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Chapter 7 • Theory & Derivations

Reactor Criticality & Geometric Buckling in Core Geometries

Comprehensive mathematical theory of reactor criticality and geometric buckling across canonical core shapes: derivation of the one-group Helmholtz reactor critical wave equation nabla^2 phi + B^2 phi = 0; material buckling B_m^2 = (k_infinity - 1)/M^2 versus geometric buckling B_g^2; exact analytical solutions of the boundary value problem for infinite slab, sphere, infinite cylinder, cuboid, and finite cylinder; optimum cylinder aspect ratio H/D = 1.082 and minimum critical volume theorem; spatial flux distributions, flux flatness, and peak-to-average flux peaking factors; two-region core-reflector diffusion theory, reflector thermal flux peaking, and analytical determination of reflector savings delta.

§7.1 The One-Group Reactor Equation: From Diffusion to Helmholtz Wave Form

1. Derivation of the Steady-State Reactor Equation

Consider a bare, homogeneous nuclear reactor operating at steady state. Thermal neutrons are lost by leakage ($-D \nabla^2\phi$) and absorption ($\Sigma_a \phi$). In a multiplying medium, thermal fission generates $k_\infty \Sigma_a \phi$ fast neutrons, which slow down to thermal energy. In one-group diffusion theory: $$-D \nabla^2 \phi(\vec{r}) + \Sigma_a \phi(\vec{r}) = k_\infty \Sigma_a \phi(\vec{r})$$ Rearranging terms: $$-D \nabla^2 \phi(\vec{r}) = (k_\infty - 1) \Sigma_a \phi(\vec{r})$$ Dividing both sides by $D$: $$\nabla^2 \phi(\vec{r}) + \frac{(k_\infty - 1) \Sigma_a}{D} \phi(\vec{r}) = 0$$ Recalling that the thermal diffusion area is $L^2 = D / \Sigma_a$: $$\mathbf{\nabla^2 \phi(\vec{r}) + B^2 \phi(\vec{r}) = 0}$$ This is the famous Helmholtz Reactor Critical Wave Equation!

2. The Separation of Variables

The eigenvalue problem $\nabla^2\phi + B^2\phi = 0$ requires that the neutron flux $\phi(\vec{r})$:

  1. Must be non-negative everywhere inside the physical core: $\phi(\vec{r}) \ge 0$.
  2. Must vanish at the extrapolated boundaries: $\phi(\vec{r}_{\text{extrapolated}}) = 0$.
  3. Must be finite, real, and continuous throughout the interior.
The lowest eigenvalue $B^2$ corresponding to the fundamental strictly positive eigenmode defines the geometric buckling $B_g^2$ of the reactor core!

§7.2 Material Buckling Bm^2 vs Geometric Buckling Bg^2 & The Criticality Condition

1. Material Buckling $B_m^2$

The material buckling $B_m^2$ depends strictly on the nuclear, isotopic, and material composition of the fuel-moderator mixture: $$\mathbf{B_m^2 \equiv \frac{k_\infty - 1}{M^2} = \frac{k_\infty - 1}{L^2 + \tau}}$$ It characterizes the intrinsic neutron production capacity per unit migration area of the nuclear composition, completely independent of the core shape or size!

2. Geometric Buckling $B_g^2$

The geometric buckling $B_g^2$ depends strictly on the physical size and geometric shape of the reactor core, determined by the spatial Laplacian curvature: $$\mathbf{B_g^2 \equiv - \frac{\nabla^2 \phi}{\phi}}$$ Large cores have small geometric curvature (low leakage, small $B_g^2$). Small cores have sharp curvature (high surface-to-volume ratio, intense leakage, large $B_g^2$).

3. The Criticality Balance

Recall the Six-Factor formula $k_{\text{eff}} = \frac{k_\infty}{1 + M^2 B_g^2}$. Rearranging: $$k_{\text{eff}} = 1 \iff 1 + M^2 B_g^2 = k_\infty \iff \mathbf{B_g^2 = \frac{k_\infty - 1}{M^2} = B_m^2}$$ Hence, the fundamental reactor criticality criterion is:

  • Subcritical ($k_{\text{eff}} < 1$): $B_g^2 > B_m^2$ (Core is too small; leakage dominates production).
  • Critical ($k_{\text{eff}} = 1$): $\mathbf{B_g^2 = B_m^2}$ (Exact balance between geometry and nuclear material).
  • Supercritical ($k_{\text{eff}} > 1$): $B_g^2 < B_m^2$ (Core is larger than critical size).

§7.3 Helmholtz Solutions: Infinite Slab & Bare Spherical Reactor Cores

1. Infinite Slab Reactor (Thickness $a$)

Consider an infinite slab bounded by planes at $x = \pm a/2$. With extrapolated thickness $\tilde{a} = a + 2d$: $$\frac{d^2\phi}{dx^2} + B^2 \phi = 0$$ General solution: $\phi(x) = A \cos(B x) + C \sin(B x)$. By spatial symmetry across the midplane $x = 0$, $C = 0$. Boundary condition: $\phi(\pm \tilde{a}/2) = 0 \implies \cos(B \tilde{a}/2) = 0 \implies B \frac{\tilde{a}}{2} = \frac{\pi}{2}$. $$\mathbf{B_g^2 = \left( \frac{\pi}{\tilde{a}} \right)^2, \qquad \phi(x) = \phi_0 \cos\left( \frac{\pi x}{\tilde{a}} \right)}$$

2. Bare Spherical Reactor (Radius $R$)

Consider a sphere of physical radius $R$ and extrapolated radius $\tilde{R} = R + d$. In spherical coordinates: $$\frac{1}{r^2} \frac{d}{dr}\left( r^2 \frac{d\phi}{dr} \right) + B^2 \phi = 0$$ Substitute $w(r) = r \phi(r)$: $$\frac{d^2 w}{dr^2} + B^2 w = 0 \implies w(r) = A \sin(B r) + C \cos(B r)$$ Since the flux at the center must be finite, $\lim_{r \to 0} \frac{w(r)}{r} < \infty \implies C = 0$: $$\phi(r) = A \frac{\sin(B r)}{r}$$ Boundary condition: $\phi(\tilde{R}) = 0 \implies \sin(B \tilde{R}) = 0 \implies B \tilde{R} = \pi$. $$\mathbf{B_g^2 = \left( \frac{\pi}{\tilde{R}} \right)^2, \qquad \phi(r) = \phi_0 \frac{\sin(\pi r / \tilde{R})}{\pi r / \tilde{R}}}$$ where $\phi_0 = A B$ is the central peak flux.

§7.4 Helmholtz Solutions: Infinite Cylinder & Rectangular Parallelepiped

1. Infinite Cylindrical Reactor (Radius $R$)

In cylindrical coordinates with axial and azimuthal symmetry: $$\frac{1}{r} \frac{d}{dr}\left( r \frac{d\phi}{dr} \right) + B^2 \phi = 0$$ This is Bessel's differential equation of order zero. The general solution is: $$\phi(r) = A J_0(B r) + C Y_0(B r)$$ Since the Bessel function of the second kind diverges logarithmically at the origin ($Y_0(0) \to -\infty$), physical regularity requires $C = 0$: $$\phi(r) = \phi_0 J_0(B r)$$ Boundary condition: $\phi(\tilde{R}) = 0 \implies J_0(B \tilde{R}) = 0$. The first positive zero of the zeroth-order Bessel function is $\nu_{0, 1} \approx 2.40483 \approx 2.405$: $$B \tilde{R} = 2.405 \implies \mathbf{B_g^2 = \left( \frac{2.405}{\tilde{R}} \right)^2, \qquad \phi(r) = \phi_0 J_0\left( \frac{2.405 r}{\tilde{R}} \right)}$$

2. Rectangular Parallelepiped (Cuboid $a \times b \times c$)

Separating variables $\phi(x, y, z) = X(x) Y(y) Z(z)$ with origin at the center: $$\frac{X''}{X} + \frac{Y''}{Y} + \frac{Z''}{Z} + B^2 = 0 \implies -B_x^2 - B_y^2 - B_z^2 + B^2 = 0$$ Enforcing zero flux at $\pm \tilde{a}/2, \pm \tilde{b}/2, \pm \tilde{c}/2$: $$\mathbf{B_g^2 = \left(\frac{\pi}{\tilde{a}}\right)^2 + \left(\frac{\pi}{\tilde{b}}\right)^2 + \left(\frac{\pi}{\tilde{c}}\right)^2}$$ $$\mathbf{\phi(x, y, z) = \phi_0 \cos\left( \frac{\pi x}{\tilde{a}} \right) \cos\left( \frac{\pi y}{\tilde{b}} \right) \cos\left( \frac{\pi z}{\tilde{c}} \right)}$$ For a perfect cube ($\tilde{a} = \tilde{b} = \tilde{c}$): $B_g^2 = 3 (\pi/\tilde{a})^2$.

§7.5 Finite Cylindrical Reactors, Optimum Dimensions & Minimum Critical Volume

1. Solution for the Finite Cylinder (Radius $R$, Height $H$)

Combining radial Bessel dependence with axial cosine dependence: $$\nabla^2 \phi = \frac{1}{r} \frac{\partial}{\partial r}\left( r \frac{\partial \phi}{\partial r} \right) + \frac{\partial^2 \phi}{\partial z^2}$$ Separating variables $\phi(r, z) = \mathcal{R}(r) \mathcal{Z}(z)$: $$\mathbf{B_g^2 = B_r^2 + B_z^2 = \left( \frac{2.405}{\tilde{R}} \right)^2 + \left( \frac{\pi}{\tilde{H}} \right)^2}$$ The 2D spatial flux profile is: $$\mathbf{\phi(r, z) = \phi_0 J_0\left( \frac{2.405 r}{\tilde{R}} \right) \cos\left( \frac{\pi z}{\tilde{H}} \right)}$$

2. The Optimum Cylinder Dimensions ($H/D = 1.082$)

For a given critical material buckling $B_m^2$, what cylinder radius $R$ and height $H$ minimize the total physical volume $V = \pi R^2 H$? We seek to minimize $V(\tilde{R}, \tilde{H}) = \pi \tilde{R}^2 \tilde{H}$ subject to constraint $\left( \frac{2.405}{\tilde{R}} \right)^2 + \left( \frac{\pi}{\tilde{H}} \right)^2 = B^2$. Using Lagrange multipliers or substitution $\tilde{H} = \frac{\pi}{\sqrt{B^2 - (2.405/\tilde{R})^2}}$: $$\frac{dV}{d\tilde{R}} = 0 \implies \tilde{H}^2 = 2 \left( \frac{\pi}{2.405} \right)^2 \tilde{R}^2 = 2 \left( \frac{3.14159}{2.405} \right)^2 \tilde{R}^2 \approx 3.409 \, \tilde{R}^2$$ $$\frac{\tilde{H}}{\tilde{R}} = \sqrt{3.409} \approx 1.846 \implies \mathbf{\frac{\tilde{H}}{\tilde{D}} = \frac{1.846}{2} \approx \mathbf{1.082}}$$ A finite cylinder achieves minimum critical volume when its height is approximately $8.2\%$ greater than its diameter!

3. Canonical Geometry Comparison Table

Geometry Buckling $B_g^2$ Flux Distribution $\phi(\vec{r}) / \phi_0$ Critical Volume $V_c$
Sphere (Radius $\tilde{R}$) $(\pi/\tilde{R})^2$ $\frac{\sin(\pi r / \tilde{R})}{\pi r / \tilde{R}}$ $\mathbf{129.88 / B^3}$ (Absolute Minimum!)
Optimum Cylinder ($\tilde{H} = 1.082 \tilde{D}$) $(2.405/\tilde{R})^2 + (\pi/\tilde{H})^2$ $J_0(2.405 r/\tilde{R}) \cos(\pi z/\tilde{H})$ $\mathbf{148.28 / B^3}$ ($+14.2\%$ vs Sphere)
Cube (Side $\tilde{a}$) $3(\pi/\tilde{a})^2$ $\cos(\pi x/\tilde{a})\cos(\pi y/\tilde{a})\cos(\pi z/\tilde{a})$ $\mathbf{161.45 / B^3}$ ($+24.3\%$ vs Sphere)

The sphere has the smallest surface-to-volume ratio, minimizing neutron leakage and thus requiring the smallest critical mass of fissile fuel.

§7.6 Peak-to-Average Flux Ratios & Power Peaking Factors in Critical Cores

1. The Flux Peaking Factor $\Omega$

Because neutron fission power is proportional to local flux $P(\vec{r}) \propto \phi(\vec{r})$, the thermal margin (critical heat flux, fuel centerline melting limit) is dictated by the peak-to-average flux ratio $\Omega$: $$\mathbf{\Omega \equiv \frac{\phi_{\max}}{\bar{\phi}} = \frac{\phi_0}{\frac{1}{V} \int_V \phi(\vec{r}) \, dV}}$$ Values for bare geometries:

  • Infinite Slab: $$\bar{\phi} = \frac{1}{\tilde{a}} \int_{-\tilde{a}/2}^{\tilde{a}/2} \phi_0 \cos\left( \frac{\pi x}{\tilde{a}} \right) dx = \frac{2}{\pi} \phi_0 \implies \mathbf{\Omega_{\text{slab}} = \frac{\pi}{2} \approx 1.571}$$
  • Bare Sphere: $$\bar{\phi} = \frac{1}{\frac{4}{3}\pi \tilde{R}^3} \int_0^{\tilde{R}} \phi_0 \frac{\sin(\pi r/\tilde{R})}{\pi r/\tilde{R}} 4\pi r^2 dr = \frac{3}{\pi^2} \phi_0 \implies \mathbf{\Omega_{\text{sphere}} = \frac{\pi^2}{3} \approx 3.290}$$
  • Finite Cylinder: $$\Omega_{\text{cyl}} = \Omega_{\text{radial}} \times \Omega_{\text{axial}} = \left[ \frac{2.405}{2 J_1(2.405)} \right] \times \left[ \frac{\pi}{2} \right] \approx 2.316 \times 1.571 \approx \mathbf{3.638}$$
A bare finite cylinder has a peak power density $3.64$ times greater than its core average! Real power reactors flatten this distribution using reflectors, fuel zoning, and burnable poison loading.

§7.7 Reflected Reactor Theory: Two-Region Equations & Reflector Savings

1. Physics of the Reflector

Surrounding a bare multiplying core with an unmultiplied moderating shell (the reflector, e.g. $\text{H}_2\text{O}, \text{D}_2\text{O}, \text{Be}, \text{C}$) fundamentally improves reactor economics:

  1. Neutron Economy: Fast and thermal neutrons leaking from the core scatter in the reflector and return to the core (neutron albedo effect).
  2. Critical Mass Reduction: Returning neutrons reduce the required critical core dimensions from $R_{\text{bare}}$ to $R_{\text{core}}$.
  3. Flux Flattening: Reflected neutrons thermalize in the reflector, producing a characteristic thermal flux peak near the core-reflector interface, greatly reducing peak-to-average power peaking!

2. Two-Region Diffusion Formulation

For a reflected spherical core with core radius $R$ and reflector outer radius $R_R$:

  • Core Region ($0 \le r \le R$): Multiplying medium: $$\nabla^2 \phi_c + B^2 \phi_c = 0 \implies \phi_c(r) = A \frac{\sin(B r)}{r}$$
  • Reflector Region ($R \le r \le \tilde{R}_R$): Non-multiplying medium: $$\nabla^2 \phi_r - \frac{1}{L_r^2} \phi_r = 0 \implies \phi_r(r) = C \frac{\sinh\left( \frac{\tilde{R}_R - r}{L_r} \right)}{r}$$
Enforcing flux and current continuity at the core-reflector interface $r = R$: $$\phi_c(R) = \phi_r(R), \qquad D_c \left.\frac{d\phi_c}{dr}\right|_R = D_r \left.\frac{d\phi_r}{dr}\right|_R$$ Dividing the current boundary condition by the flux condition yields the logarithmic derivative matching condition: $$D_c \left[ B \cot(B R) - \frac{1}{R} \right] = D_r \left[ -\frac{1}{L_r} \coth\left(\frac{\tilde{R}_R - R}{L_r}\right) - \frac{1}{R} \right]$$

3. Reflector Savings $\delta$

The reflector savings $\delta$ is the reduction in core dimension enabled by the reflector: $$\mathbf{\delta \equiv R_{\text{bare}} - R_{\text{reflected}}}$$ For an infinite reflector ($R_R \to \infty$) with matched diffusion properties ($D_c \approx D_r$): $$\mathbf{\delta \approx L_r}$$ The reflector savings is approximately equal to the thermal diffusion length $L_r$ of the reflector material! For graphite ($L_r \approx 50\text{ cm}$), reflector savings can exceed $30\text{ to }40\text{ cm}$, shrinking critical core volume by over $50\%$!

ADVANCED UNIVERSITY HONORS PROBLEMS

Step-by-Step Solved Examination Problems

Comprehensive analytical derivations, quantitative calculations, and step-by-step examination solutions for Unit 1.

Solved Problem Example 7.1: Critical Radius, Critical Mass, and Minimum Volume of a Bare Spherical Reactor

A bare spherical reactor is fueled with a homogeneous mixture of $20\%$ enriched uranium dioxide ($\text{UO}_2$) and graphite moderator. The material parameters of the mixture are:

  • Infinite multiplication factor $k_\infty = 1.250$
  • Thermal diffusion area $L^2 = 320\text{ cm}^2$
  • Fermi age $\tau = 280\text{ cm}^2$
  • Extrapolation distance $d = 2.1\text{ cm}$
  • Fuel atom density $N_{235} = 4.20 \times 10^{20}\text{ atoms/cm}^3$

(a) Calculate the material buckling $B_m^2$ and the critical buckling $B_g^2$. (b) Calculate the extrapolated critical radius $\tilde{R}$, the physical critical radius $R$, and the critical volume $V_c$ in liters. (c) Calculate the critical mass of Uranium-235 ($M_{235}$) loaded into the bare sphere in kilograms.

(a) Material Buckling $B_m^2$: Migration area:

$$M^2 = L^2 + \tau = 320\text{ cm}^2 + 280\text{ cm}^2 = 600\text{ cm}^2$$

Material buckling:

$$B_m^2 = \frac{k_\infty - 1}{M^2} = \frac{1.250 - 1}{600\text{ cm}^2} = \frac{0.250}{600\text{ cm}^2} \approx \mathbf{4.1667 \times 10^{-4}\text{ cm}^{-2}}$$

At criticality, $B_g^2 = B_m^2 = 4.1667 \times 10^{-4}\text{ cm}^{-2}$. The critical buckling parameter is:

$$B = \sqrt{4.1667 \times 10^{-4}} \approx \mathbf{0.020412\text{ cm}^{-1}}$$

(b) Critical Radii and Volume: For a bare sphere:

$$B_g = \frac{\pi}{\tilde{R}} \implies \tilde{R} = \frac{\pi}{B} = \frac{3.14159265}{0.020412\text{ cm}^{-1}} \approx \mathbf{153.91\text{ cm}}$$

Physical critical radius:

$$R = \tilde{R} - d = 153.91\text{ cm} - 2.10\text{ cm} \approx \mathbf{151.81\text{ cm}} \approx \mathbf{1.518\text{ m}}$$

Critical volume:

$$V_c = \frac{4}{3} \pi R^3 = \frac{4}{3} \pi (151.81\text{ cm})^3 \approx 1.465 \times 10^7\text{ cm}^3 = \mathbf{14{,}650\text{ liters}} \approx \mathbf{14.65\text{ m}^3}$$

(c) Critical Mass of $^{235}\text{U}$: Total number of $^{235}\text{U}$ nuclei in the critical volume:

$$N_{\text{tot}} = N_{235} \times V_c = (4.20 \times 10^{20}\text{ atoms/cm}^3) \times (1.465 \times 10^7\text{ cm}^3) \approx 6.153 \times 10^{27}\text{ atoms}$$

Critical mass:

$$M_{235} = \frac{N_{\text{tot}} \times 235.044\text{ g/mol}}{6.02214 \times 10^{23}\text{ atoms/mol}} \approx 2.401 \times 10^6\text{ g} = \mathbf{2401\text{ kg}} = \mathbf{2.40\text{ metric tons}}$$

The critical mass of $^{235}\text{U}$ is $2401\text{ kg}$.

Solved Problem Example 7.2: Optimization of Dimensions and Power Peaking in a Finite Cylindrical Reactor

A bare cylindrical reactor has critical buckling $B^2 = 4.00 \times 10^{-4}\text{ cm}^{-2}$. (a) For an optimum cylinder where height equals $1.082 \times \text{diameter}$ ($\tilde{H} = 2.164 \tilde{R}$), calculate the extrapolated radius $\tilde{R}$, diameter $\tilde{D}$, and height $\tilde{H}$ in meters. (b) Calculate the minimum critical volume $V_{\text{opt}}$ in $\text{m}^3$ and compare it with a non-optimum cylinder having squashed pancake proportions $\tilde{H} = \tilde{R}$. (c) The peak thermal neutron flux at the core center is $\phi_0 = 4.5 \times 10^{13}\text{ neutrons/cm}^2\cdot\text{s}$. Calculate the core-average thermal flux $\bar{\phi}$ and the total peak-to-average flux peaking factor $\Omega$.

(a) Optimum Cylinder Dimensions: For a finite cylinder:

$$B^2 = \left( \frac{2.405}{\tilde{R}} \right)^2 + \left( \frac{\pi}{\tilde{H}} \right)^2$$

Substituting $\tilde{H} = 2.164 \tilde{R}$:

$$B^2 = \frac{2.405^2}{\tilde{R}^2} + \frac{\pi^2}{(2.164 \tilde{R})^2} = \frac{5.784}{\tilde{R}^2} + \frac{9.8696}{4.6829 \tilde{R}^2} = \frac{5.784 + 2.1076}{\tilde{R}^2} = \frac{7.8916}{\tilde{R}^2}$$

Solving for $\tilde{R}$:

$$\tilde{R}^2 = \frac{7.8916}{B^2} = \frac{7.8916}{4.00 \times 10^{-4}\text{ cm}^{-2}} = 19{,}729\text{ cm}^2$$
$$\tilde{R} = \sqrt{19{,}729} \approx \mathbf{140.46\text{ cm}} = \mathbf{1.405\text{ m}}$$

Diameter:

$$\tilde{D} = 2 \tilde{R} = 2 \times 140.46\text{ cm} \approx \mathbf{280.92\text{ cm}} = \mathbf{2.809\text{ m}}$$

Height:

$$\tilde{H} = 2.164 \times 140.46\text{ cm} \approx \mathbf{303.96\text{ cm}} = \mathbf{3.040\text{ m}}$$

(b) Volume Comparison: Optimum volume:

$$V_{\text{opt}} = \pi \tilde{R}^2 \tilde{H} = \pi (1.4046\text{ m})^2 (3.0396\text{ m}) \approx \mathbf{18.84\text{ m}^3}$$

For squashed cylinder ($\tilde{H} = \tilde{R}$):

$$B^2 = \frac{5.784 + 9.8696}{\tilde{R}_{\text{sq}}^2} = \frac{15.6536}{\tilde{R}_{\text{sq}}^2} \implies \tilde{R}_{\text{sq}}^2 = \frac{15.6536}{4.00 \times 10^{-4}} = 39{,}134\text{ cm}^2$$
$$\tilde{R}_{\text{sq}} = 197.82\text{ cm} = 1.978\text{ m}, \qquad \tilde{H}_{\text{sq}} = 1.978\text{ m}$$

Squashed volume:

$$V_{\text{sq}} = \pi (1.9782)^2 (1.9782) \approx \mathbf{24.32\text{ m}^3}$$

Penalty of non-optimum aspect ratio:

$$\frac{V_{\text{sq}} - V_{\text{opt}}}{V_{\text{opt}}} \times 100\% = \frac{24.32 - 18.84}{18.84} \times 100\% \approx \mathbf{+29.1\%}$$

Operating off the optimum $H/D$ increases required core volume and fuel mass by nearly $30\%$!

(c) Peak-to-Average Flux and Peaking Factor: Peaking factor:

$$\Omega = \left[ \frac{2.405}{2 J_1(2.405)} \right] \times \left[ \frac{\pi}{2} \right]$$

Given $J_1(2.405) \approx 0.51915$:

$$\Omega_{\text{radial}} = \frac{2.405}{2 \times 0.51915} = \frac{2.405}{1.0383} \approx 2.3163$$
$$\Omega_{\text{axial}} = \frac{\pi}{2} \approx 1.5708$$
$$\Omega = 2.3163 \times 1.5708 \approx \mathbf{3.6384}$$

Average thermal neutron flux:

$$\bar{\phi} = \frac{\phi_0}{\Omega} = \frac{4.5 \times 10^{13}}{3.6384} \approx \mathbf{1.237 \times 10^{13}\text{ neutrons/cm}^2\cdot\text{s}}$$
Solved Problem Example 7.3: Two-Region Reflected Slab Reactor and Exact Calculation of Reflector Savings

A critical reactor consists of an infinite multiplying fuel slab of half-thickness $a$ surrounded on both sides by an infinitely thick graphite reflector. The diffusion properties are:

  • Core: $D_c = 0.90\text{ cm}, M^2 = 250\text{ cm}^2, k_\infty = 1.150$
  • Reflector: $D_r = 0.85\text{ cm}, L_r = 50.0\text{ cm}$

(a) Calculate the material buckling $B_c^2$ of the core and determine the bare slab half-thickness $a_{\text{bare}}$ (neglecting extrapolation distance). (b) From two-region diffusion theory, derive the transcendental criticality condition:

$$\cot(B_c a) = \frac{D_r}{D_c B_c L_r}$$

(c) Solve for the reflected half-thickness $a$ and calculate the reflector savings $\delta = a_{\text{bare}} - a$ in centimeters.

(a) Bare Core Half-Thickness $a_{\text{bare}}$: Core material buckling:

$$B_c^2 = \frac{k_\infty - 1}{M^2} = \frac{1.150 - 1}{250\text{ cm}^2} = \frac{0.150}{250} = 6.00 \times 10^{-4}\text{ cm}^{-2}$$
$$B_c = \sqrt{6.00 \times 10^{-4}} \approx \mathbf{0.024495\text{ cm}^{-1}}$$

For a bare slab with midplane symmetry, $B_c = \pi / (2 a_{\text{bare}})$:

$$a_{\text{bare}} = \frac{\pi}{2 B_c} = \frac{\pi}{2 \times 0.024495\text{ cm}^{-1}} \approx \mathbf{64.128\text{ cm}}$$

(b) Derivation of Criticality Condition:

  • In the core ($-a \le x \le a$): $\phi_c(x) = A \cos(B_c x)$.
  • In the right reflector ($x \ge a$): $\phi_r(x) = C e^{-(x - a)/L_r}$.

Matching boundary conditions at $x = a$:

  1. Flux continuity: $\phi_c(a) = \phi_r(a) \implies A \cos(B_c a) = C$
  2. Current continuity: $-D_c \left.\frac{d\phi_c}{dx}\right|_a = -D_r \left.\frac{d\phi_r}{dx}\right|_a \implies D_c A B_c \sin(B_c a) = D_r \frac{C}{L_r}$

Dividing the current equation by the flux equation:

$$D_c B_c \tan(B_c a) = \frac{D_r}{L_r} \implies \tan(B_c a) = \frac{D_r}{D_c B_c L_r}$$

Taking reciprocal:

$$\mathbf{\cot(B_c a) = \frac{D_c B_c L_r}{D_r}} \quad \text{or} \quad \mathbf{\tan(B_c a) = \frac{D_r}{D_c B_c L_r}} \quad \text{(Q.E.D.)}$$

(c) Reflected Slab Half-Thickness and Reflector Savings: Evaluate the right-hand side of the tangent formula:

$$\frac{D_r}{D_c B_c L_r} = \frac{0.85\text{ cm}}{(0.90\text{ cm}) \times (0.024495\text{ cm}^{-1}) \times (50.0\text{ cm})} = \frac{0.85}{1.102275} \approx 0.77113$$

Therefore:

$$\tan(B_c a) = 0.77113 \implies B_c a = \arctan(0.77113) \approx 0.65706\text{ radians}$$

Solving for $a$:

$$a = \frac{0.65706}{B_c} = \frac{0.65706}{0.024495\text{ cm}^{-1}} \approx \mathbf{26.824\text{ cm}}$$

Reflector savings:

$$\delta = a_{\text{bare}} - a = 64.128\text{ cm} - 26.824\text{ cm} \approx \mathbf{37.30\text{ cm}}$$

The graphite reflector reduces the required core half-thickness from $64.1\text{ cm}$ down to $26.8\text{ cm}$, saving $37.3\text{ cm}$ and reducing core fuel volume by $58.2\%$!