wedjspiaphigjiopgaedgda

1. ash activated carbon dry hydratedlime
vd
62
101
ppm mg/Nm3
6 6
ash 20% hydrated limesolution
Reagent Pump
180
155
27
22
%O2:
CO:
NOx:
SOx:
HCl:
PM:
225
250
78
27
60
0.00 4413
ash 60 113711
0.00 113.4
ash 160 549
0.00 4413
60 113711
sootblowers
ash
ash
3.8 5.26 3.8 5.26 0.50 147.51 15.0% FGR 2495.8
30 22904 30 22904 160 16420
wtr:
alts &slip: 286
calcium carbonateCaCO3
AdiabaticT 15.0% FGR
1224
n
‐0.30 374.05 ash 138.14
359 125890 1121
* inash
Cooling Water Pump
ash
1.01 764.6 0.10 234.5 0.14 2691.9
180 0 56 330 110 4226
* inash 1.55 5.26 0.11 377.0 0.11 377.0
30 68711 1.01 764.6 1.01 90 58224 90 29
180.3185 0 0
Fuel 1 12,466 83.1 1.01 2913.8
123.3 237 0
0.00 0.0 5.35 549.8 0.17 125.6
130 1450 5.88 550.2 0.60 377.0 30 54950
Fuel2 0 0.0 0.77 546.7 130 61419 90 0
0.00 0.0 130 61419
0.00 0.0 0.40 2818.6
180 0
Fuel3 0 0.0 0.57 597.7
0.00 0.0 142 61419
0.00 0.0
‐ #DIV/0!
54,950 55.18 0.40 335.2 0.10 334.9 ‐ 0
335 0.34 0.30 2724.9 0.10 377.0 80 0 80 0
2,313 2.32 134 87 0.11 2679.2 90 58195
912 0.91 102 13
0 0.00 0.00 0.00
15 0.01 5.38 1177.8 5.88 550.2
6,111 6.11 269 305 0.11 428.8 130 61419
0.47 64.4%
60.28 12.23
76,576 76.91 0.30 561.5 102 205
24,029 24.13 ash 134 218 0.27 377.0 0.27 2720.1
90 58195 130 3
8,588 8.63
15,442 15.51
0.00 903.0
1100 371
1.24 125.6 1.34 125.6 0.17 125.6
0.27 546.4 30 335 30 335 30 335
130 61419
m
3
/hr kWe
bottom ash
371 kg/hr
0.46 m3/hr
PlantWastes
fly ash & cake
1124 kg/hr
1.37 m3/hr
sludge
277 kg/hr
0.25 m3/hr
waste water
15442 kg/hr
15.51 m3/hr
Service Water
Blr Make UpWater
Cooling Wtr MkUp
Net kgstmprocess/unitfuel3
Make‐up Pump
0.32 64.4%
55.18 7.62
Predicted Utility Consumptions & Effluents
kg/hr m3
/hr
Net kWe/unit 0.82
fuel1
Net kWe/unitfuel2
Gross Effluent
Gross Heat Rate (lhv): 14462 kJ/kWhr
Net Heat Rate (lhv): 16456 kJ/kWhr
Spreader Fan & Motor
Net kgstmprocess/unitfuel1
Net kg /unit
stmprocess fuel2
Ca(OH) +CaCO
2dry 3dry
Net kWe/unitfuel3
Ca(OH)2aq orNaOHaq
Grate Pump
0.20 63.0%
66 22.3
NetEffluent
Feedwater Pump
5.61 69.8%
65.51 139.31
LEGEND 1
MPaa/kPag kJ/kg
°C kg/hr
Evap+Reclaimed+used
Activated Carbon
Scrubber Mk UpWtr
Total RawWater
G
Pumps &Fans
ΔP (MPa/kPa) %h
LEGEND 2
H2O dew point˚C:
SO3 dew point ˚C:
Make‐up Pump
RecirculationPump
TurbineGenerator
Primary FD Fan &Motor
Secondary FD Fan & Motor
FGR Fan & Motor
Evaporation & DriftLoss
Process Energy Use
Process ReturnPump
0.30 63.0%
ID Fan &Motor
information provided in this document is strictly confidential and for the sole use of BIB & it's Clients
PROJ: QS‐15060125 TURB: Condensing45 bar /400˚C Rev: 0c
PREDICTED POWER PLANT PERFORMANCE
Bolier Efficiency: 79.1% hhv
Bolier Efficiency: 88.2% lhv
Plant Net Efficiency: 19.6% hhv
Plant Net Efficiency: 21.9% lhv
Turbine Efficiency: 76.7% isentropic
Gross Gen. Power: 13000 kWe
Steam Plant Power: 550 kWe
Balance of Power Block Power: 1025 kWe
Fuel Prep'n + BoP Power: 1175 kWe
Net Power: 10250 kWe
BANGKOK INDUSTRIAL BOILERS CO., LTD.
223/29 Sanphawut Rd, 10th Flr, Country Tower A, Bangna, Bangkok 10260
tel: +66 2 361 5340 fax: +66 2 3615344
FULL HEAT & MASS BALANCE DIAGRAM
PROJECT: 13.0 MWe Gross CLIENT NAME: ARI for NAMBOINTEGRATED LANDFILL
DATE: 9‐Nov‐2015 LOAD: 100% FIRING CASE: 100% NB RDF3600
0.00 5.0
30 15
0.45 21.5
30 912
5.38 2790.9
269 0
0.00 113.4
160 74
0.35 64.4%
0.9 0.1
4.70 3214.1
405 61000
0.00 113.4
160 966
3.55 77.7%
140890 178.7
0.50 147.51
160 109470
‐0.20 939.82
816 125890
‐0.55 147.51
160 125890
‐1.55 147.51
160 125890
5.65 1025.8
244 59940
3.80 72.5%
19276 28.05
0.00 113.4
160 713
0 24.00
40 12466
0.00 3.55
30 0
1.55 5.26
30 68711
1.55 5.26
30 68711
0.45 251.02
60 912
5.78 550.0
130 59940
4.60 3203.8
400 300
2.50 60.5%
5992 6.88
0.25 69.0%
153.30 15.43
5.35 2790.9
269 59635
4.80 3212.4
405 61000
5.05 74.4%
20609 38.8
Fuel 1Name: NB RDF 3600
Mass Input: 100.0% hhv(kJ/kg): 16,826
HeatInput: 100.0% lhv(kJ/kg): 15,073
C: 39.00% O2: 17.28%
H: 5.20% H2O: 25.00%
N: 1.10% ASH: 11.50%
S: 0.42% Cl: 0.50%
UBC*: 3.50% ExcessAir: 40%
0 0
0 0
0 24.00
40 0
0 0
0 0 0.10 171.6
41 273600
‐0.24 708.89
635 125890
0.01 191.8
46 0 5.78 550.1
130 59940
0.01 2347.0
48 53668
Fuel 2 Name: NB RDF 3350
Mass Input: 0.0% hhv (kJ/kg): 15,724
HeatInput: 0.0% lhv(kJ/kg): 14,026
C: 37.00% O2: 16.58%
H: 4.95% H2O: 25.00%
N: 1.05% ASH: 14.50%
S: 0.42% Cl: 0.50%
UBC*: 3.50% ExcessAir: 40%
5.38 2790.9
269 59635
‐0.30 300.2
359 1040
1.01 2913.8
237 0
5.78 550.1
130 29
1.20 2969.4
265 330
3.8 5.26
30 22904
1.01 2913.8
237 2805
1.01 2913.8
237 0
0.40 75.0%
3734.96 601
1.01 2913.8
237 0
1.01 2913.8
237 2805
5.65 1025.8
244 59940
‐0.55 147.51
160 125890
0.01 199.3
48 53668
5.38 2790.9
269 59635
0 24.00
40 0
Fuel 3 Name: NB RDF3850
Mass Input: 0.0% hhv (kJ/kg): 17,928
HeatInput: 0.0% lhv(kJ/kg): 16,119
C: 41.00% O2: 17.98%
H: 5.45% H2O: 25.00%
N: 1.15% ASH: 8.50%
S: 0.42% Cl: 0.50%
UBC*: 3.50% ExcessAir: 40%
0.00 280.6
359 74
0.00 3.6
30 0
0.35 64.4%
6.14 0.93
0.10 126.2
30 6111
1.70 3143.9
350 85 0.00 29.3
60 5
‐0.20 664.4
816 1114
0 5.26
Air
30 22904
o
C RH
0 5.26 30 70%
30 68711
4.60 3203.8
400 60700 1.55 72.5%
59098 35.08
Gross Power (kWe): 13000
Turbine Generator ɳ(%):
Turbine Isentropic ɳ (%):
25.1
76.7
Rankin Cycle ɳ (%): 29.3% 0.101 1632.5
37 53588
117 kW fan power
0.005% driftloss
28 wet bulb °C dsg
50 Cycles of
Concentration
0.10 171.6
41 3715454
0.50 138.1
33 3715694
0.50 138.1
33 3441854
0.49 125.6
30 54950
Primary SHTR
Fuel 1
Combustion
Steam
Drum
Economizer 1
Deaerator
Feedwater Pump
0.11 272.1
65 445
Stack
Primary FD Fan
IDFan
Flash
Tank
Condenser Cooling
Tower
Make‐Up Pump
Make‐up Pump
1.17 63.0%
0.34 0.17
Feedwater
Preheater
Secondary FD Fan
Air Preheater #2
Condensate Condensate Pump
Pump
Secondary
Air
Primary
Air
Secondary
Air
PrimaryAir
‐0.55 147.51
160 125890
Secondary Air
Process
Cooling Pump
Fuel 2
Cooling
Make‐up
Pump
Ash
Primary
Air
Blowdown
Tank
Ejector
Attemperation Pump
0.70 63.0%
0.00 0.00
Process Return Pump
Air Preheater #1
Cyclone
Separator
Condensate
Tank
Evaporator
Bank
Dry ‐ WetAPC
Make‐Up
Preheater
seeMake‐Up
Preheater
Grate Pump
water‐
cooled
grate
Turbine G
Auxiliary
Cooling
to
Blowdown
0.11 138.1
33 240
from CoolingTower
system losses
MP
DE
DE
to
Process
from
MP
Fuel 3
LP Htr
LP
LP
Secondary SHTR
Primary Air Heater
Economizer 2
Secondary Air Heater