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Question 12.6: R134a Properties Find the enthalpy change in a process in wh......

R134a Properties

Find the enthalpy change in a process in which 38  lb_{m} of R134a at 80% quality is heated to 300°F in a constant-pressure process at 200 psia (lbf/in.² absolute).

Given: p_{ini} = 200  psia, x_{ini} = 0.80

Figure: Figure 12.7, the p–h diagram for R134a

Assumptions: Thermodynamic equilibrium exists.
Find: The enthalpy change ΔH

12.7
12.7.2
Step-by-Step
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The solution to this problem is most quickly done by using the p–h diagram since the process is just a horizontal line at 200 psia with the left endpoint at the 80% quality-line intersection. The right end of the process line is at the intersection of the 200 psia line and the 300°F line. The enthalpy at the left endpoint can be approximated by first finding the enthalpies at saturated liquid (55  Btu/lb_{m}) and saturated vapor (120  Btu/lb_{m}) and then interpolating.
The enthalpy at the right endpoint can be read directly from the p–h diagram.
Thus, the left and right endpoints are
h_{1} = 55 + (120  –  55) \times 0.8 = 107  Btu/lb_{m}
and
h_{2} = 165.0  Btu/lb_{m}
The enthalpy change is the product of the enthalpy change per unit mass and the mass:
\Delta H = 38  lb_{m} \times (165  –  107)  Btu/lb_{m} = 2204  Btu

Comments
For a more accurate calculation, the reader may use the saturated table (Table A6) and the superheated R134a tables (Table A8).

TABLE A.6
(IP Units) Properties of Saturated Liquid and Saturated Vapor of R-134a
Temp. (°F) Pressure (psia) Density (lb/ft³)   Volume (ft³/lb) Enthalpy (Btu/lb) Entropy (Btu/lb · °F)
Liquid Vapor Liquid Vapor Liquid Vapor
-153.94 0.057 99.34 564.85 32.989 80.235 0.09154 0.2788
-150 0.072 98.95 449.29 31.902 80.783 0.08801 0.27588
-140 0.130 97.98 259.15 29.093 82.190 0.07908 0.26903
-130 0.222 97.01 155.69 26.238 83.618 0.07029 0.26294
-120 0.367 96.05 97.027 23.359 85.066 0.06169 0.25752
-110 0.586 95.09 62.509 20.467 86.531 0.05330 0.2527
-100 0.906 94.13 41.496 17.569 88.011 0.04513 0.24842
-90 1.363 93.17 28.303 14.665 89.504 0.03717 0.24462
-80 1.997 92.21 19.783 11.755 91.005 0.02940 0.24125
-75 2.396 91.73 16.680 10.297 91.759 0.02559 0.23972
-70 2.859 91.25 14.138 8.837 92.514 0.02182 0.23827
-65 3.393 90.77 12.045 7.374 93.270 0.01809 0.23691
-60 4.006 90.28 10.310 5.907 94.026 0.01440 0.23563
-55 4.707 89.80 8.8656 4.437 94.783 0.01075 0.23443
-50 5.505 89.31 7.6569 2.963 95.539 0.00713 0.23331
-45 6.409 88.82 6.6405 1.484 96.295 0.00355 0.23225
-40 7.429 88.32 5.7819 0.000 97.050 0.00000 0.23125
-35 8.577 87.83 5.0533 1.489 97.804 0.00352 0.23032
-30 9.862 87.33 4.4325 2.984 98.556 0.00701 0.22945
-25 11.297 86.82 3.9014 4.484 99.306 0.01048 0.22863
-20 12.895 86.32 3.4452 5.991 100.054 0.01392 0.22786
-15 14.667 85.81 3.0519 7.505 100.799 0.01733 0.22714
−14.92 14.696 85.80 3.0462 7.529 100.811 0.01739 0.22713
-10 16.626 85.29 2.7116 9.026 101.542 0.02073 0.22647
-5 18.787 84.77 2.4161 10.554 102.280 0.02409 0.22584
0 21.162 84.25 2.1587 12.090 103.015 0.02744 0.22525
5 23.767 83.72 1.9337 13.634 103.745 0.03077 0.2247
10 26.617 83.18 1.7365 15.187 104.471 0.03408 0.22418
15 29.726 82.64 1.5630 16.748 105.192 0.03737 0.2237
20 33.110 82.10 1.4101 18.318 105.907 0.04065 0.22325
25 36.785 81.55 1.2749 19.897 106.617 0.04391 0.22283
30 40.768 80.99 1.1550 21.486 107.320 0.04715 0.22244
35 45.075 80.42 1.0484 23.085 108.016 0.05038 0.22207
40 49.724 79.85 0.9534 24.694 108.705 0.05359 0.22172
45 54.732 79.26 0.8685 26.314 109.386 0.05679 0.22140
50 60.116 78.67 0.7925 27.944 110.058 0.05998 0.22110
55 65.895 78.07 0.7243 29.586 110.722 0.06316 0.22081
60 72.087 77.46 0.6630 31.239 111.376 0.06633 0.22054
65 78.712 76.84 0.6077 32.905 112.019 0.06949 0.22028
70 85.787 76.21 0.5577 34.583 112.652 0.07264 0.22003
75 93.333 75.57 0.5125 36.274 113.272 0.07578 0.21979
80 101.370 74.91 0.4715 37.978 113.880 0.07892 0.21957
85 109.920 74.25 0.4343 39.697 114.475 0.08205 0.21934
90 119.000 73.57 0.4004 41.430 115.055 0.08518 0.21912
95 128.630 72.87 0.3694 43.179 115.619 0.08830 0.2189
100 138.830 72.16 0.3411 44.943 116.166 0.09142 0.21868
105 149.630 71.43 0.3153 46.725 116.694 0.09454 0.21845
110 161.050 70.68 0.2915 48.524 117.203 0.09766 0.21822
115 173.110 69.91 0.2697 50.343 117.690 0.10078 0.21797
120 185.840 69.12 0.2497 52.181 118.153 0.10391 0.21772
125 199.250 68.31 0.2312 54.040 118.591 0.10704 0.21744
130 213.380 67.47 0.2141 55.923 119.000 0.11018 0.21715
135 228.250 66.60 0.1983 57.830 119.377 0.11333 0.21683
140 243.880 65.70 0.1836 59.764 119.720 0.11650 0.21648
145 260.310 64.77 0.1700 61.727 120.024 0.11968 0.21609
150 277.570 63.80 0.1574 63.722 120.284 0.12288 0.21566
155 295.690 62.78 0.1455 65.752 120.495 0.12611 0.21517
160 314.690 61.72 0.1345 67.823 120.650 0.12938 0.21463
165 334.620 60.60 0.1241 69.939 120.739 0.13268 0.214
170 355.510 59.42 0.1144 72.106 120.753 0.13603 0.21329
175 377.400 58.16 0.1052 74.335 120.677 0.13945 0.21247
180 400.340 56.80 0.0965 76.636 120.493 0.14295 0.21151
185 424.370 55.33 0.0881 79.027 120.175 0.14655 0.21037
190 449.550 53.70 0.0801 81.534 119.684 0.15029 0.20901
195 475.950 51.86 0.0723 84.196 118.963 0.15423 0.20733
200 503.640 49.70 0.0646 87.088 117.906 0.15847 0.20519
205 532.720 47.00 0.0566 90.368 116.289 0.16326 0.20226
210 563.340 43.03 0.0474 94.548 113.411 0.16933 0.19750
213.85 588.270 32.04 0.0312 103.775 103.775 0.18128 0.18128
Source:    Courtesy of ASHRAE, Handbook of Fundamentals, American Society of Heating, Refrigerating and Air-Conditioning Engineers, Atlanta, GA, 1997. With permission.
Notes:    Values shown in italics are at the boiling point. Values shown in bold are at the critical point.

 

TABLE A.6
(SI Units) Properties of Saturated Liquid and Saturated Vapor of R-134a
Temp. (°C) Pressure (MPa) Density (kg/m3)  Volume (m³/kg) Enthalpy (kJ/kg)     Entropy (kJ/kg · K)
Liquid Vapor Liquid Vapor Liquid Vapor
-103.3 0.00039 1591.2 35.263 71.89 335.07 0.4143 1.9638
-100 0.00056 1581.9 25.039 75.71 337.00 0.4366 1.9456
-90 0.00153 1553.9 9.7191 87.59 342.94 0.5032 1.8975
-80 0.00369 1526.2 4.2504 99.65 349.03 0.5674 1.8585
-70 0.00801 1498.6 2.0528 111.78 355.23 0.6286 1.8269
-60 0.01594 1471.0 1.0770 123.96 361.51 0.6871 1.8016
-50 0.02945 1443.1 0.60560 136.21 367.83 0.7432 1.7812
-40 0.05122 1414.8 0.36095 148.57 374.16 0.7973 1.7649
-30 0.08436 1385.9 0.22596 161.10 380.45 0.8498 1.7519
-28 0.09268 1380.0 0.20682 163.62 381.70 0.8601 1.7497
-26.07 0.10132 1374.3 0.19016 166.07 382.90 0.8701 1.7476
-26 0.10164 1374.1 0.18961 166.16 382.94 0.8704 1.7476
-24 0.11127 1368.2 0.17410 168.70 384.19 0.8806 1.7455
-22 0.12160 1362.2 0.16010 171.26 385.43 0.8908 1.7436
-20 0.13268 1356.2 0.14744 173.82 386.66 0.9009 1.7417
-18 0.14454 1350.2 0.13597 176.39 387.89 0.9110 1.7399
-16 0.15721 1344.1 0.12556 178.97 389.11 0.9211 1.7383
-14 0.17074 1338.0 0.11610 181.56 390.33 0.9311 1.7367
-12 0.18516 1331.8 0.10749 184.16 391.55 0.9410 1.7351
-10 0.20052 1325.6 0.09963 186.78 392.75 0.9509 1.7337
-8 0.21684 1319.3 0.09246 189.40 393.95 0.9608 1.7323
-6 0.23418 1313.0 0.08591 192.03 395.15 0.9707 1.7310
-4 0.25257 1306.6 0.07991 194.68 396.33 0.9805 1.7297
-2 0.27206 1300.2 0.07440 197.33 397.51 0.9903 1.7285
0 0.29269 1293.7 0.06935 200.00 398.68 1.0000 1.7274
2 0.31450 1287.1 0.06470 202.68 399.84 1.0097 1.7263
4 0.33755 1280.5 0.06042 205.37 401.00 1.0194 1.7252
6 0.36186 1273.8 0.05648 208.08 402.14 1.0291 1.7242
8 0.38749 1267.0 0.05284 210.80 403.27 1.0387 1.7233
10 0.41449 1260.2 0.04948 213.53 404.40 1.0483 1.7224
12 0.44289 1253.3 0.04636 216.27 405.51 1.0579 1.7215
14 0.47276 1246.3 0.04348 219.03 406.61 1.0674 1.7207
16 0.50413 1239.3 0.04081 221.80 407.70 1.0770 1.7199
18 0.53706 1232.1 0.03833 224.59 408.78 1.0865 1.7191
20 0.57159 1224.9 0.03603 227.40 409.84 1.0960 1.7183
22 0.60777 1217.5 0.03388 230.21 410.89 1.1055 1.7176
24 0.64566 1210.1 0.03189 233.05 411.93 1.1149 1.7169
26 0.68531 1202.6 0.03003 235.90 412.95 1.1244 1.7162
28 0.72676 1194.9 0.02829 238.77 413.95 1.1338 1.7155
30 0.77008 1187.2 0.02667 241.65 414.94 1.1432 1.7149
32 0.81530 1179.3 0.02516 244.55 415.90 1.1527 1.7142
34 0.86250 1171.3 0.02374 247.47 416.85 1.1621 1.7135
36 0.91172 1163.2 0.02241 250.41 417.78 1.1715 1.7129
38 0.96301 1154.9 0.02116 253.37 418.69 1.1809 1.7122
40 1.01650 1146.5 0.01999 256.35 419.58 1.1903 1.7115
42 1.07210 1137.9 0.01890 259.35 420.44 1.1997 1.7108
44 1.13000 1129.2 0.01786 262.38 421.28 1.2091 1.7101
46 1.19010 1120.3 0.01689 265.42 422.09 1.2185 1.7094
45 1.25270 1111.3 0.01598 268.49 422.88 1.2279 1.7086
50 1.31770 1102.0 0.01511 271.59 423.63 1.2373 1.7078
52 1.38520 1092.6 0.01430 274.71 424.35 1.2468 1.7070
54 1.45530 1082.9 0.01353 277.86 425.03 1.2562 1.7061
56 1.52800 1073.0 0.01280 281.04 425.68 1.2657 1.7051
58 1.60330 1062.8 0.01212 284.25 426.29 1.2752 1.7041
60 1.68150 1052.4 0.01146 287.49 426.86 1.2847 1.7031
62 1.76250 1041.7 0.01085 290.77 427.37 1.2943 1.7019
64 1.84640 1030.7 0.01026 294.08 427.84 1.3039 1.7007
66 1.93340 1019.4 0.00970 297.44 428.25 1.3136 1.6993
68 2.02340 1007.7 0.00917 300.84 428.61 1.3234 1.6979
70 2.11650 995.6 0.00867 304.29 428.89 1.3332 1.6963
72 2.21300 983.1 0.00818 307.79 429.1 1.3430 1.6945
74 2.31270 970.0 0.00772 311.34 429.23 1.3530 1.6926
76 2.41590 956.5 0.00728 314.96 429.27 1.3631 1.6905
78 2.52270 942.3 0.00686 318.65 429.20 1.3733 1.6881
80 2.63310 927.4 0.00646 322.41 429.02 1.3837 1.6855
85 2.92590 886.2 0.00550 332.27 427.91 1.4105 1.6775
90 3.24450 836.9 0.00461 343.01 425.48 1.4392 1.6663
95 3.59160 771.6 0.00374 355.43 420.60 1.4720 1.6490
100 3.97210 646.7 0.00265 374.02 407.08 1.5207 1.6093
101.03 4.05600 513.3 0.002 389.79 389.79 1.5593 1.5593
Source:    Courtesy of ASHRAE, Handbook of Fundamentals, American Society of Heating, Refrigerating and Air-Conditioning Engineers, Atlanta, GA, 1997. With permission.
Notes:   Values shown in bold italics are at the triple point. Values shown in italics are at the boiling point. Values shown in bold are at the critical point.

 

TABLE A.8
(IP Units) Properties of Superheated Vapor of R-134a
Pressure (psia) Properties Temperature
−22°F −4°F 14°F 32°F 50°F 68°F 86°F 104°F 122°F 140°F 158°F
11.6 Volume (ftS/lb) 3.819 4.001 4.181 4.358 4.533 4.706 4.878 5.048 5.218 5.387 5.555
Enthalpy (Btu/lb) 99.9 103.3 106.7 110.3 113.9 117.5 121.3 125.1 129 132.9 136.9
Entropy (Btu/lb· R) 0.229 0.236 0.244 0.251 0.258 0.265 0.272 0.279 0.286 0.293 0.299
13.05 Volume (ftS/lb) 3.541 3.703 3.861 4.018 4.173 4.327 4.479 4.631 4.782 4.932
Enthalpy (Btu/lb) 103.1 106.6 110.1 113.8 117.4 121.2 125 128.9 132.9 136.9
Entropy (Btu/lb· R) 0.234 0.241 0.249 0.256 0.263 0.27 0.277 0.284 0.29 0.297
14.5 Volume (ftS/lb) 3.173 3.32 3.464 3.607 3.747 3.886 4.024 4.161 4.297 4.433
Enthalpy (Btu/lb) 103 106.5 110 113.7 117.3 121.1 124.9 128.8 132.8 136.8
Entropy (Btu/lb· R) 0.231 0.239 0.246 0.254 0.261 0.268 0.275 0.281 0.288 0.295
14.7 Volume (ftS/lb) 3.129 3.275 3.418 3.558 3.697 3.834 3.971 4.106 4.241 4.374
Enthalpy (Btu/lb) 102.9 106.4 110 113.6 117.3 121.1 124.9 128.8 132.8 136.8
Entropy (Btu/lb· R) 0.231 0.239 0.246 0.253 0.26 0.267 0.274 0.281 0.288 0.294
17.4 Volume (ftS/lb) 2.62 2.745 2.868 2.989 3.108 3.225 3.342 3.457 3.571 3.685
Enthalpy (Btu/lb) 102.6 106.2 109.8 113.4 117.2 120.9 124.8 128.7 132.7 136.7
Entropy (Btu/lb· R) 0.227 0.235 0.242 0.25 0.257 0.264 0.271 0.278 0.284 0.291
20.31 Volume (ftS/lb) 2.335 2.442 2.548 2.651 2.753 2.854 2.954 3.052 3.151
Enthalpy (Btu/lb) 105.9 109.5 113.2 117 120.8 124.6 128.6 132.5 136.6
Entropy (Btu/lb· R) 0.231 0.239 0.246 0.254 0.261 0.268 0.274 0.281 0.288
26.11 Volume (ftS/lb) 1.787 1.874 1.959 2.042 2.123 2.203 2.282 2.361 2.438
Enthalpy (Btu/lb) 105.3 109 112.8 116.6 120.4 124.3 128.3 132.3 136.4
Entropy (Btu/lb· R) 0.226 0.233 0.241 0.248 0.255 0.262 0.269 0.276 0.283
29.01 Volume (ftS/lb) 1.595 1.675 1.753 1.829 1.903 1.976 2.047 2.118 2.189
Enthalpy (Btu/lb) 105 108.8 112.6 116.4 120.3 124.2 128.1 132.2 136.3
Entropy (Btu/lb· R) 0.223 0.231 0.238 0.246 0.253 0.26 0.267 0.274 0.281
36.26 Volume (ftS/lb) 1.316 1.381 1.444 1.506 1.566 1.624 1.682 1.74
Enthalpy (Btu/lb) 108.1 112 115.9 119.8 123.8 127.8 131.9 136
Entropy (Btu/lb· R) 0.226 0.233 0.241 0.248 0.255 0.262 0.269 0.276
43.51 Volume (ftS/lb) 1.133 1.188 1.241 1.292 1.342 1.392 1.44
Enthalpy (Btu/lb) 111.4 115.4 119.4 123.4 127.4 131.5 135.7
Entropy (Btu/lb· R) 0.229 0.236 0.244 0.251 0.258 0.265 0.272
50.76 Volume (ftS/lb) 0.955 1.004 1.051 1.096 1.141 1.184 1.226
Enthalpy (Btu/lb) 110.8 114.9 118.9 123 127.1 131.2 135.4
Entropy (Btu/lb· R) 0.225 0.233 0.24 0.248 0.255 0.262 0.269
58.02 Volume (ftS/lb) 0.822 0.866 0.909 0.95 0.989 1.028 1.066
Enthalpy (Btu/lb) 110.2 114.3 118.4 122.6 126.7 130.9 135.1
Entropy (Btu/lb· R) 0.221 0.229 0.237 0.244 0.252 0.259 0.266
65.27 Volume (ftS/lb) 0.758 0.798 0.835 0.871 0.907 0.941
Enthalpy (Btu/lb) 113.8 118 122.1 126.3 130.6 134.8
Entropy (Btu/lb· R) 0.226 0.234 0.242 0.249 0.256 0.263
72.52 Volume (ftS/lb) 0.672 0.709 0.744 0.777 0.809 0.841
Enthalpy (Btu/lb) 113.2 117.5 121.7 126 130.2 134.5
Entropy (Btu/lb· R) 0.223 0.231 0.239 0.246 0.254 0.261
87.02 Volume (ftS/lb) 0.575 0.606 0.635 0.663 0.691
Enthalpy (Btu/lb) 116.4 120.8 125.2 129.5 133.9
Entropy (Btu/lb· R) 0.226 0.234 0.242 0.249 0.256
101.53 Volume (ftS/lb) 0.478 0.507 0.533 0.559 0.583
Enthalpy (Btu/lb) 115.3 119.9 124.4 128.8 133.3
Entropy (Btu/lb· R) 0.222 0.23 0.238 0.245 0.253
116.03 Volume (ftS/lb) 0.432 0.457 0.48 0.502
Enthalpy (Btu/lb) 118.9 123.5 128.1 132.6
Entropy (Btu/lb· R) 0.226 0.234 0.242 0.249
130.54 Volume (ftS/lb) 0.373 0.397 0.419 0.439
Enthalpy (Btu/lb) 117.9 122.6 127.3 131.9
Entropy (Btu/lb· R) 0.222 0.231 0.238 0.246
145.04 Volume (ftS/lb) 0.326 0.348 0.369 0.389
Enthalpy (Btu/lb) 116.8 121.7 126.5 131.2
Entropy (Btu/lb· R) 0.219 0.227 0.235 0.243
159.54 Volume (ftS/lb) 0.308 0.329 0.347
Enthalpy (Btu/lb) 120.7 125.7 130.5
Entropy (Btu/lb· R) 0.224 0.232 0.24
174.05 Volume (ftS/lb) 0.275 0.294 0.312
Enthalpy (Btu/lb) 119.7 124.8 129.8
Entropy (Btu/lb· R) 0.221 0.23 0.238
188.55 Volume (ftS/lb) 0.246 0.265 0.283
Enthalpy (Btu/lb) 118.6 123.9 129
Entropy (Btu/lb· R) 0.218 0.227 0.235
203.06 Volume (ftS/lb) 0.24 0.257
Enthalpy (Btu/lb) 123 128.2
Entropy (Btu/lb· R) 0.224 0.233
217.56 Volume (ftS/lb) 0.218 0.235
Enthalpy (Btu/lb) 122 127.4
Entropy (Btu/lb· R) 0.221 0.23
253.82 Volume (ftS/lb) 0.189
Enthalpy (Btu/lb) 125.1
Entropy (Btu/lb· R) 0.224
Source:    Courtesy of ASHRAE, Handbook of Fundamentals, American Society of Heating, Refrigerating and Air-Conditioning Engineers, Atlanta, GA, 1997. With permission.

 

TABLE A.8
(SI Units) Properties of Superheated Vapor of R-134a
Pressure (kPa) Properties Temperature
−30°C −20°C −10°C 0°C 10°C 20°C 30°C 40°C 50°C 60°C 70°C
80 Volume (mS/kg) 0.238 0.249 0.261 0.272 0.282 0.293 0.304 0.315 0.325 0.336 0.346
Enthalpy (kJ/kg) 380.2 388.1 396.2 404.4 412.8 421.3 430 438.9 447.9 457.1 466.5
Entropy (kJ/kg· K) 1.755 1.787 1.818 1.849 1.879 1.908 1.937 1.966 1.995 2.023 2.05
90 Volume (mS/kg) 0.221 0.231 0.241 0.25 0.26 0.27 0.279 0.289 0.298 0.307
Enthalpy (kJ/kg) 387.8 395.9 404.2 412.6 421.1 429.8 438.7 447.8 457 466.3
Entropy (kJ/kg· K) 1.776 1.807 1.838 1.868 1.898 1.927 1.956 1.985 2.013 2.04
100 Volume (mS/kg) 0.198 0.207 0.216 0.225 0.233 0.242 0.251 0.259 0.268 0.276
Enthalpy (kJ/kg) 387.4 395.6 403.9 412.3 420.9 429.6 438.5 447.6 456.8 466.2
Entropy (kJ/kg· K) 1.766 1.798 1.829 1.859 1.889 1.918 1.947 1.976 2.004 2.031
101 Volume (mS/kg) 0.195 0.204 0.213 0.222 0.23 0.239 0.247 0.256 0.264 0.273
Enthalpy (kJ/kg) 387.4 395.5 403.8 412.3 420.9 429.6 438.5 447.6 456.8 466.2
Entropy (kJ/kg· K) 1.765 1.797 1.828 1.858 1.888 1.917 1.946 1.975 2.003 2.03
120 Volume (mS/kg) 0.163 0.171 0.179 0.186 0.194 0.201 0.208 0.215 0.223 0.23
Enthalpy (kJ/kg) 386.7 394.9 403.3 411.8 420.5 429.2 438.2 447.3 456.5 465.9
Entropy (kJ/kg· K) 1.749 1.781 1.812 1.843 1.873 1.902 1.931 1.96 1.988 2.016
140 Volume (mS/kg) 0.145 0.152 0.159 0.165 0.172 0.178 0.184 0.19 0.196
Enthalpy (kJ/kg) 394.3 402.7 411.3 420 428.9 437.8 447 456.2 465.7
Entropy (kJ/kg· K) 1.767 1.798 1.829 1.859 1.889 1.918 1.947 1.975 2.003
180 Volume (mS/kg) 0.111 0.117 0.122 0.127 0.132 0.137 0.142 0.147 0.152
Enthalpy (kJ/kg) 392.9 401.6 410.3 419.1 428.1 437.1 446.3 455.7 465.2
Entropy (kJ/kg· K) 1.742 1.774 1.806 1.836 1.866 1.896 1.925 1.953 1.981
200 Volume (mS/kg) 0.099 0.104 0.109 0.114 0.119 0.123 0.128 0.132 0.136
Enthalpy (kJ/kg) 392.3 401 409.8 418.7 427.7 436.8 446 455.4 464.9
Entropy (kJ/kg· K) 1.732 1.764 1.796 1.827 1.857 1.886 1.915 1.944 1.972
250 Volume (mS/kg) 0.082 0.086 0.09 0.094 0.098 0.101 0.105 0.108
Enthalpy (kJ/kg) 399.5 408.5 417.5 426.6 435.9 445.2 454.6 464.2
Entropy (kJ/kg· K) 1.742 1.774 1.805 1.836 1.866 1.895 1.924 1.953
300 Volume (mS/kg) 0.071 0.074 0.077 0.081 0.084 0.087 0.09
Enthalpy (kJ/kg) 407.1 416.3 425.6 434.9 444.4 453.9 463.6
Entropy (kJ/kg· K) 1.756 1.788 1.819 1.849 1.879 1.908 1.936
350 Volume (mS/kg) 0.06 0.063 0.065 0.068 0.071 0.074 0.076
Enthalpy (kJ/kg) 405.7 415.1 424.5 434 443.5 453.2 462.9
Entropy (kJ/kg· K) 1.739 1.772 1.803 1.834 1.864 1.893 1.922
400 Volume (mS/kg) 0.051 0.054 0.057 0.059 0.062 0.064 0.066
Enthalpy (kJ/kg) 404.2 413.8 423.4 433 442.7 452.4 462.2
Entropy (kJ/kg· K) 1.724 1.758 1.79 1.821 1.851 1.881 1.91
450 Volume (mS/kg) 0.047 0.05 0.052 0.054 0.056 0.059
Enthalpy (kJ/kg) 412.6 422.3 432 441.8 451.6 461.5
Entropy (kJ/kg· K) 1.745 1.777 1.809 1.84 1.869 1.899
500 Volume (mS/kg) 0.042 0.044 0.046 0.048 0.05 0.052
Enthalpy (kJ/kg) 411.2 421.2 431 440.9 450.8 460.8
Entropy (kJ/kg· K) 1.732 1.766 1.798 1.829 1.859 1.889
600 Volume (mS/kg) 0.036 0.038 0.04 0.041 0.043
Enthalpy (kJ/kg) 418.8 429 439.1 449.2 459.4
Entropy (kJ/kg· K) 1.745 1.778 1.81 1.841 1.871
700 Volume (mS/kg) 0.03 0.032 0.033 0.035 0.036
Enthalpy (kJ/kg) 416.2 426.8 437.2 447.6 457.9
Entropy (kJ/kg· K) 1.726 1.76 1.793 1.824 1.855
800 Volume (mS/kg) 0.027 0.028 0.03 0.031
Enthalpy (kJ/kg) 424.5 435.3 445.9 456.4
Entropy (kJ/kg· K) 1.743 1.777 1.809 1.841
900 Volume (mS/kg) 0.023 0.025 0.026 0.027
Enthalpy (kJ/kg) 422.1 433.2 444.1 454.8
Entropy (kJ/kg· K) 1.728 1.763 1.796 1.828
1000 Volume (mS/kg) 0.02 0.022 0.023 0.024
Enthalpy (kJ/kg) 419.6 431.1 442.2 453.2
Entropy (kJ/kg· K) 1.713 1.749 1.783 1.815
1100 Volume (mS/kg) 0.019 0.02 0.022
Enthalpy (kJ/kg) 428.8 440.3 451.6
Entropy (kJ/kg· K) 1.735 1.771 1.804
1200 Volume (mS/kg) 0.017 0.018 0.019
Enthalpy (kJ/kg) 426.4 438.3 449.8
Entropy (kJ/kg· K) 1.722 1.759 1.793
1300 Volume (mS/kg) 0.015 0.017 0.018
Enthalpy (kJ/kg) 423.8 436.2 448.1
Entropy (kJ/kg· K) 1.709 1.747 1.782
1400 Volume (mS/kg) 0.015 0.016
Enthalpy (kJ/kg) 434 446.2
Entropy (kJ/kg· K) 1.736 1.772
1500 Volume (mS/kg) 0.014 0.015
Enthalpy (kJ/kg) 431.6 444.2
Entropy (kJ/kg· K) 1.724 1.762
1750 Volume (mS/kg) 0.012
Enthalpy (kJ/kg) 438.9
Entropy (kJ/kg· K) 1.737
Source:    Courtesy of ASHRAE, Handbook of Fundamentals, American Society of Heating, Refrigerating and Air-Conditioning Engineers, Atlanta, 1997. With permission.

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