[A] BOILER DUTY FOR INITIAL HEATING OIL INSIDE TANK
Service = To heat up oil temperature inside tank to specified temperature
HFO Temperature Initial = 10
HFO Temperature Final = 40
HFO Gross Volume = 6,500 Refer to bid document 1.6.1. Tank Dimension
HFO Net Working Volume = 6,150
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,094,650 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 18,283,950 kg
Pumping frequency = 96 hr
= 345,600 sec
= 4 days Refer to bid document 2.2.4. Pipework
Heating duty = 2,725,134 Joule/sec
= 2.725 MW
Hot water operating pressure = 3 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,397 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 16 kg/sec
= 56,214 kg/hr Refer to manual calculation
= 56,269 kg/hr Refer to Hysis simulation
[2] BOILER DUTY DURING INITIAL OPERATION
Boiler heating duty = 2.725 MW
Boiler heating capacity = 4.500 MW
Note = Oke becauce boiler is over capacity
[1] DUTY FOR HEATING HEAVY FUEL OIL [HFO] "INSIDE" STORAGE TANK
oC
oC
m3
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
6500 m3
[3] FASTEST PERIOD FOR HEATING 3 OIL STORAGE
Service = To heat up oil temperature inside tank to specified temperature
HFO Temperature Initial = 10
HFO Temperature Final = 40
HFO Volume = 6,500 Refer to bid document 1.6.1. Tank Dimension
HFO Net Working Volume = 6,150
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,094,650 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 18,283,950 kg
Maximum time for heating up = 58 hr
= 209,316 sec
= 2 days
Pumping frequency period = 96 hr
= 4 days Refer to bid document 2.2.4. Pipework
Note = Oke because shorther than pumping frequency period
Boiler duty = 4,499,442 Joule/sec
= 4.50 MW
Boiler design duty = 4.50 MW Refer to bid document data
Heat balance = 1
Hot water operating pressure = 3 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,397 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 26 kg/sec
= 92,826 kg/hr Refer to manual calculation
= 92,921 kg/hr Refer to Hysis simulation
.
[B] BOILER DUTY DURING NORMAL OPERATION
Service = To heat up pumped oil temperature to specified value
HFO Temperature Inlet = 40
HFO Temperature Outlet = 50
HFO Mass Flow = 600 ton/hr
= 600,000 kg/hr
HFO Specific Heat = 1,717 Refer to reference
Heating duty = 10,302,000,000 Joule/hr
= 2.862 MW
oC
oC
m3
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
[1] DUTY FOR HEATING UP HEAVY FUEL OIL [HFO] "OUTLET" STORAGE TANK
oC
oC
Joule/kg.oC
HFO Inlet HFO Outlet
Hot Water Inlet Hot Water Outlet
Hot water operating pressure = 3 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,397 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 16 kg/sec
= 59,030 kg/hr Refer to manual calculation
= 59,098 kg/hr Refer to Hysis simulation
Service = To maintain oil temperature inside tank to specified temperature
HFO Temperature Initial = 35
HFO Temperature Final = 40
HFO Volume = 6,500
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,441,500 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 19,324,500 kg
Maximum time for heating up = 120 hr Refer to bid document 4.10.8. HFO Storage Tank Heating Coil
= 432,000 sec
= 5 days
Heating duty = 384,030 Joule/sec
= 0.3840 MW
Hot water operating pressure = 3 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,397 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 2 kg/sec
= 7,922 kg/hr Refer to manual calculation
= 7,929 kg/hr Refer to Hysis simulation
[3] BOILER DUTY DURING NORMAL OPERATION
Boiler heating duty = 3.25 MW
Boiler heating capacity = 4.50 MW
Note = Oke becauce boiler is over capacity
oC
Joule/kg.oC
oC
Joule/kg.oC
[2] DUTY FOR HEATING HEAVY FUEL OIL [HFO] "INSIDE" STORAGE TANK
oC
oC
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
6500 m3
[C] HOT WATER SUMMARY
Hot water mass rate = 56,269 kg/hr Initial heating up period for 4 days
= 92,921 kg/hr Initial heating up period with maximum boiler capacity
= 67,027 kg/hr Heating up duty during normal operation
Selected hot water mass rate = 92,921 kg/hr Higher value is selected
[D] MAKE UP WATER CALCULATION
Boiler cycle of concentration = 10 Typical boiler 10 ~ 50 COC
% Blow down = 10 % Initial heating up period with maximum boiler capacity
Boiler feed water mass rate = 6,894 kg/hr Refer to Hysis Simulation
Boiler blow down mass rate = 689 kg/hr
Boiler make up water = 689 kg/hr
= 0.6894
Condition :
Steam mass rate = 6,894 kg/hr
Steam operating pressure = 3 barg Refer to Hysis Simulation
Steam operating pressure = 143.7 Refer to Hysis Simulation
[E] WASTE HEAT RECOVERY IN FORT VICTORIA POWER STATION
[1] FORT VICTORIA POWER STATION
Fort Victoria power plant capacity = 90 MW Refer to data googling
Fort Victoria power plant capacity for design heat recovery = 45 MW Assume
Machine = diesel engine generator Refer to data googling
Engine brand = Wartsila
Number of engine = 6 ea Refer to data googling
Capacity each engine = 15 MW Refer to data googling
Efficiency = 45 % Refer to product bulletin (if no data use value 30 ~ 35 %)
Total fuel heat combustion = 100 MW
Total heat loss = 55 MW
Heat loss carried by flue gas = 60 % total heat loss Refer to reference
= 33 MW
Heat loss carried by engine cooling system = 40 % total heat loss Refer to reference
= 22 MW
Net caloric value = 40 MJ/kg Refer to reference
Total HFO mass rate to engine = 2.5 kg/sec
= 9,000 kg/hr
[2] PRE-HEATER DUTY
Hot water operating pressure = 3 barg
Max hot water mass rate = 92,921 kg/hr Refer to Hysis simulation
Hot water inlet temperature = 60
Cp hot water inlet = 4,329 Refer to Hysis simulation
Hot water outlet temperature = 80
Cp hot water outlet = 4,356 Refer to Hysis simulation
Preheater duty = 8,070,203,531 Joule/hr
= 2.242 MW Refer to manual calculation
= 2.241 MW Refer to Hysis simulation
Heat available in Fort Victoria Power Plant = 22 MW
Note = Heat recovery is available
Hot water operating pressure = 6 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,396 Refer to Hysis simulation
Hot water outlet temperature = 70
Cp hot water outlet = 4,341 Refer to Hysis simulation
Hot water mass rate = 17 kg/sec
m3/hr
oC
oC
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
= 61,559 kg/hr Refer to manual calculation
= 61,597 kg/hr Refer to Hysis simulation
[F] HEAT BALANCE AROUND STEAM DRUM DURING NORMAL OPERATION
Steam condition = saturated
Steam mass rate = 4,680 kg/hr Calculated
Steam temperature = 143.72 Refer to Hysis simulation
Steam pressure = 3.00 barg Refer to Hysis simulation
Make up water condition = subcooled
Make up water mass rate = 689 kg/hr Refer to Hysis simulation
Make up water temperature = 20.00 Assume
Make up water pressure = 3.00 barg Refer to Hysis simulation
Hot water inlet tank condition = subcooled
Hot water inlet water mass rate = 67,027 kg/hr Refer to Hysis simulation
Hot water inlet water temperature = 100.00 Assume
Hot water inlet water pressure = 3.00 barg Refer to Hysis simulation
Hot water outlet tank condition = subcooled
Hot water outlet water mass rate = 62,347 kg/hr Calculated
Hot water outlet water temperature = 60.00 Assume
Hot water outlet water pressure = 3.00 barg Refer to Hysis simulation
Blow down water condition = subcooled
Blow down water mass rate = 689 kg/hr Refer to Hysis simulation
Blow down water temperature = 100.00 Assume
Blow down water pressure = 3.00 barg Refer to Hysis simulation
Steam mass flow rate during normal condition = 4,680 kg/hr Refer to Hysis simulation
Boiler design capacity = 6,894 kg/hr Refer to Hysis simulation
Note = Oke due to steam demand is lower than steam design capacity
oC
oC
oC
oC
oC
[A] BOILER DUTY FOR INITIAL HEATING OIL INSIDE TANK
Service = To heat up oil temperature inside tank to specified temperature
HFO Temperature Initial = 10
HFO Temperature Final = 40
HFO Gross Volume = 6,500 Refer to bid document 1.6.1. Tank Dimension
HFO Net Working Volume = 6,150
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,094,650 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 18,283,950 kg
Pumping frequency = 96 hr
= 345,600 sec
= 4 days Refer to bid document 2.2.4. Pipework
Heating duty = 2,725,134 Joule/sec
= 2.725 MW
Hot water operating pressure = 5 barg
Hot water inlet temperature = 140
Cp hot water inlet = 4,526 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 8 kg/sec
= 27,698 kg/hr Refer to manual calculation
= 27,830 kg/hr Refer to Hysis simulation
[2] BOILER DUTY DURING INITIAL OPERATION
Boiler heating duty = 2.725 MW
Boiler heating capacity = 4.500 MW
Note = Oke becauce boiler is over capacity
[1] DUTY FOR HEATING HEAVY FUEL OIL [HFO] "INSIDE" STORAGE TANK
oC
oC
m3
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
6500 m3
[3] FASTEST PERIOD FOR HEATING 3 OIL STORAGE
Service = To heat up oil temperature inside tank to specified temperature
HFO Temperature Initial = 10
HFO Temperature Final = 40
HFO Volume = 6,500 Refer to bid document 1.6.1. Tank Dimension
HFO Net Working Volume = 6,150
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,094,650 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 18,283,950 kg
Maximum time for heating up = 58 hr
= 209,316 sec
= 2 days
Pumping frequency period = 96 hr
= 4 days Refer to bid document 2.2.4. Pipework
Note = Oke because shorther than pumping frequency period
Boiler duty = 4,499,442 Joule/sec
= 4.50 MW
Boiler design duty = 4.50 MW Refer to bid document data
Heat balance = 1
Hot water operating pressure = 5 barg
Hot water inlet temperature = 140
Cp hot water inlet = 4,526 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 13 kg/sec
= 45,737 kg/hr Refer to manual calculation
= 45,955 kg/hr Refer to Hysis simulation
.
[B] BOILER DUTY DURING NORMAL OPERATION
Service = To heat up pumped oil temperature to specified value
HFO Temperature Inlet = 40
HFO Temperature Outlet = 50
HFO Mass Flow = 600 ton/hr
= 600,000 kg/hr
HFO Specific Heat = 1,717 Refer to reference
Heating duty = 10,302,000,000 Joule/hr
= 2.862 MW
oC
oC
m3
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
[1] DUTY FOR HEATING UP HEAVY FUEL OIL [HFO] "OUTLET" STORAGE TANK
oC
oC
Joule/kg.oC
HFO Inlet HFO Outlet
Hot Water Inlet Hot Water Outlet
Hot water operating pressure = 5 barg
Hot water inlet temperature = 140
Cp hot water inlet = 4,526 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 8 kg/sec
= 29,085 kg/hr Refer to manual calculation
= 29,231 kg/hr Refer to Hysis simulation
Service = To maintain oil temperature inside tank to specified temperature
HFO Temperature Initial = 35
HFO Temperature Final = 40
HFO Volume = 6,500
HFO Mass Density = 0.991 kg/lt Refer to reference
= 991
HFO Specific Heat = 1,717 Refer to reference
HFO Mass Stock = 6,441,500 kg
Number of HFO Tank = 3 ea
Total HFO Mass Stock = 19,324,500 kg
Maximum time for heating up = 120 hr Refer to bid document 4.10.8. HFO Storage Tank Heating Coil
= 432,000 sec
= 5 days
Heating duty = 384,030 Joule/sec
= 0.3840 MW
Hot water operating pressure = 5 barg
Hot water inlet temperature = 140
Cp hot water inlet = 4,526 Refer to Hysis simulation
Hot water outlet temperature = 60
Cp hot water outlet = 4,329 Refer to Hysis simulation
Hot water mass rate = 1.08 kg/sec
= 3,903 kg/hr Refer to manual calculation
= 3,931 kg/hr Refer to Hysis simulation
oC
Joule/kg.oC
oC
Joule/kg.oC
[2] DUTY FOR HEATING HEAVY FUEL OIL [HFO] "INSIDE" STORAGE TANK
oC
oC
m3
kg/m3
Joule/kg.oC
oC
Joule/kg.oC
oC
Joule/kg.oC
6500 m3
[3] BOILER DUTY DURING NORMAL OPERATION
Boiler heating duty = 3.25 MW
Boiler heating capacity = 4.50 MW
Note = Oke becauce boiler is over capacity
[C] HOT WATER SUMMARY
Hot water mass rate = 27,830 kg/hr Initial heating up period for 4 days
= 45,955 kg/hr Initial heating up period with maximum boiler capacity
= 33,162 kg/hr Heating up duty during normal operation
Selected hot water mass rate = 45,955 kg/hr Higher value is selected
[D] MAKE UP WATER CALCULATION
Boiler cycle of concentration = 10 Typical boiler 10 ~ 50 COC
% Blow down = 10 % Initial heating up period with maximum boiler capacity
Boiler feed water mass rate = 7,381 kg/hr Refer to Hysis Simulation
Boiler blow down mass rate = 738 kg/hr
Boiler make up water = 738 kg/hr
= 0.7381
Condition :
Steam mass rate = 7,381 kg/hr
Steam operating pressure = 5 barg Refer to Hysis Simulation
Steam operating pressure = 159.0 Refer to Hysis Simulation
[E] WASTE HEAT RECOVERY IN FORT VICTORIA POWER STATION
[1] FORT VICTORIA POWER STATION
Fort Victoria power plant capacity = 90 MW Refer to data googling
Fort Victoria power plant capacity for design heat recovery = 45 MW Assume
Machine = diesel engine generator Refer to data googling
Engine brand = Wartsila
Number of engine = 6 ea Refer to data googling
Capacity each engine = 15 MW Refer to data googling
Efficiency = 45 % Refer to product bulletin (if no data use value 30 ~ 35 %)
Total fuel heat combustion = 100 MW
Total heat loss = 55 MW
Heat loss carried by flue gas = 60 % total heat loss Refer to reference
= 33 MW
Heat loss carried by engine cooling system = 40 % total heat loss Refer to reference
= 22 MW
Net caloric value = 40 MJ/kg Refer to reference
Total HFO mass rate to engine = 2.5 kg/sec
= 9,000 kg/hr
[2] PRE-HEATER DUTY
Hot water operating pressure = 5 barg
Max hot water mass rate = 45,955 kg/hr Refer to Hysis simulation
Hot water inlet temperature = 60
Cp hot water inlet = 4,329 Refer to Hysis simulation
Hot water outlet temperature = 80
Cp hot water outlet = 4,356 Refer to Hysis simulation
Preheater duty = 3,991,155,665 Joule/hr
= 1.109 MW Refer to manual calculation
= 1.108 MW Refer to Hysis simulation
Heat available in Fort Victoria Power Plant = 22 MW
m3/hr
oC
oC
Joule/kg.oC
oC
Joule/kg.oC
Note = Heat recovery is available
Hot water operating pressure = 6 barg
Hot water inlet temperature = 100
Cp hot water inlet = 4,396 Refer to Hysis simulation
Hot water outlet temperature = 70
Cp hot water outlet = 4,341 Refer to Hysis simulation
Hot water mass rate = 8 kg/sec
= 30,436 kg/hr Refer to manual calculation
= 30,479 kg/hr Refer to Hysis simulation
[F] HEAT BALANCE AROUND STEAM DRUM DURING NORMAL OPERATION
Steam condition = saturated
Steam mass rate = 4,640 kg/hr Calculated
Steam temperature = 158.96 Refer to Hysis simulation
Steam pressure = 5.00 barg Refer to Hysis simulation
Make up water condition = subcooled
Make up water mass rate = 738 kg/hr Refer to Hysis simulation
Make up water temperature = 20.00 Assume
Make up water pressure = 5.00 barg Refer to Hysis simulation
Hot water inlet tank condition = subcooled
Hot water inlet water mass rate = 33,162 kg/hr Refer to Hysis simulation
Hot water inlet water temperature = 140.00 Assume
Hot water inlet water pressure = 5.00 barg Refer to Hysis simulation
Hot water outlet tank condition = subcooled
Hot water outlet water mass rate = 28,522 kg/hr Calculated
Hot water outlet water temperature = 60.00 Assume
Hot water outlet water pressure = 5.00 barg Refer to Hysis simulation
Blow down water condition = subcooled
Blow down water mass rate = 738 kg/hr Refer to Hysis simulation
Blow down water temperature = 140.00 Assume
Blow down water pressure = 5.00 barg Refer to Hysis simulation
Steam mass flow rate during normal condition = 4,640 kg/hr Refer to Hysis simulation
Boiler design capacity = 7,381 kg/hr Refer to Hysis simulation
Note = Oke due to steam demand is lower than steam design capacity
oC
Joule/kg.oC
oC
Joule/kg.oC
oC
oC
oC
oC
oC
Dearator Dimension Calculator
Internal Diameter : 1.000 m Select Units
Tan-Tan Length : 2.000 m
Volume of two heads : 0.26 m³ Select Head Type
Shell Volume : 1.57 m³
Total Volume : 1.83 m³
Heads SA : 2.17 m² Number of heads included in level calcula
Shell SA : 6.28 m²
Surface Area : 8.5 m²
Level SettingLevels Vapour Volume Volume Wetted Area
m m m³ % m²
Low low 0.100 0.90 0.089 4.9 1.40
Low 0.200 0.80 0.251 13.7 2.16
Normal 0.500 0.50 0.916 50.0 4.23
High 0.850 0.15 1.669 91.1 6.66
High High 0.900 0.10 1.744 95.1 7.05
Overflow 1.000 0.00 1.833 100.0 8.45
Total Residence Time :
Working Volume : 1.42 m³
Utilisation : 77.4 %
Flowrate : 0.74
Residence Time : 128.43 minutes Oke
Residence Time Specified by Client : 10.00 minutes
Venting
® BETWEEN LLL AND HLL (LV ON/OFF ACTION)
m3/hr
® For accomodating surge and hold up
Refer to Spiraxsarco (Typical 10 ~ 20 minutes)
Vendor to Advice
ID = 1000 mm
(L/ID) = 2
L = 2000 mm
Dearator Inlet Water Flow
Dearator Inlet Steam Flow
Shell
Wetted AreaTotal Vol. Retention Time Retention Time
From LALL Between Level Between Level
% m³ hours Minutes
16.6 - 0.121 7.24
25.6 0.2 0.219 13.15
50.0 0.8 0.902 54.09
78.8 1.6 1.020 61.18
83.4 1.7 0.101 6.06
100.0 1.7 0.121 7.24
Total Residence Time : 2.483 148.97
Volume of one head
Venting
BETWEEN LLL AND HLL (LV ON/OFF ACTION)
For accomodating surge and hold up
Vendor to Advice
Vendor to Advice
Overflow = 1000 mm
High high level = 900 mm
High level = 850 mm
Normal level = 500 mm
Low level = 200 mm
Low low level = 100 mm
Pressure 760 mmHg = 1 atm
Temperature
ppm ppm
0 14.4 14.425
10 11.3 11.219
20 8.85 8.839
30 7.2 7.172
40 6.2 6.036
50 5.6 5.213
60 4.95 4.482
70 4 3.661
80 3.05 2.639
90 1.8 1.414
100 0 0.125
A = 3.00E-09
B = -6.00E-07
C = 1.00E-05
D = 0.0042
E = -0.363
F = 14.425
Pressure 760 mmHg = 1 atm
Temperature Air solubility
gr/liter gr/liter ppm = mg/liter
40 4 0.0258 0.023 22.611
50 10 0.0223 0.022 21.500
60 16 0.0197 0.020 20.389
70 21 0.0177 0.019 19.278
80 27 0.0161 0.018 18.167
90 32 0.0147 0.017 17.056
100 38 0.0136 0.016 15.944
110 43 0.0126 0.015 14.833
120 49 0.0117 0.014 13.722
130 54 0.0107 0.013 12.611
140 60 0.0098 0.012 11.500
150 66 0.0089 0.010 10.389
160 71 0.0079 0.009 9.278
170 77 0.0068 0.008 8.167
180 82 0.0055 0.007 7.056
190 88 0.0041 0.006 5.944
200 93 0.0024 0.005 4.833
210 99 0.0004 0.004 3.722
A = -2.00E-04
B = 2.35E-02
O2 solubilityoC
oF oC
0 10 20 30 40 50 60 70 80 90 100
0
2
4
6
8
10
12
14
16
f(x) = 0.00000000288462 x⁵ − 0.000000622086 x⁴ + 0.0000128059 x³ + 0.00424636 x² − 0.3630111 x + 14.425175R² = 0.999694182664363
O2 solubility vs temperature
temperature, oC
o2
so
lub
ilit
y,
pp
m
0 10 20 30 40 50 60 70 80 90 100 110
0.0000
0.0050
0.0100
0.0150
0.0200
0.0250
0.0300
f(x) = − 0.000228761609907121 x + 0.0235249054007568R² = 0.971841437190846
air solubility vs temperature
temp, C
air
solu
bili
ty, g
r/lit
er
0 10 20 30 40 50 60 70 80 90 100
0
2
4
6
8
10
12
14
16
f(x) = 0.00000000288462 x⁵ − 0.000000622086 x⁴ + 0.0000128059 x³ + 0.00424636 x² − 0.3630111 x + 14.425175R² = 0.999694182664363
O2 solubility vs temperature
temperature, oC
o2
so
lub
ilit
y,
pp
m
0 10 20 30 40 50 60 70 80 90 100 110
0.0000
0.0050
0.0100
0.0150
0.0200
0.0250
0.0300
f(x) = − 0.000228761609907121 x + 0.0235249054007568R² = 0.971841437190846
air solubility vs temperature
temp, C
air
solu
bili
ty, g
r/lit
er
21962,Water-pp414-416
Wartsila-O-E-RT-WHR
steam9_blowdown
steam9_blowdown
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
presentation4-casestudyboiler
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
GTMEIC
5510-0136-00pp_low
5510-0136-00pp_low
21962,Water-pp414-416
21962,Water-pp414-416
21962,Water-pp414-416
21962,Water-pp414-416
21962,Water-pp414-416
21962,Water-pp414-416
21962,Water-pp414-416
Basic_Water_ocr
e481017
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
The Nalco Guide to Boiler Failure Analysis
GPSA Sect 18
http://www.gc3.com/Default.aspx?tabid=92
http://www.cewater.com/A55_BoilerSystem.html
http://www.cewater.com/A55_BoilerSystem.html
http://www.cewater.com/A55_BoilerSystem.html
http://gc3.com/Default.aspx?tabid=91
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http://gc3.com/Default.aspx?tabid=91
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http://gc3.com/Default.aspx?tabid=91
24_WaterTreatment_BoilerWater
24_WaterTreatment_BoilerWater
http://www.cleaverbrooks.com/Reference-Center/Boiler-Basics/Steam-or-Hot-Water.aspx
http://books.google.co.id/books?id=gK03hTP7NNcC&pg=PA84&lpg=PA84&dq=heat+losses+in+diesel+engine&source=bl&ots=_r4JXBz2Ls&sig=Y3urFd1KU7TfJZmVI_Enhu8W_Bo&hl=en&sa=X&ei=2MrxU6nHB4K3uAShk4CgDA&ved=0CDIQ6AEwAw#v=onepage&q=heat%20losses%20in%20diesel%20engine&f=false
214091248-Diesel-Engine-Power-Plants
http://www.engineeringtoolbox.com/air-solubility-water-d_639.html
http://www.engineeringtoolbox.com/air-solubility-water-d_639.html
Nalco Water Handbook
Deaerator in steam industrial system
http://www.spiraxsarco.com/resources/steam-engineering-tutorials/the-boiler-house/pressurised-deaerators.asp
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
Power-Plants-Product-Catalogue-2012-2nd-edition
GTMEIC
5510-0136-00pp_low
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
Nalco Water Handbook
GPSA Sect 18
AWT-2
http://www.gc3.com/Default.aspx?tabid=92
http://www.cewater.com/A55_BoilerSystem.html
http://www.cewater.com/A55_BoilerSystem.html
http://www.cewater.com/A55_BoilerSystem.html
http://gc3.com/Default.aspx?tabid=91
http://gc3.com/Default.aspx?tabid=91
http://gc3.com/Default.aspx?tabid=91
http://gc3.com/Default.aspx?tabid=91
http://gc3.com/Default.aspx?tabid=91
http://gc3.com/Default.aspx?tabid=91
EBMUD_WaterSmart_Guide_Thermodynamic_Processes
EBMUD_WaterSmart_Guide_Thermodynamic_Processes
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
Essentials for a Sound Boiler Water Treatment Program
http://www.cleaverbrooks.com/Reference-Center/Boiler-Basics/Steam-or-Hot-Water.aspx
http://books.google.co.id/books?id=gK03hTP7NNcC&pg=PA84&lpg=PA84&dq=heat+losses+in+diesel+engine&source=bl&ots=_r4JXBz2Ls&sig=Y3urFd1KU7TfJZmVI_Enhu8W_Bo&hl=en&sa=X&ei=2MrxU6nHB4K3uAShk4CgDA&ved=0CDIQ6AEwAw#v=onepage&q=heat%20losses%20in%20diesel%20engine&f=false
http://www.engineeringtoolbox.com/air-solubility-water-d_639.html
Nalco Water Handbook
Deaerator in steam industrial system
http://www.spiraxsarco.com/resources/steam-engineering-tutorials/the-boiler-house/pressurised-deaerators.asp
http://books.google.co.id/books?id=gK03hTP7NNcC&pg=PA84&lpg=PA84&dq=heat+losses+in+diesel+engine&source=bl&ots=_r4JXBz2Ls&sig=Y3urFd1KU7TfJZmVI_Enhu8W_Bo&hl=en&sa=X&ei=2MrxU6nHB4K3uAShk4CgDA&ved=0CDIQ6AEwAw#v=onepage&q=heat%20losses%20in%20diesel%20engine&f=false
http://www.spiraxsarco.com/resources/steam-engineering-tutorials/the-boiler-house/pressurised-deaerators.asp
http://books.google.co.id/books?id=gK03hTP7NNcC&pg=PA84&lpg=PA84&dq=heat+losses+in+diesel+engine&source=bl&ots=_r4JXBz2Ls&sig=Y3urFd1KU7TfJZmVI_Enhu8W_Bo&hl=en&sa=X&ei=2MrxU6nHB4K3uAShk4CgDA&ved=0CDIQ6AEwAw#v=onepage&q=heat%20losses%20in%20diesel%20engine&f=false
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