Data series

Zwolinski (Executive Officer) "International Data Series Selected Data on Mixtures," Thermodynamics Research Center, Chemistry Department, Texas A M University, College Station, Texas 77843 (continuing since 1973). ... 

Majer V and Svoboda V 1985 (lUPAC Chemical Data Series No 32) Enthalpies of Vaporization of Organic Compounds (Oxford Blackwell)... 

Source C. E. Moore, National Standard Reference Data Series 34, U.S. Government Printing Office, Washington, D.C.,... 

References D. D. Wagman, et ah, The NBS Tables of Chemical Thermodynamic Properties, in J. Phys. Chem. Ref. Data, 11 2,1982 M. W. Chase, et ah, JANAF Thermochemical Tables, 3rd ed., American Chemical Society and the American Institute of Physics, 1986 (supplements to JANAF appear in J. Phys. Chem. Ref. Data) Thermodynamic Research Center, TRC Thermodynamic Tables, Texas A M University, College Station, Texas I. Barin and O. Knacke, Thermochemical Properties of Inorganic Substances, Springer-Verlag, Berlin, 1973 J. B. Pedley, R. D. Naylor, and S. P. Kirby, Thermochemical Data of Organic Compounds, 2nd ed.. Chapman and Hall, London, 1986 V. Majer and V. Svoboda, Enthalpies of Vaporization of Organic Compounds, International Union of Pure and Applied Chemistry, Chemical Data Series No. 32, Blackwell, Oxford, 1985. 

The data refer to various temperatures between 18 and 25°C, and were compiled from values cited by Bjerrum, Schwarzenbach, and Sillen, Stability Constants of Metal Complexes, part II, Chemical Society, London, 1958, and values taken from publications of the lUPAC Solubility Data Project Solubility Data Series, International Union of Pure and Applied Chemistry, Pergamon Press, Oxford, 1979-1992 H. L. Clever, and F. J. Johnston, J. Phys. Chem. Ref Data, 9 751 (1980) Y. Marcus, Ibid. 9 1307 (1980) H. L. Clever, S. A. Johnson, and M. E. Derrick, Ibid. 14 631 (1985), and 21 941 (1992). 

A. S. Kertes and co-workers. Solubility Data Series, Pergamon Press, Oxford, UK, 1979. 

J. Gmehling and U. Onken, Hapor-EiquidEquilibrium Data Collection, Chemistry Data Series, Dechema, Frankfurt, 1977 ff... 

W. H. Stahl, ed.. Compilation of Odor andTaste Threshold Values Data, American Society for Testing and Materials Data Series 48, Philadelphia, Pa., 1973. 

J. Wisniak and A. Tamir, Eiquid—Eiquid Equilibrium and Extraction, Physical Science Data Series 7, Elsevier, Amsterdam, the Netherlands, 1981 J. Wisniak and A. Tamir, Eiquid—Eiquid Equilibrium and Extraction, Physical Science Data Series 23, Elsevier, Amsterdam, the Netherlands, 1985. 

J. M. Sorenson and W. Adt, Eiquid—Eiquid Equilibrium Data Collection, Dechema Chemistry Data Series, Frankfurt, Germany, Part 1,1980. 

R. Battiao, ed.. Nitrogen andNf Solubihty Data Series, Vol. 10, Pergamon Press, New York, 1982. 

Physical Constants of Hydrocarbons C to C ASTM Data Series Pubhcation DS 4A, ASTM, Philadelphia, Pa., 1971. 

CHETAH-The MSTM Chemical Thermodynamic and Energy Release Evaluation Program, ASTM Data Series Pubheation DS 51, American Society for Testing Materials, Philadelphia, 1974, original, updated. 

G. Sorensen and J. M. W. Arit, Hquid-lJquid Equilibrium Data Collection, Binay Systems, DECHEMA Chemistry Data Series, Vol. 5, part 1, Schon Wetzel GmbH, Frankfurt/Main, Germany, 1979. 

D. R. Stull and H. Prophet, project dinectots, JMNMF Thermochemical Tables, 2nd ed.. National Standards Reference Data Series, U.S. National Bureau of Standards, No. 37, June 1971, available from U.S. Government Printing Office, Supetintendent of Documents, Washington, D.C. 

J. Gmehhng and U. Onken, Chemist Data Series, Hapor—EiquidEquilibrium Data Collection, Dechema, Frankfurt, Germany, 1977ff... 

H. Knapp, R. Doting, L. OeUrich, U. Plocker, and J. M. Prausnit2, Vapor—Eiquid Equilibriafor Mixtures of Eow Boiling Substances, Chemistry Data Series, Vol VI, Dechema, 1982. 

Again subscript i identifies species, and J and I are dummy indicies. Values for the parameters r, qi, and (up — tip) are given by Gmehhng, Onken, and Ant (Vapor-Liquid Equilibrium Data Collection, Chemistry Data Series, vol. I, parts 1-8, DECHEMA, FrankfurUMain, 1974-1990). 

Worth noting is the fact that Barkers method does not require experimental yf values. Thus the correlating parameters Ot, b, and so on, can be ev uated from a P-X data subset. Common practice now is, in fact, to measure just such data. They are, of course, not subject to a test for consistency by the Gibbs/Duhem equation. The worlds store of X T.E data has been compiled by Gmehling et al. (Vapor-Liquid Lquilibiium Data Collection, Chemistiy Data Series, vol. I, parts 1-8, DECHEMA, Frankfurt am Main, 1979-1990). 

A comprehensive treatment of LLE is given by Sorensen, et al. Fluid Phase Equilibria, 2, pp. 297-309 [1979] 3, pp. 47-82 [1979] 4, pp. 151-163 [1980]). Data for LLE are collected in a three-part set compiled by Sorensen and Arlt Liquid-Liquid Equilibrium Data Collection, Chemistry Data Series, vol. V, parts 1-3, DECHEMA, Frankfurt am Main, 1979-1980). 

American Society for Testing and Materials (ASTM) (1994). CHETAH, Version 7-0 The ASTM Computer Program for Chemical Thermodynamic and Energy Release Evaluation. ASTM Data Series DS 51B. Philadelphia, PA American Society for Testing and Materials. 

An acidity list covering more than 5000 organic compounds has been published E.I . Serjeant and B. Dempsey (eds.), "Ionization Constants ol Organic Acids in Aqueous Solution." IUPAC Chemical Data Series No. 23, Pergamon Press, Oxford, 1979. 

J. Barthel, R. Neueder in Electrolyte Data Collection (Ed. G. Kreysa), Chemistry Data Series, Vol. XII, Part 1, DECHEMA, Frankfurt, 1992. 

Marenco, A., Gouget H., Nedelec P., Pages, J.-P. and Karcher, F. (1994). Evidence of a long-term trend in tropospheric ozone from Pic du Midi data series consequences positive radiative forcing. /. Geophys. Res. 99,16617-16632. 

R. W. Ohse, ed., Handbook of Thermodynamic and Transport Properties of Alkali Metals, lUPAC Chemical Data Series No. 30, Blackwell, Oxford, 1985. 

In the ASTER system a data series is measured for an argon and a hydrogen plasma running at 13.56 MHz, in which the power (5-30 W) and pressure (5-50 Pa) are varied [265,295], The probe tip is positioned exactly between powered and grounded electrode, at the center of the discharge. 

Figure 8 shows PAMPA data for a subset of compounds from the two series in Fig. 7. The potential concern about low permeability for Series D is confirmed between the MDCK and PAMPA data. Series C, with the exception of one compound, also demonstrates good correlation between MDCK and PAMPA permeability the compound with low PAMPA permeability should be further analyzed for relevant structure-permeability information.

DECHEMA (1977ff) DECHEMA Chemistry Data Series (DECHEMA). 

The most comprehensive source of equilibrium data for liquid-liquid systems is the DECHEMA data series, Sorensen and Arlt (1979). Equilibrium data for some systems is also given by Perry et al. (1997). 

Sorensen, J. M. and Arlt, W. (1979) Liquid-Liquid Equilibrium Data Collection, Chemical Data Series Vols V/2, V/3 (DECHEMA). 

Mineral Oil Hydraulic Fluids and Polyalphaolefin Hydraulic Fluids. Very little public information is collected on the production volume and methods, import/export, applications, and disposal practices for the different types of mineral oil and polyalphaolefin hydraulic fluids. This is largely because public data series will generally not distinguish between hydraulic fluids and lubricants. Because of the extremely large number of workers and people in the general population exposed to these hydraulic fluids, development of more carefully defined data would allow a more accurate estimate of the numbers of people exposed and would allow development of likely routes of exposure and environmental loss. 

ShawDG, ed. 1989. Solubility data series. Volume 38 Hydrocarbons with water and seawater. Part II Hydrocarbons C8 to C36. New York Pergamon Press, 546-547. 

The complete data series is used to calculate the temperature response, but only certain parts of the experimental data are used to calculate the error. An example of a calibration run is given in Figure 53, the final calibrated TRNSYS model run is shown in Figure 54. Using the first part of the data (with constant heat flux) an estimate of ground thermal conductivity of 2.15 was obtained. Yavatzturk s method yielded an estimate of 2.18, while the estimate obtained with the TRNSYS parameter estimation method was 2.10. 

IAEA, 1998, Nuclear Power Reactors in the World, April 1998 Edition, Reference Data Series No. 2, International Atomic Energy Agency, Vienna. 

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