Stainless steel Iss Nuclear waste 9, w aconv T5,0 -Tsi • Constant properties • Negligible radiation on the surface • There is no contact resistance between the waste and the container Water hwater Twater Radioactive wastes [Arw= 20 W/(K·m)] are stored in a spherical, stainless steel [Ass= 15 W/(K·m)] container of inner and outer radii equal to r;= 0.5 m and ro = 0.6 m. Heat is generated volumetrically within the wastes at a uniform rate of g = 1.2 x 105 W/m³, and the outer surface of the container is exposed to a water flow for which h = 1000 W/(m²K) and Twater = 25°C. Calculate considering the following hypotheses: • Steady state • One-dimensional conduction in the radial direction In spherical coordinates and for one-dimensional flow, the Fourier heat diffusion law is expressed as: 1 d 금(?)=-읏 dr (note that the boundary condition for r = 0 is that dT/dr = 0)
Stainless steel Iss Nuclear waste 9, w aconv T5,0 -Tsi • Constant properties • Negligible radiation on the surface • There is no contact resistance between the waste and the container Water hwater Twater Radioactive wastes [Arw= 20 W/(K·m)] are stored in a spherical, stainless steel [Ass= 15 W/(K·m)] container of inner and outer radii equal to r;= 0.5 m and ro = 0.6 m. Heat is generated volumetrically within the wastes at a uniform rate of g = 1.2 x 105 W/m³, and the outer surface of the container is exposed to a water flow for which h = 1000 W/(m²K) and Twater = 25°C. Calculate considering the following hypotheses: • Steady state • One-dimensional conduction in the radial direction In spherical coordinates and for one-dimensional flow, the Fourier heat diffusion law is expressed as: 1 d 금(?)=-읏 dr (note that the boundary condition for r = 0 is that dT/dr = 0)
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Chapter1: Basic Modes Of Heat Transfer
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![1 The temperature of the outer surface of the container T5,0
2 The temperature of the inside surface of the container Ts,i
3 The temperature at the center of the waste sphere (r = 0)
°℃
°℃
°℃](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F6ce82829-b009-480f-ad12-be6a8e7dac6b%2Fd7ae5540-6a69-4ba7-9c45-7cfb6f4d8912%2Fl1nfljmi_processed.png&w=3840&q=75)
Transcribed Image Text:1 The temperature of the outer surface of the container T5,0
2 The temperature of the inside surface of the container Ts,i
3 The temperature at the center of the waste sphere (r = 0)
°℃
°℃
°℃
![Stainless steel
Iss
1 d
Nuclear
waste
==
9, w
g
A
a conv
Radioactive wastes [Arw= 20 W/(K-m)] are stored in a spherical, stainless steel [Ass= 15 W/(K·m)] container of inner and outer radii equal to r₂ =
0.5 m and ro = 0.6 m.
T5,0
-Tsi
Heat is generated volumetrically within the wastes at a uniform rate of g = 1.2 x 105 W/m³, and the outer surface of the container is exposed
to a water flow for which h = 1000 W/(m²K) and Twater = 25°C.
Calculate considering the following hypotheses:
• Steady state
• One-dimensional conduction in the radial direction
• Constant properties
• Negligible radiation on the surface
• There is no contact resistance between the waste and the container
Water
hwater
Twater
In spherical coordinates and for one-dimensional flow, the Fourier heat diffusion law is expressed as:
- (₁2 dT)
dr
dr
(note that the boundary condition for r = 0 is that dT/dr = 0)](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F6ce82829-b009-480f-ad12-be6a8e7dac6b%2Fd7ae5540-6a69-4ba7-9c45-7cfb6f4d8912%2Fzsdtt4s_processed.png&w=3840&q=75)
Transcribed Image Text:Stainless steel
Iss
1 d
Nuclear
waste
==
9, w
g
A
a conv
Radioactive wastes [Arw= 20 W/(K-m)] are stored in a spherical, stainless steel [Ass= 15 W/(K·m)] container of inner and outer radii equal to r₂ =
0.5 m and ro = 0.6 m.
T5,0
-Tsi
Heat is generated volumetrically within the wastes at a uniform rate of g = 1.2 x 105 W/m³, and the outer surface of the container is exposed
to a water flow for which h = 1000 W/(m²K) and Twater = 25°C.
Calculate considering the following hypotheses:
• Steady state
• One-dimensional conduction in the radial direction
• Constant properties
• Negligible radiation on the surface
• There is no contact resistance between the waste and the container
Water
hwater
Twater
In spherical coordinates and for one-dimensional flow, the Fourier heat diffusion law is expressed as:
- (₁2 dT)
dr
dr
(note that the boundary condition for r = 0 is that dT/dr = 0)
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