Fixed | Measured | |
---|---|---|
Mole fraction of Propane (1) - Liquid | Temperature, K - Liquid | Mole fraction of Propane (1) - Gas |
0.0000 | 273.15 | 0.0000 |
0.0000 | 283.15 | 0.0000 |
0.0000 | 293.15 | 0.0000 |
0.0000 | 303.15 | 0.0000 |
0.0000 | 313.15 | 0.0000 |
0.0624 | 303.15 | 0.1449 |
0.0656 | 313.15 | 0.1238 |
0.0728 | 273.15 | 0.1449 |
0.0829 | 293.15 | 0.1629 |
0.0848 | 283.15 | 0.1652 |
0.2226 | 313.15 | 0.3138 |
0.2326 | 303.15 | 0.3489 |
0.2331 | 273.15 | 0.4219 |
0.2333 | 293.15 | 0.3734 |
0.2452 | 283.15 | 0.3967 |
0.5473 | 303.15 | 0.6135 |
0.5542 | 293.15 | 0.6265 |
0.5600 | 283.15 | 0.6286 |
0.5771 | 273.15 | 0.6408 |
0.5844 | 313.15 | 0.6008 |
0.5851 | 273.15 | 0.6661 |
0.6102 | 313.15 | 0.6447 |
0.6176 | 283.15 | 0.6479 |
0.6254 | 293.15 | 0.6641 |
0.6436 | 303.15 | 0.6562 |
0.6979 | 293.15 | 0.7129 |
0.7011 | 273.15 | 0.7215 |
0.7054 | 303.15 | 0.7069 |
0.7061 | 283.15 | 0.7202 |
0.7065 | 313.15 | 0.7041 |
0.7542 | 293.15 | 0.7488 |
0.7565 | 273.15 | 0.7568 |
0.7592 | 283.15 | 0.7547 |
0.7633 | 313.15 | 0.7448 |
0.7652 | 303.15 | 0.7484 |
0.8178 | 273.15 | 0.8053 |
0.8282 | 313.15 | 0.8035 |
0.8297 | 303.15 | 0.7974 |
0.8312 | 293.15 | 0.7982 |
0.8343 | 283.15 | 0.8087 |
1.0000 | 273.15 | 1.0000 |
1.0000 | 283.15 | 1.0000 |
1.0000 | 293.15 | 1.0000 |
1.0000 | 303.15 | 1.0000 |
1.0000 | 313.15 | 1.0000 |
Temperature, K - Liquid | Azeotropic composition: mole fraction of Ethane, 1,1-difluoro- (2) - Liquid |
---|---|
254.31 | 0.2620 |
259.27 | 0.2660 |
269.26 | 0.2740 |
279.47 | 0.2820 |
287.94 | 0.2880 |
Pressure, kPa - Liquid | Azeotropic composition: mole fraction of Ethane, 1,1-difluoro- (2) - Liquid |
---|---|
293.00 | 0.2620 |
348.00 | 0.2660 |
482.00 | 0.2740 |
655.00 | 0.2820 |
831.00 | 0.2880 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,1-difluoro- (2) - Liquid | Temperature, K - Liquid | Mole fraction of Ethane, 1,1-difluoro- (2) - Gas |
0.0000 | 254.31 | 0.0000 |
0.0000 | 259.27 | 0.0000 |
0.0000 | 269.26 | 0.0000 |
0.0000 | 279.47 | 0.0000 |
0.0000 | 287.94 | 0.0000 |
0.1900 | 254.31 | 0.2220 |
0.1900 | 259.27 | 0.2230 |
0.1900 | 269.26 | 0.2240 |
0.1900 | 279.47 | 0.2260 |
0.1930 | 287.94 | 0.2270 |
0.2410 | 287.94 | 0.2590 |
0.2420 | 269.26 | 0.2530 |
0.2420 | 279.47 | 0.2570 |
0.2440 | 254.31 | 0.2480 |
0.2460 | 259.27 | 0.2500 |
0.2570 | 254.31 | 0.2520 |
0.2570 | 259.27 | 0.2550 |
0.2580 | 269.26 | 0.2600 |
0.2580 | 279.47 | 0.2640 |
0.2580 | 287.94 | 0.2680 |
0.2620 | 259.27 | 0.2531 |
0.2620 | 269.26 | 0.2540 |
0.2620 | 279.47 | 0.2650 |
0.2620 | 287.94 | 0.2660 |
0.2650 | 254.31 | 0.2560 |
0.2810 | 279.47 | 0.2770 |
0.2820 | 287.94 | 0.2800 |
0.3260 | 269.26 | 0.2920 |
0.3300 | 259.27 | 0.2840 |
0.3330 | 254.31 | 0.2770 |
0.3330 | 279.47 | 0.3120 |
0.3340 | 287.94 | 0.3080 |
0.6120 | 287.94 | 0.4400 |
0.6150 | 254.31 | 0.3670 |
0.6180 | 279.47 | 0.4200 |
0.6210 | 259.27 | 0.3660 |
0.6210 | 269.26 | 0.4000 |
0.7560 | 254.31 | 0.4330 |
0.7560 | 259.27 | 0.4570 |
0.7580 | 269.26 | 0.4840 |
0.7620 | 279.47 | 0.5080 |
1.0000 | 254.31 | 1.0000 |
1.0000 | 259.27 | 1.0000 |
1.0000 | 269.26 | 1.0000 |
1.0000 | 279.47 | 1.0000 |
1.0000 | 287.94 | 1.0000 |
Fixed | Measured | |
---|---|---|
Mole fraction of Propane (1) - Liquid | Temperature, K - Liquid | Mole fraction of Propane (1) - Gas |
0.0000 | 273.15 | 0.0000 |
0.0000 | 283.15 | 0.0000 |
0.0000 | 293.15 | 0.0000 |
0.0000 | 303.15 | 0.0000 |
0.0000 | 313.15 | 0.0000 |
0.0624 | 303.15 | 0.1449 |
0.0656 | 313.15 | 0.1238 |
0.0728 | 273.15 | 0.1449 |
0.0829 | 293.15 | 0.1629 |
0.0848 | 283.15 | 0.1652 |
0.2226 | 313.15 | 0.3138 |
0.2326 | 303.15 | 0.3489 |
0.2331 | 273.15 | 0.4219 |
0.2333 | 293.15 | 0.3734 |
0.2452 | 283.15 | 0.3967 |
0.5473 | 303.15 | 0.6135 |
0.5542 | 293.15 | 0.6265 |
0.5600 | 283.15 | 0.6286 |
0.5771 | 273.15 | 0.6408 |
0.5844 | 313.15 | 0.6008 |
0.5851 | 273.15 | 0.6661 |
0.6102 | 313.15 | 0.6447 |
0.6176 | 283.15 | 0.6479 |
0.6254 | 293.15 | 0.6641 |
0.6436 | 303.15 | 0.6562 |
0.6979 | 293.15 | 0.7129 |
0.7011 | 273.15 | 0.7215 |
0.7054 | 303.15 | 0.7069 |
0.7061 | 283.15 | 0.7202 |
0.7065 | 313.15 | 0.7041 |
0.7542 | 293.15 | 0.7488 |
0.7565 | 273.15 | 0.7568 |
0.7592 | 283.15 | 0.7547 |
0.7633 | 313.15 | 0.7448 |
0.7652 | 303.15 | 0.7484 |
0.8178 | 273.15 | 0.8053 |
0.8282 | 313.15 | 0.8035 |
0.8297 | 303.15 | 0.7974 |
0.8312 | 293.15 | 0.7982 |
0.8343 | 283.15 | 0.8087 |
1.0000 | 273.15 | 1.0000 |
1.0000 | 283.15 | 1.0000 |
1.0000 | 293.15 | 1.0000 |
1.0000 | 303.15 | 1.0000 |
1.0000 | 313.15 | 1.0000 |
Temperature, K - Liquid | Azeotropic composition: mole fraction of Ethane, 1,1-difluoro- (2) - Liquid |
---|---|
254.31 | 0.2620 |
259.27 | 0.2660 |
269.26 | 0.2740 |
279.47 | 0.2820 |
287.94 | 0.2880 |
Pressure, kPa - Liquid | Azeotropic composition: mole fraction of Ethane, 1,1-difluoro- (2) - Liquid |
---|---|
293.00 | 0.2620 |
348.00 | 0.2660 |
482.00 | 0.2740 |
655.00 | 0.2820 |
831.00 | 0.2880 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,1-difluoro- (2) - Liquid | Temperature, K - Liquid | Mole fraction of Ethane, 1,1-difluoro- (2) - Gas |
0.0000 | 254.31 | 0.0000 |
0.0000 | 259.27 | 0.0000 |
0.0000 | 269.26 | 0.0000 |
0.0000 | 279.47 | 0.0000 |
0.0000 | 287.94 | 0.0000 |
0.1900 | 254.31 | 0.2220 |
0.1900 | 259.27 | 0.2230 |
0.1900 | 269.26 | 0.2240 |
0.1900 | 279.47 | 0.2260 |
0.1930 | 287.94 | 0.2270 |
0.2410 | 287.94 | 0.2590 |
0.2420 | 269.26 | 0.2530 |
0.2420 | 279.47 | 0.2570 |
0.2440 | 254.31 | 0.2480 |
0.2460 | 259.27 | 0.2500 |
0.2570 | 254.31 | 0.2520 |
0.2570 | 259.27 | 0.2550 |
0.2580 | 269.26 | 0.2600 |
0.2580 | 279.47 | 0.2640 |
0.2580 | 287.94 | 0.2680 |
0.2620 | 259.27 | 0.2531 |
0.2620 | 269.26 | 0.2540 |
0.2620 | 279.47 | 0.2650 |
0.2620 | 287.94 | 0.2660 |
0.2650 | 254.31 | 0.2560 |
0.2810 | 279.47 | 0.2770 |
0.2820 | 287.94 | 0.2800 |
0.3260 | 269.26 | 0.2920 |
0.3300 | 259.27 | 0.2840 |
0.3330 | 254.31 | 0.2770 |
0.3330 | 279.47 | 0.3120 |
0.3340 | 287.94 | 0.3080 |
0.6120 | 287.94 | 0.4400 |
0.6150 | 254.31 | 0.3670 |
0.6180 | 279.47 | 0.4200 |
0.6210 | 259.27 | 0.3660 |
0.6210 | 269.26 | 0.4000 |
0.7560 | 254.31 | 0.4330 |
0.7560 | 259.27 | 0.4570 |
0.7580 | 269.26 | 0.4840 |
0.7620 | 279.47 | 0.5080 |
1.0000 | 254.31 | 1.0000 |
1.0000 | 259.27 | 1.0000 |
1.0000 | 269.26 | 1.0000 |
1.0000 | 279.47 | 1.0000 |
1.0000 | 287.94 | 1.0000 |
Fixed | Measured | |
---|---|---|
Mole fraction of Propane (1) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
0.0000 | 273.15 | 265.80 |
0.0000 | 283.15 | 372.80 |
0.0000 | 293.15 | 513.30 |
0.0000 | 303.15 | 689.90 |
0.0000 | 313.15 | 909.40 |
0.0624 | 303.15 | 775.10 |
0.0656 | 313.15 | 1005.30 |
0.0728 | 273.15 | 319.10 |
0.0829 | 293.15 | 587.60 |
0.0848 | 283.15 | 437.40 |
0.2226 | 313.15 | 1196.40 |
0.2326 | 303.15 | 940.70 |
0.2331 | 273.15 | 412.60 |
0.2333 | 293.15 | 726.90 |
0.2452 | 283.15 | 553.30 |
0.5473 | 303.15 | 1146.50 |
0.5542 | 293.15 | 876.30 |
0.5600 | 283.15 | 669.90 |
0.5771 | 273.15 | 504.90 |
0.5844 | 313.15 | 1467.80 |
0.5851 | 273.15 | 514.20 |
0.6102 | 313.15 | 1501.80 |
0.6176 | 283.15 | 674.50 |
0.6254 | 293.15 | 902.70 |
0.6436 | 303.15 | 1166.70 |
0.6979 | 293.15 | 901.40 |
0.7011 | 273.15 | 507.20 |
0.7054 | 303.15 | 1161.00 |
0.7061 | 283.15 | 677.90 |
0.7065 | 313.15 | 1479.50 |
0.7542 | 293.15 | 894.20 |
0.7565 | 273.15 | 506.50 |
0.7592 | 283.15 | 676.10 |
0.7633 | 313.15 | 1464.10 |
0.7652 | 303.15 | 1154.40 |
0.8178 | 273.15 | 512.90 |
0.8282 | 313.15 | 1479.40 |
0.8297 | 303.15 | 1162.30 |
0.8312 | 293.15 | 904.20 |
0.8343 | 283.15 | 671.30 |
1.0000 | 273.15 | 472.50 |
1.0000 | 283.15 | 633.90 |
1.0000 | 293.15 | 832.94 |
1.0000 | 303.15 | 1077.00 |
1.0000 | 313.15 | 1370.00 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,1-difluoro- (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
0.0000 | 254.31 | 257.00 |
0.0000 | 259.27 | 303.00 |
0.0000 | 269.26 | 422.00 |
0.0000 | 279.47 | 574.00 |
0.0000 | 287.94 | 727.00 |
0.1900 | 254.31 | 293.00 |
0.1900 | 259.27 | 347.00 |
0.1900 | 269.26 | 480.00 |
0.1900 | 279.47 | 650.00 |
0.1930 | 287.94 | 825.00 |
0.2410 | 287.94 | 829.00 |
0.2420 | 269.26 | 482.00 |
0.2420 | 279.47 | 655.00 |
0.2440 | 254.31 | 293.00 |
0.2460 | 259.27 | 348.00 |
0.2570 | 254.31 | 293.00 |
0.2570 | 259.27 | 348.00 |
0.2580 | 269.26 | 482.00 |
0.2580 | 279.47 | 655.00 |
0.2580 | 287.94 | 831.00 |
0.2620 | 259.27 | 348.00 |
0.2620 | 269.26 | 481.00 |
0.2620 | 279.47 | 655.00 |
0.2620 | 287.94 | 831.00 |
0.2650 | 254.31 | 293.00 |
0.2810 | 279.47 | 655.00 |
0.2820 | 287.94 | 831.00 |
0.3260 | 269.26 | 480.00 |
0.3300 | 259.27 | 345.00 |
0.3330 | 254.31 | 292.00 |
0.3330 | 279.47 | 654.00 |
0.3340 | 287.94 | 830.00 |
0.6120 | 287.94 | 773.00 |
0.6150 | 254.31 | 274.00 |
0.6180 | 279.47 | 610.00 |
0.6210 | 259.27 | 325.00 |
0.6210 | 269.26 | 449.00 |
0.7560 | 254.31 | 251.00 |
0.7560 | 259.27 | 297.00 |
0.7580 | 269.26 | 409.00 |
0.7620 | 279.47 | 556.00 |
1.0000 | 254.31 | 127.00 |
1.0000 | 259.27 | 156.00 |
1.0000 | 269.26 | 231.00 |
1.0000 | 279.47 | 331.00 |
1.0000 | 287.94 | 437.00 |
Fixed | Measured | |
---|---|---|
Mole fraction of Propane (1) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
0.0000 | 273.15 | 265.80 |
0.0000 | 283.15 | 372.80 |
0.0000 | 293.15 | 513.30 |
0.0000 | 303.15 | 689.90 |
0.0000 | 313.15 | 909.40 |
0.0624 | 303.15 | 775.10 |
0.0656 | 313.15 | 1005.30 |
0.0728 | 273.15 | 319.10 |
0.0829 | 293.15 | 587.60 |
0.0848 | 283.15 | 437.40 |
0.2226 | 313.15 | 1196.40 |
0.2326 | 303.15 | 940.70 |
0.2331 | 273.15 | 412.60 |
0.2333 | 293.15 | 726.90 |
0.2452 | 283.15 | 553.30 |
0.5473 | 303.15 | 1146.50 |
0.5542 | 293.15 | 876.30 |
0.5600 | 283.15 | 669.90 |
0.5771 | 273.15 | 504.90 |
0.5844 | 313.15 | 1467.80 |
0.5851 | 273.15 | 514.20 |
0.6102 | 313.15 | 1501.80 |
0.6176 | 283.15 | 674.50 |
0.6254 | 293.15 | 902.70 |
0.6436 | 303.15 | 1166.70 |
0.6979 | 293.15 | 901.40 |
0.7011 | 273.15 | 507.20 |
0.7054 | 303.15 | 1161.00 |
0.7061 | 283.15 | 677.90 |
0.7065 | 313.15 | 1479.50 |
0.7542 | 293.15 | 894.20 |
0.7565 | 273.15 | 506.50 |
0.7592 | 283.15 | 676.10 |
0.7633 | 313.15 | 1464.10 |
0.7652 | 303.15 | 1154.40 |
0.8178 | 273.15 | 512.90 |
0.8282 | 313.15 | 1479.40 |
0.8297 | 303.15 | 1162.30 |
0.8312 | 293.15 | 904.20 |
0.8343 | 283.15 | 671.30 |
1.0000 | 273.15 | 472.50 |
1.0000 | 283.15 | 633.90 |
1.0000 | 293.15 | 832.94 |
1.0000 | 303.15 | 1077.00 |
1.0000 | 313.15 | 1370.00 |
Fixed | Measured | |
---|---|---|
Mole fraction of Ethane, 1,1-difluoro- (2) - Liquid | Temperature, K - Liquid | Vapor or sublimation pressure, kPa - Liquid |
0.0000 | 254.31 | 257.00 |
0.0000 | 259.27 | 303.00 |
0.0000 | 269.26 | 422.00 |
0.0000 | 279.47 | 574.00 |
0.0000 | 287.94 | 727.00 |
0.1900 | 254.31 | 293.00 |
0.1900 | 259.27 | 347.00 |
0.1900 | 269.26 | 480.00 |
0.1900 | 279.47 | 650.00 |
0.1930 | 287.94 | 825.00 |
0.2410 | 287.94 | 829.00 |
0.2420 | 269.26 | 482.00 |
0.2420 | 279.47 | 655.00 |
0.2440 | 254.31 | 293.00 |
0.2460 | 259.27 | 348.00 |
0.2570 | 254.31 | 293.00 |
0.2570 | 259.27 | 348.00 |
0.2580 | 269.26 | 482.00 |
0.2580 | 279.47 | 655.00 |
0.2580 | 287.94 | 831.00 |
0.2620 | 259.27 | 348.00 |
0.2620 | 269.26 | 481.00 |
0.2620 | 279.47 | 655.00 |
0.2620 | 287.94 | 831.00 |
0.2650 | 254.31 | 293.00 |
0.2810 | 279.47 | 655.00 |
0.2820 | 287.94 | 831.00 |
0.3260 | 269.26 | 480.00 |
0.3300 | 259.27 | 345.00 |
0.3330 | 254.31 | 292.00 |
0.3330 | 279.47 | 654.00 |
0.3340 | 287.94 | 830.00 |
0.6120 | 287.94 | 773.00 |
0.6150 | 254.31 | 274.00 |
0.6180 | 279.47 | 610.00 |
0.6210 | 259.27 | 325.00 |
0.6210 | 269.26 | 449.00 |
0.7560 | 254.31 | 251.00 |
0.7560 | 259.27 | 297.00 |
0.7580 | 269.26 | 409.00 |
0.7620 | 279.47 | 556.00 |
1.0000 | 254.31 | 127.00 |
1.0000 | 259.27 | 156.00 |
1.0000 | 269.26 | 231.00 |
1.0000 | 279.47 | 331.00 |
1.0000 | 287.94 | 437.00 |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mass fraction of Propane (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
248.15 | 0.3497 | 0.0146 |
248.24 | 0.2008 | 0.0153 |
248.37 | 0.4922 | 0.0139 |
253.14 | 0.3497 | 0.0140 |
253.15 | 0.4922 | 0.0133 |
253.19 | 0.2008 | 0.0147 |
258.10 | 0.3497 | 0.0132 |
258.10 | 0.4922 | 0.0126 |
258.15 | 0.2008 | 0.0140 |
263.10 | 0.3497 | 0.0124 |
263.18 | 0.4922 | 0.0119 |
263.19 | 0.2008 | 0.0133 |
268.13 | 0.3497 | 0.0118 |
268.16 | 0.4922 | 0.0112 |
268.19 | 0.2008 | 0.0127 |
273.08 | 0.4922 | 0.0105 |
273.15 | 0.3497 | 0.0112 |
273.19 | 0.2008 | 0.0120 |
278.16 | 0.3497 | 0.0103 |
278.18 | 0.2008 | 0.0114 |
278.18 | 0.4922 | 0.0099 |
283.16 | 0.2008 | 0.0105 |
283.16 | 0.3497 | 0.0098 |
283.18 | 0.4922 | 0.0091 |
288.15 | 0.3497 | 0.0092 |
288.17 | 0.4922 | 0.0085 |
288.18 | 0.2008 | 0.0098 |
293.13 | 0.3497 | 0.0085 |
293.16 | 0.2008 | 0.0091 |
293.16 | 0.4922 | 0.0079 |
298.10 | 0.2008 | 0.0085 |
298.10 | 0.3497 | 0.0078 |
298.15 | 0.4922 | 0.0073 |
303.15 | 0.3497 | 0.0070 |
303.18 | 0.2008 | 0.0077 |
303.20 | 0.4922 | 0.0066 |
308.11 | 0.2008 | 0.0071 |
308.11 | 0.3497 | 0.0063 |
308.46 | 0.4922 | 0.0060 |
313.16 | 0.4922 | 0.0054 |
313.18 | 0.3497 | 0.0057 |
313.19 | 0.2008 | 0.0065 |
318.13 | 0.3497 | 0.0051 |
318.14 | 0.2008 | 0.0059 |
318.14 | 0.4922 | 0.0049 |
323.16 | 0.3497 | 0.0046 |
323.17 | 0.4922 | 0.0043 |
323.18 | 0.2008 | 0.0052 |
328.12 | 0.2008 | 0.0046 |
328.12 | 0.3497 | 0.0040 |
328.15 | 0.4922 | 0.0038 |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mass fraction of Propane (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
248.15 | 0.3497 | 0.0146 |
248.24 | 0.2008 | 0.0153 |
248.37 | 0.4922 | 0.0139 |
253.14 | 0.3497 | 0.0140 |
253.15 | 0.4922 | 0.0133 |
253.19 | 0.2008 | 0.0147 |
258.10 | 0.3497 | 0.0132 |
258.10 | 0.4922 | 0.0126 |
258.15 | 0.2008 | 0.0140 |
263.10 | 0.3497 | 0.0124 |
263.18 | 0.4922 | 0.0119 |
263.19 | 0.2008 | 0.0133 |
268.13 | 0.3497 | 0.0118 |
268.16 | 0.4922 | 0.0112 |
268.19 | 0.2008 | 0.0127 |
273.08 | 0.4922 | 0.0105 |
273.15 | 0.3497 | 0.0112 |
273.19 | 0.2008 | 0.0120 |
278.16 | 0.3497 | 0.0103 |
278.18 | 0.2008 | 0.0114 |
278.18 | 0.4922 | 0.0099 |
283.16 | 0.2008 | 0.0105 |
283.16 | 0.3497 | 0.0098 |
283.18 | 0.4922 | 0.0091 |
288.15 | 0.3497 | 0.0092 |
288.17 | 0.4922 | 0.0085 |
288.18 | 0.2008 | 0.0098 |
293.13 | 0.3497 | 0.0085 |
293.16 | 0.2008 | 0.0091 |
293.16 | 0.4922 | 0.0079 |
298.10 | 0.2008 | 0.0085 |
298.10 | 0.3497 | 0.0078 |
298.15 | 0.4922 | 0.0073 |
303.15 | 0.3497 | 0.0070 |
303.18 | 0.2008 | 0.0077 |
303.20 | 0.4922 | 0.0066 |
308.11 | 0.2008 | 0.0071 |
308.11 | 0.3497 | 0.0063 |
308.46 | 0.4922 | 0.0060 |
313.16 | 0.4922 | 0.0054 |
313.18 | 0.3497 | 0.0057 |
313.19 | 0.2008 | 0.0065 |
318.13 | 0.3497 | 0.0051 |
318.14 | 0.2008 | 0.0059 |
318.14 | 0.4922 | 0.0049 |
323.16 | 0.3497 | 0.0046 |
323.17 | 0.4922 | 0.0043 |
323.18 | 0.2008 | 0.0052 |
328.12 | 0.2008 | 0.0046 |
328.12 | 0.3497 | 0.0040 |
328.15 | 0.4922 | 0.0038 |