Heisler Charts
editHeisler Charts are a set of two charts per included geometry introduced in 1947 by M. P. Heisler[1] which were supplemented by a third chart per geometry in 1961 by H. Gröber. They are used to provide a graphical analysis tool for the evaluation the central temperature for transient heat conduction through an infinitely long plane wall, an infinitely long cylinder of radius ro, and a sphere of radius ro.
Though the Heisler-Gröber Charts are faster and simpler alternative to the exact solutions of these problems, it should be noted that there are some limitations. First, the body must be at uniform temperature initially. Additionally, the temperature of the surroundings and the convective heat transfer coefficient must remain constant and uniform. Also, there must be no heat generation from the body itself.[2][3][4]
Infinitely Long Plane Wall (of thickness 2L)
editThese first Heisler-Gröber Charts were based upon the first term of the exact Fourier Series solution for an infinite plane wall:
[2]
x is the location in the plane wall
The first chart for the plane wall is plotted using 3 different variables. Plotted along the vertical axis of the chart is θo*, where θo* . Plotted along the horizontal axis is the Fourier Number, Fo=αt/L2 . The curves within the graph are a selection of values for the inverse of the Biot Number, where "Bi = hL/k. k is the thermal conductivity of the material and h is the heat transfer coefficient.[2]
[5]
The second chart is used to determine the variation of temperature within the plane wall for different Biot Numbers. The vertical axis is the ration of a given temperature to that at the centerline θ/θo where the x/L curve is the position at which T is taken. The horizontal axis is the value of Bi-1.
The third chart in each set was supplemented by Gröber in 1961 and this particular one shows the dimensionless heat transferred from the wall as a function of a dimensionless time variable. The vertical axis is a plot of Q/Qo , the ratio of actual heat transfer to the amount of total possible heat transfer before T=T∞ . On the horizontal axis is the plot of (Bi2)(Fo), a dimensionless time variable.
Infinitely Long Cylinder
editSphere
editModern Alternatives
editReferences
edit- ↑ Transactions ASME, 69, 227-236, 1947
- 1 2 3 4 5 Cengel, Yunus A. (2007). Heat and Mass Transfer: A Practical Approach (3rd edition ed.). McGraw Hill. pp. 231-236. ISBN 978-0-07-312930-3.
- ↑ http://www.slideshare.net/erlaurito/unsteady-state-basics-presentation
- ↑ http://www.scribd.com/doc/17462198/Heat-conduction-in-cylinder
- 1 2 3 4 5 6 7 8 9 Lee Ho Sung, http://www.mae.wmich.edu/faculty/Lee/me431/ch05_supp_heisler.pdf
- ↑ http://faculty.virginia.edu/ribando/modules/OneDTransient/
- ↑ http://www.che.utexas.edu/cache/newsletters/summer2006_JAVA.pdf






