Tài liệu Vật lí - Bảng tính chất bão hòa doc

Bảng 6: Tính chất vật lý amoniăc trên đường bão hòa t o C p bar C’ p k/J/kgK C’’ p k/J/kgK ë’ 10 - 2 W/mK ë’’ 10 -3 W/mK ç’ 10 -4 Ns/m 2 ç’’ 10 -4 Ns/m 2 Pr’ Pr’’ ù’’ m/s ä 10 - 3 N/m - 70 0.110 - 2.02 70.5 14.9 (4.85) (7.5) - 1.04 361.6 - - 60 0.120 4.38 2.05 68.3 15.3 (4.10) (7.8) 2.63 1.02 370.0 - - 50 0.410 4.41 2.09 66.0 16.9 3.46 8.15 2.31 1.00 377.2 38.0 - 40 0.719 4.44 2.14 63.8 18.0 2.41 8.45 2.03 1.00 383.8 35.7 - 30 1.198 4.73 2.21 61.4 19.1 2.50 8.75 1.82 1.01 389.6 33.4 - 20 1.906 4.51 2.30 59.0 20.6 2.18 9.10 1.68 1.01 394.8 31.1 - 10 2.914 4.55 2.41 56.6 22.3 1.93 9.40 1.58 1.02 399.4 28.9 0 4.301 4.60 2.54 54.3 24.2 1.74 9.70 1.49 1.03 403.0 26.6 10 6.158 4.65 2.70 52.0 26.2 1.59 10.05 1.42 1.04 405. 4 24.3 20 8.582 4.71 2.88 49.7 28.4 1.45 10.40 1.37 1.06 406.9 22.0 30 11.68 4.78 3.10 47.3 31.0 1.33 10.75 1.34 1.08 407.2 19.6 40 15.56 4.86 3.36 45.0 33.7 1.22 11.15 1.32 1.11 406.3 17.4 50 20.35 4.96 3.68 42.5 36.6 1.11 11.55 1.31 1.16 404.2 15.1 60 26.46 5.15 4.06 40.0 39.6 1.01 12.00 1.30 1.23 400.7 12.8 70 33.15 5.32 4.55 37.7 42.8 (0.91) 12.45 1.30 1.32 395.7 (10.5) 80 41.4 5 5.53 5.12 35.0 46.8 (0.82) 12.90 1.30 1.41 388.8 ()8.2 Bảng 7: Tính chất vật lý R12 trên đường bão hòa t o C p bar C’ p k/J/kg.K C’’ p k/J/kg.K ë’ 10 - 2 W/mK ë’’ 10 -3 W/mK ç’ 10 -4 Ns/m 2 ç’’ 10 -5 Ns/m 2 Pr’ Pr’’ ù’’ m/s ä 10 - 3 N/m - 70 0.1226 0.859 0.500 9.67 3.27 5.99 0.897 5.32 1.37 126.8 - - 60 0.2261 0.684 0.524 9.40 4.00 5.20 0.938 4.78 1.23 129.0 19.7 - 50 0.3913 0.871 0.540 9.13 4.70 4.56 0.980 4.35 1.13 131.0 18.3 - 40 0.6415 0.879 0.565 8.85 5.42 4.05 1.022 4.02 1.05 132.6 17.0 - 1.004 0.888 0.590 8.58 6.16 3.63 1.067 3.76 0.99 134.0 15.7 trường đại học công nghiệp hà nội 132 bài tập kỹ thuật nhiệt 30 - 20 1.509 0.900 0.615 8.30 6.88 3.28 1.109 3.55 0.98 135.2 14.4 - 10 2.191 0.915 0.640 8.03 7.59 2.98 1.150 3.39 0.90 135.9 13.1 -0 3.086 0.931 0.660 7.75 8.30 2.72 1.194 3.27 0.92 136.1 11.8 10 4.233 0.951 0.685 7.47 9.02 2.50 1.237 3.18 0.92 136.0 10.5 20 5.672 0.975 0.710 7.20 9.74 2.30 1.286 3.12 0.94 135.3 9.3 30 7.449 1.005 0.745 6.92 10.50 2.13 1.340 3.10 0.95 134.2 8.0 40 9.606 1.04 0.785 6.65 11.28 1.98 1.398 3.09 0.98 132.2 6.7 50 12.19 1.09 0.840 6.37 12.10 1.84 1.461 3.15 1.02 129.6 5.5 60 15.26 1.15 0.905 6.10 12.97 1.72 1.529 3.24 1.08 126.4 4.4 70 18.86 1.24 0.995 (5.83) 13.88 1.60 1.616 3.40 1.16 122.0 3.4 80 23.05 1.37 1.140 5.65 14.90 1.50 1.718 3.64 1.32 116.7 2.3 Bảng 8: Bảng hơi bão hòa của amoniac. t o C p bar ρ’ kg/dm 3 ρ’’ kg/m 3 v’ dm 3 /kg v’’ m 3 /kg h’ kJ/kg h’’ kJ/kg r’ kJ/kg s’ kJ/kg.K s’’ kJ/kg.K - 7 5 7.5142 -02 0.7311 7.8001 -02 1.3679 1.2820 +01 161.8 1645.1 1483.2 -0.4430 7.0425 - 7 4 8.1178 -02 0.7299 8.3864 -02 1.3700 1.1924 +01 166.2 1647.0 1480.7 -0.4208 7.0144 - 7 3 8.7622 -02 0.7288 9.0092 -02 1.3721 1.1100 +01 170.6 1648.8 1478.2 -0.3988 6.9866 - 7 2 9.449 5 -02 0.7277 9.6702 -02 1.3742 1.0341 +01 175.0 1650.7 1475.6 -0.3768 6.9592 - 7 1 1.0182 -01 0.7265 1.0371 -01 1.3764 9.6421 +00 179.5 1652.5 1473.1 -0.3549 6.9322 - 7 0 1.0962 -01 0.7254 1.1114 -01 1.3785 8.9976 +00 183.9 1654. 4 1470.5 -0.3332 6.9055 - 6 9 1.1792 -01 0.7243 1.1901 -01 1.3807 8.4029 +00 188.3 1656.2 1468.0 -0.3115 6.8791 - 6 8 1.2675 -01 0.7231 1.2733 -01 1.3829 7.8535 +00 192.7 1658.1 1465. 4 -0.2899 6.8531 - 6 7 1.3612 -01 0.7220 1.3613 -01 1.3851 7.3458 +00 197.1 1659.9 1462.8 -0.2684 6.8274 trường đại học công nghiệp hà nội 133 bài tập kỹ thuật nhiệt - 6 6 1.4608 -01 0.7208 1.4543 -01 1.3873 6.8760 +00 201.5 1661.8 1460.2 -0.2470 6.8021 - 6 5 1.5664 -01 0.7197 1.5526 -01 1.3895 6.4410 +00 206.0 1663.6 1457.6 -0.2257 7770 - 6 4 1.6784 -01 0.7185 1.6562 -01 1.3917 6.0379 +00 210.4 1665.4 1455.0 -0.2045 6.7523 - 6 3 17970 -01 0.7174 1.7655 -01 1.3940 5.6641 +00 214.8 1667.2 14524 -0.1834 6.7278 - 6 2 19226 -01 0.7162 1.8807 -01 1.3962 5.3172 +00 219.3 1669.0 1449. 8 -0.1623 6.7037 - 6 1 20554 -01 0.7151 2.0020 -01 1.38985 4.9950 +00 223.7 1670.8 1447. 1 - 1414 6799 - 6 0 2.1959 -01 0.7139 2.1297- 01 1.4008 4.6956+00 228.1 1672.6 1444. 5 -0.1205 6.6563 - 5 9 2.3443 -01 0.7127 2.2640- 01 1.4030 1.4170+00 232.6 1674. 4 1441. 8 -0.0997 6.6330 - 5 8 2.5009 -01 0.7116 2.4052- 01 1.4053 4.1577+00 237.0 1676.2 1439.2 -0.0790 6.6101 - 5 7 2.6663 -01 0.7104 2.5535- 01 1.4077 3.9162+00 241.5 1678.0 1436.5 -0.0584 6.5873 - 5 6 2.8406 -01 0.7092 2.7092- 01 1.4100 3.6911+00 245.9 1679.7 1433.8 -0.0379 6.5649 - 5 5 3.0243 -01 0.7081 2.8727- 01 1.4123 3.4811+00 250.4 1681.5 1431.1 -0.0174 6.5427 - 5 4 3.2178 -01 0.7069 3.0441- 01 1.4147 3.2850+00 254.8 1683.2 1428.4 0.0030 6.5207 - 5 3 3.4214 -01 0.7057 3.2238- 01 1.4170 3.1019+00 259.3 1685.0 1425.6 0.0233 6.4991 - 5 2 3.6356 -01 0.7045 3.4121- 01 1.4194 2.9308+00 263.8 1686.7 1422.9 0.0435 6.4776 - 5 1 3.8608 -01 0.7033 3.6092- 01 1.4218 27707+00 268.2 1688.4 1420.2 0.0636 6.4564 trường đại học công nghiệp hà nội 134 bài tập kỹ thuật nhiệt - 5 0 4.0975 -01 0.7021 3.8155- 01 1.4242 2.6209+00 272.7 1690.1 1417. 4 0.0837 6.4355 - 4 9 4.346 0 -01 0.7009 4.0312- 01 1.4226 2.4806+00 277.2 1691.8 1414. 6 0.1037 6.4148 - 4 8 4.6067 -01 0.6998 4.2568- 01 1.4291 2.3492+00 281.7 1693.5 1411.8 0.1236 6.3943 - 4 7 4.8803 -01 0.6986 4.4926- 01 1.4315 2.2259+00 286.1 1695.2 1409.9 0.1435 6.3740 - 4 6 5.1671 -01 0.6974 4.7388- 01 1.4340 2.1103+00 290.6 1696.9 1406.2 0.1632 6.3540 - 4 5 5.4676 -01 0.6962 - 014.9958 1.4365 20017+00 295.1 1698.5 1403. 4 0.1829 6.3342 - 4 4 5.7823 -01 0.6949 5.2640- 01 1.4390 1.8997+00 299.6 1700.2 1400.6 0.2026 6.3146 - 4 3 6.1117 -01 0.6937 5.5437- 01 1.4415 1.8039+00 304.1 1701.8 1397.7 0.2221 6.2952 - 4 2 6.4563 -01 0.6925 5.8353- 01 1.4440 1.7137+00 308.6 1703.4 1394.8 0.2416 6.2760 - 4 1 6.8167 -01 0.6913 6.1391- 01 1.4465 1.6289+00 313.1 1705.1 1392.0 0-2610 6.2570 - 4 0 7.1934 -01 0.6901 6.4555- 01 1.4491 1.5491+00 317.6 1706.7 1389.1 0.2803 6.2382 Bảng 8: Bảng hơi bão hòa của amoniac (tiếp) t o C p bar ρ’ kg/dm 3 ρ’’ kg/m 3 v’ dm 3 /kg v’’ m 3 /kg h’ kJ/kg h’’ kJ/kg r’ kJ/kg s’ kJ/kg.K s’’ kJ/kg.K - 3 9 7.5869 -01 0.6889 6.7850-01 1.4516 1.4738+00 322.1 1708.3 1386.2 0.2996 6.2196 - 3 8 7.9977 -01 0.6877 7.1278-01 1.4542 1.4030+00 326.6 1709.9 1383.2 0.3188 6.2012 - 3 7 8.4265 -01 0.6864 7.4845-01 14.568 1.3361+00 331.1 1711.4 1380.2 0.3379 6.1830 trường đại học công nghiệp hà nội 135 bài tập kỹ thuật nhiệt - 3 6 8.8738 -01 0.6852 7.8553-01 1.4594 1.2730+00 335.7 1713.0 1377.4 0.3570 6.1849 - 3 5 9.3402 -01 0.6840 8.2407-01 1.4621 1.2135+00 340.2 1714.6 1374. 4 0.3759 6.1471 - 3 4 9.8263 -01 0.6827 8.6411-01 1.4647 1.1573+00 344. 7 1716.1 1371.4 0.3949 6.1294 - 3 3 1.0333 +00 0.6815 9.0570-01 1.4674 1.1041+00 349.2 1717.6 1368.4 0.4137 6.1119 - 3 2 1.0860 +00 0.6802 9.4887-01 1.4701 1.0539+00 353.7 1719.1 1365.4 0.4325 6.0946 - 3 1 1.1409 +00 0.6790 9.9367-01 1.4726 1.0064-01 358.3 1720.7 1362.4 0.4512 6.0774 - 3 0 1.1980 +00 0.6777 1.0402+00 1.4755 9.6140-01 362.8 1722.1 1359.3 0.4699 6.0604 - 2 9 1.2574 +00 0.6765 1.0883+00 1.4782 9.1882-01 367.3 1723.6 1356.3 0.4884 6.0136 - 2 8 1.3191 +00 0.6752 1.1383+00 1.4810 8.7850-01 371.9 1725.1 1353.2 0.5070 6.0269 - 2 7 1.3833 +00 0.0740 1.1901+00 1.4837 8.4028-01 376.4 1726.5 1350.1 0.5254 6.0104 - 2 6 1.4499 +00 0.6727 1.2437+00 1.4865 8.0404-01 381.0 1728.0 1347.0 0.5428 5.9940 - 2 5 1.5191 +00 0.6714 1.2993+00 1.4893 7.6967-01 385.5 1729.4 1343.9 0.5621 5.9778 - 2 4 1.5910 +00 0.6702 1.3567+00 1.4921 7.3706-01 390.1 1730.8 1340.8 0.5804 5.9617 - 2 3 1.6655 +00 0.6689 1.4162+00 1.4950 7.0609-01 394.6 1732.2 1337.6 0.5986 5.9458 - 2 2 1.7428 +00 0.6676 1.4778+00 1.4979 6.7668-01 399.2 1733.6 1334. 4 0.6167 5.9300 - 2 1 1.8229 +00 0.6663 1.5415+00 1.5007 6.4874-01 403.7 1735.0 1331.2 0.6347 5.9143 trường đại học công nghiệp hà nội 136 bài tập kỹ thuật nhiệt - 2 0 1.9059+00 0.6651 1.6073+00 1.5036 6.2217-01 408.3 1736.3 1328.0 0.6527 5.8988 - 1 9 1.9920+00 0.6638 1.6753+00 1.5066 5.9691-01 412.9 1737.7 1324.8 0.6707 5.8835 - 1 8 2.0811+00 0.6625 1.7456+00 1.5095 5.7287-01 417. 4 1739.0 1321.6 0.6886 5.8682 - 1 7 2.1733+00 0.6612 1.8182+00 1.5125 5.5000-01 422.0 1740.3 1318.3 0.7064 5.8531 - 1 6 2.2688+00 0.6599 1.8932+00 1.5154 5.2821-01 426.6 1741.6 1315.1 0.7241 5.8381 - 1 5 2.3675+00 0.6586 1.9706+00 1.5184 5.0746-01 431.1 1742.9 1311.8 0.7418 5.8233 - 1 4 2.4697+00 0.6573 2.0505+00 1.5215 4.6885-01 435.7 1744.2 1308.5 0.7594 5.8085 - 1 3 2.5753+00 0.6560 2.1329+00 1.5245 4.5087-01 440. 3 1745.4 1305.2 0.7770 5.7939 - 1 2 2.6844+00 0.6546 2.2179+00 1.5276 4.3372-01 444. 9 1746.7 1301.8 0.7945 5.7794 - 1 1 2.7972+00 0.6533 2.3056+00 1.5307 4.1736-01 449. 4 1747.9 1298.5 0.8119 5.7650 - 1 0 2.9136+00 0.6520 2.3960+00 1.5338 4.0173-01 454. 0 1749.1 1295.1 0.8293 5.7508 -9 3.0339+00 0.6507 2.4892+00 1.5369 3.8681-01 458.6 1750.3. 1291.7 0.8467 5.7366 -8 3.1580+00 0.6493 2.5852+00 1.5401 3.7255-01 463.2 1751.5 1288.3 0.8639 5.7226 -7 3.2861+00 0.6480 2.6842+00 1.5432 3.5893-01 467.8 1752.6 1284.8 0.8811 5.7086 -6 3.4183+00 0.6466 2.7861+00 1.5464 3.4590-01 472.4 1753.8 1281.4 0.8983 5.6948 -5 3.5546+00 0.6453 2.8910+00 1.5497 3.3344-01 477.0 1754.9 1277.9 0.9154 5.6811 Bảng 8: Bảng hơi bão hòa của amoniac (tiếp) t o C p bar ρ’ kg/dm 3 ρ’’ kg/m 3 v’ dm 3 /kg v’’ m 3 /kg h’ kJ/kg h’’ kJ/kg r’ kJ/kg s’ kJ/kg.K s’’ kJ/kg.K -4 3.6951+00 0.6440 2.9990+00 1.5529 3.2152- 01 481.6 1756.0 1274.4 0.9324 5.6674 trường đại học công nghiệp hà nội 137 bài tập kỹ thuật nhiệt -3 3.8400+00 0.6426 3.1102+00 1.5562 3.1011- 01 486.2 1757.1 1270.9 0.4949 5.6539 -2 3.9892+00 0.6412 3.2246+00 1.5595 2.9919- 01 490.8 1758.2 1267.4 0.9663 5.6405 -1 4.1430+00 0.6399 3.3424+00 1.5628 2.8873- 01 495. 4 1759.2 1263.9 0.9832 5.6272 0 4.3013+00 0.6385 3.4634+00 1.5662 2.7871- 01 500.0 1760.3 1260.3 1.0000 5.6139 1 4.4643+00 0.6371 3.5880+00 1.5695 2.6911- 01 504.6 1761.3 1256.7 1.0168 5.6008 2 4.6322+00 0.6358 3.7160+00 1.5729 2.5990- 01 509.2 1762.3 1253.1 1.0335 5.5877 3 4.8048+00 0.6344 3.8476+00 1.5764 2.5107- 01 513.8 1763.3 1249.5 1.0501 5.5748 4 4.9925+00 0.6330 3.9829+00 1.5798 2.4260- 01 518.5 1764.3 1245.8 1.0667 5.5619 5 5.1652+00 0.6316 4.1219+00 1.5833 2.3448- 01 523.1 1765.3 1242.2 1.0832 5.5491 6 5.3531+00 0.6302 4.2648+00 1.5868 2.2668- 01 527.7 1766.2 1238.5 1.0997 5.5364 7 5.5463+00 0.6288 4.4115+00 1.5904 2.1919- 01 532.3 1767.1 1234.8 1.1162 5.5238 8 5.7448+00 0.6274 4.5622+00 1.5939 2.1200- 01 537.0 1768.0 1231.1 1.1326 5.5112 9 5.9487+00 0.6260 4.7169+00 1.5975 2.0510- 01 541.6 1768.9 1227.5 1.1489 5.4988 10 6.15836+00 0.6245 4.8757+00 1.6012 1.9846- 01 546.2 1769.8 1223.5 1.1652 5.4864 11 6.3735+00 0.6231 5.0388+00 1.6046 1.9208- 01 550.9 1770.6 1229.7 1.1814 5.4741 12 6.5944+00 0.6217 5.2062+00 1.6085 1.8595- 01 555.5 1771.5 15.9 1.1976 5.4618 13 6.8213+00 0.6203 5.3779+00 1.6122 1.8005- 01 560.2 1772.3 12.1 1.2138 5.4497 1 4 7.0541+00 0.6188 5.5541+00 1.6160 1.7437- 01 564.8 1773.1 1208.2 1.2299 5.4376 15 7.2929+00 0.6174 5.7349+00 1.6198 1.6891- 01 569.5 1773.8 1204.4 1.2459 5.4255 16 7.5380+00 0.6159 5.9204+00 1.6236 1.6365- 01 574.1 1774.6 1200.5 1.2619 5.4136 17 7.7893+00 0.6145 6.1105+00 1.6274 1.5859- 01 578.8 1775.3 1196.5 1.2779 5.17 18 8.0471+00 0.6130 6.3055+00 1.6313 1.5372- 01 583.5 1776.0 1192.6 1.2938 5.3899 19 8.3113+00 0.6115 6.5055+00 1.653 1.5372- 598.1 1776.7 11.88.6 1.3097 53781 trường đại học công nghiệp hà nội 138 bài tập kỹ thuật nhiệt 01 20 8.582+00 0.6101 6.7105+00 1.6392 1.4902- 01 592.8 1777.4 1184.6 1.3255 5.3664 21 8.8597+00 0.6086 6.9206+00 1.6432 1.4450- 01 597.5 1778.1 1180.6 1.3413 5.3548 22 9.1441+00 0.6071 7.1359+00 1.6472 1.4014- 01 602.2 1778.7 1176.5 1.3070 5.3432 23 9.4354+00 0.6056 7.3566+00 1.6513 1.3593- 01 609.9 1779.3 1172.4 1.3727 5.3317 24 9.7838+00 0.6041 7.5827+00 1.6354 1.3183- 01 611.6 1779.9 1168.3 1.3884 5.3202 25 1.0039+01 0.6026 7.8144+00 1.6595 1.2797- 01 616.3 1780.5 1164.2 1.4040 5.3098 26 1.0352+01 0.6011 8.0517+00 1.6637 1.2420- 01 621.0 1781.0 1160.1 1.4196 5.2975 27 1.0672+01 0.5995 8.2948+00 1.6679 1.2056- 01 625.7 1791.6 1155.9 1.4352 5.2862 28 1.1000+01 0.5980 8.5438+00 1.6722 1.1704- 01 630.4 1782.1 1151.7 1.4507 5.2749 29 1.1335+01 0.5965 8.7988+00 1.6765 1.1365- 01 635.1 1782.6 1147.4 1.4662 5.237 30 1.1678+01 0.5949 9.0599+00 1.6808 1.1038- 01 639.9 1783.0 1143.2 1.4816 5.2525 31 1.2029+01 0.5934 9.3273+00 1.6852 1.0721- 01 644. 6 1783.5 1138.9 1.4970 5.2414 Bảng 8: Bảng hơi bão hòa của amoniac (tiếp) t o C p bar ρ’ kg/dm 3 ρ’’ kg/m 3 v’ dm 3 /kg v’’ m 3 /kg h’ kJ/kg h’’ kJ/kg r’ kJ/kg s’ kJ/kg.K s’’ kJ/kg.K 32 1.2338+01 0.5918 906010+00 1.6897 1.0416- 01 649. 4 1783.9 1134.5 1.5124 5.2304 33 1.2755+01 0.5903 9.8813+00 1.6941 1.0120- 01 654.1 1784.3 1130.2 1.5277 5.2193 3 4 1.3130+01 0.5887 1.0168+01 1.6987 9.8346- 02 658.9 1784.7 1125.8 1.5431 5.2084 35 1.3513+01 0.5871 1.0462+01 1.7032 9.5566- 02 663.6 1785.0 1121.4 1.5584 5.1974 36 1.3905+01 0.5855 1.0762+01 1.7078 9.2916- 02 668.4 1785.4 1116.9 1.5736 5.1865 37 1.3906+01 0.5839 1.1070+01 1.7125 9.0335- 02 673.2 1785.7 1112.5 1.5889 5.1757 38 1.4715+01 0.5807 1.1385+01 1.7172 8.7837- 02 678.0 1785.9 1107.9 1.6041 5.1648 39 1.5133+01 0.5807 1.1707+01 1.7220 8.5420- 682.8 1786.2 1103.4 1.6192 5.1551 trường đại học công nghiệp hà nội 139 bài tập kỹ thuật nhiệt 02 4 0 1.5559+01 0.5791 1.2037+01 1.7268 8.3080- 02 687.6 1786.4 1098.8 1.6344 5.1433 4 1 1.5995+01 0.5775 1.2374+01 1.7317 8.0816- 02 692.4 1786.8 1094.2 1.6495 5.1326 42 1.6440+01 0.5758 1.2719+01 1.7366 7.8623- 02 697.3 1787.0 1089.5 1.6647 5.1219 4 3 1.6895+01 0.5742 1.3072+01 1.7416 7.6500- 02 702.1 1787.0 1084.9 1.6798 5.1112 4 4 1.7358+01 0.5725 1.3433+01 1.7466 7.4443- 02 707.0 1787.1 1080.1 1.6948 5.1006 4 5 1.7832+01 0.5709 1.3803+01 1.7517 7.2450- 02 711.8 1787.2 1075.4 1.7099 5.0899 4 6 1.8315+01 0.5692 1.4181+01 1.7568 7.0518- 02 716.7 1787.3 1070.6 1.7249 5.0794 4 7 1.8807+01 0.5675 1.4567+01 1.7620 6.8646- 02 721.6 1787.3 1065.7 1.7400 5.0688 4 8 1.89310+01 0.5658 1.4963+01 1.7673 6.6832- 02 726.5 1787.4 1060.8 1.7550 5.0582 4 9 1.9823+01 0.5641 1.5368+01 1.7726 6.5072- 02 731.4 1787.3 1055.9 1.7700 5.0477 50 2.0346+01 0.5624 1.5781+01 1.7780 6.3366- 02 736.4 1787.3 1051.0 1.7850 5.0372 51 2.0879+01 0.5607 1.6205+01 1.7835 6.1710- 02 741.3 1787.3 1045.9 1.8000 5.0267 52 2.1423+01 0.5590 1.6638+01 1.7890 6.0104- 02 746.3 1787.2 1040.9 1.8149 5.0162 53 2.1977+01 0.5572 1.7081+01 1.7946 5.8545- 02 751.2 1797.0 1035.8 1.8299 5.0057 5 4 2.2542+01 0.5555 1.7534+01 1.8002 5.7033- 02 756.2 1786.9 1030.7 1.8448 4.9953 55 2.3118+01 0.5537 1.7997+01 1.8060 5.5564- 02 761.2 1786.7 1025.5 1.8598 4.9848 56 2.3705+01 0.5519 1.8471+01 1.8118 5.4138- 02 766.2 1796.5 1020.2 1.8748 4.9744 57 2.4303+01 0.5502 1.8956+01 1.8177 5.2723- 02 771.3 1786.2 1015.0 1.8897 4.9639 58 2.4912+01 0.5484 1.9452+01 1.8236 5.1408- 02 776.3 1786.0 1009.6 1.9047 4.9535 59 2.5532+01 0.5465 1.9959+01 1.2897 5.0101- 02 781.4 1785.6 1004.2 1.9196 4.9431 60 26165+01 0.5447 2.0478+01 1.8358 4.8832- 02 786.5 1785.3 998.8 1.9346 4.9326 61 2.6808+01 0.5429 2.1009+01 1.8420 4.7598- 02 791.6 1784.9 993.3 1.9495 4.9222 trường đại học công nghiệp hà nội 140 bài tập kỹ thuật nhiệt 62 2.7464+01 0.54.10 2.1553+01 1.8483 4.6398- 02 796.7 1794.5 987.8 1.9645 4.9117 63 2.8131+01 0.5392 2.1108+01 1.8547 4.5232- 02 801.9 1784.1 982.2 1.9795 4.9013 6 4 2.8811+01 0.5373 2.2677+01 1.8611 4.4098- 02 807.1 1783.6 976.5 1.9945 4.8908 65 2.9503+01 0.5354 2.3259+01 1.8677 4.2995- 02 812.3 1783.0 970.8 2.0095 4.8803 66 3.0207+01 0.5335 2.3854+01 1.8744 4.1922- 02 817.5 1782.5 965.0 2.0245 4.8698 67 3.0924+01 0.5316 2.4463+01 1.8811 4.0378- 02 822.7 1781.9 959.2 2.0395 4.8593 Bảng 8: Bảng hơi bão hòa của amoniac (tiếp) t o C p bar ρ’ kg/dm 3 ρ’’ kg/m 3 v’ dm 3 /kg v’’ m 3 /kg h’ kJ/kg h’’ kJ/kg r’ kJ/kg s’ kJ/kg.K s’’ kJ/kg.K 68 3.1654+01 0.5297 2.0587+01 1.8889 3.9862- 02 828.0 1781.2 953.3 2.0515 4.8488 69 3.2396+01 0.5277 2.5725+01 1.8949 3.0873- 02 833.3 1780.6 947.3 2.0696 4.8383 70 3.3151+01 0.5256 2.6378+01 1.9020 3.7911- 02 838.6 1779.8 941.3 2.0847 4.8277 71 3.3991+01 0.5238 2.7046+01 1.9092 3.6974- 02 843.9 1779.1 935.1 2.0998 4.8171 72 3.4701+01 0.5218 2.7731+01 1.9165 3.6061- 02 849.3 1778.3 929.0 2.1149 4.8061 73 3.5496+01 0.5193 2.8432+01 1.9239 3.5172- 02 854.7 1777.4 2922.7 2.1301 4.7958 74 3.6304+01 0.5177 2.911+01 1.9315 3.4306- 02 860.1 1776.3 916.4 2.1453 4.7851 75 3.7127+01 0.5157 2.9384+01 1.9319 3.3463- 02 865.5 1775.5 910.0 2.1605 4.7753 76 3.7963+01 0.5136 3.0637+01 1.9469 3.2640- 02 871.0 1774.5 903.5 2.1758 4.7635 77 3.8813+01 0.5116 3.1403+01 1.9548 3.1839- 02 876.5 1773.5 897.0 2.1911 4.7527 78 3.9677+01 0.5094 3.2198+01 1.9629 3.1057- 02 882.1 1772.4 890.3 2.2064 4.7418 79 4.0556+01 0.5073 3.3008+01 1.9711 3.0296- 02 887.7 1771.3 883.6 2.2218 4.7309 80 4.1449+01 0- 5052 3.3838+01 1.9795 2.9553- 02 893.3 1770.0 876.8 2.2372 4.7199 85 4.6137+01 0.4941 3.8315+01 2.0237 2.6100- 921.9 1763.2 841.2 2.3151 4.6639 trường đại học công nghiệp hà nội 141 bài tập kỹ thuật nhiệt [...]... 2,2 Bảng 12: Tính chất vật lý trên đường bão hoà của R50 C’’p k/J/kgK λ' λ'' η’ η ’’ t o C p bar C’p k/J/kgK -9 0 0.07 0.73 -8 0 0.15 0.77 0.535 10.55 4.8 6.48 0.83 4.73 -7 0 0.28 0.82 0.553 10.16 5.4 5.43 0.88 -6 0 0.49 0.86 0.572 9.77 6.1 4.65 -5 0 0.81 0.91 0.595 9.38 6.8 -4 0 1.30 0.95 0.618 8.98 -3 0 1.98 0.99 0.640 -2 0 2.91 1.04 -1 0 4.14 0 -4 10 Ns/m2 1 0-4 Ns/m2 Pr’ Pr’’ ω ’’ δ m/s 103 N/m 0.94 127 -. .. 681.58 242.73 01 0.7561 1.8642 -5 4 5.217 8-0 1 1.4490 2.5328+00 0.6902 3.948201 440.8 8 682.06 421.19 0.7607 1.8613 -5 3 5.503 2-0 1 1.4463 2.6616+00 441.9 0 682.05 240.65 0.7654 1.8585 -5 2 5.800 9-0 1 1.4435 2.7954+00 0.6927 3.577 3- 442.93 683.03 240.10 01 0.7700 1.8557 -5 1 6.111 5-0 1 1.4408 2.9346+00 0.6941 -5 0 6.435 2-0 1 1.4381 3.0791+00 -4 9 6.772 6-0 1 1.4353 -4 8 7.123 9-0 1 -4 7 0.6914 3.757201 438.8 4 3.407701... 3.964 4-0 1 1.4623 1.9613+00 0.6838 5.098 7- 435.79 679.64 243.85 01 0.7373 1.8760 -5 8 4.193 2-0 1 1.4597 2.0664+00 0.6851 4.839 3- 436.80 680.13 243.32 01 0.7420 1.8730 -5 7 4.423 6-0 1 1.4570 2.1760+00 0.6863 4.595 5- 437.82 680.61 242.80 01 0.7467 1.8700 -5 6 4.682 9-0 1 1.4543 2.2902+00 0.6876 4.366401 681.10 242.26 0.7514 1.8670 -5 5 4.944 6-0 1 1.4517 24091+00 0.6889 4.151 0- 439.85 681.58 242.73 01 0.7561 1.8642 -5 4... 259.37 0.5795 2.0034 -9 0 4.895102 1.5408 2.790 4-0 1 0.6490 3.5837+00 405.4 8 664.4 0 258.91 0.5847 1.9983 -8 9 5.303 3- 1.5384 02 3.007 4-0 1 0.6500 3.3251+00 406.4 4 664.89 258.45 0.5898 1.9933 -8 8 5.739 9- 1.5359 02 3.238 3-0 1 0.6511 3.0880+00 407.39 665.38 257.99 0.5950 1.9984 -8 7 6.206 5- 1.5335 02 3.483 6-0 1 0.6521 2.8706+00 665.87 2.57.53 0.6001 1.9836 -8 6 6.204 6- 1.5310 02 3.744 2-0 1 0.6532 2.6708+00... 247.95 0.6992 1.9020 -6 6 2.630 6- 1.4806 01 1.3390+00 0.6754 7.468 5-0 1 428.78 676.22 247.44 0.7040 1.8986 -6 5 2.794 8- 1.0781 01 1.4165+00 0.6766 7.059 5-0 1 429.77 676.71 246.94 0.7088 1.8952 r kJ/kg s’ kJ/kg.K s’’ kJ/kg.K 418.9 4 Bảng 10: Hơi bão hòa của R22 (tiếp) t C p bar ρ’ kg/dm3 ρ’’ kg/m3 -6 4 2.967 2-0 1 1.4755 1.4977+00 0.6778 6.676 9- 430.77 677.20 246.43 01 0.7136 1.9819 -6 3 3.148 2-0 1 1.4728 1.5825+00... 257.07 0.6053 1.9788 -8 5 7.235902 15285 4.020 6-0 1 0.6542 2.4872+00 110.25 666.36 256.60 0.6104 1.9742 -8 4 7.802102 1.5261 4.313 6-0 1 0.6553 2.3183+00 411.21 667.35 256.14 0.6154 1.9696 -8 3 8.405 0- 1.5236 02 4.624 0-0 1 0.6563 2.1626+00 412.17 667.84 255.67 0.6205 1.9651 -8 2 9.046 6- 1.5211 02 4.952 5-0 1 0.6574 2.0192+00 413.13 668.33 255.20 0.6255 1.9606 -8 1 9.728 5- 1.5186 02 5.300 0-0 1 0.6585 1.8868+00... 0.6750 1.9200 -7 1 1.923901 1.4935 1.0006+00 0.6696 9.994 0-0 1 423.83 673.76 249.93 0.6799 1.9163 -7 0 2.051001 1.4909 1.0620+00 0.6707 9-4 15 9-0 1 424.82 674.25 249.44 0.6848 1.9126 -6 9 2.185001 1.4884 1.1265+00 0.6719 8.877 3-0 1 425.80 674.75 248.94 0.6996 1.9090 -6 8 2.326 0- 1.4858 01 1.1940+00 0.6730 8.375 0-0 1 426.79 675.24 248.45 0.6944 1.9055 -6 7 2.474 5- 1.4832 01 1.2648+00 0.6742 7.906 3-0 1 427.78 675.73... 8 1 1.3667 -0 1 1.590 1 9.637 8-0 1 0.6289 1.0376+00 422.92 607.45 184.53 0.6708 1.6311 8 0 1.4620 -0 1 1.5872 1.026 1-0 1 0.630 0 9.745 6-0 1 423.68 606.9 5 184.27 0.6747 1.6288 7 9 1.562701 1.584 3 1.091 7-0 1 0.631 2 9.160 1-0 1 424.45 608.4 6 184.00 0.6787 1.6265 7 8 1.6691 -0 1 1.581 3 1.160 7-0 1 0.632 4 9.615 8-0 1 425.23 608.9 7 183.74 0.6827 1.6242 7 7 1.7815 -0 1 1.5784 1.233 1-0 1 0.633 6 8.109 4-0 1 426.01 609.4... 0.633 6 8.109 4-0 1 426.01 609.4 7 183.47 0.6867 1.6220 7 6 1.9001 -0 1 1.5754 1.309 3-0 1 0.634 7 7.638 0-0 1 426.79 609.9 8 183.19 0.6906 1.6198 7 5 2.025 1- 1.5725 01 1.389 2-0 1 0.635 9 7.198 6-0 1 427.58 610.4 9 182.91 0.6946 1.6177 7 4 2.156 9- 1.5695 01 1.473 0-0 1 0.637 1 6.789 0-0 1 428.37 610.9 9 182.26 3 0.6986 1.6156 - 2.295 6- 1.560 8-0 1 0.638 6.409 8-0 1 429.76 611.5 18.2.34 0.7026 1.6136 1.566 trường đại học... 4 7 2 2.4416 -0 1 1.563 5 1.652 9-0 1 0.639 6 6.049 9-0 1 429.97 612.0 1 18.2.04 0.7066 1.6116 7 1 2.595201 1.560 6 1.749 3-0 1 0.640 8 5.716 5-0 1 430.77 612.52 181.75 0.7106 1.6096 7 0 2.756 6- 1.5576 01 1.850 2-0 1 0.6420 5.404 7-0 1 431.58 613.0 3 181.45 0.7146 1.6077 6 9 2.926201 1.544 6 1 95 8-0 1 0.643 3 5.113 0-0 1 432.40 613.5 4 181.14 0.7185 1.6058 6 8 3.1043 -0 1 1.551 6 1.066 2-0 1 0.6445 4.839 8-0 1 433 2 1 614.0 . Bảng 6: Tính chất vật lý amoniăc trên đường bão hòa t o C p bar C’ p k/J/kgK C’’ p k/J/kgK ë’ 10 - 2 W/mK ë’’ 10 -3 W/mK ç’ 10 -4 Ns/m 2 ç’’ 10 -4 Ns/m 2 Pr’. ()8.2 Bảng 7: Tính chất vật lý R12 trên đường bão hòa t o C p bar C’ p k/J/kg.K C’’ p k/J/kg.K ë’ 10 - 2 W/mK ë’’ 10 -3 W/mK ç’ 10 -4 Ns/m 2 ç’’ 10 -5 Ns/m 2 Pr’