用法1：在C 5格内直接输入压力（kPaA）即可； 注：使用压力为20~5800kPaA水与蒸汽性质（参考）表用法2：若已知温度或工程压力（B6或D6单元格内），可点上方的“宏按钮”求得。序号温度压力工程压力物性数据重 度 比热粘 度导热系数热 焓表面张力汽化热CKPaAkg/cm2AKG/M3KCAL/KG-CCPKCAL/HMCKCAL/KGDYNE/CMKCAL/KG23.19 160.00618.86.31汽相3.2600.544440.014570.02553657.86160.0直接输入 10.00液相907.131.013810.168960.59013161.23 46.68 496.63可变,点击上方的宏按钮23158.856003.167 908.260.01452580.1702107146.93 657.58160.03497.550.025450.590424164.977003.663902.2323610.014776890.1635402445.57 659.08166.40492.680.025910.5890DENSITYVISCOSITYSURFACEENTHALPYTHERMAL CONDUCTIVITYNO.TEMPPRESVAPOR LIQUIDVAPOR LIQUIDTENSIONVAPOR LIQUIDboiloffVAPOR LIQUIDCKPaAKG/M3CPDYNE/CMKCAL/KGKCAL/KGKCAL/HR-M-C160.07200.131983.115541.05E-024.62E-0166.44 623.77 59.99 563.791.89E-025.60E-01269.11300.191978.236451.09E-024.05E-0164.91 627.44 69.01 558.431.94E-025.67E-01375.87400.250974.2790531.11E-023.69E-0163.73 630.18 75.78 554.401.98E-025.72E-01481.33500.308970.9030761.14E-023.45E-0162.75 632.27 81.24 551.032.01E-025.75E-01585.94600.366967.9332281.16E-023.26E-0161.91 634.10 85.86 548.242.04E-025.78E-01689.95700.423965.265931.17E-023.11E-0161.16 635.63 89.88 545.752.07E-025.80E-01793.50800.479962.8342291.19E-022.99E-0160.49 636.96 93.45 543.502.09E-025.81E-01896.70900.535960.5920411.20E-022.88E-0159.88 638.15 96.67 541.482.11E-025.83E-01999.621000.590 958.511.21E-022.80E-0159.32 639.20 99.61 539.602.13E-025.84E-0110102.311100.645956.5522461.22E-022.72E-0158.80 640.19102.31537.882.15E-025.85E-0111104.801200.700954.7106321.23E-022.65E-0158.31 641.07104.83536.242.16E-025.86E-0112107.131300.754952.9666141.24E-022.59E-0157.85 641.89107.18534.712.18E-025.87E-0113109.311400.808951.3081061.25E-022.53E-0157.41 642.65109.38533.272.19E-025.88E-0114111.371500.862949.725221.26E-022.49E-0157.00 643.35111.45531.902.21E-025.88E-0115113.321600.916948.2098391.27E-022.44E-0156.61 644.02...
