FTFS Chap18 P069

# FTFS Chap18 P069 - Chapter 18 Transient Heat Conduction...

This preview shows pages 1–3. Sign up to view the full content.

This preview has intentionally blurred sections. Sign up to view the full version.

View Full Document
This is the end of the preview. Sign up to access the rest of the document.

Unformatted text preview: Chapter 18 Transient Heat Conduction Transient Heat Conduction in Multidimensional Systems 18-69C The product solution enables us to determine the dimensionless temperature of two- or three- dimensional heat transfer problems as the product of dimensionless temperatures of one-dimensional heat transfer problems. The dimensionless temperature for a two-dimensional problem is determined by determining the dimensionless temperatures in both directions, and taking their product. 18-70C The dimensionless temperature for a three-dimensional heat transfer is determined by determining the dimensionless temperatures of one-dimensional geometries whose intersection is the three dimensional geometry, and taking their product. 18-71C This short cylinder is physically formed by the intersection of a long cylinder and a plane wall. The dimensionless temperatures at the center of plane wall and at the center of the cylinder are determined first. Their product yields the dimensionless temperature at the center of the short cylinder. 18-72C The heat transfer in this short cylinder is one-dimensional since there is no heat transfer in the axial direction. The temperature will vary in the radial direction only. 18-55 Chapter 18 Transient Heat Conduction 18-73 A short cylinder is allowed to cool in atmospheric air. The temperatures at the centers of the cylinder and the top surface as well as the total heat transfer from the cylinder for 15 min of cooling are to be determined. Assumptions 1 Heat conduction in the short cylinder is two-dimensional, and thus the temperature varies in both the axial x- and the radial r- directions. 2 The thermal properties of the cylinder are constant. 3 The heat transfer coefficient is constant and uniform over the entire surface. 4 The Fourier number is τ > 0.2 so that the one-term approximate solutions (or the transient temperature charts) are applicable (this assumption will be verified). Properties The thermal properties of brass are given to be ρ = 8530 kg / m 3 , C kJ/kg 389 . ° ⋅ = p C , C W/m 110 ° ⋅ = k , and α = ×- 3 39 10 5 . m / s 2 . Analysis This short cylinder can physically be formed by the intersection of a long cylinder of radius D /2 = 4 cm and a plane wall of thickness 2 L = 15 cm. We measure x from the midplane. ( a ) The Biot number is calculated for the plane wall to be 02727 . ) C W/m. 110 ( ) m 075 . )( C . W/m 40 ( 2 = ° ° = = k hL Bi The constants λ 1 1 and A corresponding to this Biot number are, from Table 18-1, 0050 . 1 and 164 . 1 1 = = A λ The Fourier number is τ α = = × × =- t L 2 5 339 10 0 075 5424 0 2 ( . ( . . . m / s)(15 min 60 s / min) m) 2 2 Therefore, the one-term approximate solution (or the transient temperature charts) is applicable. Then the dimensionless temperature at the center of the plane wall is determined from 869 . ) 0050 . 1 ( ) 424 . 5 ( ) 164 . ( 1 , 2 2 1 = = =-- = θ- τ λ- ∞ ∞ e e A T T T T i wall o We repeat the same calculations for the long cylinder, 01455...
View Full Document

{[ snackBarMessage ]}

### Page1 / 25

FTFS Chap18 P069 - Chapter 18 Transient Heat Conduction...

This preview shows document pages 1 - 3. Sign up to view the full document.

View Full Document
Ask a homework question - tutors are online