RJ
RAW JUICE 1 RAW JUICE 2
JUICE INLET PIPE CALCULATION JUICE INLET PIPE CALCULATION
Juice Flow Rate (ton/hr) 114.86 Juice Flow Rate (ton/hr)
Density of Juice (g/cm3) 1.05 Density of Juice (g/cm3)
Juice Flow Rate (m3/hr) 109.39 Juice Flow Rate (m3/hr)
Specific Heat of Juice 0.91 Specific Heat of Juice
Juice Inlet Temp (deg C) 33.2 Juice Inlet Temp (deg C)
Juice Outlet Temp (deg C) 49.1 Juice Outlet Temp (deg C)
Vapor Temperature (deg C) 55 Vapor Temperature (deg C)
Velocity of Juice (m/sec) 2 Velocity of Juice (m/sec)
Area of Juice Inlet Pipe (m2) 0.0152 Area of Juice Inlet Pipe (m2)
Juice Inlet Pipe Dia (m) 0.1391 Juice Inlet Pipe Dia (m)
Juice Inlet Pipe Dia (20% Margin) (m) 0.1669 Juice Inlet Pipe Dia (20% Margin) (m)
Juice Inlet Pipe Dia (20% Margin) (mm) 166.94 Juice Inlet Pipe Dia (20% Margin) (mm)
VAPOR LINE CALCULATION VAPOR LINE CALCULATION
Latent Heat 566.06 Latent Heat
Vapor Flow Rate (ton/hr) 2.94 Amt of Vapor required for RJ 2nd (ton/hr)
Specific Volume (m3/kg) 9.58 Vapor Flow Rate (ton/hr)
Velocity of Vapor (m/sec) 77.40 Specific Volume (m3/kg)
Vapor Flow Rate (m3/hr) 28176.96 Velocity of Vapor (m/sec)
Area of Vapor Line (m2) 0.10 Vapor Flow Rate (m3/hr)
Vapor Line Inlet Dia (m) 0.359 Area of Vapor Line (m2)
Vapor Line Inlet Dia (20% Margin) (m) 0.431 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (mm) 430.71 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm)
Page 1
RJ
Leg Required from RJ2 to Reaction Tank
114.86 Vapor Pr. at RJ2 (Bar) 0.64
1.05 Vapor Pr. RJ2 (N/m2) 63700
109.39 Vapor Pr. at Reaction Tank (Bar) 1.00
0.91 Vapor Pr. Reaction Tank (N/m2) 100000
49.1 ΔP (N/m2) or (kg/m sec2) 36300.00
80 Density (kg/m3) 1050
87.5 Gravity (m/sec2) 9.8
1.5 Therefore Leg required (m) 3.53
0.02 20% margin 4.23
0.16
0.19
192.77
547.03
5.92
5.92
2.63
40.54
15569.60
0.11
0.37
0.44
442.36
Page 2
SJ
SULPHITED JUICE CALCULATION
SJ1 SJ2
JUICE INLET PIPE CALCULATION JUICE INLET PIPE CALCULATION
Juice Flow Rate (ton/hr) 122.78 Juice Flow Rate (ton/hr)
Density of Juice (g/cm3 or ton/m3) 1.05 Density of Juice (g/cm3 or ton/m3)
Juice Flow Rate (m3/hr) 116.93 Juice Flow Rate (m3/hr)
Specific Heat of Juice 0.91 Specific Heat of Juice
Juice Inlet Temp (deg C) 79 Juice Inlet Temp (deg C)
Juice Outlet Temp (deg C) 99 Juice Outlet Temp (deg C)
Vapor Temperature (deg C) 100.9 Vapor Temperature (deg C)
Velocity of Juice (m/sec) 2 Velocity of Juice (m/sec)
Area of Juice Inlet Pipe (m2) 0.02 Area of Juice Inlet Pipe (m2)
Juice Inlet Pipe Dia (m) 0.14 Juice Inlet Pipe Dia (m)
Juice Inlet Pipe Dia (20% Margin) (m) 0.17 Juice Inlet Pipe Dia (20% Margin) (m)
Juice Inlet Pipe Dia (20% Margin) (mm) 172.60 Juice Inlet Pipe Dia (20% Margin) (mm)
VAPOR LINE CALCULATION VAPOR LINE CALCULATION
Latent Heat 538.86 Latent Heat
Amt of Vapor required for SJ 1st (ton/hr) 4.27 Amt of Vapor required for SJ 2nd (ton/hr)
Vapor Flow Rate (ton/hr) 4.27 Vapor Flow Rate (ton/hr)
Specific Volume (m3/kg) 1.67 Specific Volume (m3/kg)
Velocity of Vapor (m/sec) 32.34 Velocity of Vapor (m/sec)
Vapor Flow Rate (m3/hr) 7143.71 Vapor Flow Rate (m3/hr)
Area of Vapor Line (m2) 0.06 Area of Vapor Line (m2)
Vapor Line Inlet Dia (m) 0.28 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (m) 0.34 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm) 335.52 Vapor Line Inlet Dia (20% Margin) (mm)
Page 3
SJ
Leg Required from SJ1 to SJ2 Calculated
127.05 Vapor Pr. at SJ1 (Bar) 1.05
1.05 Vapor Pr. SJ1 (N/m2) 104700
121.00 Vapor Pr. at SJ2 (Bar) 1.37
0.91 Vapor Pr. SJ2 (N/m2) 136600
99 ΔP (N/m2) or (kg/m sec2) 31900.00
102 Density (kg/m3) 1050
108.6 Gravity (m/sec2) 9.8
1.5 Therefore Leg required (m) 3.10
0.02 20% margin 3.72
0.17
0.20
202.74
Leg Required from SJ2 to Flash tank
533.81
0.67 Vapor Pr. at SJ2 (Bar) 1.37
0.67 Vapor Pr. SJ2 (N/m2) 136600
1.29 Vapor Pr. at Flash tank (Bar) 1.00
28.38 Vapor Pr. Flash tank (N/m2) 100000
863.29 ΔP (N/m2) or (kg/m sec2) 36600.00
0.01 Density (kg/m3) 1050
0.10 Gravity (m/sec2) 9.8
0.12 Therefore Leg required (m) 3.56
124.50 20% margin(mm) 4268.22
Page 4
CJ
CLEAR JUICE CALCULATION
JUICE INLET PIPE CALCULATION
Juice Flow Rate (ton/hr) 144.1
Density of Juice 1.05
Juice Flow Rate (m3/hr) 137.24
Specific Heat of Juice 0.91
Juice Inlet Temp (deg C) 95
Juice Outlet Temp (deg C) 99.4
Vapor Temperature (deg C) 100
Velocity of Juice (m/sec) 1.5
Area of Juice Inlet Pipe (m2) 0.03
Juice Inlet Pipe Dia (m) 0.18
Juice Inlet Pipe Dia (20% Margin) (m) 0.22
Juice Inlet Pipe Dia (20% Margin) (mm) 215.92
VAPOR LINE CALCULATION
Latent Heat 538.86
Amt of Vapor required for CJ 1st (ton/hr) 1.07
Vapor Flow Rate (ton/hr) 1.07
Specific Volume (m3/kg) 1.67
Velocity of Vapor (m/sec) 32.34
Vapor Flow Rate (m3/hr) 1791.34
Area of Vapor Line (m2) 0.02
Vapor Line Inlet Dia (m) 0.14
Vapor Line Inlet Dia (20% Margin) (m) 0.17
Vapor Line Inlet Dia (20% Margin) (mm) 168.01
Page 5
JUICE PIPE CALCULATION
INLET (1st Body) INLET (2nd Body)
Juice Flow Rate (ton/hr) 114.57 Juice Flow Rate (ton/hr)
Density of Juice 1.05 Density of Juice
Juice Flow Rate (m3/hr) 109.11 Juice Flow Rate (m3/hr)
Velocity of Juice (m/sec) 1.5 Velocity of Juice (m/sec)
Area of Juice Inlet Pipe (m2) 0.02 Area of Juice Inlet Pipe (m2)
Juice Inlet Pipe Dia (m) 0.16 Juice Inlet Pipe Dia (m)
Juice Inlet Pipe Dia (20% Margin) (m) 0.19 Juice Inlet Pipe Dia (20% Margin) (m)
Juice Inlet Pipe Dia (20% Margin) (mm) 192.53 Juice Inlet Pipe Dia (20% Margin) (mm)
VAPOR PIPE CALCULATION
1st Body
INLET OUTLET
Steam Temp. 120.2 Steam Temp.
Latent Heat 525.89 Latent Heat
Vapor Flow Rate (ton/hr) 27.14 Vapor Flow Rate (ton/hr)
Specific Volume (m3/kg) 0.89 Specific Volume (m3/kg)
Velocity of Vapor (m/sec) 23.60 Velocity of Vapor (m/sec)
Vapor Flow Rate (m3/sec) 6.72 Vapor Flow Rate (m3/sec)
Area of Vapor Line (m2) 0.28 Area of Vapor Line (m^2)
Vapor Line Inlet Dia (m) 0.60 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (m) 0.72 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm) 722.66 Vapor Line Inlet Dia (20% Margin) (mm)
2nd Body
INLET OUTLET
Steam Temp. 114.5 Steam Temp.
Latent Heat 529.89 Latent Heat
Vapor Flow Rate (ton/hr) 22.45 Vapor Flow Rate (ton/hr)
Specific Volume (m3/kg) 1.07 Specific Volume (m3/kg)
Velocity of Vapor (m/sec) 25.84 Velocity of Vapor (m/sec)
Vapor Flow Rate (m3/sec) 6.66 Vapor Flow Rate (m3/sec)
Area of Vapor Line (m2) 0.26 Area of Vapor Line (m2)
Vapor Line Inlet Dia (m) 0.57 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (m) 0.69 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm) 687.71 Vapor Line Inlet Dia (20% Margin) (mm)
3rd Body
INLET OUTLET
Steam Temp. 108.6 Steam Temp.
Latent Heat 533.81 Latent Heat
Vapor Flow Rate (ton/hr) 22.82 Vapor Flow Rate (ton/hr)
Specific Volume (m3/kg) 1.29 Specific Volume (m3/kg)
Velocity of Vapor (m/sec) 28.38 Velocity of Vapor (m/sec)
Vapor Flow Rate (m3/sec) 8.17 Vapor Flow Rate (m3/sec)
Area of Vapor Line (m2) 0.29 Area of Vapor Line (m2)
Vapor Line Inlet Dia (m) 0.61 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (m) 0.73 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm) 726.61 Vapor Line Inlet Dia (20% Margin) (mm)
4th Body
INLET OUTLET
Steam Temp. 100.9 Steam Temp.
Latent Heat 538.86 Latent Heat
Vapor Flow Rate (ton/hr) 19.10 Vapor Flow Rate (ton/hr)
Specific Volume (m3/kg) 1.67 Specific Volume (m3/kg)
Velocity of Vapor (m/sec) 32.34 Velocity of Vapor (m/sec)
Vapor Flow Rate (m3/sec) 8.88 Vapor Flow Rate (m3/sec)
Area of Vapor Line (m2) 0.27 Area of Vapor Line (m2)
Vapor Line Inlet Dia (m) 0.59 Vapor Line Inlet Dia (m)
Vapor Line Inlet Dia (20% Margin) (m) 0.71 Vapor Line Inlet Dia (20% Margin) (m)
Vapor Line Inlet Dia (20% Margin) (mm) 709.60 Vapor Line Inlet Dia (20% Margin) (mm)
VAPOR LINE TO CONDENSER
Steam Temp. 72
Latent Heat 556.17
Vapor Flow Rate (ton/hr) 11.12
Specific Volume (m3/kg) 4.66
Velocity of Vapor (m/sec) 53.96
Vapor Flow Rate (m3/sec) 14.39
Area of Vapor Line (m2) 0.27
Vapor Line Inlet Dia (m) 0.58
Vapor Line Inlet Dia (20% Margin) (m) 0.70
Vapor Line Inlet Dia (20% Margin) (mm) 699.40
INLET (3rd Body)
92.12 Juice Flow Rate (ton/hr) 68.88
1.05 Density of Juice 1.05
87.73 Juice Flow Rate (m3/hr) 65.60
1.5 Velocity of Juice (m/sec) 1.5
0.02 Area of Juice Inlet Pipe (m2) 0.01
0.14 Juice Inlet Pipe Dia (m) 0.12
0.17 Juice Inlet Pipe Dia (20% Margin) (m) 0.15
172.64 Juice Inlet Pipe Dia (20% Margin) (mm) 149.28
CONENSATE PIPE LINE CAL.
114.5 Flow Rate (ton/hr) 27.14
529.89 Velocity (m/sec) 0.7
22.45 Area of Juice Inlet Pipe (m2) 0.011
1.07 Juice Inlet Pipe Dia (m) 0.117
25.84 Juice Inlet Pipe Dia (20% Margin) (m) 0.141
6.66 Juice Inlet Pipe Dia (20% Margin) (mm) 140.56
0.26
0.57
0.69
687.71
CONENSATE PIPE LINE CAL.
108.6 Flow Rate (ton/hr) 22.45
533.81 Velocity (m/sec) 0.7
23.49 Area of Juice Inlet Pipe (m2) 0.009
1.29 Juice Inlet Pipe Dia (m) 0.107
28.38 Juice Inlet Pipe Dia (20% Margin) (m) 0.128
8.41 Juice Inlet Pipe Dia (20% Margin) (mm) 127.84
0.30
0.61
0.74
737.20
CONENSATE PIPE LINE CAL.
100.9 Flow Rate (ton/hr) 22.82
538.86 Velocity (m/sec) 0.7
24.15 Area of Juice Inlet Pipe (m2) 0.009
1.67 Juice Inlet Pipe Dia (m) 0.107
32.34 Juice Inlet Pipe Dia (20% Margin) (m) 0.129
11.22 Juice Inlet Pipe Dia (20% Margin) (mm) 128.89
0.35
0.66
0.80
797.92
CONENSATE PIPE LINE CAL.
87.5 Flow Rate (ton/hr) 19.10
547.03 Velocity (m/sec) 0.7
21.24 Area of Juice Inlet Pipe (m2) 0.008
2.63 Juice Inlet Pipe Dia (m) 0.098
40.54 Juice Inlet Pipe Dia (20% Margin) (m) 0.118
15.52 Juice Inlet Pipe Dia (20% Margin) (mm) 117.91
0.38
0.70
0.84
837.90
INLET (4th Body) OUTLET (4TH Body)
Juice Flow Rate (ton/hr) Juice Flow Rate (ton/hr) 25.71
Density of Juice Density of Juice 1.2
Juice Flow Rate (m3/hr) Juice Flow Rate (m3/hr) 21.43
Velocity of Juice (m/sec) Velocity of Juice (m/sec) 1.5
Area of Juice Inlet Pipe (m2) Area of Juice Inlet Pipe (m2) 0.00
Juice Inlet Pipe Dia (m) Juice Inlet Pipe Dia (m) 0.07
Juice Inlet Pipe Dia (20% Margin) (m) Juice Inlet Pipe Dia (20% Margin) (m) 0.09
Juice Inlet Pipe Dia (20% Margin) Juice Inlet Pipe Dia (20% Margin) (mm) 85.31
1st VAPOR TO FOLLOWING
2nd VAPOR TO FOLLOWING (t/hr)
SJ2 heating
CJ heating
3rd VAPOR TO FOLLOWING (t/hr)
Graining+B&C Pans
A Pans
SJ1 Heating
B&C Melter
Molasses Conditioning
4th VAPOR TO FOLLOWING (t/hr)
MJ1
MJ2
Leg Calculation
Leg Required from 1st Chamber to 2nd Chamber
2nd vap. Temp. 108.6
Vapor Pr. at 1st Chamber (Bar) 1.37
Vapor Pr. 1st Chamber (N/m2) 136500
3rd vap. Temp. 100.9
Vapor Pr. at 2nd Chamber (Bar) 1.05
Vapor Pr. 2nd Chamber (N/m2) 104700
ΔP (N/m2) or (kg/m sec2) 31800.00
Density of Condensate (kg/m3) 1000
Gravity (m/sec2) 9.8
Therefore Leg required (m) 3.24
20% margin 3.89
Leg Required from 2nd Chamber to 3rd Chamber
3rd vap. Temp. 100.9
Vapor Pr. at 2nd Chamber (Bar) 1.05
Vapor Pr. 2nd Chamber (N/m2) 104700
4th vap. Temp. 87.5
Vapor Pr. at 3rd Chamber (Bar) 0.64
Vapor Pr. 3rd Chamber (N/m2) 63700
ΔP (N/m2) or (kg/m sec2) 41000.00
Density of Condensate (kg/m3) 1000
Gravity (m/sec2) 9.8
Therefore Leg required (m) 4.18
20% margin 5.02
Leg Required from 3rd Chamber to 4th Chamber
Vapor Pr. at 3rd Chamber (Bar) 0.64
Vapor Pr. 3rd Chamber (N/m2) 63700
4th vap. Temp. 87.5
Vapor Pr. at 4th Chamber (Bar) 0.39
Vapor Pr. 4th Chamber (N/m2) 38900
ΔP (N/m2) or (kg/m sec2) 24800.00
Density of Condensate (kg/m3) 1000
Gravity (m/sec2) 9.8
Therefore Leg required (m) 2.53
20% margin 3.04
Line Size Calculation Flashing Line Calculation
1st Chamber to 2nd Chamber line size 1st Chamber to 1st vapor header
Condensate from2nd body FFE (ton/hr) 22.45 2nd vap. Temp. 108.6
Flash vap. Qty. (ton/hr) 0.25 Flash vap. Qty. (ton/hr) 0.250
Condensate from 1st to 2nd Chamber (ton/hr) 22.20 Specific Volume (m3/kg) 1.288
Total cond. Flow Rate (m3/hr) 22.20 Mass Flow Rate (m3/hr) 322.123
Density (g/cm3)or(t/m3) 1 Velocity of Vapor (m/sec) 28.378
Velocity of Condensate (m/sec) 0.7 Area of Flashing Pipe (m2) 0.003
Area of Condensate Pipe (m2) 0.009 Diameter (m) 0.063
Diameter (m) 0.106 20% Margin (mm) 76.053
20% Margin (mm) 127.123
2nd Chamber to 3rd Chamber line size 2nd Chamber to 2nd vapor header
Condensate from 3rd body FFE (t/hr) 22.82 3rd vap. Temp. 100.900
Flash vap. Qty. (ton/hr) 0.650 Flash vap. Qty. (ton/hr) 0.650
Condensate from 1st chamber (t/hr) 22.20 Specific Volume (m3/kg) 1.673
Condensate from 2nd to 3rd Chamber (ton/hr) 44.37 Mass Flow Rate (m3/hr) 1087.450
Total cond. Flow Rate (m3/hr) 44.37 Velocity of Vapor (m/sec) 32.336
Density (g/cm3)or(t/m3) 1 Area of Flashing Pipe (m2) 0.009
Velocity of Condensate (m/sec) 0.7 Diameter (m) 0.109
Area of Condensate Pipe (m2) 0.018 20% Margin (mm) 130.905
Diameter (m) 0.150
20% Margin (mm) 179.718
3rd Chamber to 4th Chamber line size 3rd Chamber to 3rd vapor header
Pan Condensate (t/hr) 18.26 Flash vap. Qty. (ton/hr) 1.103
Condensate from 4th body FFE (t/hr) 19.10 Specific Volume (m3/kg) 1.673
Condensate from 3rd chamber (t/hr) 43.27 Mass Flow Rate (m3/hr) 1845.926
Condensate from 3rd to 4th Chamber (ton/hr) 80.63 Velocity of Vapor (m/sec) 32.336
Total cond. Flow Rate (m3/hr) 80.63 Area of Flashing Pipe (m2) 0.016
Density (g/cm3)or(t/m3) 1 Diameter (m) 0.142
Velocity of Condensate (m/sec) 0.7 20% Margin (mm) 170.553
Area of Condensate Pipe (m2) 0.032
Diameter (m) 0.202
20% Margin (mm) 242.262
4th Chamber to Pump line size 4th Chamber to 4th vapor header
RJ Condensate (t/hr) 8.41 Flash vap. Qty. (ton/hr) 0.000
Condensate from 4th Chamber (ton/hr) 80.63 Specific Volume (m3/kg) 2.630
Mass Flow Rate (t/hr) 89.04 Mass Flow Rate (m3/hr) 0.000
Total cond. Flow Rate (m3/hr) 89.04 Velocity of Vapor (m/sec) 40.543
Density (g/cm3)or(t/m3) 1 Area of Flashing Pipe (m2) 0.000
Velocity of Condensate (m/sec) 0.7 Diameter (m) 0.000
Area of Condensate Pipe (m2) 0.032 20% Margin (mm) 0.000
Diameter (m) 0.202
20% Margin (mm) 242.262
TEMPERATURE SATURATED PRESSURE SPECIFIC VOLUME SENSIBLE HEAT LATENT HEAT
t °c Kgf/cm^2 m^3/Kg Kcal/Kg Kcal/Kg
0 0.0062 206.30 0 597.2
1 0.0067 192.70 1.01 596.59
2 0.0072 180.00 2.01 595.99
3 0.0077 168.10 3.02 595.48
4 0.0083 157.30 4.02 594.98
5 0.0089 147.20 5.03 594.37
6 0.0095 137.80 6.03 593.77
7 0.0102 129.10 7.03 593.17
8 0.0109 121.00 8.04 592.66
9 0.0117 113.40 9.04 592.06
10 0.0125 106.40 10.04 591.56
11 0.0134 99.92 11.04 590.96
12 0.0143 93.85 12.04 590.46
13 0.0152 88.19 13.04 589.86
14 0.0163 82.91 14.04 589.36
15 0.0174 77.99 15.04 588.76
16 0.0185 73.39 16.04 588.26
17 0.0197 69.10 17.04 587.66
18 0.021 65.10 18.04 587.06
19 0.0224 61.35 19.03 586.57
20 0.0238 57.84 20.03 585.97
21 0.0253 54.56 21.03 585.47
22 0.0269 51.49 22.03 584.87
23 0.0286 48.63 23.02 584.28
24 0.0304 45.94 24.02 583.78
25 0.0323 43.41 25.02 583.18
26 0.0342 41.04 26.01 582.59
27 0.0363 38.82 27.01 582.09
28 0.0385 36.73 28.01 581.49
29 0.0408 34.77 29 581
30 0.0432 32.93 30 580.4
31 0.0458 31.20 31 579.8
32 0.0485 29.58 32 579.3
33 0.0513 28.05 32.99 578.71
34 0.0542 26.61 33.99 578.11
35 0.0573 25.25 34.99 577.51
36 0.0606 23.97 35.99 577.01
37 0.064 22.77 36.98 576.42
38 0.0675 21.63 37.98 575.92
39 0.0713 20.56 38.98 575.32
40 0.0752 19.55 39.98 574.72
41 0.0793 18.60 40.98 574.22
42 0.0836 17.70 41.97 573.63
43 0.0881 16.85 42.97 573.03
44 0.0928 16.04 43.97 572.43
45 0.0977 15.28 44.96 571.84
46 0.1028 14.56 45.96 571.24
47 0.1082 13.88 46.96 570.74
48 0.1138 13.24 47.95 570.15
49 0.1197 12.61 48.95 569.55
50 0.1258 12.05 49.95 569.05
51 0.1322 11.50 50.95 568.45
52 0.1388 10.98 51.95 567.85
53 0.1457 10.49 52.94 567.26
54 0.153 10.03 53.94 566.66
55 0.1605 9.58 54.94 566.06
56 0.1683 9.16 55.94 565.56
57 0.1765 8.76 56.94 564.96
58 0.185 8.39 57.94 564.36
59 0.1939 8.03 58.94 563.76
60 0.2031 7.68 59.94 563.26
61 0.2127 7.36 60.94 562.66
62 0.2227 7.05 61.94 562.06
63 0.233 6.75 62.94 561.46
64 0.2438 6.47 63.94 560.86
65 0.255 6.21 64.93 560.27
66 0.2666 5.95 65.93 559.67
67 0.2787 5.71 66.93 559.07
68 0.2912 5.48 67.93 558.47
69 0.3042 5.26 68.93 557.97
70 0.3177 5.05 69.93 557.37
71 0.3317 4.85 70.93 556.77
72 0.3463 4.66 71.93 556.17
73 0.3613 4.48 72.93 555.57
74 0.3779 4.30 73.94 554.96
75 0.3931 4.14 74.94 554.36
76 0.4098 3.98 75.94 553.76
77 0.4272 3.83 76.94 553.16
78 0.4451 3.68 77.95 552.55
79 0.4637 3.54 78.95 551.95
80 0.4829 3.41 79.95 551.35
81 0.5028 3.28 80.95 550.75
82 0.5234 3.16 81.95 549.95
83 0.5447 3.05 82.96 549.34
84 0.5667 2.94 83.96 548.84
85 0.5894 2.83 84.96 548.24
86 0.6129 2.73 85.96 547.64
87 0.6372 2.63 86.97 547.03
88 0.6623 2.54 87.97 546.43
89 0.6882 2.45 88.98 545.72
90 0.7149 2.36 89.98 545.12
91 0.7425 2.28 90.98 544.52
92 0.771 2.20 91.99 543.91
93 0.8004 2.12 93 543.3
94 0.8307 2.05 94 542.6
95 0.8619 1.98 95.01 541.99
96 0.8942 1.91 96.01 541.39
97 0.9274 1.85 97.02 540.78
98 0.9616 1.79 98.02 540.18
99 0.9969 1.73 99.03 539.47
100 1.0332 1.67 100.04 538.86
101 1.071 1.62 101.07 538.31
102 1.109 1.56 102.08 537.67
103 1.149 1.51 103.09 537.03
104 1.19 1.47 104.1 536.39
105 1.232 1.42 105.11 535.75
106 1.275 1.37 106.12 535.1
107 1.319 1.33 107.13 534.46
108 1.365 1.29 108.14 533.81
109 1.412 1.25 109.15 533.16
110 1.461 1.21 110.16 532.51
111 1.511 1.17 111.17 531.86
112 1.562 1.14 112.18 531.2
113 1.614 1.10 113.19 530.54
114 1.668 1.07 114.2 529.89
115 1.724 1.04 115.22 529.22
116 1.781 1.00 116.23 528.56
117 1.839 0.97 117.24 527.23
118 1.899 0.95 118.26 527.23
119 1.961 0.92 119.27 526.56
120 2.024 0.89 120.29 525.89
121 2.089 0.87 121.3 525.21
122 2.156 0.84 122.32 524.54
123 2.224 0.82 123.33 523.86
124 2.294 0.79 124.35 523.18
125 2.366 0.77 125.37 522.5
126 2.44 0.75 126.39 521.81
127 2.516 0.73 127.4 521.12
128 2.593 0.71 128.42 520.43
129 2.673 0.69 129.44 519.74
130 2.754 0.67 130.46 519.05
131 2.837 0.65 131.48 518.35
132 2.923 0.63 132.5 517.65
133 3.01 0.61 133.52 516.95
134 3.1 0.60 134.54 516.95
135 3.192 0.58 135.56 515.54
136 3.286 0.57 136.59 514.83
137 3.382 0.55 137.61 514.12
138 3.48 0.54 138.63 513.4
139 3.581 0.52 139.66 512.68
140 3.684 0.51 140.68 511.96
141 3.79 0.50 141.71 511.24
142 3.898 0.48 142.73 510.52
143 4.008 0.47 143.76 509.79
144 4.121 0.46 144.79 509.06
145 4.236 0.45 145.81 508.33
146 4.354 0.43 146.84 507.59
147 4.475 0.42 147.87 506.85
148 4.598 0.41 148.9 506.11
149 4.724 0.40 149.93 505.36
150 4.853 0.39 150.96 504.62
Enter Temprature of steam 109
Saturation Pressure Kgf/cm^2 (Absolute) 1.412
Sp. Volume of Vapour m^3/Kg 1.248
SENSIBLE HEAT Kcal/Kg 109.15
LATENT HEAT Kcal/Kg 533.16
Temp Density Vac Leg
100 1 0.00 0.00 -0.60
80 1 0.55 5.50
Difference 5.503
210 623.13 541.85 13.55 54.19
175 432.73 376.29 9.41 37.63
200 565.20 491.48 12.29 49.15
0.6182
0.639
0.6603
0.6823
0.7048
0.7279
0.7517
0.7761
0.8011
0.8267
0.8531
0.8801
0.9078
0.9361
0.9653
0.9951
1.0257
1.057
1.0891
1.122
1.1557
1.19
1.2255
1.2616
1.2986
1.3365
1.3753
1.415
1.4556
1.4971
1.5395
1.583
1.6274
1.6728
1.7192
1.7667
1.8151
1.8647
1.9153
1.9671
2.0199
2.0739
2.129
2.1853
2.2428
2.3015
2.3614
2.4226
2.485
2.5487
