math>-direction, which means that all flow quantities and the cross-section area will vary with the axial coordinate <math>x</math>. | ||
<math | {{NumEqn|<math> | ||
A=A(x),\ \rho=\rho(x),\ u=u(x),\ p=p(x),\ ... | A=A(x),\ \rho=\rho(x),\ u=u(x),\ p=p(x),\ ... | ||
</math> | </math>}} | ||
We will further assume steady-state flow, which means that unsteady terms will be zero. | We will further assume steady-state flow, which means that unsteady terms will be zero. | ||
| Line 32: | Line 42: | ||
Applying the integral form of the continuity equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | Applying the integral form of the continuity equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | ||
<math | {{NumEqn|<math> | ||
\underbrace{\frac{d}{dt}\iiint_{\Omega}\rho d{V}}_{=0}+\iint_{\partial \Omega}\rho {\mathbf{v}}\cdot {\mathbf{n}}dS=0 | \underbrace{\frac{d}{dt}\iiint_{\Omega}\rho d{V}}_{=0}+\iint_{\partial \Omega}\rho {\mathbf{v}}\cdot {\mathbf{n}}dS=0 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\iint_{\partial \Omega}\rho {\mathbf{v}}\cdot {\mathbf{n}}dS=-\rho_1 u_1 A_1+\rho_2 u_2 A_2 | \iint_{\partial \Omega}\rho {\mathbf{v}}\cdot {\mathbf{n}}dS=-\rho_1 u_1 A_1+\rho_2 u_2 A_2 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\rho_1 u_1 A_1=\rho_2 u_2 A_2 | \rho_1 u_1 A_1=\rho_2 u_2 A_2 | ||
</math> | </math>}} | ||
==== Momentum Equation ==== | ==== Momentum Equation ==== | ||
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Applying the integral form of the momentum equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | Applying the integral form of the momentum equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | ||
<math | {{NumEqn|<math> | ||
\underbrace{\frac{d}{dt}\iiint_{\Omega}\rho{\mathbf{v}} d{V}}_{=0}+\iint_{\partial \Omega}\left[\rho ({\mathbf{v}}\cdot {\mathbf{n}}){\mathbf{v}}+p{\mathbf{n}}\right]dS=0 | \underbrace{\frac{d}{dt}\iiint_{\Omega}\rho{\mathbf{v}} d{V}}_{=0}+\iint_{\partial \Omega}\left[\rho ({\mathbf{v}}\cdot {\mathbf{n}}){\mathbf{v}}+p{\mathbf{n}}\right]dS=0 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\iint_{\partial \Omega} \rho ({\mathbf{v}}\cdot {\mathbf{n}}){\mathbf{v}}dS=-\rho_1u_1^2A_1+\rho_2u_2^2A_2 | \iint_{\partial \Omega} \rho ({\mathbf{v}}\cdot {\mathbf{n}}){\mathbf{v}}dS=-\rho_1u_1^2A_1+\rho_2u_2^2A_2 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\iint_{\partial \Omega} p{\mathbf{n}}dS=-p_1A_1+p_2A_2-\int_{A_1}^{A_2}pdA | \iint_{\partial \Omega} p{\mathbf{n}}dS=-p_1A_1+p_2A_2-\int_{A_1}^{A_2}pdA | ||
</math> | </math>}} | ||
collecting terms | collecting terms | ||
<math | {{NumEqn|<math> | ||
\left(\rho_1u_1^2+p_1\right)A_1+\int_{A_1}^{A_2}pdA=\left(\rho_2u_2^2+p_2\right)A_2 | \left(\rho_1u_1^2+p_1\right)A_1+\int_{A_1}^{A_2}pdA=\left(\rho_2u_2^2+p_2\right)A_2 | ||
</math> | </math>}} | ||
==== Energy Equation ==== | ==== Energy Equation ==== | ||
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Applying the integral form of the energy equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | Applying the integral form of the energy equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives | ||
<math | {{NumEqn|<math> | ||
\underbrace{\frac{d}{dt}\iiint_{\Omega}\rho e_o d{V}}_{=0}+\iint_{\partial \Omega}\left[\rho h_o ({\mathbf{v}}\cdot{\mathbf{n}})\right]dS=0 | \underbrace{\frac{d}{dt}\iiint_{\Omega}\rho e_o d{V}}_{=0}+\iint_{\partial \Omega}\left[\rho h_o ({\mathbf{v}}\cdot{\mathbf{n}})\right]dS=0 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\iint_{\partial \Omega}\left[\rho h_o ({\mathbf{v}}\cdot{\mathbf{n}})\right]dS=-\rho_1u_1h_{o_1}A_1+\rho_2u_2h_{o_2}A_2 | \iint_{\partial \Omega}\left[\rho h_o ({\mathbf{v}}\cdot{\mathbf{n}})\right]dS=-\rho_1u_1h_{o_1}A_1+\rho_2u_2h_{o_2}A_2 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
\rho_1u_1h_{o_1}A_1=\rho_2u_2h_{o_2}A_2 | \rho_1u_1h_{o_1}A_1=\rho_2u_2h_{o_2}A_2 | ||
</math> | </math>}} | ||
Now, using the continuity equation <math>\rho_1u_1A_1=\rho_2u_2A_2</math> gives | Now, using the continuity equation <math>\rho_1u_1A_1=\rho_2u_2A_2</math> gives | ||
<math | {{NumEqn|<math> | ||
h_{o_1}=h_{o_2} | h_{o_1}=h_{o_2} | ||
</math> | </math>}} | ||
==== Differential Form ==== | ==== Differential Form ==== | ||
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The continuity equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as | The continuity equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as | ||
<math | {{NumEqn|<math> | ||
\rho_1u_1A_1=\rho_2u_2A_2=const | \rho_1u_1A_1=\rho_2u_2A_2=const | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
d(\rho uA)=0 | d(\rho uA)=0 | ||
</math> | </math>}} | ||
The momentum equation (Eqn. \ref{eq:governing:mom:b}) is rewritten in differential form as | The momentum equation (Eqn. \ref{eq:governing:mom:b}) is rewritten in differential form as | ||
<math | {{NumEqn|<math> | ||
\left(\rho_1u_1^2+p_1\right)A_1+\int_{A_1}^{A_2}pdA=\left(\rho_2u_2^2+p_2\right)A_2\Rightarrow d\left[(\rho u^2+p)A\right]=pdA | \left(\rho_1u_1^2+p_1\right)A_1+\int_{A_1}^{A_2}pdA=\left(\rho_2u_2^2+p_2\right)A_2\Rightarrow d\left[(\rho u^2+p)A\right]=pdA | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
d(\rho u^2A)+d(pA)=pdA | d(\rho u^2A)+d(pA)=pdA | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
ud(\rho uA)+\rho uAdu+Adp+\cancel{pdA}=\cancel{pdA} | ud(\rho uA)+\rho uAdu+Adp+\cancel{pdA}=\cancel{pdA} | ||
</math> | </math>}} | ||
From the continuity equation we have <math>d(\rho uA)</math> and thus | From the continuity equation we have <math>d(\rho uA)</math> and thus | ||
<math | {{NumEqn|<math> | ||
\rho u\cancel{A}du+\cancel{A}dp=0\Rightarrow | \rho u\cancel{A}du+\cancel{A}dp=0\Rightarrow | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
dp=-\rho udu | dp=-\rho udu | ||
</math> | </math>}} | ||
which is the momentum equation on differential form. Also referred to as Euler's equation. Finally, the energy equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as | which is the momentum equation on differential form. Also referred to as Euler's equation. Finally, the energy equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as | ||
<math | {{NumEqn|<math> | ||
h_{o_1}=h_{o_2}=const\Rightarrow dh_o=0 | h_{o_1}=h_{o_2}=const\Rightarrow dh_o=0 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
h_o=h+\frac{1}{2}u^2\Rightarrow dh+\frac{1}{2}d(u^2)=0 | h_o=h+\frac{1}{2}u^2\Rightarrow dh+\frac{1}{2}d(u^2)=0 | ||
</math> | </math>}} | ||
<math | {{NumEqn|<math> | ||
dh+udu=0 | dh+udu=0 | ||
</math> | </math>}} | ||
==== Summary ==== | ==== Summary ==== | ||
<div style="border: 1px solid;"> | |||
{{OpenInfoBox|<math> | |||
<math | |||
d(\rho uA)=0 | d(\rho uA)=0 | ||
</math> | </math>|description=Continuity:}} | ||
<math | {{OpenInfoBox|<math> | ||
dp=-\rho udu | dp=-\rho udu | ||
</math> | </math>|description=Momentum:}} | ||
{{OpenInfoBox|<math> | |||
<math | |||
dh+udu=0 | dh+udu=0 | ||
</math> | </math>|description=Energy:}} | ||
</div> | |||
The equations are valid for: | The equations are valid for: | ||
* quasi-one-dimensional flow | * quasi-one-dimensional flow | ||
Latest revision as of 18:53, 1 April 2026
Governing Equations
In the following quasi-one-dimensional flow will be assumed. That means that the cross-section is allowed to vary smoothly but flow quantities varies in one direction only. The equations that are derived will thus describe one-dimensional flow in axisymmetric tubes. Let's assume flow in the -direction, which means that all flow quantities and the cross-section area will vary with the axial coordinate .
| (Eq. 5.1) |
We will further assume steady-state flow, which means that unsteady terms will be zero.
The equations are derived with the starting point in the governing flow equations on integral form
Continuity Equation
Applying the integral form of the continuity equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives
| (Eq. 5.2) |
| (Eq. 5.3) |
| (Eq. 5.4) |
Momentum Equation
Applying the integral form of the momentum equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives
| (Eq. 5.5) |
| (Eq. 5.6) |
| (Eq. 5.7) |
collecting terms
| (Eq. 5.8) |
Energy Equation
Applying the integral form of the energy equation on the quasi-one-dimensional flow control volume (Fig. \ref{fig:cv}) gives
| (Eq. 5.9) |
| (Eq. 5.10) |
| (Eq. 5.11) |
Now, using the continuity equation gives
| (Eq. 5.12) |
Differential Form
The integral term appearing the momentum equation is undesired and therefore the governing equations are converted to differential form.
The continuity equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as
| (Eq. 5.13) |
| (Eq. 5.14) |
The momentum equation (Eqn. \ref{eq:governing:mom:b}) is rewritten in differential form as
| (Eq. 5.15) |
| (Eq. 5.16) |
| (Eq. 5.17) |
From the continuity equation we have and thus
| (Eq. 5.18) |
| (Eq. 5.19) |
which is the momentum equation on differential form. Also referred to as Euler's equation. Finally, the energy equation (Eqn. \ref{eq:governing:cont:b}) is rewritten in differential form as
| (Eq. 5.20) |
| (Eq. 5.21) |
| (Eq. 5.22) |
Summary
| Continuity: |
| Momentum: |
| Energy: |
The equations are valid for:
- quasi-one-dimensional flow
- steady state
- all gas models (no gas model assumptions made)
- inviscid flow
It should be noted that equations are exact but they are applied to a physical model that is approximate, i.e., the approximation that flow quantities varies in one dimension with a varying cross-section area. In reality, a variation of cross-section area would imply flow in three dimensions.