GASTHERM 1990 - Uses B672 H2O(l) 18.01 1 1.000 2 H2O(l) -1.507 -0.008 1.145 1.818 2.237 2.509 2.690 2.811 *B672 H2O(l) 2.893 2.946 2.980 3.000 3.009 H2O(l) 0.2248878E+02-0.3026498E+04 0.3239667E-03 0.3741010E+04-0.5651173E+01 Page 180: l,g 298.15K -56690 -68315 16.718 373.15K -53831 -67747 20.765 liq -53831 -57987 46.921 gas Page 182: gas 298.15K: DG DH DS -54634 -57795 45.106 ______________________________________________________________________________________ GASTHERM 3000 - Uses HP2011 H2O gas and Supcrt92 hard coded water H2O(l) 18.01 1 1.000 2 H2O(l) -1.511 0.001 0.054 0.109 0.162 0.211 0.256 0.297 HP11 H2O(l) 0.334 0.369 0.400 0.429 0.455 H2O(l) -0.2315582E+03 0.2413531E+05-0.1309938E-01-0.2792639E+07 0.7454108E+02 H2O,gas H2O H2O,gas H(2)O(1) HP2011 31.DEC.11 -54626.1 -57794.0 45.124 0.000 9.584130 2.068834 1.165153 -60.038241 1800.00 ______________________________________________________________________________________ ______________________________________________________________________________________ H2O,g STEAM * 17 ... Johnson, J.W., Personal calculation, Earth Sciences Dept., H2O(g) H(2)O * Lawrence Livermore National Lab., Livermore, CA. ref:17 24.Mar.90 * Parameters given provide smooth metastable -54524.8 -57935.1 44.763 0.000 * extrapolation of one-bar steam properties predicted 12.664700 -10.404100 0.013078 * by the Haar et al. (1984) equation of state to 2523.15 * temperatures < the saturation temperature (99.632 C).