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  • 1
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 17 (1996), S. 803-822 
    ISSN: 1572-9567
    Keywords: difluoromethane ; pentafluoroethane ; p-ϱ-T data ; saturated liquid ; vapor pressure
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Thep-ϱ-T-relationships were measured for difluoromethane (R32) and pentafluoroethane (R125) by an isochoric method with gravimetric determinations of the amount of substance. Temperatures ranged from 142 to 396 K for R32 and from 178 to 398 K for R125, while pressures were up to 35 MPa. Measurements were conducted on compressed liquid samples. Determinations of vapor pressures were made for each substance. I have used vapor pressure data and thep-ϱ-T data to estimate saturated liquid densities by extrapolating each isochore to the vapor pressure, and determining the temperature and density at the intersection. Publishedp-ϱ-T data are in good agreement with this study. For thep ϱ T apparatus. the uncertainty of the temperature is ±0.03 K. and for pressure it is ±0.01%, atp 〉 3 MPa and ±0.05% atp 〈 3 MPa. The principal source of uncertainty is the cell volume (28.5193 cm3 at 0 K and 0 M Pa), which has a standard uncertainty of ±0.003 cm3. When all components of experimental uncertainty are considered. the expanded uncertainty (at the two-sigma level) of the density measurements is estimated to be 0.05%.
    Type of Medium: Electronic Resource
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  • 2
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 19 (1998), S. 1381-1395 
    ISSN: 1572-9567
    Keywords: density ; 1,1-difluoroethane ; p-ρ-T data ; R143a ; R152a ; saturated liquid ; 1,1,1-trifluoroethane
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract The p-ρ-T relationships have been measured for 1,1-difluoroethane (R152a) and 1,1,1-trifluoroethane (R143a) by an isochoric method with gravimetric determinations of the amount of substance. Temperatures ranged from 158 to 400 K for R152a and from 166 to 400 K for R143a, while pressures were up to 35 MPa. Measurements were conducted on compressed liquid samples. Determinations of saturated liquid densities were made by extrapolating each isochore to the vapor pressure, and determining the temperature and density at the intersection. Published p-ρ-T data are in good agreement with this study. For the p-ρ-T apparatus, the uncertainty of the temperature is ±0.03 K, and for pressure it is ±0.01% at p〉3 MPa and ±0.05% at p<3 MPa. The principal source of uncertainty is the cell volume (∼28.5 cm3), which has a standard uncertainty of ±0.003 cm3. When all components of experimental uncertainty are considered, the expanded relative uncertainty (with a coverage factor k=2 and thus a two-standard deviation estimate) of the density measurements is estimated to be ±0.05%.
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  • 3
    ISSN: 1572-9567
    Keywords: 1,1-difluoroethane ; enthalpy of fusion ; heat capacity ; 1,1,1-trifluoroethane ; triple point ; R143a ; R152a ; vapor pressure
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Molar heat capacities at constant volume (C v) of 1,1-difluoroethane (R152a) and 1,1,1-trifluoroethane (R143a) have been measured with an adiabatic calorimeter. Temperatures ranged from their triple points to 345 K, and pressures up to 35 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase ((C v (2) ), saturated-liquid (C σ or C x ' ), and single-phase (C v) molar heat capacities. The C σ data were used to estimate vapor pressures for values less than 105 kPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. The triple-point temperature and the enthalpy of fusion were also measured for each substance. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded relative uncertainty (with a coverage factor k=2 and thus a two-standard deviation estimate) for C v is estimated to be 0.7%, for C v (2) it is 0.5%, and for C σ it is 0.7%.
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 9 (1988), S. 547-557 
    ISSN: 1572-9567
    Keywords: carbon dioxide ; density ; high pressure ; isochoric ; mixtures
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Comprehensive isochoric (p, v, T) measurements have been obtained for (0.98 CO2+0.02 CH4) at densities from 1 to 26mol·dm−3. Supplemental isochoric (p, v, T) measurements have been obtained for high-purity CO2 at densities from 12 to 24 mol·dm−3. Measurements of p(T) cover a broad range of temperature, 225 to 400 K, at pressures to 35 MPa. Comparisons have been made with independent sources and with a predictive method based on corresponding states.
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 21 (2000), S. 1373-1405 
    ISSN: 1572-9567
    Keywords: associating fluids, critical state ; crossover theory ; equation of state ; enthalpies ; heat capacities ; n-alkanols ; thermodynamic properties ; speed of sound ; vapor–liquid equilibrium
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract In this work we have developed a new equation of state (EOS) for propan-1-ol on the basis of the crossover modification (CR) of the statistical-associating-fluid-theory (SAFT) EOS recently developed and applied to n-alkanes. The CR SAFT EOS reproduces the nonanalytical scaling laws in the asymptotic critical region and reduces to the analytical-classical SAFT EOS far away from the critical point. Unlike the previous crossover EOS, the new CR SAFT EOS is based on the parametric sine model for the universal crossover function and is able to represent analytically connected van der Waals loops in the metastable fluid region. The CR SAFT EOS contains 10 system-dependent parameters and allows an accurate representation of the thermodynamic properties of propan-1-ol over a wide range thermodynamic states including the asymptotic singular behavior in the nearest vicinity of the critical point. The EOS was tested against experimental isochoric and isobaric specific heats, speed of sound, PVT, and VLE data in and beyond the critical region. In the one-phase region, the CR SAFT equation represents the experimental values of pressure with an average absolute deviation (AAD) of less than 1% in the critical and supercritical regions and the liquid densities with an AAD of about 1%. A corresponding states principle is used for the extension of the new CR SAFT EOS for propan-1-ol to higher n-alkanols.
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  • 6
    ISSN: 1572-9567
    Keywords: 1-chloro-1,2,2,2-tetrafluoroethane ; density ; 2,2-dichloro-1,1,1-trifluoroethane ; p–ρ–T data ; R123 ; R124 ; saturated liquid
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract The p–ρ–T relationships were measured for 2,2-dichloro-1,1,1-trifluoroethane (R123) and 1-chloro-1,2,2,2-tetrafluoroethane (R124) by an isochoric method with gravimetric determinations of the amount of substance. Temperatures ranged from 176 to 380 K for R123 and from 104 to 400 K for R124, while pressures extended up to 35 MPa. Measurements were conducted on compressed liquid samples. Most published p–ρ–T data are in good agreement with this study. The uncertainty is 0.03 K for temperature and 0.01% for pressure at p〉3 MPa and 0.05% at p〈3 MPa. The principal source of uncertainty is the cell volume (∼28.5 cm3), with a standard uncertainty of 0.003 cm3. When all components of experimental uncertainty are considered, the expanded relative uncertainty (with a coverage factor k=2 and, thus, a 2-SD estimate) of the density measurements is estimated to be 0.05%.
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  • 7
    ISSN: 1572-9567
    Keywords: 1-chloro-1,2,2,2-tetrafluoroethane ; 2,2-dichloro-1,1,1-trifluoroethane ; heat capacity ; R123 ; R124 ; vapor pressure
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Molar heat capacities at a constant volume (C v) of 2,2-dichloro-1,1,1-trifluoroethane (R123) and 1-chloro-1,2,2,2-tetrafluoroethane (R124) were measured with an adiabatic calorimeter. Temperatures ranged from 167 K for R123 and from 94 K for R124 to 341 K, and pressures were up to 33 MPa. Measurements were conducted on the liquid in equilibrium with its vapor and on compressed liquid samples. The samples were of a high purity, verified by chemical analysis of each fluid. For the samples, calorimetric results were obtained for two-phase (C (2) v), saturated liquid (C σ or C′ x ), and single-phase (C v) molar heat capacities. The C σ data were used to estimate vapor pressures for values less than 100 kPa by applying a thermodynamic relationship between the saturated liquid heat capacity and the temperature derivatives of the vapor pressure. Due to the tendency of both R123 and R124 to subcool, the triple-point temperature (T tr) and the enthalpy of fusion (Δ fus H) could not be measured. The principal sources of uncertainty are the temperature rise measurement and the change-of-volume work adjustment. The expanded uncertainty (at the 2σ level) for C v is estimated to be 0.7%, for C (2) v it is 0.5%, and for C σ it is 0.7%.
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 10 (1989), S. 47-59 
    ISSN: 1572-9567
    Keywords: carbon dioxide ; corresponding states ; ethane ; mixture ; PVT data
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Comprehensive isochoric PVT measurements have been obtained for the system (0.99 CO2 + 0.01 C2H6). The range of state points studied includes those with densities from 2 to 24 mol·dm−3, temperatures from 245 to 400 K, and pressures to 35 MPa. Extensive comparisons have been made with two predictive conformai solution models, one which uses the 32-term BWR-type equation of Stewart and Jacobsen as a reference and the other using the newer Schmidt-Wagner functional form. Results obtained with the Schmidt-Wagner equation are better in the near-critical region owing to the flatter critical isotherm associated with this functional form.
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  • 9
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 15 (1994), S. 849-861 
    ISSN: 1572-9567
    Keywords: air ; calorimeter ; heat capacity ; high pressure ; isochoric
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Measurements of the molar heat capacity at constant volumeC v for air were conducted with an adiabatic calorimeter. Temperatures ranged from 67 to 300 K, and pressures ranged up to 35 MPa. Measurements were conducted at 17 densities which ranged from gas to highly compressed liquid states. In total, 227C v values were obtained. The air sample was prepared gravimetrically from research purity gases resulting in a mole fraction composition of 0.78112 N2 + 0.20966 O2 + 0.00922 Ar. The primary sources of uncertainty are the estimated temperature rise and the estimated quantity of substance in the calorimeter. Overall, the uncertainty (± 2σ) of theC v values is estimated to be less than ± 2% for the gas and ±0.5% for the liquid.
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  • 10
    Electronic Resource
    Electronic Resource
    Springer
    International journal of thermophysics 15 (1994), S. 881-902 
    ISSN: 1572-9567
    Keywords: air ; density ; high pressure ; isochoric ; mixtures ; vapor
    Source: Springer Online Journal Archives 1860-2000
    Topics: Physics
    Notes: Abstract Comprehensive isochoricp-π-T measurements have been carried out on liquid and gaseous air along 16 isochores at densities ranging from 2 to 32 mol · dm−3. The air mixture has a nominal composition of 0.7813 N2 + 0.2096 O2 + 0.0092 Ar. Thep-π-T data cover a temperature range from 67 to 400 K at pressures up to 35 MPa. Comparisons with experimental results from independent sources are presented using a fundamental equation of state based. in part, on thep-π-T data from this study.
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