uniquely determines A and conversely, is uniquely determined by A. EA is a Boolean homomorphism from the Borel subsets of R into the latticeQ of self-adjoint projections of H. In analogy with probability theory, given a state S, we introduce the distribution of A under S which is the probability measure defined on the Borel subsets of R by
Similarly, the expected value of A is defined in terms of the probability distribution DA by
Note that this expectation is relative to the mixed state S which is used in the definition of DA.
Remark. For technical reasons, one needs to consider separately the positive and negative parts of A defined by the Borel functional calculus for unbounded operators.
Of particular significance for describing randomness of a state is the von Neumann entropy of Sformally defined by
.
Actually, the operator S log2S is not necessarily trace-class. However, if S is a non-negative self-adjoint operator not of trace class we define Tr(S) = +∞. Also note that any density operator S can be diagonalized, that it can be represented in some orthonormal basis by a (possibly infinite) matrix of the form
and we define
The convention is that ,
since an event with probability zero should not contribute to the
entropy. This value is an extended real number (that is in [0, ∞]) and
this is clearly a unitary invariant of S.
Remark. It is indeed possible that H(S) = +∞ for some density operator S. In fact T be the diagonal matrix
T is non-negative trace class and one can show T log2T is not trace-class.
Theorem. Entropy is a unitary invariant.
In analogy with classical entropy (notice the similarity in the definitions), H(S) measures the amount of randomness in the state S. The more dispersed the eigenvalues are, the larger the system entropy. For a system in which the space H is finite-dimensional, entropy is maximized for the states S which in diagonal form have the representation
For such an S, H(S) = log2n. The state S is called the maximally mixed state.
Consider an ensemble of systems described by a Hamiltonian H with average energy E. If H has pure-point spectrum and the eigenvalues of H go to +∞ sufficiently fast, e−r H will be a non-negative trace-class operator for every positive r.
Where β is such that the ensemble average of energy satisfies
and
This is called the partition function; it is the quantum mechanical version of the canonical partition function
of classical statistical mechanics. The probability that a system
chosen at random from the ensemble will be in a state corresponding to
energy eigenvalue is
Under certain conditions, the Gibbs canonical ensemble maximizes the
von Neumann entropy of the state subject to the energy conservation
requirement.
For open systems where the energy and numbers of particles may fluctuate, the system is described by the grand canonical ensemble, described by the density matrix
where the N1, N2, ... are the
particle number operators for the different species of particles that
are exchanged with the reservoir. Note that this is a density matrix
including many more states (of varying N) compared to the canonical
ensemble.
Heat transfer is a discipline of thermal engineering that concerns the generation, use, conversion, and exchange of thermal energy (heat) between physical systems. Heat transfer is classified into various mechanisms, such as thermal conduction, thermal convection, thermal radiation, and transfer of energy by phase changes. Engineers also consider the transfer of mass of differing chemical species (mass transfer in the form of advection),
either cold or hot, to achieve heat transfer. While these mechanisms
have distinct characteristics, they often occur simultaneously in the
same system.
Heat conduction, also called diffusion, is the direct microscopic
exchanges of kinetic energy of particles (such as molecules) or
quasiparticles (such as lattice waves) through the boundary between two
systems. When an object is at a different temperature from another body or its surroundings, heat flows so that the body and the surroundings reach the same temperature, at which point they are in thermal equilibrium.
Such spontaneous heat transfer always occurs from a region of high
temperature to another region of lower temperature, as described in the second law of thermodynamics.
Heat convection occurs when the bulk flow of a fluid (gas or
liquid) carries its heat through the fluid. All convective processes
also move heat partly by diffusion, as well. The flow of fluid may be
forced by external processes, or sometimes (in gravitational fields) by
buoyancy forces caused when thermal energy expands the fluid (for
example in a fire plume), thus influencing its own transfer. The latter
process is often called "natural convection". The former process is
often called "forced convection." In this case, the fluid is forced to
flow by use of a pump, fan, or other mechanical means.
Heat transfer is the energy exchanged between materials (solid/liquid/gas) as a result of a temperature difference. The thermodynamic free energy is the amount of work that a thermodynamic system can perform. Enthalpy is a thermodynamic potential, designated by the letter "H", that is the sum of the internal energy of the system (U) plus the product of pressure (P) and volume (V). Joule is a unit to quantify energy, work, or the amount of heat.
Heat transfer is a process function (or path function), as opposed to functions of state; therefore, the amount of heat transferred in a thermodynamic process that changes the state of a system depends on how that process occurs, not only the net difference between the initial and final states of the process.
Thermodynamic and mechanical heat transfer is calculated with the heat transfer coefficient, the proportionality between the heat flux
and the thermodynamic driving force for the flow of heat. Heat flux is a
quantitative, vectorial representation of heat flow through a surface.
In engineering contexts, the term heat is taken as synonymous with thermal energy. This usage has its origin in the historical interpretation of heat as a fluid (caloric) that can be transferred by various causes, and that is also common in the language of laymen and everyday life.
The transport equations for thermal energy (Fourier's law), mechanical momentum (Newton's law for fluids), and mass transfer (Fick's laws of diffusion) are similar,
and analogies among these three transport processes have been developed
to facilitate the prediction of conversion from any one to the others.
The transfer of energy between objects that are in physical contact. Thermal conductivity is the property of a material to conduct heat and is evaluated primarily in terms of Fourier's law for heat conduction.
The transfer of energy between an object and its environment, due to
fluid motion. The average temperature is a reference for evaluating
properties related to convective heat transfer.
By
transferring matter, energy—including thermal energy—is moved by the
physical transfer of a hot or cold object from one place to another.
This can be as simple as placing hot water in a bottle and heating a
bed, or the movement of an iceberg in changing ocean currents. A
practical example is thermal hydraulics. This can be described by the formula:
where
On a microscopic scale, heat conduction occurs as hot, rapidly moving
or vibrating atoms and molecules interact with neighboring atoms and
molecules, transferring some of their energy (heat) to these neighboring
particles. In other words, heat is transferred by conduction when
adjacent atoms vibrate against one another, or as electrons move from
one atom to another. Conduction is the most significant means of heat
transfer within a solid or between solid objects in thermal contact. Fluids—especially gases—are less conductive. Thermal contact conductance is the study of heat conduction between solid bodies in contact.
The process of heat transfer from one place to another place without
the movement of particles is called conduction, such as when placing a
hand on a cold glass of water—heat is conducted from the warm skin to
the cold glass, but if the hand is held a few inches from the glass,
little conduction would occur since air is a poor conductor of heat.
Steady-state conduction is an idealized model of conduction that happens
when the temperature difference driving the conduction is constant so
that after a time, the spatial distribution of temperatures in the
conducting object does not change any further (see Fourier's law).
In steady state conduction, the amount of heat entering a section is
equal to amount of heat coming out, since the temperature change (a
measure of heat energy) is zero.
An example of steady state conduction is the heat flow through walls of
a warm house on a cold day—inside the house is maintained at a high
temperature and, outside, the temperature stays low, so the transfer of
heat per unit time stays near a constant rate determined by the
insulation in the wall and the spatial distribution of temperature in
the walls will be approximately constant over time.
Transient conduction (see Heat equation)
occurs when the temperature within an object changes as a function of
time. Analysis of transient systems is more complex, and analytic
solutions of the heat equation are only valid for idealized model
systems. Practical applications are generally investigated using
numerical methods, approximation techniques, or empirical study.
The flow of fluid may be forced by external processes, or sometimes
(in gravitational fields) by buoyancy forces caused when thermal energy
expands the fluid (for example in a fire plume), thus influencing its
own transfer. The latter process is often called "natural convection".
All convective processes also move heat partly by diffusion, as well.
Another form of convection is forced convection. In this case, the fluid
is forced to flow by using a pump, fan, or other mechanical means.
Convective heat transfer, or simply, convection, is the transfer of heat from one place to another by the movement of fluids, a process that is essentially the transfer of heat via mass transfer. The bulk motion of fluid enhances heat transfer in many physical situations, such as between a solid surface and the fluid.
Convection is usually the dominant form of heat transfer in liquids and
gases. Although sometimes discussed as a third method of heat transfer,
convection is usually used to describe the combined effects of heat
conduction within the fluid (diffusion) and heat transference by bulk
fluid flow streaming.
The process of transport by fluid streaming is known as advection, but
pure advection is a term that is generally associated only with mass
transport in fluids, such as advection of pebbles in a river. In the
case of heat transfer in fluids, where transport by advection in a fluid
is always also accompanied by transport via heat diffusion (also known
as heat conduction) the process of heat convection is understood to
refer to the sum of heat transport by advection and
diffusion/conduction.
Free, or natural, convection occurs when bulk fluid motions
(streams and currents) are caused by buoyancy forces that result from
density variations due to variations of temperature in the fluid. Forced
convection is a term used when the streams and currents in the fluid
are induced by external means—such as fans, stirrers, and pumps—creating
an artificially induced convection current.
The rate of heat loss of a body is proportional to the temperature difference between the body and its surroundings.
However, by definition, the validity of Newton's law of cooling
requires that the rate of heat loss from convection be a linear function
of ("proportional to") the temperature difference that drives heat
transfer, and in convective cooling this is sometimes not the case. In
general, convection is not linearly dependent on temperature gradients, and in some cases is strongly nonlinear. In these cases, Newton's law does not apply.
Convection vs. conduction
In
a body of fluid that is heated from underneath its container,
conduction, and convection can be considered to compete for dominance.
If heat conduction is too great, fluid moving down by convection is
heated by conduction so fast that its downward movement will be stopped
due to its buoyancy,
while fluid moving up by convection is cooled by conduction so fast
that its driving buoyancy will diminish. On the other hand, if heat
conduction is very low, a large temperature gradient may be formed and
convection might be very strong.
The Rayleigh number () is the product of the Grashof () and Prandtl () numbers. It is a measure that determines the relative strength of conduction and convection.
where
g is the acceleration due to gravity,
ρ is the density with being the density difference between the lower and upper ends,
The Rayleigh number can be understood as the ratio between the rate
of heat transfer by convection to the rate of heat transfer by
conduction; or, equivalently, the ratio between the corresponding
timescales (i.e. conduction timescale divided by convection timescale),
up to a numerical factor. This can be seen as follows, where all
calculations are up to numerical factors depending on the geometry of
the system.
The buoyancy force driving the convection is roughly , so the corresponding pressure is roughly . In steady state, this is canceled by the shear stress due to viscosity, and therefore roughly equals , where V is the typical fluid velocity due to convection and the order of its timescale. The conduction timescale, on the other hand, is of the order of .
Convection occurs when the Rayleigh number is above 1,000–2,000.
Radiation
Radiative heat transfer is the transfer of energy via thermal radiation, i.e., electromagnetic waves. It occurs across vacuum or any transparentmedium (solid or fluid or gas). Thermal radiation is emitted by all objects at temperatures above absolute zero, due to random movements of atoms and molecules in matter. Since these atoms and molecules are composed of charged particles (protons and electrons), their movement results in the emission of electromagnetic radiation
which carries away energy. Radiation is typically only important in
engineering applications for very hot objects, or for objects with a
large temperature difference.
When the objects and distances separating them are large in size
and compared to the wavelength of thermal radiation, the rate of
transfer of radiant energy is best described by the Stefan-Boltzmann equation. For an object in vacuum, the equation is:
For radiative transfer between two objects, the equation is as follows:
where
Radiation from the sun, or solar radiation, can be harvested for heat and power.
Unlike conductive and convective forms of heat transfer, thermal
radiation – arriving within a narrow-angle i.e. coming from a source
much smaller than its distance – can be concentrated in a small spot by
using reflecting mirrors, which is exploited in concentrating solar power generation or a burning glass. For example, the sunlight reflected from mirrors heats the PS10 solar power tower and during the day it can heat water to 285 °C (545 °F).
The reachable temperature at the target is limited by the temperature of the hot source of radiation. (T4-law lets the reverse flow of radiation back to the source rise.) The (on its surface) somewhat 4000 K hot sun
allows to reach coarsely 3000 K (or 3000 °C, which is about 3273 K) at a
small probe in the focus spot of a big concave, concentrating mirror of
the Mont-Louis Solar Furnace in France.
Phase transition
Phase transition or phase change, takes place in a thermodynamic system from one phase or state of matter to another one by heat transfer. Phase change examples are the melting of ice or the boiling of water.
The Mason equation explains the growth of a water droplet based on the effects of heat transport on evaporation and condensation.
The boiling point of a substance is the temperature at which the vapor pressure of the liquid equals the pressure surrounding the liquid and the liquid evaporates resulting in an abrupt change in vapor volume.
In a closed system, saturation temperature and boiling point
mean the same thing. The saturation temperature is the temperature for a
corresponding saturation pressure at which a liquid boils into its
vapor phase. The liquid can be said to be saturated with thermal energy.
Any addition of thermal energy results in a phase transition.
At standard atmospheric pressure and low temperatures, no
boiling occurs and the heat transfer rate is controlled by the usual
single-phase mechanisms. As the surface temperature is increased, local
boiling occurs and vapor bubbles nucleate, grow into the surrounding
cooler fluid, and collapse. This is sub-cooled nucleate boiling,
and is a very efficient heat transfer mechanism. At high bubble
generation rates, the bubbles begin to interfere and the heat flux no
longer increases rapidly with surface temperature (this is the departure from nucleate boiling, or DNB).
At similar standard atmospheric pressure and high temperatures, the hydrodynamically quieter regime of film boiling
is reached. Heat fluxes across the stable vapor layers are low but rise
slowly with temperature. Any contact between the fluid and the surface
that may be seen probably leads to the extremely rapid nucleation of a
fresh vapor layer ("spontaneous nucleation"). At higher temperatures still, a maximum in the heat flux is reached (the critical heat flux, or CHF).
The Leidenfrost Effect
demonstrates how nucleate boiling slows heat transfer due to gas
bubbles on the heater's surface. As mentioned, gas-phase thermal
conductivity is much lower than liquid-phase thermal conductivity, so
the outcome is a kind of "gas thermal barrier".
Condensation
Condensation occurs when a vapor is cooled and changes its phase to a liquid. During condensation, the latent heat of vaporization must be released. The amount of heat is the same as that absorbed during vaporization at the same fluid pressure.
There are several types of condensation:
Homogeneous condensation, as during the formation of fog.
Condensation in direct contact with subcooled liquid.
Condensation on direct contact with a cooling wall of a heat exchanger: This is the most common mode used in industry:
Filmwise
condensation is when a liquid film is formed on the subcooled surface,
and usually occurs when the liquid wets the surface.
Dropwise
condensation is when liquid drops are formed on the subcooled surface,
and usually occurs when the liquid does not wet the surface.
Dropwise condensation is difficult to sustain reliably; therefore,
industrial equipment is normally designed to operate in filmwise
condensation mode.
Melting
Melting is a thermal process that results in the phase transition of a substance from a solid to a liquid. The internal energy of a substance is increased, typically through heat or pressure, resulting in a rise of its temperature to the melting point,
at which the ordering of ionic or molecular entities in the solid
breaks down to a less ordered state and the solid liquefies. Molten
substances generally have reduced viscosity with elevated temperature;
an exception to this maxim is the element sulfur, whose viscosity increases to a point due to polymerization and then decreases with higher temperatures in its molten state.
Modeling approaches
Heat transfer can be modeled in various ways.
Heat equation
The heat equation is an important partial differential equation
that describes the distribution of heat (or temperature variation) in a
given region over time. In some cases, exact solutions of the equation
are available; in other cases the equation must be solved numerically using computational methods such as DEM-based models for thermal/reacting particulate systems (as critically reviewed by Peng et al.).
Lumped system analysis
Lumped
system analysis often reduces the complexity of the equations to one
first-order linear differential equation, in which case heating and
cooling are described by a simple exponential solution, often referred
to as Newton's law of cooling.
System analysis by the lumped capacitance model
is a common approximation in transient conduction that may be used
whenever heat conduction within an object is much faster than heat
conduction across the boundary of the object. This is a method of
approximation that reduces one aspect of the transient conduction
system—that within the object—to an equivalent steady-state system. That
is, the method assumes that the temperature within the object is
completely uniform, although its value may change over time.
In this method, the ratio of the conductive heat resistance
within the object to the convective heat transfer resistance across the
object's boundary, known as the Biot number, is calculated. For small Biot numbers, the approximation of spatially uniform temperature within the object
can be used: it can be presumed that heat transferred into the object
has time to uniformly distribute itself, due to the lower resistance to
doing so, as compared with the resistance to heat entering the object.
Climate models
Climate models study the radiant heat transfer by using quantitative methods to simulate the interactions of the atmosphere, oceans, land surface, and ice.
Thermal insulators are materials specifically designed to reduce the flow of heat by limiting conduction, convection, or both. Thermal resistance
is a heat property and the measurement by which an object or material
resists to heat flow (heat per time unit or thermal resistance) to
temperature difference.
Radiance, or spectral radiance, is a measure of the quantity of radiation that passes through or is emitted. Radiant barriers are materials that reflect
radiation, and therefore reduce the flow of heat from radiation
sources. Good insulators are not necessarily good radiant barriers, and
vice versa. Metal, for instance, is an excellent reflector and a poor
insulator.
The effectiveness of a radiant barrier is indicated by its reflectivity,
which is the fraction of radiation reflected. A material with a high
reflectivity (at a given wavelength) has a low emissivity (at that same
wavelength), and vice versa. At any specific wavelength, reflectivity=1 -
emissivity. An ideal radiant barrier would have a reflectivity of 1,
and would therefore reflect 100 percent of incoming radiation. Vacuum flasks, or Dewars, are silvered to approach this ideal. In the vacuum of space, satellites use multi-layer insulation, which consists of many layers of aluminized (shiny) Mylar to greatly reduce radiation heat transfer and control satellite temperature.
A thermocouple
is a temperature-measuring device and a widely used type of temperature
sensor for measurement and control, and can also be used to convert
heat into electric power.
A thermoelectric cooler
is a solid-state electronic device that pumps (transfers) heat from one
side of the device to the other when an electric current is passed
through it. It is based on the Peltier effect.
A heat exchanger is used for more efficient heat transfer or to dissipate heat. Heat exchangers are widely used in refrigeration, air conditioning, space heating, power generation, and chemical processing. One common example of a heat exchanger is a car's radiator, in which the hot coolant fluid is cooled by the flow of air over the radiator's surface.
Common types of heat exchanger flows include parallel flow,
counter flow, and cross flow. In parallel flow, both fluids move in the
same direction while transferring heat; in counter flow, the fluids move
in opposite directions; and in cross flow, the fluids move at right angles to each other. Common types of heat exchangers include shell and tube, double pipe,
extruded finned pipe, spiral fin pipe, u-tube, and stacked plate. Each
type has certain advantages and disadvantages over other types.
A heat sink
is a component that transfers heat generated within a solid material to
a fluid medium, such as air or a liquid. Examples of heat sinks are the
heat exchangers used in refrigeration and air conditioning systems or
the radiator in a car. A heat pipe
is another heat-transfer device that combines thermal conductivity and
phase transition to efficiently transfer heat between two solid
interfaces.
Applications
Architecture
Efficient energy use is the goal to reduce the amount of energy required in heating or cooling. In architecture, condensation and air currents can cause cosmetic or structural damage. An energy audit
can help to assess the implementation of recommended corrective
procedures. For instance, insulation improvements, air sealing of
structural leaks, or the addition of energy-efficient windows and doors.
Thermal transmittance
is the rate of transfer of heat through a structure divided by the
difference in temperature across the structure. It is expressed in watts
per square meter per kelvin, or W/(m2K). Well-insulated
parts of a building have a low thermal transmittance, whereas
poorly-insulated parts of a building have a high thermal transmittance.
Thermostat is a device to monitor and control temperature.
An alternative method is passive daytime radiative cooling, which enhances terrestrial heat flow to outer space through the infrared window (8–13 μm). Rather than merely blocking solar radiation, this method increases outgoing longwave infrared (LWIR) thermal radiation heat transfer with the extremely cold temperature of outer space (~2.7 K) to lower ambient temperatures while requiring zero energy input.
Greenhouse effect
The greenhouse effect
is a process by which thermal radiation from a planetary surface is
absorbed by atmospheric greenhouse gases and clouds, and is re-radiated
in all directions, resulting in a reduction in the amount of thermal
radiation reaching space relative to what would reach space in the
absence of absorbing materials. This reduction in outgoing radiation
leads to a rise in the temperature of the surface and troposphere until
the rate of outgoing radiation again equals the rate at which heat
arrives from the Sun.
The principles of heat transfer in engineering systems can be applied
to the human body to determine how the body transfers heat. Heat is
produced in the body by the continuous metabolism of nutrients which
provides energy for the systems of the body.
The human body must maintain a consistent internal temperature to
maintain healthy bodily functions. Therefore, excess heat must be
dissipated from the body to keep it from overheating. When a person
engages in elevated levels of physical activity, the body requires
additional fuel which increases the metabolic rate and the rate of heat
production. The body must then use additional methods to remove the
additional heat produced to keep the internal temperature at a healthy
level.
Heat transfer by convection
is driven by the movement of fluids over the surface of the body. This
convective fluid can be either a liquid or a gas. For heat transfer from
the outer surface of the body, the convection mechanism is dependent on
the surface area of the body, the velocity of the air, and the
temperature gradient between the surface of the skin and the ambient
air.
The normal temperature of the body is approximately 37 °C. Heat
transfer occurs more readily when the temperature of the surroundings is
significantly less than the normal body temperature. This concept
explains why a person feels cold when not enough covering is worn when
exposed to a cold environment. Clothing can be considered an insulator
which provides thermal resistance to heat flow over the covered portion
of the body.
This thermal resistance causes the temperature on the surface of the
clothing to be less than the temperature on the surface of the skin.
This smaller temperature gradient between the surface temperature and
the ambient temperature will cause a lower rate of heat transfer than if
the skin were not covered.
To ensure that one portion of the body is not significantly
hotter than another portion, heat must be distributed evenly through the
bodily tissues. Blood flowing through blood vessels acts as a
convective fluid and helps to prevent any buildup of excess heat inside
the tissues of the body. This flow of blood through the vessels can be
modeled as pipe flow in an engineering system. The heat carried by the
blood is determined by the temperature of the surrounding tissue, the
diameter of the blood vessel, the thickness of the fluid,
the velocity of the flow, and the heat transfer coefficient of the
blood. The velocity, blood vessel diameter, and fluid thickness can all
be related to the Reynolds Number, a dimensionless number used in fluid mechanics to characterize the flow of fluids.
Latent heat
loss, also known as evaporative heat loss, accounts for a large
fraction of heat loss from the body. When the core temperature of the
body increases, the body triggers sweat glands in the skin to bring
additional moisture to the surface of the skin. The liquid is then
transformed into vapor which removes heat from the surface of the body. The rate of evaporation heat loss is directly related to the vapor pressure at the skin surface and the amount of moisture present on the skin.
Therefore, the maximum of heat transfer will occur when the skin is
completely wet. The body continuously loses water by evaporation but the
most significant amount of heat loss occurs during periods of increased
physical activity.
Cooling techniques
Evaporative cooling
Evaporative cooling
happens when water vapor is added to the surrounding air. The energy
needed to evaporate the water is taken from the air in the form of
sensible heat and converted into latent heat, while the air remains at a
constant enthalpy.
Latent heat describes the amount of heat that is needed to evaporate
the liquid; this heat comes from the liquid itself and the surrounding
gas and surfaces. The greater the difference between the two
temperatures, the greater the evaporative cooling effect. When the
temperatures are the same, no net evaporation of water in the air
occurs; thus, there is no cooling effect.
Sympathetic cooling
is a process in which particles of one type cool particles of another
type. Typically, atomic ions that can be directly laser-cooled are used
to cool nearby ions or atoms. This technique allows the cooling of ions
and atoms that cannot be laser-cooled directly.
Magnetic evaporative cooling
is a process for lowering the temperature of a group of atoms, after
pre-cooled by methods such as laser cooling. Magnetic refrigeration
cools below 0.3K, by making use of the magnetocaloric effect.
Radiative cooling
Radiative cooling is the process by which a body loses heat by radiation. Outgoing energy is an important effect in the Earth's energy budget.
In the case of the Earth-atmosphere system, it refers to the process by
which long-wave (infrared) radiation is emitted to balance the
absorption of short-wave (visible) energy from the Sun. The thermosphere
(top of atmosphere) cools to space primarily by infrared energy
radiated by carbon dioxide (CO2) at 15 μm and by nitric oxide (NO) at 5.3 μm.
Convective transport of heat and evaporative transport of latent heat
both remove heat from the surface and redistribute it in the atmosphere.
Thermal energy storage
Thermal energy storage includes technologies for collecting and storing energy
for later use. It may be employed to balance energy demand between day
and nighttime. The thermal reservoir may be maintained at a temperature
above or below that of the ambient environment. Applications include
space heating, domestic or process hot water systems, or generating
electricity.
In 1701, Isaac Newton anonymously published an article in Philosophical Transactions noting (in modern terms) that the rate of temperature change of a body is proportional to the difference in temperatures (graduum caloris, "degrees of heat") between the body and its surroundings.
The phrase "temperature change" was later replaced with "heat loss",
and the relationship was named Newton's law of cooling. In general, the
law is valid only if the temperature difference is small and the heat
transfer mechanism remains the same.
Thermal conduction
In heat conduction, the law is valid only if the thermal conductivity
of the warmer body is independent of temperature. The thermal
conductivity of most materials is only weakly dependent on temperature,
so in general the law holds true.
Thermal convection
In
convective heat transfer, the law is valid for forced air or pumped
fluid cooling, where the properties of the fluid do not vary strongly
with temperature, but it is only approximately true for buoyancy-driven
convection, where the velocity of the flow increases with temperature
difference.
Thermal radiation
In the case of heat transfer by thermal radiation, Newton's law of cooling holds only for very small temperature differences.
Thermal conductivity of different metals
In a 1780 letter to Benjamin Franklin, Dutch-born British scientist Jan Ingenhousz relates an experiment which enabled him to rank seven different metals according to their thermal conductivities:
You remembre you gave me a wire of
five metals all drawn thro the same hole Viz. one, of gould, one of
silver, copper steel and iron. I supplyed here the two others Viz. the
one of tin the other of lead. I fixed these seven wires into a wooden
frame at an equal distance of one an other ... I dipt the seven wires
into this melted wax as deep as the wooden frame ... By taking them out
they were covred with a coat of wax ... When I found that this crust was
there about of an equal thikness upon all the wires, I placed them all
in a glased earthen vessel full of olive oil heated to some degrees
under boiling, taking care that each wire was dipt just as far in the
oil as the other ... Now, as they had been all dipt alike at the same
time in the same oil, it must follow, that the wire, upon which the wax
had been melted the highest, had been the best conductor of heat. ...
Silver conducted heat far the best of all other metals, next to this was
copper, then gold, tin, iron, steel, Lead.
During the years 1784 – 1798, the British physicist Benjamin Thompson (Count Rumford) lived in Bavaria, reorganizing the Bavarian army for the Prince-electorCharles Theodore
among other official and charitable duties. The Elector gave Thompson
access to the facilities of the Electoral Academy of Sciences in Mannheim. During his years in Mannheim and later in Munich, Thompson made a large number of discoveries and inventions related to heat.
Conductivity experiments
"New Experiments upon Heat"
In 1785 Thompson performed a series of thermal conductivity experiments, which he describes in great detail in the Philosophical Transactions article "New Experiments upon Heat" from 1786. The fact that good electrical conductors are often also good heat conductors and vice versa must have been well known at the time, for Thompson mentions it in passing.
He intended to measure the relative conductivities of mercury, water,
moist air, "common air" (dry air at normal atmospheric pressure), dry
air of various rarefication, and a "Torricellian vacuum".
From the striking analogy between
the electric fluid and heat respecting their conductors and
non-conductors (having found that bodies, in general, which are
conductors of the electric fluid, are likewise good conductors of heat,
and, on the contrary, that electric bodies, or such as are bad
conductors of the electric fluid, are likewise bad conductors of heat), I
was led to imagine that the Torricellian vacuum, which is known to
afford so ready a passage to the electric fluid, would also have
afforded a ready passage to heat.
Medium
Relative conductivity
Mercury
1000
Moist air
330
Water
313
Dry air (1 atm)
80.41
Dry air (1/4 atm)
80.23
Dry air (1/24 atm)
78
Torricellian vacuum
55
For these experiments, Thompson employed a thermometer inside a
large, closed glass tube. Under the circumstances described, heat
may—unbeknownst to Thompson—have been transferred more by radiation than by conduction. These were his results.
After the experiments, Thompson was surprised to observe that a
vacuum was a significantly poorer heat conductor than air "which of
itself is reckoned among the worst", but only a very small difference between common air and rarefied air. He also noted the great difference between dry air and moist air, and the great benefit this affords.
I cannot help observing, with what
infinite wisdom and goodness Divine Providence appears to have guarded
us against the evil effects of excessive heat and cold in the
atmosphere; for if it were possible for the air to be equally damp
during the severe cold of the winter ... as it sometimes is in summer,
its conducing power, and consequently its apparent coldness ... would
become quite intolerable; but, happily for us, its power to hold water
in solution is diminished, and with it its power to rob us of our animal
heat.
Every body
knows how very disagreeable a very moderate degree of cold is when the
air is very damp; and from hence it appears, why the thermometer is not
always a just measure of the apparent or sensible heat of the
atmosphere. If colds ... are occasioned by our bodies being robbed of
our animal heat, the reason is plain why those disorders prevail most
during the cold autumnal rains, and upon the breaking up of the frost in
the spring. It is likewise plain [why] ... inhabiting damp houses, is
so very dangerous; and why the evening air is so pernicious in summer
... and why it is not so during the hard frosts of winter.
Temperature vs. sensible heat
Thompson concluded with some comments on the important difference between temperature and sensible heat.
The ... sensation of hot or cold
depends not intirely upon the temperature of the body exciting in us
those sensations ... but upon the quantity of heat it is capable of
communicating to us, or receiving from us ... and this depends in a
great measure upon the conducing powers of the bodies in question. The
sensation of hot is the entrance of heat into our bodies; that of cold
is its exit ... This is another proof that the thermometer cannot be a
just measure of sensible heat ... or rather, that the touch does not
afford us a just indication of ... real temperatures.
This
motion of heat takes place in three ways, which a common fire-place
very well illustrates. If, for instance, we place a thermometer directly
before a fire, it soon begins to rise, indicating an increase of
temperature. In this case the heat has made its way through the space
between the fire and the thermometer, by the process termed radiation.
If we place a second thermometer in contact with any part of the grate,
and away from the direct influence of the fire, we shall find that this
thermometer also denotes an increase of temperature; but here the heat
must have travelled through the metal of the grate, by what is termed conduction.
Lastly, a third thermometer placed in the chimney, away from the direct
influence of the fire, will also indicate a considerable increase of
temperature; in this case a portion of the air, passing through and near
the fire, has become heated, and has carried up the chimney the
temperature acquired from the fire. There is at present no single term
in our language employed to denote this third mode of the propagation of
heat; but we venture to propose for that purpose, the term convection, [in footnote: [Latin] Convectio, a carrying or conveying] which not only expresses the leading fact, but also accords very well with the two other terms.
Later, in the same treatise VIII, in the book on meteorology, the concept of convection is also applied to "the process by which heat is communicated through water".