This document discusses heat transfer on Earth. It notes that the main sources of heat on Earth are the Sun and Earth's interior. Heat is transferred via three main mechanisms: conduction, convection, and radiation. Conduction and convection are most important in Earth's lithosphere. The heat flux is directly proportional to the temperature gradient according to Fourier's Law. Heat flow measurements show the highest heat loss at mid-ocean ridges and lowest at old oceanic crust. The geotherm can be determined from the conservation of energy and appropriate boundary conditions.
Very useful for the beginners in the field of heat and the mass transfer field. It also gives the idea about the different modes of heat transfer and the measurement of energy transfer rate.
As companies examine their total cost of operations, energy usage and heat recovery deliver cost savings through increased energy utilization and efficiency. Heat exchangers offer companies the opportunity to reuse energy generated for a specific purpose instead of venting that energy to the atmosphere. Shell and tube heat exchangers are in wide use throughout the Food, Dairy, Beverage, Pharmaceutical, Chemicals, Petroleum Refining, and Utility industries. This paper briefly explores three modes of heat transfer and basic designs found in shell and tube heat exchangers. Also included are several case studies from different industries where
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Very useful for the beginners in the field of heat and the mass transfer field. It also gives the idea about the different modes of heat transfer and the measurement of energy transfer rate.
As companies examine their total cost of operations, energy usage and heat recovery deliver cost savings through increased energy utilization and efficiency. Heat exchangers offer companies the opportunity to reuse energy generated for a specific purpose instead of venting that energy to the atmosphere. Shell and tube heat exchangers are in wide use throughout the Food, Dairy, Beverage, Pharmaceutical, Chemicals, Petroleum Refining, and Utility industries. This paper briefly explores three modes of heat transfer and basic designs found in shell and tube heat exchangers. Also included are several case studies from different industries where
Enerquip’s heat exchangers have saved the operators energy and money.
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2. Heat transfer: the sources
Sun
Earth
From the sun:
• 2x1017 W
• 4x102 Wm-2
Derives surface processes:
• Water cycle
• Biosphere
• Rain
• Erosion
From the Earth interior:
• 4x1013 W
• 8x10-2 Wm-2
Derives deep Processes:
• Mantle convection
• Geodynamo
• Plate tectonics
• Metamorphism
• Volcanism
Earthquakes: 1011 W
3. Heat transfer: the mechanisms
Three mechanisms for heat transfer: conduction, convection and
radiation.
4. Heat transfer: the mechanisms
Conduction:
A diffusive process wherein
molecules transmit their kinetic
energy to other molecules by
colliding with them.
5. Heat transfer: the mechanisms
Convection:
A process associated with the
motion of the medium. When a
hot material flows into a cold
material, it will heat the region
- and vise versa.
6. Heat transfer: the mechanisms
Radiation:
The transfer of heat via electromagnetic radiation. Example - the
Sun.
7. Heat transfer: the mechanisms
• In the Earth, both conduction and convection are important.
• In the lithosphere, the temperature gradient is controlled mainly
by conduction.
• Convection in the lithosphere does play a role in:
• Mid-ocean ridges in the form of hydrothermal ocean
circulation.
• Volcanism and emplacement of magmatic bodies.
8. Heat transfer: heat flux
Heat flux is the flow per unit area and per unit time of heat. It is
directly proportional to the temperature gradient.
One dimensional Fourier's law:
where:
q is the heat flux
k is the coefficient of thermal conductivity
T is the temperature
y is a spatial coordinate
Question: why is the minus sign?
q k
dT
dy
,
Question: is q a vector or a scalar?
9. Heat transfer: heat flux
Units:
• q is in [Wm-2]
• k is in [Wm-1K-1]
where W is read “watt”, and is equal to Joule per second.
A substance with a large value of k is a good thermal conductor,
whereas a substance with a small value of k is a poor thermal
conductor or a good thermal insulator.
10. Heat transfer: heat flux
Example 1: a slab of thickness l, and a temperature difference of
T:
The heat flux is given by:
q k
T
l
.
11. Heat transfer: heat flux
Example 2: a composite slab
heat
k2 k1
T2 Tx T1
L2 L1
H.F. through slab 2:
H.F. through slab 1:
In steady-state q1=q2, we get:
Or more generally:
Note the trade-off between thermal conductivity, k, and the
medium thickness, L. Thus, the important quantity is L/k, often
referred to as thermal resistance.
q2 k2
T2 Tx
L2
.
q1 k1
Tx T1
L1
.
q1 q2
T2 T1
(L1 /k1) (L2 /k2)
.
qn
Tn T1
Li /ki
i1,n
.
12. Heat transfer: world-wide heat flow
• Highest heat loss at mid-
ocean ridges and lowest at
old oceanic crust.
• With temperature
gradient of 20-30 K/km,
and thermal conductivity of
2-3 WK-1m-1, the heat flux
is 40-90 mWm-2.
13. Heat transfer: measurements
Heat flow measurements: the global heat flow map on the
previous slide is based on a compilation of individual
measurements whose distribution is shown below.
For practical reasons, the vast majority of the measurements are
from continental areas.
Map from: www.heatflow.und.edu/
14. Heat transfer: heat flow over stable continental areas
• The surface heat flow is
strongly correlated with the
surface concentration of the
radioactive heat producing
elements.
Eastern US
Norway+Sweden
Sierra Nevada
Figure from Turcotte and Schubert textbook
15. Heat transfer: heat flow over stable continental areas
• In the stable continental
areas, surface heat flow
systematically decreases with
the age of the surface rocks.
• Latter we will see that this
effect can be attributed to the
decrease in the crustal
concentrations of the heat
producing isotopes due to
progressive erosion.
16. Heat transfer: heat flow over oceanic crust
What is the contribution from radioactive elements in the ocean?
• The concentration of the heat producing isotopes in oceanic
crust is about an order of magnitude less than in continental crust.
• The oceanic crust is about a factor of 5 thinner than the
continental crust.
Thus, the contribution of heat producing elements is negligible!
17. Heat transfer: heat flow over oceanic crust
• There is a systematic
dependence of the surface
heat flow on the age of the
sea floor.
• Later we will see that this
can be understood as
gradual cooling.
18. Heat transfer: conservation of energy in 1-dimension
Consider a slab of infinitesimal
thickness y; the heat flux out
of the slab is q(y + y), and the
heat flux into the slab q(y).
The net heat flow out of the
slab, per unit time and per unit
area of the slab's face, is:
q(y y)q(y).
19. Heat transfer: conservation of energy in 1-dimension
In the absence of internal heat production, conservation of
energy requires that:
q(y y)q(y) 0.
Since y is infinitesimal, we can expand q(y+y) in a Taylor series
as:
q(y y) q(y) y
dq
dy
(y)2
2
d2
q
dy2
Ignoring terms higher than the first order term, leads to:
q(y y) q(y) y
dq
dy
y k
d2
T
dy2
0.
Thus: d2
T
dy2
0.
20. Heat transfer: conservation of energy in 1-dimension
Question: in the absence of internal heat production, how does
the geotherm look like?
If there's nonzero net heat flow per unit area out of the slab, this
heat must be generated internally in the slab. In that case:
q(y y) q(y) y
dq
dy
y k
d2
T
dy2
yH,
where:
H is the heat production rate per unit mass
is the density
Question: what is the source for steady-state internal heating in
the Earth lithosphere?
21. Heat transfer: geotherm
The previous result may be integrated to determine the geotherm,
i.e. the temperature as a function of depth.
Hereafter we consider a half-space,
with a surface at y=0, where y is a
depth coordinate increasing
downward.
Boundary conditions are:
1) q=-q0 at y=0
2) T=T0 at y=0
22. Heat transfer: geotherm
Starting with:
and integrating once gives:
The 1st b.c. requires that: C1=q0, leading to:
Additional integration gives:
The 2nd b.c. requires that C2=kT0, giving:
H k
d2
T
dy2
0,
Hy k
dT
dy
C1.
Hy k
dT
dy
q0.
H
y2
2
kT q0y C2.
T T0
q0
k
y
H
2k
y2
.