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Tarzimanov, Amin A.; Yuzmukhametov, F. D.; Габитов, Ф. Р.; Шарафутдинов, Р А; Shakirov, Nail

doi:10.1023/a:1019658912515

Cited by 13 publications

(10 citation statements)

References 3 publications

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“…Comparison between Reported and Present Values of Thermal Conductivity. A comparison between the previously reported data in the literature − and the present results is shown chronologically in Table except for the cases of some materials for which the thermal conductivity was not found. These were not intentionally selected, and their uncertainty is mostly unclear.…”

Section: Resultssupporting

confidence: 75%

Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Watanabe¹,

Kato²

2004

J. Chem. Eng. Data

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Experimental values of the thermal conductivity λ and thermal diffusivity a of 29 pure substances are presented in the temperature range of -15 °C to 65 °C under atmospheric or saturation pressure. The materials measured were as follows: alkenes (1-pentene, 1-hexene, 1-heptene, 1-octene, 2,3-dimethyl-1-butene, 2,3-dimethyl-2-butene), cycloalkenes (cyclopentene, cyclohexene), cycloalkanes (cyclopentane, cyclohexane, methylcyclopentane, cycloheptane, cyclooctane), aromatics and their relatives (benzene, ethylbenzene, o-, m-, and p-xylenes, propylbenzene, isopropylbenzene, hemimellitene, pseudocumene, mesitylene, 1,3-cyclohexadiene, 1,4-cyclohexadiene, bicyclo[2.2.1]hepta-2,5-diene [norbornadiene]), and deuterated hydrocarbons (benzene-d 6 , cyclohexane-d 12 , toluene-d 8 ). Measurements were made with the transient hot-wire method in the manner previously presented, and the thermal diffusivity values were corrected by reference to the heat capacity of heptane as a reference material. Heat capacities (volumic, c p F; massic, c p ; molar, C m,p ) were complementally derived from the relationship c p F ) λ/a, with values for the density and the molar mass. The uncertainty of the data is estimated to be 0.4% for the thermal conductivity (absolutely measured) and about 1.8% for the thermal diffusivity (with a coverage factor of k p ) 2; p ) 95%), although that of λ (not of a) is possibly inferior for a few substances containing slightly more impurities (i.e., mainly other isomers).

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Section: Resultssupporting

confidence: 75%

Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Watanabe¹,

Kato²

2004

J. Chem. Eng. Data

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“…A bank of solutions was generated, data from [23][24][25][26][27][28][29] were used as the reference ones. Fig.…”

Section: Resultsmentioning

confidence: 99%

Heat transfer under high-power heating of liquids. 1. Experiment and inverse algorithm

Rutin

Smotritskiy

Старостин

et al. 2013

International Journal of Heat and Mass Transfer

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a b s t r a c tA new approach to fluids behavior study in the course of highpower heating has been developed by us. The approach combines experimental method of controlled pulse heating of a wire probe and numerical method of thermoph ysical properties temperature dependencies recovery from the experimental data. Short (millisecond) characteristic time scale allows working with short-lived fluids, including superheated (with respect to the liquid-vapor equilibrium temperature and/or to the temperature of thermal decomposition onset) ones. Numerical method gives a set of inverse heat conductio n problem solutions, based on the results of single pulse experiment. Numerical technique, based on the heat transfer parameters optimization model, is built using genetic algorithms. The approach was applied to saturated hydrocarbons in the temperature range 300-625 K.

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“…6, 11–13, 15 Tarzimanov and Mashirov 27 observed decomposition of n- hexadecane at temperatures over 675 K, and thus measurements from 660 K and higher, were disregarded and not included in the primary data set. Additionally, the seven 1990 liquid-phase measurements of Tarzimanov et al 31 were not included in the primary data set, as they are unexplainably lower by up to 15% than all other measurements. The measurements of Feja and Hanzelmann 20 were performed in a concentric-cylinder instrument with a 3% uncertainty, and were included in the primary data set, as a full description of the instrument and the calibration procedures was given.…”

Section: The Correlationmentioning

confidence: 99%

Reference Correlation for the Thermal Conductivity of n-Hexadecane from the Triple Point to 700 K and up to 50 MPa

Monogenidou

Assael

Huber

2018

Journal of Physical and Chemical Reference Data

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This paper presents a new wide-ranging correlation for the thermal conductivity of n-hexadecane based on critically evaluated experimental data. The correlation is designed to be used with a recently published equation of state, and it is valid from the triple point up to 700 K and pressures up to 50 MPa. We estimate the uncertainty at a 95% confidence level to be 4% over the aforementioned range, with the exception of the dilute-gas range where the uncertainty is 2.7% over the temperature range 583 to 654 K. The correlation behaves in a physically reasonable manner when extrapolated to the full range of the equation of state, but the uncertainties are larger outside of the validated range, and also in the critical region.

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Cited by 13 publications

References 3 publications

Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Heat transfer under high-power heating of liquids. 1. Experiment and inverse algorithm

Reference Correlation for the Thermal Conductivity of n-Hexadecane from the Triple Point to 700 K and up to 50 MPa

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