Mixing Prog

ENTER PARAMETERS OF CARGO TO BE MIXED:

Propane
Butane

Quantity Temp © Atm Pressure
20
-15
1.004
10
-2

Results
Mix temp.
-11.03 C
Abs Pressure
2.516
Guage Pressure
1.512
Propane % in Vapour
93.11 %
Butane % In Vapour
6.89 %
********* calculation of mixture temperature *************************
temp Propane
258.1 K
-15
-14
Temp Butane
271.1 k
-1
Qty Propane
20000 kg
Qty Butane
10000 kg
Specific Heat Propane
2.38
2.38
0
0
Specific Heat Propane
2380
Enthalpy of Butane
65.3
65.8
specific Heat Butane
2093.1
0.4397268908 119.20996
1.4397268908 377.30996
262.0705096963 -11.02949 T
-11
-12
************************* Calculation of Vapour Pressure*******************
S.V.P.Propane AT T
3.23163
3.3419 -0.107018 3.2348819
S.V.P.Butane AT T
0.63
0.66 -0.029115 0.6308847
molecular wt Propane
44.09721
molecular wt Butane
58.1243
No of moles Propane
0.4535434 0.6255885 Total moles
No of moles Butane
0.1720451
%mole Propane
72.498683
%mole Butane
27.501317
Pressure Propane
2.3428892
Pressure Butane
0.1732583 2.5161475
% propane in gas
93.114144
% Butane in gas
6.8858563

0

-0.97051
*************

THERMODYNAMIC PROPERTIES OF PROPAMIC PROPERTIES OF PROPANE
Molecular Weight:44
Boiling Point(at 1 bar ):-42.8'C
Limits Of Inflammability:2.1-->9.5%
Ignition Temperature:460'C
Ignition Energy: approx.1 millijoule
Viscosity In Liquid Phase(at -40'C):0.205 Centipoises
Viscosity In Gasseous Phase(at 0'C):0.00793 Centipoises
Condensing ratio (dm3/1m3gas)
3.38
(Amt of liq in dm3 which will co
PROPERTIES OF LIQUID AND SATURATED VAPOUR
Temp.
C
-50
-45
-44
-43
-42
-41
-40
-39
-38
-37
-36
-35
-34
-33
-32
-31
-30
-29
-28
-27
-26
-25
-24
-23
-22
-21
-20
-19
-18
-17
-16
-15
-14
-13

Vapour Pressure
bars
0.70432
0.88909
0.93021
0.97281
1.01692
1.06257
1.10981
1.15866
1.20916
1.26136
1.31528
1.37098
1.42847
1.48782
1.54904
1.61219
1.67731
1.74442
1.81358
1.88482
1.95818
2.03371
2.11144
2.19142
2.27369
2.35829
2.44526
2.53465
2.6265
2.72085
2.81774
2.91722
3.01933
3.12412

0.58
0.467
0.447
0.428
0.411
0.395
0.38
0.366
0.353
0.341
0.329
0.317
0.305
0.294
0.283
0.272
0.262
0.252
0.243
0.234
0.226
0.218
0.21
0.202
0.195
0.188
0.182
0.176
0.171
0.166
0.161
0.156
0.151
0.146

Specific Volume m3/Kg Density Kg/m3
Vapour
Liquid
Vapour
0.00169
1.72
0.001707
2.14
0.001711
2.24
0.001714
2.34
0.001718
2.43
0.001721
2.53
0.001725
2.63
0.001729
2.73
0.001732
2.83
0.001736
2.93
0.001739
3.04
0.001743
3.15
0.001747
3.28
0.00175
3.41
0.001754
3.54
0.001757
3.68
0.001761
3.82
0.001765
3.97
0.001768
4.12
0.001772
4.27
0.001776
4.42
0.00178
4.59
0.001784
4.77
0.001787
4.95
0.001791
5.13
0.001795
5.31
0.001799
5.49
0.001803
5.67
0.001807
5.84
0.001811
6.02
0.001816
6.21
0.00182
6.41
0.001824
6.62
0.001829
6.85

-12
-11
-10
-9
-8
-7
-6
-5
-4
-3
-2
-1
0
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34

3.23163
3.3419
3.45498
3.57092
3.68975
3.81153
3.93629
4.06409
4.32898
4.32898
4.46615
4.60655
4.75021
4.89719
5.04752
5.20126
5.35845
5.51915
5.68339
5.85123
6.02271
6.19788
6.3768
6.55951
6.74605
6.93649
7.13086
7.32921
7.5316
7.73808
7.94869
8.16349
8.38253
8.60585
8.83351
9.06556
9.30205
9.54303
9.78855
10.03867
10.29344
10.55291
10.81713
11.08616
11.36005
11.63885
11.92262

0.141
0.1365
0.132
0.128
0.124
0.1205
0.117
0.1135
0.11
0.1065
0.1035
0.1005
0.0974
0.0948
0.0922
0.0896
0.0871
0.0846
0.0821
0.0797
0.0774
0.0752
0.0731
0.0711
0.0692
0.0674
0.0656
0.0639
0.0622
0.0606
0.0591
0.0576
0.0561
0.0547
0.0533
0.052
0.0507
0.0495
0.0482
0.047
0.0458
0.0446
0.0435
0.0424
0.0414
0.0404
0.0394

0.001833
0.001837
0.001842
0.001846
0.001851
0.001855
0.00186
0.001864
0.001869
0.001873
0.001878
0.001882
0.001887
0.001891
0.001896
0.001901
0.001906
0.001911
0.001916
0.00192
0.001925
0.00193
0.001935
0.00194
0.001946
0.001951
0.001957
0.001963
0.001968
0.001974
0.00198
0.001986
0.001992
0.001998
0.002004
0.00201
0.002016
0.002023
0.002029
0.002035
0.002041
0.002048
0.002055
0.002063
0.002071
0.002079
0.002087

7.09
7.33
7.58
7.82
8.06
8.3
8.55
8.81
9.09
9.38
9.67
9.97
10.27
10.6
10.9
11.2
11.5
11.8
12.2
12.5
12.9
13.3
13.7
14.1
14.4
14.8
15.2
15.6
16.1
16.5
16.9
17.4
17.8
18.3
18.8
19.2
19.7
20.2
20.7
21.3
21.8
22.4
23
23.6
24.2
24.8
25.4

35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50

12.21141
12.50527
12.80427
13.10845
13.41924
13.7326
14.05267
14.37816
14.70912
15.0456
15.38766
15.73537
16.08878
16.44795
16.81294
17.18381

0.0385
0.0375
0.0366
0.0357
0.0348
0.0339
0.0331
0.0324
0.0316
0.0309
0.0302
0.0295
0.0288
0.0281
0.0274
0.0268

0.002095
0.002103
0.002111
0.002119
0.002127
0.002135
0.002144
0.002152
0.002161
0.00217
0.002178
0.002187
0.002196
0.002204
0.002213
0.002222

26
26.7
27.3
28
28.7
29.5
30.2
30.9
31.6
32.4
33.1
33.9
34.7
35.6
36.5
37.3

Note 1. - Enthalpy based on zero at -129'C. in liquid phase

PROPERTIES OF SUPERHEADTED VAPOUR
v - specific volume, m3/kg:

Temp.
'C.
-40
-30
-20
-10
0
10
20
30
40
50
60
70
80
90

P = 1.0 bar
v
0.43
0.447
0.461
0.482
0.5
0.52
0.54
0.561
0.582
0.604
0.626
0.649
0.672
0.695

h - enthalpy, kcal/kg: P - absolute pressure

P = 1.1 bar
v
h

h
179.1
182.7
186.3
190.1
193.9
197.9
201.9
206.1
210.3
214.7
219.1
223.5
227.9
232.4

0.391
0.41
0.429
0.448
0.467
0.486
0.505
0.524
0.543
0.562
0.581
0.6
0.619
0.638

P = 1.5 bar
v
179
182.6
185.2
190
193.8
197.8
201.8
206
210.2
214.6
213.9
223.3
227.7
232.1

0
0.293
0.305
0.317
0.329
0.341
0.351
0.366
0.379
0.392
0.405
0.418
0.431
0.444

100
110
120
130
140
150
160
170

0.719
0.743
0.767
0.791
0.815
0.839
0.863
0.887

236.9
241.4
245.9
250.4
254.9
259.4
263.9
268.4

0.658
0.678
0.698
0.718
0.738
0.758
0.778
0.798

236.5
241
245.5
249.9
254.3
258.8
263.3
267.8

0.457
0.47
0.483
0.496
0.509
0.522
0.535
0.548

of liq in dm3 which will condense from 1 m3 of gas)

ty Kg/m3
Liquid
591.7
585.8
584.6
583.4
582.2
581
579.7
578.5
577.3
576.1
574.9
573.7
572.5
571.4
570.2
569.1
567.9
566.7
565.5
564.2
563
561.8
560.6
559.5
558.3
557.1
555.9
554.6
553.4
552.1
550.8
549.5
548.2
546.9

Enthalpy Kcal/Kg
Vapour
Liquid
175.9
177.3
177.6
178
178.3
178.6
178.9
179.2
179.6
179.9
180.3
180.6
180.9
181.3
181.6
181.9
182.3
182.6
182.9
183.3
183.6
183.9
184.2
184.4
184.7
185
185.2
185.5
185.8
186
186.3
186.6
186.9
187.2

72.7
75.3
75.8
76.4
76.9
77.4
78
78.5
79.1
79.6
80.2
80.7
81.2
81.8
82.3
82.8
83.4
84
84.5
85.1
85.6
86.1
86.7
87.2
87.8
88.3
88.8
89.4
89.9
90.4
91
91.5
92.1
92.6

Latent Heat Specific Heat
Kcal/Kg
kj/kg.k
103.2
2.25
102
2.26
101.8
2.26
101.6
2.27
101.4
2.27
101.2
2.27
100.9
2.28
100.7
2.28
100.5
2.28
100.3
2.29
100.1
2.29
99.9
2.29
99.7
2.3
99.5
2.3
99.3
2.3
99.1
2.31
98.9
2.31
98.6
2.31
98.4
2.32
98.2
2.32
98
2.32
97.7
2.33
97.5
2.33
97.2
2.34
96.9
2.34
96.7
2.35
96.4
2.35
96.1
2.36
95.9
2.36
95.6
2.37
95.3
2.37
95.1
2.38
94.8
2.38
94.5
2.39

545.6
544.3
542.9
541.6
540.3
539
537.7
536.4
535.1
533.8
532.5
531.2
529.9
528.6
528.7
527.3
526
524.6
523.3
522
520.7
519.4
518.1
516.8
515.4
513.9
512.5
511
509.5
508
506.5
505
503.5
502
500.5
499
497.5
496
494.4
492.9
491.4
489.9
488.3
486.6
484.8
482.9
481.1

187.4
187.7
188
188.2
188.5
188.7
188.9
189.2
189.4
189.7
189.9
190.2
190.4
190.7
190.9
191.1
191.4
191.6
191.8
192
192.3
192.5
192.7
193
193.2
193.4
193.7
193.9
194.1
194.3
194.5
194.7
194.9
195.1
195.3
195.5
195.7
195.9
196.1
196.3
196.5
196.7
196.9
197.1
197.3
197.4
197.6

93.2
93.7
94.3
94.8
95.4
95.9
96.5
97.1
97.6
98.2
98.8
99.4
100
100.6
101.1
101.7
102.3
102.9
103.4
104
104.6
105.2
105.8
106.4
107
107.6
108.2
108.8
109.3
109.9
110.5
111.1
111.7
112.3
112.9
113.5
114.1
114.7
115.3
115.9
116.5
117.1
117.8
118.4
119.1
119.7
120.4

94.2
94
93.7
93.4
93.1
92.8
92.4
92.1
91.8
91.5
91.2
90.8
90.4
90.1
89.8
89.4
89.1
88.7
88.4
88
87.7
87.3
86.9
86.6
86.2
85.9
85.5
85.1
84.8
84.4
84
83.6
83.2
82.8
82.4
82
81.6
81.2
80.8
80.4
80
79.6
79.1
78.7
78.2
77.7
77.2

2.4
2.41
2.41
2.42
2.43
2.43
2.44
2.45
2.45
2.46
2.47
2.48
2.49
2.49
2.5
2.51
2.52
2.52
2.53
2.54
2.55
2.56
2.57
2.58
2.58
2.59
2.6
2.61
2.62
2.63
2.64
2.65
2.66
2.67
2.68
2.69
2.7
2.71
2.73
2.74
2.75
2.76
2.78
2.79
2.8
2.81
2.83

479.2
477.4
475.6
473.8
472
470
468.4
466.5
464.7
462.8
460.9
459.1
457.2
455.4
453.7
450.1

197.8
198
198.2
198.3
198.5
198.7
198.9
199
199.2
199.4
199.6
199.7
199.9
200
200.2
200.3

121.1
121.7
122.4
123
123.7
124.4
125.1
125.8
126.5
127.2
127.9
128.5
129.2
129.8
130.5
131.2

76.7
76.3
75.8
75.3
74.8
74.3
73.8
73.2
72.7
72.2
71.7
71.2
70.7
70.2
69.7
69.1

2.84
2.85
2.87
2.88
2.9
2.91
2.93
2.95
2.96
2.98
3
3.02
3.04
3.06
3.08
3.1

/kg: P - absolute pressure

= 1.5 bar

P = 2.0 bar
v
h

h
0
182.5
186.1
189.8
193.6
197.6
201.6
205.8
210.1
214.3
218.6
223
227.4
231.9

0
0
0.222
0.232
0.242
0.252
0.262
0.272
0.282
0.292
0.302
0.312
0.323
0.334

P = 5.0 bar
v
h
0
0
186
189.8
193.6
197.5
201.5
205.7
210
214.2
218.5
222.9
227.3
231.7

0
0
0
0
0
0.094
0.098
0.102
0.106
0.11
0.114
0.118
0.123
0.128

P = 15.0 bar
v
h
0
0
0
0
0
194.1
198.6
203.1
207.6
212.1
216.6
221.1
225.6
230.3

0
0
0
0
0
0
0
0
0
0.032
0.033
0.034
0.036
0.038

0
0
0
0
0
0
0
0
0
202.7
208
213.3
218.7
224.1

236.4
240.9
245.5
249.8
254.3
258.8
263.3
267.8

0.345
0.356
0.367
0.378
0.389
0.4
0.411
0.422

235.2
240.7
245.5
249.6
254.1
258.6
263.1
267.5

0.133
0.138
0.143
0.148
0.153
0.158
0.163
0.168

234.9
239.5
244.1
248.7
253.3
258
262.7
267.4

0.04
0.042
0.044
0.046
0.048
0.05
0.052
0.054

229.5
234.9
240.3
245.7
251.1
256.5
261.9
267.3

THERMODYNAMIC PROPE THERMODYNAMIC PROPERTIES OF n-BUTANE
Molecular Weight:58.1
Boiling Point(at 1bar):0.6'C
LImits Of Inflammability:1.8--> 8.5
Ignition Temperature:410'C
Ignition Energy:approx. 1millijoule
Viscosity in liquid phase(at 0'C):0.21 centipose
Viscosity in gasseous phase(at 20'C): 0.0071 centipose
Condensing ratio (dm3/1m3gas)
4.32
PROPERTIES OF LIQUID AND SATURATED VAPOUR
temp.
C
-50
-49
-48
-47
-46
-45
-44
-43
-42
-41
-40
-39
-38
-37
-36
-35
-34
-33
-32
-31
-30
-29
-28
-27
-26
-25
-24
-23
-22
-21
-20
-19
-18
-17

Vapour pressure
bars
0.1
0.1
0.11
0.11
0.12
0.12
0.13
0.14
0.15
0.16
0.17
0.18
0.19
0.2
0.21
0.22
0.23
0.24
0.25
0.26
0.28
0.3
0.31
0.32
0.34
0.36
0.38
0.39
0.41
0.43
0.45
0.47
0.49
0.51

Specific Volume m3/Kg
Vapour
Liquid
1.92
0.001534
1.89
0.001536
1.85
0.001539
1.81
0.001541
1.76
0.001543
1.72
0.001546
1.68
0.001548
1.64
0.001551
1.59
0.001553
1.54
0.001556
1.49
0.001559
1.45
0.001561
1.4
0.001564
1.35
0.001566
1.3
0.001569
1.25
0.001572
1.21
0.001574
1.17
0.001577
1.13
0.00158
1.09
0.001582
1.05
0.001585
1.01
0.001587
0.98
0.00159
0.95
0.001593
0.92
0.001595
0.89
0.001598
0.86
0.0016
0.83
0.001603
0.8
0.001605
0.78
0.001608
0.75
0.001611
0.73
0.001614
0.7
0.001617
0.68
0.00162

-16
-15
-14
-13
-12
-11
-10
-9
-8
-7
-6
-5
-4
-3
-2
-1
0
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30

0.53
0.56
0.58
0.61
0.63
0.66
0.69
0.72
0.75
0.78
0.81
0.84
0.87
0.91
0.94
0.98
1.02
1.06
1.1
1.14
1.19
1.24
1.29
1.34
1.39
1.44
1.49
1.54
1.6
1.66
1.72
1.78
1.84
1.9
1.97
2.03
2.1
2.16
2.24
2.31
2.38
2.46
2.53
2.61
2.69
2.77
2.86

0.65
0.63
0.61
0.58
0.56
0.53
0.51
0.49
0.47
0.45
0.44
0.42
0.41
0.39
0.38
0.37
0.35
0.34
0.33
0.32
0.31
0.3
0.29
0.28
0.27
0.27
0.26
0.25
0.24
0.23
0.23
0.22
0.21
0.21
0.2
0.19
0.19
0.18
0.18
0.17
0.17
0.16
0.16
0.15
0.15
0.14
0.14

0.001622
0.001625
0.001628
0.001631
0.001633
0.001636
0.001639
0.001642
0.001645
0.001647
0.00165
0.001653
0.001656
0.001659
0.001662
0.001664
0.001667
0.00167
0.001672
0.001675
0.001678
0.001681
0.001684
0.001687
0.00169
0.001693
0.001696
0.001699
0.001702
0.001705
0.001708
0.001711
0.001714
0.001717
0.001721
0.001724
0.001727
0.00173
0.001734
0.001737
0.001741
0.001744
0.001748
0.001752
0.001755
0.001759
0.001762

31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50

2.95
3.04
3.13
3.22
3.32
3.42
3.52
3.62
3.72
3.82
3.92
4.03
4.14
4.26
4.38
4.51
4.64
4.78
4.92
5.06

0.14
0.13
0.13
0.13
0.12
0.12
0.12
0.11
0.11
0.11
0.1
0.1
0.1
0.1
0.1
0.09
0.09
0.09
0.09
0.08

0.001766
0.00177
0.001774
0.001777
0.001781
0.001785
0.001789
0.001792
0.001796
0.0018
0.001804
0.001808
0.001812
0.001816
0.001821
0.001825
0.00183
0.001835
0.00184
0.001845

Note 1. - Enthal Enthalpy based on zero at -129'C liquid phase
PROPERTIES OF SUPERHEATED VAPOUR
v-specific volume,m3/kg
Temp.
'C.
0
10
20
30
40
50
60
70
80
90
100
110
120
130
140
150

P = 1.0 bar
v
0.371
0.388
0.405
0.422
0.439
0.455
0.471
0.487
0.503
0.517
0.531
0.545
0.557
0.569
0.581
0.593

P = 1.1 bar
v

h
158.1
162.2
166.3
170.5
174.7
179
183.3
187.8
192.3
197
201.7
206.4
211.1
215.8
220.8
225.8

0
0.346
0.362
0.378
0.394
0.41
0.425
0.44
0.455
0.47
0.484
0.498
0.511
0.524
0.537
0.549

h
0
161.9
166.1
170.3
174.5
178.9
183.3
187.8
192.3
197
201.7
206.4
211.1
215.8
220.8
225.8

160
170

0.605
0.617

230.8
235.8

0.564
0.573

230.8
235.8

(Amt of liq in dm3 which will condense from 1 m3 of gas)

/Kg

Density
Vapour

Kg/m3
Liquid
0.52
0.53
0.54
0.56
0.57
0.58
0.59
0.61
0.63
0.65
0.67
0.69
0.72
0.74
0.77
0.8
0.83
0.86
0.89
0.91
0.95
0.99
1.02
1.06
1.09
1.13
1.17
1.21
1.25
1.29
1.34
1.38
1.43
1.47

Enthalpy
Vapour
652
651
650
649
648
647
646
645
644
643
642
641
640
639
638
637
635
634
633
632
631
630
629
628
627
626
625
624
623
622
620
619
618
617

Kcal/Kg
Liquid
142.1
142.4
142.7
143
143.4
143.7
144
144.3
144.7
145
145.3
145.6
145.9
146.3
146.6
146.9
147.2
147.5
147.9
148.2
148.5
148.8
149.1
149.5
149.8
150.1
150.4
150.7
151.1
151.4
151.7
152
152.3
152.7

38.9
39.4
40
40.5
41.1
41.6
42.2
42.7
43.3
43.8
44.4
44.9
45.5
46.1
46.6
47.1
47.7
48.2
48.8
49.3
49.9
50.4
50.9
51.5
52.1
52.6
53.2
53.7
54.3
54.8
55.4
55.9
56.5
57

1.52
1.59
1.65
1.72
1.8
1.88
1.96
2.04
2.12
2.21
2.29
2.37
2.46
2.55
2.64
2.73
2.83
2.92
3.01
3.11
3.22
3.33
3.44
3.54
3.65
3.76
3.88
4
4.13
4.27
4.41
4.55
4.7
4.85
5
5.15
5.31
5.47
5.65
5.82
5.99
6.17
6.36
6.55
6.74
6.94
7.15

616
615
614
613
612
611
610
609
608
607
606
605
604
603
602
601
600
599
598
597
596
595
594
593
592
591
590
589
588
587
586
584.5
583.5
582.5
581.5
580.5
579
578
577
576
575
573.5
572.5
571.5
570
569
567.5

153
153.3
153.6
153.9
154.3
154.6
154.9
155.2
155.5
155.9
156.2
156.5
156.8
157.1
157.5
157.8
158.1
158.4
158.7
159.1
159.4
159.8
160.1
160.4
160.8
161.1
161.4
161.7
162
162.4
162.7
163
163.3
163.6
164
164.3
164.6
164.9
165.2
165.5
165.9
166.2
166.5
166.8
167.2
167.5
167.8

57.5
58
58.6
59.1
59.7
60.3
60.9
61.4
62
62.6
63.1
63.6
64.2
64.7
65.3
65.8
66.4
66.9
67.5
68.1
68.6
69.2
69.7
70.2
70.8
71.3
71.8
72.4
72.9
73.5
74.1
74.6
75.1
75.6
76.2
76.7
77.3
77.8
78.4
78.9
79.5
80
80.6
81.1
81.7
82.2
82.8

7.35
7.55
7.76
7.98
8.2
8.43
8.66
8.9
9.15
9.39
9.63
9.88
10.15
10.41
10.67
10.95
11.21
11.49
11.77
12.07

566.5
565
564
562.5
561.5
560
558.5
557
556
555
554
552.5
551.5
550
549
547.5
546.5
545
543.5
542

168.1
168.4
168.8
169.1
169.4
169.7
170
170.4
170.7
171
171.3
171.7
172
172.3
172.6
172.9
173.2
173.6
173.9
174.2

83.3
83.9
84.5
85
85.5
86.1
86.6
87.2
87.7
88.3
88.8
89.4
89.9
90.4
91
91.6
92.1
92.7
93.3
93.8

t -129'C liquid phase

ATED VAPOUR
:h-enthalpy kcal/kg:
P = 1.5 bar
v
0
0
0.266
0.277
0.288
0.298
0.308
0.318
0.328
0.338
0.348
0.358
0.368
0.378
0.388
0.398

: P-absolute pressure
P = 2.0 bar
v

h
0
0
165.4
169.6
173.8
178.2
182.6
187.2
191.8
196.6
201.4
206.2
211
215.8
220.8
225.8

0
0
0.197
0.206
0.215
0.224
0.232
0.24
0.248
0.256
0.264
0.271
0.278
0.285
0.291
0.297

P = 5.0 bar
v

h
0
0
164.8
169
173.2
177.6
182
186.6
191.2
196
200.8
205.8
210.8
215.8
220.8
225.8

0
0
0
0
0
0.085
0.087
0.09
0.093
0.096
0.099
0.103
0.107
0.111
0.114
0.118

0.407
0.416

230.8
235.8

0.308
0.309

230.8
235.8

0.122
0.126

Latent Heat
Kcal/Kg
103.2
103
102.7
102.5
102.3
102.1
101.8
101.6
101.4
101.2
100.9
100.7
100.4
100.2
100
99.8
99.5
99.3
99.1
98.9
98.6
98.4
98.2
98
97.7
97.5
97.2
97
96.8
96.6
96.3
96.1
95.8
95.7

95.5
95.3
95
94.8
94.6
94.3
94
93.8
93.5
93.3
93.1
92.9
92.6
92.4
92.2
92
91.7
91.5
91.2
91
90.8
90.6
90.4
90.2
90
89.8
89.6
89.3
89.1
88.9
88.6
88.4
88.2
88
87.8
87.6
87.3
87.1
86.8
86.6
86.4
86.2
85.9
85.7
85.5
85.3
85

84.8
84.5
84.3
84.1
83.9
83.6
83.4
83.2
83
82.7
82.5
82.3
82.1
81.9
81.6
81.3
81.1
80.9
80.6
80.4

P = 15.0 bar
v

h
0
0
0
0
0
174.1
178.9
183.7
188.6
193.5
198.5
203.5
208.6
213.7
218.9
224.1

0
0
0
0
0
0
0
0
0
0
0.027
0.029
0.03
0.032
0.033
0.034

h
0
0
0
0
0
0
0
0
0
0
190.3
196.1
201.9
207.8
213.7
219.7

229.3
234.5

0.035
0.036

225.7
231.7