Some thermophysical propertiesof selected materials A primary source of thermophysical properties is a document in which the experimentalist who obtained the data reports the details and
Trang 1A Some thermophysical properties
of selected materials
A primary source of thermophysical properties is a document in which
the experimentalist who obtained the data reports the details and results
of his or her measurements The term secondary source generally refers
to a document, based on primary sources, that presents other peoples’
data and does so critically This appendix is neither a primary nor a
sec-ondary source, since it has been assembled from a variety of secsec-ondary
and even tertiary sources.
We attempted to cross-check the data against different sources, and
this often led to contradictory values Such contradictions are usually
the result of differences between the experimental samples that are
re-ported or of differences in the accuracy of experiments themselves We
resolved such differences by judging the source, by reducing the
num-ber of significant figures to accommodate the conflict, or by omitting the
substance from the table The resulting numbers will suffice for most
calculations However, the reader who needs high accuracy should be
sure of the physical constitution of the material and then should seek
out one of the relevant secondary data sources.
The format of these tables is quite close to that established by R M.
Drake, Jr., in his excellent appendix on thermophysical data [A.1]
How-ever, although we use a few of Drake’s numbers directly in Table A.6,
many of his other values have been superseded by more recent
measure-ments One secondary source from which many of the data here were
obtained was the Purdue University series Thermophysical Properties of
Matter [ A.2] The Purdue series is the result of an enormous
property-gathering effort carried out under the direction of Y S Touloukian and
several coworkers The various volumes in the series are dated since
691
Trang 21970, and addenda were issued throughout the following decade In more recent years, IUPAC, NIST, and other agencies have been developing critically reviewed, standard reference data for various substances, some
of which are contained in [A.3, A.4, A.5, A.6, A.7, A.8, A.9, A.10, A.11].
We have taken many data for fluids from those publications A third
secondary source that we have used is the G E Heat Transfer Data
Book [ A.12].
Numbers that did not come directly from [A.1], [A.2], [A.12] or the sources of standard reference data were obtained from a variety of man- ufacturers’ tables, handbooks, and other technical literature While we have not documented all these diverse sources and the various compro- mises that were made in quoting them, specific citations are given below for the bulk of the data in these tables.
Table A.1 gives the density, specific heat, thermal conductivity, and thermal diffusivity for various metallic solids These values were ob- tained from volumes 1 and 4 of [A.2] or from [A.3] whenever it was pos- sible to find them there Most thermal conductivity values in the table
have been rounded off to two significant figures The reason is that k
is sensitive to very minor variations in physical structure that cannot be detailed fully here Notice, for example, the significant differences be- tween pure silver and 99.9% pure silver, or between pure aluminum and 99% pure aluminum Additional information on the characteristics and
use of these metals can be found in the ASM Metals Handbook [A.13].
The effect of temperature on thermal conductivity is shown for most
of the metals in Table A.1 The specific heat capacity is shown only at
20◦C For most materials, the heat capacity is much lower at cryogenic
temperatures For example, cp for alumimum, iron, molydenum, and tanium decreases by two orders of magnitude as temperature decreases
ti-from 200 K to 20 K On the other hand, for most of these metals, cp
changes more gradually for temperatures between 300 K and 800 K, ing by tens of percent to a factor of two At still higher temperatures,
vary-some of these metals (iron and titanium) show substantial spikes in cp, which are associated with solid-to-solid phase transitions.
Table A.2 gives the same properties as Table A.1 (where they are able) but for nonmetallic substances Volumes 2 and 5 of [A.2] and also [A.3] provided many of the data here, and they revealed even greater vari-
avail-ations in k than the metallic data did For the various sands reported,
k varied by a factor of 500, and for the various graphites by a factor of
50, for example The sensitivity of k to small variations in the packing of
fibrous materials or to the water content of hygroscopic materials forced
Trang 3Appendix A: Some thermophysical properties of selected materials 693
us to restrict many of the k values to a single significant figure The
ef-fect of water content is illustrated for soils Additional data for many
building materials can be found in [A.14].
The data for polymers come mainly from their manufacturers’ data
and are substantially less reliable than, say, those given in Table A.1
for metals The values quoted are mainly those for room temperature.
In processing operations, however, most of these materials are taken
to temperatures of several hundred degrees Celsius, at which they flow
more easily The specific heat capacity may double from room
tempera-ture to such temperatempera-tures These polymers are also produced in a variety
of modified forms; and in many applications they may be loaded with
significant portions of reinforcing fillers (e.g., 10 to 40% by weight glass
fiber) The fillers, in particular, can have a significant effect on thermal
properties.
Table A.3 gives ρ, cp, k, α, ν, Pr, and β for several liquids Data
for water are from [A.4] and [A.15]; they are in agreement with IAPWS
recommendations through 1998 Data for ammonia are from [A.5, A.16,
A.17], data for carbon dioxide are from [A.6, A.7, A.8], and data for oxygen
are from [A.9, A.10] Data for HFC-134a, HCFC-22, and nitrogen are from
[A.11] and [A.18] For these liquids, ρ has uncertainties less than 0.2%, cp
has uncertainties of 1–2%, while µ and k have typical uncertainties of 2–
5% Uncertainties may be higher near the critical point Thermodynamic
data for methanol follow [A.19], while most viscosity data follow [A.20].
Data for mercury follow [A.3] and [A.21] Sources of olive oil data include
[A.20, A.22, A.23], and those for Freon 12 include [A.14] Volumes 3, 6,
10, and 11 of [A.2] gave many of the other values of cp, k, and µ = ρν,
and occasional independently measured values of α Additional values
came from [A.24] Values of α that disagreed only slightly with k/ρcp
were allowed to stand Densities for other substances came from [A.24]
and a variety of other sources A few values of ρ and cp were taken
from [A.25].
Table A.5 provides thermophysical data for saturated vapors The
sources and the uncertainties are as described for gases in the next
para-graph.
Table A.6 gives thermophysical properties for gases at 1 atmosphere
pressure The values were drawn from a variety of sources: air data
are from [A.26, A.27], except for ρ and cp above 850 K which came
from [A.28]; argon data are from [A.29, A.30, A.31]; ammonia data were
taken from [A.5, A.16, A.17]; carbon dioxide properties are from [A.6,
A.7, A.8]; carbon monoxide properties are from [A.18]; helium data are
Trang 4from [A.32, A.33, A.34]; nitrogen data came from [A.35]; oxygen data are from [A.9, A.10]; water data were taken from [A.4] and [A.15] (in agreement with IAPWS recommendations through 1998); and a few high- temperature hydrogen data are from [A.24] with the remainding hydro- gen data drawn from [A.1] Uncertainties in these data vary among the
gases; typically, ρ has uncertainties of 0.02–0.2%, cphas uncertainties of
0.2–2%, µ has uncertainties of 0.3–3%, and k has uncertainties of 2–5%.
The uncertainties are generally lower in the dilute gas region and higher near the saturation line or the critical point The values for hydrogen and for low temperature helium have somewhat larger uncertainties.
Table A.7 lists values for some fundamental physical constants, as given in [A.36] Table A.8 points out physical data that are listed in other parts of this book.
References
[A.1] E R G Eckert and R M Drake, Jr Analysis of Heat and Mass
Transfer McGraw-Hill Book Company, New York, 1972.
[A.2] Y S Touloukian Thermophysical Properties of Matter vols 1–6,
10, and 11 Purdue University, West Lafayette, IN, 1970 to 1975 [A.3] C Y Ho, R W Powell, and P E Liley Thermal conductivity of the
elements: A comprehensive review J Phys Chem Ref Data, 3,
1974 Published in book format as Supplement No 1 to the cited volume.
[A.4] C.A Meyer, R B McClintock, G J Silvestri, and R.C Spencer ASME
Steam Tables American Society of Mechanical Engineers, New
York, NY, 6th edition, 1993.
[A.5] A Fenghour, W A Wakeham, V Vesovic, J T R Watson, J Millat,
and E Vogel The viscosity of ammonia J Phys Chem Ref Data,
24(5):1649–1667, 1995.
[A.6] A Fenghour, W A Wakeham, and V Vesovic The viscosity of
carbon dioxide J Phys Chem Ref Data, 27(1):31–44, 1998.
[A.7] V Vesovic, W A Wakeham, G A Olchowy, J V Sengers, J T R Watson, and J Millat The transport properties of carbon dioxide.
J Phys Chem Ref Data, 19(3):763–808, 1990.
Trang 5References 695
[A.8] R Span and W Wagner A new equation of state for carbon
diox-ide covering the fluid region from the triple-point temperature to
1100 K at pressures up to 800 MPa J Phys Chem Ref Data, 25
(6):1509–1596, 1996.
[A.9] A Laesecke, R Krauss, K Stephan, and W Wagner Transport
properties of fluid oxygen J Phys Chem Ref Data, 19(5):1089–
1122, 1990.
[A.10] R B Stewart, R T Jacobsen, and W Wagner Thermodynamic
properties of oxygen from the triple point to 300 K with pressures
to 80 MPa J Phys Chem Ref Data, 20(5):917–1021, 1991.
[A.11] R Tillner-Roth and H D Baehr An international
stan-dard formulation of the thermodynamic properties of
1,1,1,2-tetrafluoroethane (HFC-134a) covering temperatures from 170 K
to 455 K at pressures up to 70 MPa J Phys Chem Ref Data, 23:
657–729, 1994.
[A.12] R H Norris, F F Buckland, N D Fitzroy, R H Roecker, and D A.
Kaminski, editors Heat Transfer Data Book General Electric Co.,
Schenectady, NY, 1977.
[A.13] ASM Handbook Committee Metals Handbook ASM, International,
Materials Park, OH, 10th edition, 1990.
[A.14] R A Parsons, editor 1993 ASHRAE Handbook—Fundamentals.
American Society of Heating, Refrigerating, and Air-Conditioning
Engineers, Inc., Altanta, 1993.
[A.15] A H Harvey, A P Peskin, and S A Klein NIST/ASME Steam
Prop-erties National Institute of Standards and Technology,
Gaithers-burg, MD, March 2000 NIST Standard Reference Database 10,
Version 2.2.
[A.16] R Tufeu, D Y Ivanov, Y Garrabos, and B Le Neindre Thermal
con-ductivity of ammonia in a large temperature and pressure range
including the critical region Ber Bunsenges Phys Chem., 88:422–
427, 1984.
[A.17] R Tillner-Roth, F Harms-Watzenberg, and H D Baehr Eine neue
Fundamentalgleichung fuer Ammoniak DKV-Tagungsbericht, 20:
167–181, 1993.
Trang 6[A.18] E W Lemmon, A P Peskin, M O McLinden, and D G Friend
Ther-modynamic and Transport Properties of Pure Fluids — NIST Pure Fluids National Institute of Standards and Technology, Gaithers-
burg, MD, September 2000 NIST Standard Reference Database Number 12, Version 5 Property values are based upon the most accurate standard reference formulations then available.
[A.19] K M deReuck and R J B Craven Methanol: International
Ther-modynamic Tables of the Fluid State-12 Blackwell Scientific
Pub-lications, Oxford, 1993 Developed under the sponsorship of the International Union of Pure and Applied Chemistry (IUPAC).
[A.20] D S Viswanath and G Natarajan Data Book on the Viscosity of
Liquids Hemisphere Publishing Corp., New York, 1989.
[A.21] N B Vargaftik, Y K Vinogradov, and V S Yargin Handbook of
Physical Properties of Liquids and Gases Begell House, Inc., New
York, 3rd edition, 1996.
[A.22] D Dadarlat, J Gibkes, D Bicanic, and A Pasca Photopyroelectric
(PPE) measurement of thermal parameters in food products J.
Food Engr., 30:155–162, 1996.
[A.23] H Abramovic and C Klofutar The temperature dependence of
dynamic viscosity for some vegetable oils Acta Chim Slov., 45(1):
69–77, 1998.
[A.24] N B Vargaftik Tables on the Thermophysical Properties of Liquids
and Gases Hemisphere Publishing Corp., Washington, D.C., 2nd
edition, 1975.
[A.25] E W Lemmon, M O McLinden, and D G Friend
Thermophys-ical properties of fluid systems In W G Mallard and P J
Lin-strom, editors, NIST Chemistry WebBook, NIST Standard Reference
Database Number 69 National Institute of Standards and
Technol-ogy, Gaithersburg, MD, 2000 http://webbook.nist.gov.
[A.26] K Kadoya, N Matsunaga, and A Nagashima Viscosity and thermal
conductivity of dry air in the gaseous phase J Phys Chem Ref.
Data, 14(4):947–970, 1985.
[A.27] R.T Jacobsen, S.G Penoncello, S.W Breyerlein, W.P Clark, and E.W.
Lemmon A thermodynamic property formulation for air Fluid
Phase Equilibria, 79:113–124, 1992.
Trang 7References 697
[A.28] E.W Lemmon, R.T Jacobsen, S.G Penoncello, and D G Friend.
Thermodynamic properties of air and mixtures of nitrogen, argon,
and oxygen from 60 to 2000 K at pressures to 2000 MPa J Phys.
Chem Ref Data, 29(3):331–385, 2000.
[A.29] Ch Tegeler, R Span, and W Wagner A new equation of state for
argon covering the fluid region for temperatures from the melting
line to 700 K at pressures up to 1000 MPa J Phys Chem Ref Data,
28(3):779–850, 1999.
[A.30] B A Younglove and H J M Hanley The viscosity and thermal
con-ductivity coefficients of gaseous and liquid argon J Phys Chem.
Ref Data, 15(4):1323–1337, 1986.
[A.31] R A Perkins, D G Friend, H M Roder, and C A Nieto de Castro.
Thermal conductivity surface of argon: A fresh analysis Intl J.
Thermophys., 12(6):965–984, 1991.
[A.32] R D McCarty and V D Arp A new wide range equation of state
for helium Adv Cryo Eng., 35:1465–1475, 1990.
[A.33] E Bich, J Millat, and E Vogel The viscosity and thermal
conduc-tivity of pure monatomic gases from their normal boiling point
up to 5000 K in the limit of zero density and at 0.101325 MPa J.
Phys Chem Ref Data, 19(6):1289–1305, 1990.
[A.34] V D Arp, R D McCarty, and D G Friend Thermophysical
prop-erties of helium-4 from 0.8 to 1500 K with pressures to 2000 MPa.
Technical Note 1334, National Institute of Standards and
Technol-ogy, Boulder, CO, 1998.
[A.35] B A Younglove Thermophysical properties of fluids: Argon,
ethylene, parahydrogen, nitrogen, nitrogen trifluoride, and
oxy-gen J Phys Chem Ref Data, 11, 1982 Published in book format
as Supplement No 1 to the cited volume.
[A.36] P J Mohr and B N Taylor CODATA recommended values of the
fundamental physical constants: 1998 J Phys Chem Ref Data,
28(6):1713–1852, 1999.
Trang 10Table A.2 Properties of nonmetallic solids
Trang 11Appendix A: Some thermophysical properties of selected materials 701
Trang 12TableA.2…continued.
Trang 13Appendix A: Some thermophysical properties of selected materials 703
Trang 14Table A.3 Thermophysical properties of saturated liquids
Trang 15Appendix A: Some thermophysical properties of selected materials 705
Helium I and Helium II
• k for He I is about 0.020 W/m·K near the λ-transition (≈ 2.17 K).
• k for He II below the λ-transition is hard to measure It appears to be about
1.92 K These are the highest conductivities known (cf copper, silver, and diamond)
Trang 16TableA.3: saturated liquids…continued
Trang 17Appendix A: Some thermophysical properties of selected materials 707
Trang 18TableA.3: saturated liquids…continued
Temperature
Oils (some approximate viscosities)
Trang 19Appendix A: Some thermophysical properties of selected materials 709