Abstract
The pressure-volume-temperature data of several gases (H2, O2, CO, CH4, N2 and CO2) have been used to obtain the following corresponding states equation (P>1 kbar; T>400 K): Z(±0.0878)=A+BP r +CP /2 r (21) where Z is the compressibility factor, P r reduced pressure (P/critical P), T r reduced temperature (T/critical T) and the coefficients are given by: A=1−0.5917 T /−2 r B=0.09122 T /−1 r C=1.4164×10−4 T /−2 r −2.8349×10−6 ln T r (P>1 kbar; T>400 K). At pressures below 1 kbar, Z is given by: Z(±0.0761)=1+BP r +CP /2 r (23) where B=0.09827 T /−1 r −0.2709 T /−3 r C=0.01472 T /−4 r −0.00103 T /−1.5 r . For water (P>1 kbar; T>400 K): Z(±0.0209)=A+BP+CP 2 (22) where A=−0.7025+1.16×10−3 T+99.6799 T −1 B=0.2143 T −1−3.1423×10−14 T 3 C=−2.249×10−6 T −1−0.1459 T −3+2.1690×10−15 T 2. At pressure below 1 kbar, the equation is (P>100 bar; T >673 K): Z(±0.0601)=1+B′/V+C′/V 2 (24) where B′=−2.20960 T0.5+3.35460×10−8 T3 C′=3.4569×10−5T2.5+64.9764 ln T Fugacities of the gases may be obtained by integrating the Z equations separately and combining the results as follows:
The subscript in Z denotes the equation which is to be used for calculating Z.
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Saxena, S.K., Fei, Y. Fluids at crustal pressures and temperatures. Contr. Mineral. and Petrol. 95, 370–375 (1987). https://doi.org/10.1007/BF00371850
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DOI: https://doi.org/10.1007/BF00371850