2 0 2012 mis kro 0 journal Original Mishra, R.[Ratikant] Kroupa, A.[Ales] Terzieff, P.[Peter] Ipser, H.[Herbert] Thermochim. Acta 2012 2012-04-03 Thermochemistry of Liquid Ni-Sb-Sn Alloys Ni-Sb-Sn alloys Thermochemistry Vapor pressure measurements Antimony vapor pressures Lead-free soldering 10.1016/j.tca.2012.02.024 536 68-73 1 tin Sn 1 Commercial source 1 99.999 5 Stated by supplier 2 antimony Sb 1 Commercial source 1 99.99 4 Stated by supplier 3 nickel Ni 1 Commercial source 1 99.99 4 Stated by supplier 3 1 1 1 2 1 Principal objective of the work MRM XXX 11/30/2011 1 (Relative) activity isopiestic measurments 2 Liquid Direct value, X Pure compound Liquid Solvent: Mole fraction 3 Liquid 3 1 .75 2 Pressure, kPa 101 3 1 Temperature, K 2 Mole fraction 2 Liquid 1 1171 4 2 .8714 4 1 .946 3 1 1196 4 2 .8357 4 1 .876 3 1 1217 4 2 .7979 4 1 .82 3 1 1236 4 2 .7665 4 1 .771 3 1 1257 4 2 .7403 4 1 .717 3 1 1274 4 2 .7216 4 1 .676 3 1 1290 4 2 .7053 4 1 .638 3 1 1303 4 2 .6921 4 1 .607 3 1 1315 4 2 .6807 4 1 .579 3 1 1324 4 2 .6719 4 1 .559 3 1 1331 4 2 .6638 4 1 .543 3 1 1337 4 2 .6563 4 1 .53 3 1 1342 4 2 .6549 4 1 .519 3 1 1345 4 2 .6481 4 1 .513 3 1 1347 4 2 .6521 4 1 .509 3 1 1165 4 2 .8515 4 1 .883 3 1 1175 4 2 .8279 4 1 .856 3 1 1184 4 2 .803 3 1 .832 3 1 1192 4 2 .8095 4 1 .811 3 1 1199 4 2 .7894 4 1 .793 3 1 1205 4 2 .7894 4 1 .778 3 1 1211 4 2 .7678 4 1 .763 3 1 1217 4 2 .7578 4 1 .748 3 1 1224 4 2 .7573 4 1 .73 3 1 1233 4 2 .7422 4 1 .708 3 1 1247 4 2 .7242 4 1 .673 3 1 1264 4 2 .6917 4 1 .632 3 1 1281 4 2 .6828 4 1 .592 3 1 1297 4 2 .6715 4 1 .556 3 1 1310 4 2 .6192 4 1 .527 3 1 1322 4 2 .644 3 1 .501 3 1 1333 4 2 .6329 4 1 .478 3 1 1341 4 2 .6173 4 1 .462 3 1 1093 4 2 .8877 4 1 .961 3 1 1103 4 2 .8565 4 1 .931 3 1 1122 4 2 .8421 4 1 .878 3 1 1140 4 2 .7784 4 1 .829 3 1 1162 4 2 .7569 4 1 .773 3 1 1186 4 2 .7281 4 1 .712 3 1 1206 4 2 .6856 4 1 .664 3 1 1225 4 2 .6655 4 1 .619 3 1 1244 4 2 .65 2 1 .575 3 1 1259 4 2 .6429 4 1 .541 3 1 1271 4 2 .6271 4 1 .515 3 1 1281 4 2 .6203 4 1 .493 3 1 1290 4 2 .6127 4 1 .474 3 1 1297 4 2 .6066 4 1 .46 3 1 1303 4 2 .5985 4 1 .448 3 1 1077 4 2 .8787 4 1 .948 3 1 1101 4 2 .8402 4 1 .88 3 1 1132 4 2 .7667 4 1 .797 3 1 1166 4 2 .6952 4 1 .711 3 1 1200 4 2 .6493 4 1 .629 3 1 1229 4 2 .6284 4 1 .563 3 1 1254 4 2 .6476 4 1 .507 3 1 1273 4 2 .5838 4 1 .467 3 1 1288 4 2 .6072 4 1 .436 3 1 1299 4 2 .6046 4 1 .415 3 1 1307 4 2 .5999 4 1 .4 3 1 1311 4 2 .6026 4 1 .392 3 1 1173 4 2 .8714 4 1 .946 3 1 1173 4 2 .8357 4 1 .881 3 1 1173 4 2 .7979 4 1 .836 3 1 1173 4 2 .7665 4 1 .801 3 1 1173 4 2 .7403 4 1 .766 3 1 1173 4 2 .7216 4 1 .742 3 1 1173 4 2 .7053 4 1 .72 3 1 1173 4 2 .6921 4 1 .706 3 1 1173 4 2 .6807 4 1 .691 3 1 1173 4 2 .6719 4 1 .682 3 1 1173 4 2 .6638 4 1 .674 3 1 1173 4 2 .6563 4 1 .669 3 1 1173 4 2 .6549 4 1 .66 3 1 1173 4 2 .6481 4 1 .66 3 1 1173 4 2 .6521 4 1 .652 3 1 1173 4 2 .8515 4 1 .882 3 1 1173 4 2 .8279 4 1 .856 3 1 1173 4 2 .803 3 1 .836 3 1 1173 4 2 .8095 4 1 .817 3 1 1173 4 2 .7894 4 1 .803 3 1 1173 4 2 .7894 4 1 .793 3 1 1173 4 2 .7678 4 1 .782 3 1 1173 4 2 .7578 4 1 .77 3 1 1173 4 2 .7573 4 1 .759 3 1 1173 4 2 .7422 4 1 .748 3 1 1173 4 2 .7242 4 1 .736 3 1 1173 4 2 .6917 4 1 .71 3 1 1173 4 2 .6828 4 1 .686 3 1 1173 4 2 .6715 4 1 .687 3 1 1173 4 2 .6192 4 1 .651 3 1 1173 4 2 .644 3 1 .635 3 1 1173 4 2 .6329 4 1 .616 3 1 1173 4 2 .6173 4 1 .611 3 1 1173 4 2 .8877 4 1 .958 3 1 1173 4 2 .8565 4 1 .921 3 1 1173 4 2 .8421 4 1 .868 3 1 1173 4 2 .7784 4 1 .814 3 1 1173 4 2 .7569 4 1 .766 3 1 1173 4 2 .7281 4 1 .721 3 1 1173 4 2 .6856 4 1 .693 3 1 1173 4 2 .6655 4 1 .668 3 1 1173 4 2 .65 2 1 .643 3 1 1173 4 2 .6429 4 1 .621 3 1 1173 4 2 .6271 4 1 .608 3 1 1173 4 2 .6203 4 1 .594 3 1 1173 4 2 .6127 4 1 .583 3 1 1173 4 2 .6066 4 1 .573 3 1 1173 4 2 .5985 4 1 .567 3 1 1173 4 2 .8787 4 1 .943 3 1 1173 4 2 .8402 4 1 .865 3 1 1173 4 2 .7667 4 1 .772 3 1 1173 4 2 .6952 4 1 .705 3 1 1173 4 2 .6493 4 1 .658 3 1 1173 4 2 .6284 4 1 .62 3 1 1173 4 2 .6476 4 1 .576 3 1 1173 4 2 .5838 4 1 .567 3 1 1173 4 2 .6072 4 1 .536 3 1 1173 4 2 .6046 4 1 .52 3 1 1173 4 2 .5999 4 1 .509 3 1 1173 4 2 .6026 4 1 .502 3 3 1 1 1 2 1 Principal objective of the work MRM XXX 11/30/2011 1 (Relative) activity isopiestic measurments 2 Liquid Direct value, X Pure compound Liquid Solvent: Mole fraction 3 Liquid 3 1 .6 1 Pressure, kPa 101 3 1 Temperature, K 2 Mole fraction 2 Liquid 1 1170 4 2 .8391 4 1 .87 3 1 1180 4 2 .8191 4 1 .843 3 1 1189 4 2 .8059 4 1 .82 3 1 1195 4 2 .7988 4 1 .803 3 1 1203 4 2 .782 3 1 .785 3 1 1208 4 2 .7685 4 1 .77 3 1 1214 4 2 .7628 4 1 .755 3 1 1220 4 2 .7513 4 1 .739 3 1 1228 4 2 .7282 4 1 .72 3 1 1239 4 2 .7276 4 1 .692 3 1 1256 4 2 .7081 4 1 .651 3 1 1273 4 2 .6439 4 1 .611 3 1 1290 4 2 .6597 4 1 .572 3 1 1303 4 2 .6386 4 1 .542 3 1 1316 4 2 .6306 4 1 .514 3 1 1328 4 2 .6086 4 1 .489 3 1 1338 4 2 .6016 4 1 .468 3 1 1098 4 2 .8805 4 1 .946 3 1 1113 4 2 .8489 4 1 .903 3 1 1130 4 2 .8099 4 1 .856 3 1 1150 4 2 .7602 4 1 .803 3 1 1174 4 2 .7204 4 1 .742 3 1 1196 4 2 .6901 4 1 .688 3 1 1217 4 2 .6634 4 1 .638 3 1 1234 4 2 .6362 4 1 .598 3 1 1252 4 2 .6126 4 1 .557 3 1 1265 4 2 .6065 4 1 .541 3 1 1276 4 2 .5849 4 1 .504 3 1 1285 4 2 .5742 4 1 .485 3 1 1293 4 2 .5675 4 1 .468 3 1 1300 4 2 .5591 4 1 .454 3 1 1306 4 2 .553 3 1 .442 3 1 1084 4 2 .8554 4 1 .928 3 1 1111 4 2 .7762 4 1 .825 3 1 1142 4 2 .7361 4 1 .771 3 1 1177 4 2 .683 3 1 .684 3 1 1210 4 2 .6317 4 1 .606 3 1 1238 4 2 .6003 4 1 .542 3 1 1261 4 2 .5842 4 1 .492 3 1 1279 4 2 .5566 4 1 .455 3 1 1292 4 2 .5429 4 1 .429 3 1 1302 4 2 .5325 4 1 .409 3 1 1309 4 2 .529 3 1 .398 3 1 1312 4 2 .525 3 1 .39 3 1 1173 4 2 .8391 4 1 .868 3 1 1173 4 2 .8191 4 1 .846 3 1 1173 4 2 .8059 4 1 .828 3 1 1173 4 2 .7988 4 1 .815 3 1 1173 4 2 .782 3 1 .802 3 1 1173 4 2 .7685 4 1 .791 3 1 1173 4 2 .7628 4 1 .78 3 1 1173 4 2 .7513 4 1 .769 3 1 1173 4 2 .7282 4 1 .756 3 1 1173 4 2 .7276 4 1 .734 3 1 1173 4 2 .7081 4 1 .705 3 1 1173 4 2 .6439 4 1 .694 3 1 1173 4 2 .6597 4 1 .655 3 1 1173 4 2 .6386 4 1 .641 3 1 1173 4 2 .6306 4 1 .623 3 1 1173 4 2 .6086 4 1 .616 3 1 1173 4 2 .6016 4 1 .602 3 1 1173 4 2 .8805 4 1 .917 3 1 1173 4 2 .8489 4 1 .875 3 1 1173 4 2 .8099 4 1 .833 3 1 1173 4 2 .7602 4 1 .788 3 1 1173 4 2 .7204 4 1 .743 3 1 1173 4 2 .6901 4 1 .705 3 1 1173 4 2 .6634 4 1 .672 3 1 1173 4 2 .6362 4 1 .651 3 1 1173 4 2 .6126 4 1 .629 3 1 1173 4 2 .6065 4 1 .62 3 1 1173 4 2 .5849 4 1 .602 3 1 1173 4 2 .5742 4 1 .591 3 1 1173 4 2 .5675 4 1 .581 3 1 1173 4 2 .5591 4 1 .573 3 1 1173 4 2 .553 3 1 .566 3 1 1173 4 2 .8554 4 1 .886 3 1 1173 4 2 .7762 4 1 .811 3 1 1173 4 2 .7361 4 1 .749 3 1 1173 4 2 .683 3 1 .687 3 1 1173 4 2 .6317 4 1 .64 3 1 1173 4 2 .6003 4 1 .605 3 1 1173 4 2 .5842 4 1 .573 3 1 1173 4 2 .5566 4 1 .555 3 1 1173 4 2 .5429 4 1 .538 3 1 1173 4 2 .5325 4 1 .526 3 1 1173 4 2 .529 3 1 .518 3 1 1173 4 2 .525 3 1 .513 3 3 1 1 1 2 1 Principal objective of the work MRM XXX 11/30/2011 1 Molar enthalpy of mixing with solvent, kJ/mol calculated from activity of Sb 2 Liquid Direct value, X 3 1 Liquid Pressure, kPa 101 3 Solvent: Mole fraction 3 Liquid 3 1 .75 2 1 Temperature, K 2 Mole fraction 2 Liquid 1 1171 4 2 .8714 4 1 1.1 2 1 1196 4 2 .8357 4 1 2.9 2 1 1217 4 2 .7979 4 1 5.1 2 1 1236 4 2 .7665 4 1 7.3 2 1 1257 4 2 .7403 4 1 9.6 2 1 1274 4 2 .7216 4 1 11.4 3 1 1290 4 2 .7053 4 1 13.2 3 1 1303 4 2 .6921 4 1 14.8 3 1 1315 4 2 .6807 4 1 16 2 1 1324 4 2 .6719 4 1 17 2 1 1331 4 2 .6638 4 1 17.8 3 1 1337 4 2 .6563 4 1 18.5 3 1 1342 4 2 .6549 4 1 18.6 3 1 1345 4 2 .6481 4 1 19.2 3 1 1347 4 2 .6521 4 1 18.8 3 1 1165 4 2 .8515 4 1 2 1 1 1175 4 2 .8279 4 1 3.3 2 1 1184 4 2 .803 3 1 4.8 2 1 1192 4 2 .8095 4 1 4.4 2 1 1199 4 2 .7894 4 1 5.6 2 1 1205 4 2 .7894 4 1 5.6 2 1 1211 4 2 .7678 4 1 7.2 2 1 1217 4 2 .7578 4 1 8 1 1 1224 4 2 .7573 4 1 8 1 1 1233 4 2 .7422 4 1 9.3 2 1 1247 4 2 .7242 4 1 11.1 3 1 1264 4 2 .6917 4 1 14.8 3 1 1281 4 2 .6828 4 1 15.8 3 1 1297 4 2 .6715 4 1 17 2 1 1310 4 2 .6192 4 1 21.6 3 1 1322 4 2 .644 3 1 19.6 3 1 1333 4 2 .6329 4 1 20.5 3 1 1341 4 2 .6173 4 1 21.8 3 1 1093 4 2 .8877 4 1 .4 1 1 1103 4 2 .8565 4 1 1.8 2 1 1122 4 2 .8421 4 1 2.5 2 1 1140 4 2 .7784 4 1 6.4 2 1 1162 4 2 .7569 4 1 8 1 1 1186 4 2 .7281 4 1 10.8 3 1 1206 4 2 .6856 4 1 15.3 3 1 1225 4 2 .6655 4 1 17.6 3 1 1244 4 2 .65 2 1 19 2 1 1259 4 2 .6429 4 1 19.7 3 1 1271 4 2 .6271 4 1 21 2 1 1281 4 2 .6203 4 1 21.5 3 1 1290 4 2 .6127 4 1 22.2 3 1 1297 4 2 .6066 4 1 22.5 3 1 1303 4 2 .5985 4 1 23.1 3 1 1077 4 2 .8787 4 1 .7 1 1 1101 4 2 .8402 4 1 2.6 2 1 1132 4 2 .7667 4 1 8.5 2 1 1166 4 2 .6952 4 1 14.4 3 1 1200 4 2 .6493 4 1 19.1 3 1 1229 4 2 .6284 4 1 20.9 3 1 1254 4 2 .6476 4 1 19.3 3 1 1273 4 2 .5838 4 1 24 2 1 1288 4 2 .6072 4 1 22.4 3 1 1299 4 2 .6046 4 1 22.7 3 1 1307 4 2 .5999 4 1 23 2 1 1311 4 2 .6026 4 1 22.8 3 3 1 1 1 2 1 Principal objective of the work MRM XXX 11/30/2011 1 Molar enthalpy of mixing with solvent, kJ/mol calculated from activity of Sb 2 Liquid Direct value, X 3 1 Liquid Pressure, kPa 101 3 Solvent: Mole fraction 3 Liquid 3 1 .6 1 1 Temperature, K 2 Mole fraction 2 Liquid 1 1170 4 2 .8391 4 1 6.2 2 1 1180 4 2 .8191 4 1 6.9 2 1 1189 4 2 .8059 4 1 7.4 2 1 1195 4 2 .7988 4 1 7.7 2 1 1203 4 2 .782 3 1 8.4 2 1 1208 4 2 .7685 4 1 9 1 1 1214 4 2 .7628 4 1 9.2 2 1 1220 4 2 .7513 4 1 9.7 2 1 1228 4 2 .7282 4 1 10.7 3 1 1239 4 2 .7276 4 1 10.7 3 1 1256 4 2 .7081 4 1 11.6 3 1 1273 4 2 .6439 4 1 15.9 3 1 1290 4 2 .6597 4 1 14.6 3 1 1303 4 2 .6386 4 1 16.4 3 1 1316 4 2 .6306 4 1 17.2 3 1 1328 4 2 .6086 4 1 19.4 3 1 1338 4 2 .6016 4 1 20 2 1 1098 4 2 .8805 4 1 4.5 2 1 1113 4 2 .8489 4 1 5.7 2 1 1130 4 2 .8099 4 1 7.3 2 1 1150 4 2 .7602 4 1 9.4 2 1 1174 4 2 .7204 4 1 11 2 1 1196 4 2 .6901 4 1 12.6 3 1 1217 4 2 .6634 4 1 14.4 3 1 1234 4 2 .6362 4 1 16.7 3 1 1252 4 2 .6126 4 1 19 2 1 1265 4 2 .6065 4 1 19.5 3 1 1276 4 2 .5849 4 1 21.4 3 1 1285 4 2 .5742 4 1 22.2 3 1 1293 4 2 .5675 4 1 22.7 3 1 1300 4 2 .5591 4 1 23.3 3 1 1306 4 2 .553 3 1 23.7 3 1 1084 4 2 .8554 4 1 5.5 2 1 1111 4 2 .7762 4 1 8.7 2 1 1142 4 2 .7361 4 1 10.4 3 1 1177 4 2 .683 3 1 13 2 1 1210 4 2 .6317 4 1 17.2 3 1 1238 4 2 .6003 4 1 20.2 3 1 1261 4 2 .5842 4 1 21.4 3 1 1279 4 2 .5566 4 1 23.4 3 1 1292 4 2 .5429 4 1 24.2 3 1 1302 4 2 .5325 4 1 24.8 3 1 1309 4 2 .529 3 1 25 2 1 1312 4 2 .525 3 1 25.2 3