.. data title 1.0 atm pressure, 300 K nominal temperature ******************************************* Data sources ============ ========== ============================================================ Short name Reference Source ========== ============================================================ bdg04_c \ Bosschaart, K. J. and L. P. H. de Goey (2004). Combustion and Flame 136(3): 261-269. ezl90_i \ F. N. Egolfopoulos, D. L. Zhu, C. K. Law, Proc. Combust. Inst. 23 (1991), 471-478. ggc59_a \ G.J. Gibbs, H.F. Calcote, J. Chem. Eng. Data 4 (1959) 226 hakf98_q \ Hassan, M. I., Aung, K. T., Kwon, K. C., and Faeth, G. M. J. Propul. Power 1998, 14, 479. jom05_j \ G. Jomaas, X. L. Zheng, D. L. Zhu, C. K. Law, Proc. Combust. Inst. 30 (2005), 193-200. law93_a \ C. K. Law, in: N. Peters; B. Rogg, (Eds.) Springer-Verlag: Berlin, 1993. sng52_a \ J.M. Singer, Proc. Combust. Inst. 4 (1952) 352. ve98_c \ C. M. Vagelopoulos, F. N. Egolfopoulos, Proc. Combust. Inst. 27 (1998), 513-519. vel94_b \ C. M. Vagelopoulos, F. N. Egolfopoulos, C. K. Law, Proc. Combust. Inst. 25 (1994), 1341-1347. ========== ============================================================ Plot ---- .. image:: C3H8_1.0_300K_plot.png :scale: 50% Composition =========== .. composition tables Bosschaart, K. J. and L. P. H. de Goey (2004). Combustion and Flame 136(3): 261-269. ------------------------------------------------------------------------------------ ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.60 101.3 298 0.65 101.3 298 0.70 101.3 298 0.75 101.3 298 0.80 101.3 298 0.85 101.3 298 0.90 101.3 298 0.95 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.15 101.3 298 1.20 101.3 298 1.25 101.3 298 1.30 101.3 298 1.35 101.3 298 1.40 101.3 298 1.45 101.3 298 1.50 101.3 298 ===== ========== ======== F. N. Egolfopoulos, D. L. Zhu, C. K. Law, Proc. Combust. Inst. 23 (1991), 471-478. ---------------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.53 101.3 298 0.55 101.3 298 0.57 101.3 298 0.60 101.3 298 0.62 101.3 298 0.65 101.3 298 0.70 101.3 298 0.75 101.3 298 0.80 101.3 298 0.85 101.3 298 0.90 101.3 298 0.95 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.15 101.3 298 1.20 101.3 298 1.25 101.3 298 1.30 101.3 298 1.35 101.3 298 1.40 101.3 298 1.45 101.3 298 1.50 101.3 298 1.55 101.3 298 1.60 101.3 298 1.61 101.3 298 1.75 101.3 298 ===== ========== ======== G.J. Gibbs, H.F. Calcote, J. Chem. Eng. Data 4 (1959) 226 --------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.80 101.3 298 0.85 101.3 298 0.90 101.3 298 0.95 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.25 101.3 298 1.30 101.3 298 ===== ========== ======== Hassan, M. I., Aung, K. T., Kwon, K. C., and Faeth, G. M. J. Propul. Power 1998, 14, 479. ----------------------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.80 101.3 298 0.90 101.3 298 1.00 101.3 298 1.10 101.3 298 1.20 101.3 298 1.30 101.3 298 1.40 101.3 298 1.60 101.3 298 ===== ========== ======== G. Jomaas, X. L. Zheng, D. L. Zhu, C. K. Law, Proc. Combust. Inst. 30 (2005), 193-200. -------------------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.70 101.3 298 0.80 101.3 298 0.90 101.3 298 1.00 101.3 298 1.10 101.3 298 1.20 101.3 298 1.30 101.3 298 1.40 101.3 298 ===== ========== ======== C. K. Law, in: N. Peters; B. Rogg, (Eds.) Springer-Verlag: Berlin, 1993. ------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.55 101.3 298 0.60 101.3 298 0.65 101.3 298 0.75 101.3 298 0.80 101.3 298 0.85 101.3 298 0.90 101.3 298 0.95 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.15 101.3 298 1.20 101.3 298 1.25 101.3 298 1.30 101.3 298 1.35 101.3 298 1.40 101.3 298 1.45 101.3 298 1.50 101.3 298 1.55 101.3 298 1.60 101.3 298 ===== ========== ======== J.M. Singer, Proc. Combust. Inst. 4 (1952) 352. ----------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.80 101.3 298 0.90 101.3 298 0.95 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.15 101.3 298 1.20 101.3 298 1.25 101.3 298 1.30 101.3 298 1.35 101.3 298 ===== ========== ======== C. M. Vagelopoulos, F. N. Egolfopoulos, Proc. Combust. Inst. 27 (1998), 513-519. -------------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.69 101.3 298 0.73 101.3 298 0.78 101.3 298 0.82 101.3 298 0.86 101.3 298 0.94 101.3 298 0.98 101.3 298 1.01 101.3 298 1.05 101.3 298 1.15 101.3 298 1.21 101.3 298 1.26 101.3 298 1.29 101.3 298 1.32 101.3 298 1.36 101.3 298 1.39 101.3 298 ===== ========== ======== C. M. Vagelopoulos, F. N. Egolfopoulos, C. K. Law, Proc. Combust. Inst. 25 (1994), 1341-1347. --------------------------------------------------------------------------------------------- ===== ========== ======== Phi Pres (kPa) Temp (K) ===== ========== ======== 0.60 101.3 298 0.63 101.3 298 0.67 101.3 298 0.72 101.3 298 0.76 101.3 298 0.81 101.3 298 0.85 101.3 298 0.92 101.3 298 0.97 101.3 298 1.00 101.3 298 1.05 101.3 298 1.10 101.3 298 1.15 101.3 298 1.20 101.3 298 1.26 101.3 298 1.30 101.3 298 1.35 101.3 298 1.40 101.3 298 1.45 101.3 298 1.50 101.3 298 1.60 101.3 298 ===== ========== ========