TY - JOUR
T1 - Isobaric heat capacity measurements for the n-pentane-acetone and the methanol-acetone mixtures at elevated temperatures and pressures
AU - Mulia, Kamarza
AU - Yesavage, Victor F.
N1 - Funding Information:
The authors gratefully acknowledge the financial support of the United States National Science Foundation through grant CTS-8813020.
PY - 1999
Y1 - 1999
N2 - Isobaric heat capacities for the n-pentane-acetone and the methanol-acetone binary mixtures were measured with a flow calorimeter at selected temperatures from 423.1 K to 523.1 K as a function of pressure up to 10 MPa. The compositions of each mixture were 0.25, 0.50, and 0.75 mole fractions. The uncertainties of cp measurements were less than 0.4%, depending on the magnitude of the temperature differences. As part of the measurement process, liquid densities at elevated pressure and 303.1 K were also determined and reported. Experimental cp data were compared to the cp values calculated using several equations of state. In general none of the equations of state were able to reliably predict the heat capacities in the supercritical region for either mixture. For both mixtures, the use of binary interaction parameters improved the cp representation in the critical region, by effectively translating the pressures that correspond to cp maxima. However, very close to a maxima, deviations of the calculated cp were still as large as 50%, due to the deficiencies of cubic equations of state in the critical region. Comparison results are specifically presented for the Peng-Robinson equation of state
AB - Isobaric heat capacities for the n-pentane-acetone and the methanol-acetone binary mixtures were measured with a flow calorimeter at selected temperatures from 423.1 K to 523.1 K as a function of pressure up to 10 MPa. The compositions of each mixture were 0.25, 0.50, and 0.75 mole fractions. The uncertainties of cp measurements were less than 0.4%, depending on the magnitude of the temperature differences. As part of the measurement process, liquid densities at elevated pressure and 303.1 K were also determined and reported. Experimental cp data were compared to the cp values calculated using several equations of state. In general none of the equations of state were able to reliably predict the heat capacities in the supercritical region for either mixture. For both mixtures, the use of binary interaction parameters improved the cp representation in the critical region, by effectively translating the pressures that correspond to cp maxima. However, very close to a maxima, deviations of the calculated cp were still as large as 50%, due to the deficiencies of cubic equations of state in the critical region. Comparison results are specifically presented for the Peng-Robinson equation of state
KW - Acetone
KW - Density
KW - Heat capacity
KW - Methanol
KW - Mixtures
KW - n-Pentane
UR - http://www.scopus.com/inward/record.url?scp=0033150877&partnerID=8YFLogxK
U2 - 10.1016/s0378-3812(99)00142-9
DO - 10.1016/s0378-3812(99)00142-9
M3 - Conference article
AN - SCOPUS:0033150877
SN - 0378-3812
VL - 158-160
SP - 1001
EP - 1010
JO - Fluid Phase Equilibria
JF - Fluid Phase Equilibria
T2 - Proceedings of the 1998 8th International Conference on Properties and Phase Equilibria for Product and Process Design
Y2 - 26 April 1998 through 1 May 1998
ER -