Appendix B

Thermophysical Properties

Table B.1

Thermodynamic Properties of Selected Substances

SubstanceRTPTTPPΔHfusNBPΔHboilPcTcvcZcωab
Hydrogen412413.9673.59454.520.37448.712.9633.150.03363.135− 0.218726,7850.0165
Para-hydrogen412413.870.41432.520.27446.612.8632.940.03273.228− 0.218626,6700.0165
Oxygen259.854.361.46324390.19213.250.43154.60.002173.6610.0222149,7690.0198
Nitrogen296.863.15125.2215.577.36199.233.96126.20.002803.9360.0372148,2250.0240
Helium20771114.22220.72.2755.1950.011963.967− 0.38537510.0147
Neon41224.5643288.1627.1185.7726.844.490.001883.62− 0.03723,3450.0107
Argon208.183.81688.9172.287.3169.448.63150.70.001614.002− 0.002147,5870.0200
Xenon63.32161.4827.696.72164.995.8758.4289.70.0013.1420.0036454,3640.0320
Fluorine218.853.482.413196.385.03175.252.4144.40.001633.6910.0504125,8130.0178
Ammonia488.2195.561.021486239.81369113.3405.40.005163.3810.2558458,3770.0231
Hydrogen sulfide244187.7231.9574.7212.9546.689.63373.40.002983.4010.0961491,6200.0269
Krypton99.21115.8732108.8119.8107.555.1209.40.001213.101− 0.002251,6160.0245
Methane518.390.69117544.2111.7510.845.99190.60.007342.9230.0114249,5740.0268
Methanol259.5175.60.00181314338.2110381.04513.40.005812.8280.56461.028 × 1060.0409
Ethane276.590.370.0114595.7184.6489.448.72305.30.004513.8380.0995604,7710.0405
Ethanol180.5159.10.000021017351.4848.861.48513.90.006112.4660.64421.358 × 1060.0540
n-Octane72.79216.40.01399411.5398.6302.424.97569.30.003904.2490.39284.103 × 1060.1475
Isobutane143113.60.00021482.9261.5365.536.4407.80.00493.2710.18531.444 × 1060.0724
Propane188.685.48N/A1231.1425.342.47369.80.005053.2450.15241.017 × 1060.0563
Isopentane115.2112.7N/AN/A301342.533.7460.40.004463.5240.22661.988 × 1060.0883
n-Butane143134.90.00693494272.6384.737.96425.10.003734.290.21.505 × 1060.0724
n-Decane58.44243.50.01452392.6447.4276.321.03617.70.003794.5190.49035.735 × 1060.19
n-Dodecane48.81263.60.00631381.5489.5256.318.17658.10.005143.4360.5747.534 × 1060.2343
Isobutane143113.60.00021482.9261.5365.536.4407.80.00493.2710.1851.444 × 1060.0724
Isopropanol138.40N/AN/A355.6663.147.62508.30.003634.0620.6681.715 × 1060.0690
Ethylene296.41041.226568.2169.3482.250.4282.30.004843.430.086499,9440.0362
Cyclohexane98.79279.552.49402.4353.935640.75553.60.003753.5710.20912.378 × 1060.0878
n-Heptane82.98182.60.00176441.1371.5316.927.27540.10.005562.9560.34793.382 × 1060.1281
n-Hexane96.49177.80.0035618.8342.4329.930.58507.90.004003.9980.31172.666 × 1060.1074
n-Nonane64.83219.70.0046410.3424.2288.422.81594.60.004823.50.44684.898 × 1060.1686
n-Pentane115.2143.50.00012466.130935833.64469.70.005402.9770.24992.073 × 1060.0903
Propylene197.687.95N/AN/A225.4439.246.65365.60.004583.380.1407905,5790.0506
R2296.15115.70.004715301.9232.3232.549.89369.30.002033.5030.2208864,0550.0478
R134a81.49168.93.545263.7247.121740.59374.20.001704.4080.32691.09 × 1060.0596
R290188.685.4811231.1425.342.47369.80.005053.2450.15241.0 × 1060.0563
R404a85.19− 55511226.6199.737.35345.30.001934.0650.2751.0 × 1060.0598
R21844.22125.50.02119141.1236.5105.126.43450.001693.4170.32011.4 × 1060.0845
R245fa62.03171.10.1303258.5288.319636.51427.20.002033.5610.3791.5 × 1060.0756
R507a84.1− 55511226.1196.337.14343.90.001993.9030.27931 × 1060.0599
R508b87.16− 55511184.916339.25287.10.00173.7350.2272664,0530.047

t0010

R=, gas constant (J/kg K); TPT, triple point temperature (K); TPP, triple point pressure (bar); ΔHfus=, fusion heat at triple point (kJ/kg); NBP, normal boiling point (K); ΔHboil=, boiling enthalpy at normal boiling point; P, pressure (bar); T, temperature (K); v, specific volume (m3/kg); Z, compressibility factor; subscript “c”, critical point; ω, accentric factor; a, b, constants in Peng-Robinson equation of state.

Table B.2

Properties of Air at Atmospheric Pressure

T (°C)ρ, (g/dm3)μ, (μPa s)cp, (J/kg K)k, (mW/m K)Prβ, (K− 1)c, (m/s)γ
− 20047.615.20110026.6670.78210.01367171.61.401
− 17033.777.31110029.6680.75810.009695203.71.401
− 14026.169.296100212.530.74350.00751231.41.401
− 11021.3511.16100315.260.73320.006129256.21.401
− 8018.0312.93100317.870.72510.005177278.81.401
− 5015.6114.6100320.370.71860.004481299.61.401
− 2013.7616.19100322.770.71310.00395319.11.401
1012.317.7100425.090.70860.003532337.41.4
4011.1219.15100627.320.70490.003193354.71.4
7010.1520.54100829.490.7020.002914371.21.398
1009.33421.88101131.60.69990.00268386.81.397
1308.63923.18101433.640.69850.00248401.81.395
1608.04124.43101835.640.69780.002309416.21.393
1907.5225.64102337.590.69770.002159429.91.39
2207.06326.82102839.50.69820.002028443.21.387
2506.65827.96103441.370.69910.0019124561.384
2806.29629.07104143.20.70040.001808468.31.381
3105.97330.16104745.00.70190.001715480.31.378
3405.6831.22105446.770.70380.001631491.91.374
3705.41532.26106148.510.70580.001555503.11.371
4005.17433.28106950.230.70790.001486514.11.367
4304.95334.27107651.920.71010.001422524.71.364
7603.37144.21114769.340.73140.00096796291.334
7903.27645.04115370.840.73280.0009406637.51.332
8203.18645.86115872.330.73410.00091486461.33
8503.10146.67116373.820.73530.0008904654.31.328
8803.0247.48116875.290.73640.0008672662.61.326
9102.94448.28117276.750.73740.0008452670.71.324
9402.87149.07117778.210.73830.0008243678.81.323
9702.80249.85118179.650.73910.0008044686.71.321
10002.73650.63118581.090.73980.0007855694.51.32

t0015

T, temperature; ρ, density; μ, dynamic viscosity; cp, specific heat; k,thermal conductivity; Pr, Prandtl number; β, volume expansion coefficient; c, sound speed; γ,adiabatic expansion coefficient; ω = − 0.009278,accentric factor. Critical parameters: Tc = 132.531 K, Pc = 37.86 bar, vc = 2.917 dm3/kg.

Table B.3

Thermophysical Properties of Pure Water at Atmospheric Pressure

T (°C)ρ, (kg/m3)μ, (Pa s)cp, (J/kg K)k, (W/mK)Prβ, (K− 1)c, (m/s)σ, (N/m)
510000.00151942000.557611.440.0000113514260.07494
10999.70.00130741880.56749.6420.0000874314480.07422
15999.10.00113841840.57698.2530.000152314670.07348
20998.20.00100241830.58617.1520.00020914830.07273
25997.10.000890541830.59486.2630.000259414970.07197
30995.70.000797741830.6035.5340.000305115090.07119
359940.000719641830.61074.9290.00034715200.0704
40992.20.000653341820.61784.4220.000385915280.06959
45990.20.000596341820.62443.9940.000422515340.06877
509880.000547141810.63053.6280.000457215370.06794
55985.70.000504241820.6363.3150.000490315380.0671
60983.20.000466641830.6413.0450.000522115370.06624
65980.60.000433441840.64552.810.000552815340.06536
70977.80.00040441870.64952.6050.000582715290.06448
75974.90.000377941900.6532.4250.000611815230.06358
80971.80.000354541940.65622.2660.000640215140.06267
85968.60.000333541990.65892.1250.000668215040.06175
90965.30.000314542040.661320.000695814910.06081
95961.90.000297442100.66341.8880.00072314750.05987
1000.58960.0000122720420.025060.99960.002881472.80.05891

t0020

T, temperature; ρ, density; μ,dynamic viscosity; cp, specific heat; k, thermal conductivity; Pr, Prandtl number; β, volume expansion coefficient; c, sound speed; σ, superficial tension; ω = 0.3443, accentric factor. Critical parameters: Tc = 373.984 °C, Pc = 220.64 bar, vc = 3.106 dm3/kg. Triple point parameters: Tt = 0.01 °C, Pt = 611.732 Pa.

Table B.4

Thermophysical Properties of Water at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
0.010.0061275.6410004.23547.5179213.84N/A206.01.8717.079.2161.0083.6721.33
100.012374.22999.74.19567.413079.6450.0872106.31.8717.629.4611.0063.5481.33
200.023472.73998.24.1858610027.1540.20957.781.8818.229.7271.0043.4351.33
300.042571.19995.64.18602.9797.75.5350.30532.91.8918.8810.011.0033.3321.33
400.073869.59992.24.18617.8653.34.4230.38619.531.9019.5910.311.0023.2391.33
500.123467.949884.18630.4547.13.6290.45712.041.9220.3610.621.0013.1561.33
600.199366.24983.24.18640.9466.63.0450.5227.6741.9421.1810.9313.0821.33
700.311864.48977.74.19649.54042.6050.5835.0451.9622.0611.260.99953.0171.33
800.473762.67971.84.19656.2354.52.2660.643.4091.982311.590.99932.9621.33
900.701260.81965.34.20661.3314.520.6962.3622.012411.930.99942.9171.34
1001.01358.91958.44.22665.1281.91.7870.751.6742.0425.0812.2712.8821.34
1101.43256.969514.23667.6254.81.6150.8041.2112.0826.2212.611.0012.8571.34
1201.98554.96943.24.25669.1232.11.4740.8580.8922.1227.4412.961.0042.8431.35
1302.752.93934.94.27669.72131.3570.9120.6692.1728.7313.31.0072.841.36
1403.61250.85926.24.29669.4196.61.2590.9680.5092.2330.0913.651.0122.8491.36
1504.75748.74917.14.31668.3182.51.1781.0260.3932.3031.5413.991.022.8721.37
1606.17746.59907.54.34666.4170.31.1091.0870.30712.3733.0614.341.0292.9081.39
1707.91544.4897.54.37663.7159.61.0511.1520.2432.4634.6614.681.0422.9591.40
18010.0242.19887.14.40660.2150.21.0021.2210.1942.5636.3415.031.0573.0271.42
19012.5439.94876.14.44655.9141.80.96071.2960.1562.6738.0915.371.0773.1141.44
20015.5437.67864.74.49650.7134.40.92691.3770.1272.8039.9315.711.13.2211.46
21019.0635.38852.84.54644.7127.70.89941.4670.1042.9441.8516.061.1293.3511.48
22023.1833.06840.34.60637.6121.60.87771.5670.0863.1143.8616.411.1623.5081.52
23027.9530.73827.34.67629.51160.86151.6790.0713.3045.9616.761.2033.6971.55
24033.4528.39813.54.76620.3110.90.85081.8070.063.5148.1517.121.253.9231.59
25039.7426.04799.14.86609.8106.20.84551.9540.0503.7750.4617.491.3064.1951.64
26046.8923.68783.84.97598101.70.8462.1260.0424.0652.917.881.3734.5231.70
2705521.33767.75.11584.597.550.8532.330.0364.4155.4918.281.4534.9231.77
28064.1318.99750.55.28569.493.560.86732.5760.0314.8358.2818.71.5495.4151.86
29074.3816.66732.25.48552.389.710.89082.880.0265.3361.3119.151.6666.0321.97
30085.8414.35712.45.74533.185.950.92623.2660.0225.9764.6719.651.8136.8222.11
31098.6112.086916.08511.382.220.97823.7730.0186.7868.4520.212.0017.8612.29
320112.89.858667.46.54486.878.461.0544.470.0157.8772.8420.842.2519.2782.54
330128.57.6976417.2458.874.571.175.4890.0139.4178.121.62.60311.312.91
340145.95.62610.88.24426.970.451.3597.1160.01111.884.6822.553.13714.433.47
350165.23.66574.710.1389.765.881.71110.10.008815.993.4823.814.05819.774.47
360186.61.872528.114.7344.460.392.57417.110.00725.2106.625.716.08530.796.74
370210.30.3846453.141.7280.752.257.76545.880.005070.4132.629.5715.764.5318.0
373.9220.40.0004349.4N/A210.841.95277.187.510.0034340.11803769.91104.584.5

t0025

T, temperature (°C); P, pressure (bar); σ=, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.5

Thermophysical Properties of Hydrogen at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
140.082.97777.06.99274.3624.302.2910.587.633210.5614.511.240.9074.321.69
150.132.81976.17.33581.6221.681.9511.264.704410.6915.211.270.8970.671.70
160.212.65675.37.71787.5519.391.7112.013.074210.8515.941.310.8967.821.72
170.322.49074.38.13292.2617.401.5312.872.106611.0316.691.340.8965.691.74
180.472.32173.48.57495.8515.691.4013.851.499611.2517.491.370.8864.231.77
190.132.81976.17.33581.6221.681.9511.264.704410.6915.211.270.8970.671.70
200.911.97771.39.563100.112.971.2416.180.828811.8519.211.440.8963.201.84
211.221.80470.110.1310111.921.2017.600.637012.2520.151.480.9063.631.89
221.591.63068.910.76101.111.021.1719.260.498112.7521.161.510.9164.741.95
232.041.45867.611.48100.710.261.1721.230.395113.3622.251.540.9366.612.03
242.581.28666.212.3199.89.611.1823.600.317114.1223.431.681.0169.392.12
253.211.11764.713.2898.519.031.2226.550.256915.0724.721.731.0573.322.23
263.940.95263.114.4696.948.511.2730.300.209816.2926.141.781.1178.772.37
274.780.79061.315.9595.28.001.3435.280.172217.9027.731.851.1986.382.56
285.740.63459.317.9193.47.491.4442.190.141820.0929.531.921.3197.272.82
296.820.48457.120.6991.646.951.5752.500.116823.2431.622.011.47113.613.19
308.040.34354.525.0290.026.351.7669.500.095728.1534.112.111.74140.123.76
319.420.21351.432.9988.655.652.10102.690.077536.8137.282.262.23189.424.75
3210.960.09747.153.1487.644.842.93193.050.060655.6842.112.503.31308.866.89
33.112.880.001735.32001000N/AN/A981.450.0367131.7459.933.417.501036.7115.44

t0030

T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.6

Thermophysical Properties of Oxygen at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
55N/A22.301303.51.455201747.535.41N/A80.0290.934.484.150.8618.281.39
600.0120.981283.1126.4194.3582.46379.023.4921.4630.954.984.550.8616.871.39
650.0219.661260.71.65187.2460.774.063.587.21770.965.494.960.8715.701.38
700.0618.3481237.91.657180.1373.973.443.702.89330.975.995.360.8714.701.38
750.1517.0391214.99.855172.9310.3717.693.831.33060.986.505.750.8613.841.39
800.3015.7391191.41.66165.8262.532.63N/A0.68190.977.036.150.8513.131.40
850.5714.4501167.51.669158.6225.612.374.150.38090.977.566.540.8412.581.41
900.9913.1761142.91.683151.3196.382.184.360.22810.978.126.940.8312.221.43
951.6311.9191117.71.704144172.662.044.590.14450.988.707.330.8312.031.46
1002.5410.68291091.51.731136.7152.961.944.880.09591.009.317.730.8312.041.49
1053.799.47071064.41.765129.3136.231.865.210.06611.049.968.130.8512.261.52
1105.438.28611035.91.808121.9121.741.815.620.04701.0910.668.550.8812.711.57
1157.567.13281006.01.861114.4108.971.776.130.03421.1611.428.980.9213.421.62
12010.226.0154974.21.927106.997.531.766.760.02541.2612.269.430.9714.491.70
12513.514.9387939.72.01399.4387.091.76N/A0.01921.3813.199.911.0416.051.80
13017.493.9088902.62.15292.0277.591.819.520.01461.5614.2610.441.1418.361.95
13522.252.9333861.02.3584.5468.691.9111.690.01121.8115.5011.061.2921.962.17
14027.882.0224813.12.68276.9760.202.1015.400.00862.2217.0411.821.5428.072.52
14534.481.192755.03.33769.1151.852.5023.040.00653.0019.0912.882.0240.283.17
15042.190.472675.55.22560.1642.903.7346.630.00474.9522.3914.713.2674.614.73
15449.310.036547.415.4248.0432.1310.31N/A0.003110.6329.6319.146.86218.28.44

t0035

T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.7

Thermophysical Properties of Nitrogen at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
640.1511.9581863.72.002171.5297.503.474.781.28691.065.714.440.8216.131.41
650.1711.7169859.61.994169.5282.083.324.821.09501.065.824.510.8215.951.41
700.3910.5262838.52.005159.5220.262.775.110.52741.086.354.880.8315.241.43
750.769.3624816.727.05149.5176.7531.99N/A0.28251.116.915.260.8414.821.44
801.378.2276793.92.054139.5145.112.14N/A0.16421.147.495.650.8614.691.47
852.297.1240770.12.094129.6121.311.96N/A0.10181.198.116.060.8914.891.51
903.606.0544745.02.147119.6102.831.856.940.06631.268.796.480.9315.461.56
955.415.0222718.37.073109.788.025.68N/A0.04491.359.556.940.9816.541.64
1007.784.0318689.42.30199.7175.771.759.150.03131.5510.447.431.1018.141.67
10510.833.0892659.02.43290.1565.721.7710.210.02221.4411.497.981.0018.191.80
11014.662.2025625.62.73680.7256.961.9312.900.01601.1612.808.630.7820.833.96
11519.371.3844583.83.21170.4548.232.2018.780.01152.0214.519.441.3231.693.57
12025.110.6578527.54.35159.1939.022.8733.000.00803.7416.9810.622.3456.884.00
12532.070.0829430.211.7944.9627.357.17136.450.00499.6522.5213.335.71187.71N/A
12633.650.0083378.620.1638.9322.7711.79266.830.003913.2726.6315.377.66308.908.52

t0040

T, temperature (K); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.8

Thermophysical Properties of Carbon Dioxide at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
− 56.65.1815.77671178.51.953180.4256.72.78N/A0.07270.9010.9710.950.906.111.44
− 506.8214.32481154.614.29171.8229.319.073.270.05580.9511.5111.310.936.301.46
− 458.3213.23671135.91.989165.3210.72.543.360.04600.9811.9411.580.956.501.48
− 4010.0512.16541116.52.011158.9193.82.45N/A0.03831.0312.4111.870.986.741.51
− 3512.0211.11181096.44.99152.5178.35.83N/A0.03201.0712.9012.161.017.041.54
− 3014.2810.07691075.72.377146.3164.22.673.930.02701.1313.4212.461.057.411.57
− 2516.839.06191054.22.114140151.32.284.380.02281.1913.9912.781.097.871.62
− 2019.708.06821031.72.165133.8139.32.254.740.01931.2714.6013.121.148.441.67
− 1522.917.09741008.02.227127.6128.32.245.180.01651.3615.2713.471.209.151.73
− 1026.496.1514982.92.306121.41182.245.730.01401.4716.0113.861.2710.061.81
− 530.465.2326956.22.406115.1108.42.276.440.01201.6116.8414.301.3711.231.92
034.854.3440927.42.539108.799.392.327.370.01021.7917.7714.791.4912.792.05
539.693.4893896.02.72102.290.812.428.670.00872.0318.8615.361.6514.952.23
1045.022.6737861.12.98595.4682.552.5810.590.00742.3720.1416.061.8918.122.49
1550.871.9043821.23.40588.3274.432.8713.710.00622.8921.7416.952.2523.172.88
2057.291.1924773.44.15980.4866.153.4219.520.00513.7723.8318.192.8732.323.51
2564.340.5584711.85.90371.4357.234.7333.720.00415.5426.9420.164.1453.054.69
3072.140.0582602.413.8357.6944.6810.71102.990.002910.1633.8625.037.51128.226.80
30.973.640.0025521.318.0549.0737.2513.71141.420.002411.7739.2129.168.75163.455.80

t0045

T, temperature (°C); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.9

Thermophysical Properties of Ammonia at Saturation

TPσρLcpLkLμLPrLβLvVcpVkVμVPrVβVγ
− 77.60.06144.78733.63.95821.2564.12.7131.51415.682.06219.646.840.71825.231.325
− 650.156341.51719.34.162774.8430.62.3121.5866.4782.10219.827.1620.75974.991.328
− 550.301338.95707.84.332739.3357.52.0951.633.4982.14720.077.4330.79514.861.331
− 450.544736.426964.387704.63031.8871.7172.0082.20520.437.7150.83284.771.336
− 350.930733.93683.94.439670.8261.21.7281.8041.2152.27720.888.0040.87294.721.343
− 251.51531.46671.44.489638228.31.6061.8960.76952.36521.448.30.91544.7161.352
− 152.36229.04658.64.538605.9201.71.5111.9950.50682.4722.128.5990.96034.7571.364
− 53.54926.65645.44.589574.7179.81.4362.0790.34522.59522.928.9021.0084.8461.379
55.1624.29631.84.643544.3161.41.3772.1990.24212.7423.859.2091.0584.9891.399
157.28821.98617.64.705514.7145.61.3312.3380.17412.90824.929.5191.1115.1931.424
2510.0319.71602.94.781485.7131.81.2972.4990.12793.10426.169.8341.1675.4661.456
3513.5117.49587.54.873457.4119.61.2752.6880.09563.33327.5810.161.2285.8261.497
4517.8215.32571.34.993429.6108.81.2643.0060.07263.60429.2110.51.2956.2951.549
5523.113.2554.15.143402.398.991.2653.3350.05573.9331.1110.861.3726.9121.615
6529.4811.14535.85.34375.490.061.2813.7680.04324.33433.3311.251.4637.7381.702
7537.099.154516.15.608348.681.831.3164.3590.03364.85135.9711.71.5788.8761.819
8546.097.24494.55.98732274.181.3795.210.02625.5539.2112.231.73210.521.983
9556.655.414470.26.56294.666.841.4896.5250.02036.5643.3112.91.95413.052.227
10568.953.695442.17.52266.159.71.6878.8010.01568.16848.8313.822.31217.352.622
11583.222.113407.49.49223552.352.11413.670.011611.1456.9615.222.97726.033.358
12599.70.7327357.816.29196.643.83.62931.430.008218.2571.2517.844.5750.815.121
127.5104.20.437338.721.71183.440.944.84846.110.007421.7576.3518.825.36365.596.022
130108.90.1754310.534.41165.137.057.7281.460.006526.7484.6320.446.45790.377.258
132.2113.10.0017248.564.71129.529.5514.77168.70.005532.9397.3322.967.77127.88.808

t0050

T, temperature (°C); P, pressure (bar); σ, surface tension (mN/m); ρ, density (kg/m3); cp, specific heat (kJ/kg K); k, thermal conductivity (mW/m K); μ, dynamic viscosity (μPa s); Pr, Prandtl number; β, volumetric expansion coefficient (mK− 1); v, specific volume (m3/kg); γ, isentropic expansion coefficient of saturated vapor; indices: L, liquid; V, vapor.

Table B.10

Standard Chemical Exergy of Some Elements

ElementBCCaCl2CuF2FeH2I2KMg
exch (kJ/mol)628.1410.27729.1123.7132.6505.8374.3236.12175.7336.7626.9
ElementMoN2NaNiO2PPbPtPuSiTi
exch (kJ/mol731.30.67336.7242.63.92861.3249.2141.21100855.0907.2

t0055

Source: Rivero R., Garfias M., Standard chemical exergy of elements updated. Energy 31:3310-3326.

Table B.11

Formation Enthalpy, Entropy, Gibbs Energy, and Chemical Exergy of Some Substances

Substance nameChemical formulaMΔfH0ΔfS0ΔfG0exch
AcetoneC3H6O59− 217.14295.6− 152.691788
AcetyleneC2H226228.19200.9210.671267
AmmoniaNH317− 46.1499.5− 16.5337.9
n-ButaneC4H1058− 125.78309.90− 16.5292805
Calcium carbonateCaCO3100.1− 120791.7− 112817.52
Carbon monoxideCO28− 110.53197.6− 137.17275.06
Carbon dioxideCO244− 393.49213.8− 394.35198.38
Copper oxychlorideCu2OCl2214− 384.65154.35− 369.721.08
Cupric oxideCuO79− 156.0642.59− 128.296.27
Copper(II) chlorideCuCl2134− 218.0108.07− 173.8382.47
Cuprous chlorideCuCl100− 136.8287.45− 119.4475.00
EthanolC2H5OH47− 234.94280.60− 167.711363
Iron(III) oxideFe2O3159.7− 824.20205.1− 742.2212.26
Lithium bromideLiBr86.85− 351.1474.01− 341.83101.37
MagnetiteFe3O4231.5− 1118146.1− 1015115.61
MethaneCH416− 74.60186.40− 50.53831.98
Nitrogen dioxideNO24634.19240.2052.3156.56
Nitrous oxideN2O4481.59220.00103.71106.34
n-OctaneC8H18131− 208.745.73416.257549
PropaneC3H244− 104.67130.7− 24.292151
Sodium chlorideNaCl58.44− 411.24223.1− 384.2014.353
Sulphur dioxideSO264− 296.79248.2− 300.0313.10
Uranium hexafluorideUF6352− 2198227.8− 2069644.96
WaterH2O18− 285.8169.94− 237.120.750

t0060

M, molecular mass (kg/kmol); ΔfH0, formation enthalpy (kJ/mol); formation entropy, ΔfS0 = s0 − ∑ elementsνsf,element0si1_e, J/mol K, where ν is the number of moles of the element in chemical equation of formation of the substance; Gibbs free energy of formation, ΔfG0 = ΔfH0 − T0ΔfS0, (kJ/mol); chemical exergy, exch = ΔfG0 + ∑ elementsν × exelementchsi2_e, (kJ/mol); reference temperature, T0 = 298.15 K; reference pressure, P0 = 1 bar; superscript 0 in above notations refers to standard pressure.

bm01-9780123838605
Diagram B.1 Temperature-entropy diagram of water.
bm02-9780123838605
Diagram B.2 Enthalpy-concentration diagram of ammonia-water.
bm03-9780123838605
Diagram B.3 Dürhing chart for Lithium bromide/water solution.
bm04-9780123838605
Diagram B.4 Van’t Hoff chart of vapor pressure of LiBr/water solution.
bm05-9780123838605
Diagram B.5 Enthalpy-concentration diagram for LiBr-water.
bm06-9780123838605
Diagram B.6 The temperature entropy diagram of carbon dioxide.
bm07-9780123838605
Diagram B.7 The temperature entropy diagram of ammonia.
bm08-9780123838605
Diagram B.8 The temperature entropy diagram of toluene.
..................Content has been hidden....................

You can't read the all page of ebook, please click here login for view all page.
Reset