Density and virial coefficients of gaseous butane from 265 to 450 K at pressures to 3.3 MPa

被引:22
作者
Gupta, D [1 ]
Eubank, PT [1 ]
机构
[1] TEXAS A&M UNIV,DEPT CHEM ENGN,COLLEGE STN,TX 77843
关键词
D O I
10.1021/je970034v
中图分类号
O414.1 [热力学];
学科分类号
摘要
The Burnett-isochoric (B-I) method has been used to measure gas densities and virial coefficients for butane from 265 to 450 K (IPTS, 1990; Preston-Thomas, 1990). Two independent B-I runs were performed but both with a base isotherm of 450 Il, which is well above the critical temperature of 425 K. Significant physical adsorption of butane molecules onto the highly-polished, stainless steel cell walls was found below 375 K in agreement with conclusions reached by Ewing and associates in comparing their sonic-velocity-based density virial coefficients with those from the P-V-T literature. Our data below 375 K were then corrected for adsorption errors by previously published procedures developed by our laboratory for highly polar gases. Using statistical weighting of our two B-I runs, recommended density second virial coefficients B(T) are reported from 265 to 450 K whereas third virial coefficients C(T) are reported only from 325 to 450 K as values below 325 Ii are too uncertain due to the vapor pressure dropping under 300 kPa. However, then the virial equation of state truncated after B(T) is sufficient to represent the gas densities. At the lower temperatures of this investigation, our B(T) values lie between those from sonic velocities and the more negative values from the P-T T-T literature, which are uncorrected for adsorption errors; we are closer to the values from sonic velocities and about 1/4 Of the way between the two sets. At the higher temperatures, we agree very closely with the better P-V-T measurements whereas the sonic-velocity-based values become increasingly more negative.
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页码:961 / 970
页数:10
相关论文
共 27 条
[1]   VIRIAL-COEFFICIENTS OF N-BUTANE FROM PRESSURE MEASUREMENT ONLY [J].
ABABIO, BD ;
MCELROY, PJ ;
WILLIAMSON, AG .
FLUID PHASE EQUILIBRIA, 1994, 95 :329-339
[2]  
Angus S., 1977, INT THERMODYNAMIC TA
[3]   The second virial coefficient for gas mixtures [J].
Beattie, JA ;
Stockmayer, WH .
JOURNAL OF CHEMICAL PHYSICS, 1942, 10 (07) :473-476
[4]   ISOTHERMS FOR HE-AR SYSTEM AT 50 DEGREES C, O DEGREES C AND-50 DEGREES C UP TO 700 ATM [J].
BLANCETT, AL ;
HALL, KR ;
CANFIELD, FB .
PHYSICA, 1970, 47 (01) :75-&
[5]   MEASUREMENT OF TEMPERATURE VARIATION OF VIRIAL COEFFICIENTS .I. APPLICATION TO 2ND VIRIAL COEFFICIENT OF N-BUTANE [J].
BOTTOMLEY, GA ;
SPURLING, TH .
AUSTRALIAN JOURNAL OF CHEMISTRY, 1964, 17 (05) :501-&
[6]   2ND VIRIAL-COEFFICIENTS AT 300-500 K FOR BUTANE, TETRAMETHYLSILANE AND FREON 114 [J].
BOTTOMLEY, GA ;
NAIRN, DB .
AUSTRALIAN JOURNAL OF CHEMISTRY, 1977, 30 (08) :1645-1653
[7]   IDEALITY OF NORMAL-BUTANE - ISOBUTANE SOLUTIONS [J].
CONNOLLY, JF .
JOURNAL OF PHYSICAL CHEMISTRY, 1962, 66 (06) :1082-&
[8]  
Dymond J.H., 1980, VIRIAL COEFFICIENTS
[9]   2ND VIRIAL-COEFFICIENTS FOR N-ALKANES - RECOMMENDATIONS AND PREDICTIONS [J].
DYMOND, JH ;
CHOLINSKI, JA ;
SZAFRANSKI, A ;
WYRZYKOWSKASTANKIEWICZ, D .
FLUID PHASE EQUILIBRIA, 1986, 27 :1-13
[10]  
EMBRY DL, 1980, THESIS TEXAS A M U C