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Thermal Protection Tile Heat Flux (Aerospace Engineering) Solution

Formulas & Definitions

An aerospace engineer designs a ceramic thermal protection tile for a hypersonic atmospheric re-entry vehicle. During peak atmospheric deceleration, intense aerodynamic friction generates non-uniform surface heating across the outer tile face.

The temperature distribution T(x,y)T(x, y)T(x,y) (in degrees Celsius, ∘C^\circ\text{C}∘C) across a square test section of the tile is modeled by the Gaussian heat distribution function:

T(x,y)=800e−0.1(x2+2y2)T(x, y) = 800 e^{-0.1(x^2 + 2y^2)}T(x,y)=800e−0.1(x2+2y2)
where xxx and yyy represent spatial coordinates in centimeters (cm\text{cm}cm) measured from the tile center.

  1. State the partial differentiation rules required to compute ∂T∂x\frac{\partial T}{\partial x}∂x∂T​ and ∂T∂y\frac{\partial T}{\partial y}∂y∂T​, treating the alternate coordinate as a constant coefficient.
  2. Determine the analytical expressions for the spatial temperature gradients ∂T∂x\frac{\partial T}{\partial x}∂x∂T​ and ∂T∂y\frac{\partial T}{\partial y}∂y∂T​.
  3. Evaluate the instantaneous temperature gradients at the specific monitoring sensor location (x,y)=(2,1) cm(x, y) = (2, 1)\text{ cm}(x,y)=(2,1) cm. State the units of each derivative and interpret the physical thermal behavior along the xxx and yyy directions.
  4. According to Fourier's Law of Heat Conduction, conductive heat flux across the surface is given by q⃗=−k∇T=−k⟨∂T∂x,∂T∂y⟩\vec{q} = -k \nabla T = -k \langle \frac{\partial T}{\partial x}, \frac{\partial T}{\partial y} \rangleq​=−k∇T=−k⟨∂x∂T​,∂y∂T​⟩, where k>0k > 0k>0 is thermal conductivity. Determine the direction of conductive heat flow at (2,1)(2, 1)(2,1).

Step-by-Step Solution:

  1. State the Required Differentiation Rules:

    • Exponential Chain Rule:
      ∂∂x[eu(x,y)]=eu(x,y)⋅∂u∂x\frac{\partial}{\partial x}[e^{u(x, y)}] = e^{u(x, y)} \cdot \frac{\partial u}{\partial x}∂x∂​[eu(x,y)]=eu(x,y)⋅∂x∂u​
    • Constant Isolation Rule: When differentiating with respect to xxx, treat yyy as a constant; when differentiating with respect to yyy, treat xxx as a constant. (Defined in Partial Derivatives.)
  2. Compute the Analytical Expressions:

    • Let u(x,y)=−0.1(x2+2y2)=−0.1x2−0.2y2u(x, y) = -0.1(x^2 + 2y^2) = -0.1x^2 - 0.2y^2u(x,y)=−0.1(x2+2y2)=−0.1x2−0.2y2.
    • Differentiating with respect to xxx:
      ∂u∂x=∂∂x(−0.1x2−0.2y2)=−0.2x\frac{\partial u}{\partial x} = \frac{\partial}{\partial x}(-0.1x^2 - 0.2y^2) = -0.2x∂x∂u​=∂x∂​(−0.1x2−0.2y2)=−0.2x
      ∂T∂x=800e−0.1(x2+2y2)⋅(−0.2x)=−160xe−0.1(x2+2y2)\frac{\partial T}{\partial x} = 800 e^{-0.1(x^2 + 2y^2)} \cdot (-0.2x) = -160x e^{-0.1(x^2 + 2y^2)}∂x∂T​=800e−0.1(x2+2y2)⋅(−0.2x)=−160xe−0.1(x2+2y2)
    • Differentiating with respect to yyy:
      ∂u∂y=∂∂y(−0.1x2−0.2y2)=−0.4y\frac{\partial u}{\partial y} = \frac{\partial}{\partial y}(-0.1x^2 - 0.2y^2) = -0.4y∂y∂u​=∂y∂​(−0.1x2−0.2y2)=−0.4y
      ∂T∂y=800e−0.1(x2+2y2)⋅(−0.4y)=−320ye−0.1(x2+2y2)\frac{\partial T}{\partial y} = 800 e^{-0.1(x^2 + 2y^2)} \cdot (-0.4y) = -320y e^{-0.1(x^2 + 2y^2)}∂y∂T​=800e−0.1(x2+2y2)⋅(−0.4y)=−320ye−0.1(x2+2y2)
  3. Evaluate at the Point (2,1) cm(2, 1)\text{ cm}(2,1) cm:

    • Compute the exponent at (2,1)(2, 1)(2,1):
      u(2,1)=−0.1(22+2(1)2)=−0.1(4+2)=−0.6u(2, 1) = -0.1(2^2 + 2(1)^2) = -0.1(4 + 2) = -0.6u(2,1)=−0.1(22+2(1)2)=−0.1(4+2)=−0.6
      e−0.6≈0.54881e^{-0.6} \approx 0.54881e−0.6≈0.54881
    • Evaluate ∂T∂x(2,1)\frac{\partial T}{\partial x}(2, 1)∂x∂T​(2,1):
      ∂T∂x∣(2,1)=−160(2)e−0.6=−320(0.54881)≈−175.62∘C/cm\left.\frac{\partial T}{\partial x}\right|_{(2, 1)} = -160(2) e^{-0.6} = -320(0.54881) \approx -175.62^\circ\text{C/cm}∂x∂T​​(2,1)​=−160(2)e−0.6=−320(0.54881)≈−175.62∘C/cm
    • Evaluate ∂T∂y(2,1)\frac{\partial T}{\partial y}(2, 1)∂y∂T​(2,1):
      ∂T∂y∣(2,1)=−320(1)e−0.6=−320(0.54881)≈−175.62∘C/cm\left.\frac{\partial T}{\partial y}\right|_{(2, 1)} = -320(1) e^{-0.6} = -320(0.54881) \approx -175.62^\circ\text{C/cm}∂y∂T​​(2,1)​=−320(1)e−0.6=−320(0.54881)≈−175.62∘C/cm
    • Interpretation: The units are degrees Celsius per centimeter (∘C/cm^\circ\text{C/cm}∘C/cm). Because both derivatives are negative, moving outward away from the center (increasing xxx or yyy) causes surface temperature to drop at an instantaneous rate of approximately 175.6∘C/cm175.6^\circ\text{C/cm}175.6∘C/cm.
  4. Determine Conductive Heat Flow Direction:

    • State Fourier's Law of Heat Conduction:
      q⃗=−k∇T=−k⟨∂T∂x,∂T∂y⟩\vec{q} = -k \nabla T = -k \left\langle \frac{\partial T}{\partial x}, \frac{\partial T}{\partial y} \right\rangleq​=−k∇T=−k⟨∂x∂T​,∂y∂T​⟩
    • Substituting our negative spatial gradients:
      q⃗=−k⟨−175.62,−175.62⟩=k⟨175.62,175.62⟩\vec{q} = -k \langle -175.62, -175.62 \rangle = k \langle 175.62, 175.62 \rangleq​=−k⟨−175.62,−175.62⟩=k⟨175.62,175.62⟩
    • Because k>0k > 0k>0, the conductive heat flux vector points in the direction of ⟨1,1⟩\langle 1, 1 \rangle⟨1,1⟩ (into the positive first quadrant, toward decreasing temperatures). Heat naturally diffuses from hot zones (tile center) toward cold outer edges.