3. INTER LOCK
START Normal state
BELT CONVEYOR NO.
FORM RUNING NO. FORM RUNING NO.
B.1 OFF ▬ ON 9
B.2 ON 2 ON 2
B.3 ON 1 ON 1
B.4 ON 4 ON 4
B.5 ON 3 ON 3
B.6 ON 5 OFF ▬
B.7 ON 6 OFF ▬
B.8 ON 7 OFF ▬
B.9 ON 8 ON 8
10. COMBUSTION AIR SYSTEM
ก F ก F ก Oxygen
Fก ก F F F ก 4 F
Oxygen ,
Fuel ,
Heat( F )
Chemical reaction( ก )
ก 4 F กF ก F F F F
F ก Fก
11. F F F
F ก F F ก F
กก F
Bagasse analysis
Hydrogen : 3.04 %
Carbon : 23.
23.24 %
Oxygen : 22.
22.08 %
Moisture : 50.
50.0 %
HHV : 2272Kcal / Kg
2272Kcal
13. ก F กก F F ก ก F
F Fก F F ก
ก F ก ก Fก
F 3 F ก F F
Carbon
Hydrogen
Sulphur
14. Carbon F ก F ก ก F FF
Sulphur ก กF F ก Fก ก F F F
sulphur F ก
Oxygen F F FกF F F
Nitrogen ก F F F ก F ก F
ก Fก F F
Ash F F Fก ก
- F ก F F F
- F ก ก ก ก F (Corrosion)
-ก กก F (Erosion) Fก ก ก
- ก F F ก Ash
18. F F F ก
Boiler water Quality Recommendation At Increasing Pressure ( All value,except ; given in ppm ) in Sugar Industry
Intermediate
Low to 250 psi 250 -300 psi 300 - 450 psi
IJT 60kg/cm2 0 - 15 kg/cm2 15 - 20 kg/cm2 2 0 - 30 kg/cm2
Total hardness, as Ca CO3 Nil 0 0 0
Total Alkalinty, as Ca CO3 700 700 700
Hydroxide, as Ca CO3 150 - 300 150 - 300 130
Silica, as SiO2 2.5 100 - 133 50 - 67 50 - 67
Dissolved Oxygen 0.015 0.015 0.015
Total Dissolved Solid 100 < 2,500 < 2,000 < 1,500
Suspended Solid < 600 < 300 < 200
Conductivity, micro - mho / cm 200 < 3,500 < 2,850 < 2,150
PH 9.5-10.5 11 - 11.8 11 - 11.5 10.5 - 11.5
Oil 1.0 1.0 1.0
Sodium Sulphite ; as Na2 SO3 30 - 60 30 - 40 20 - 30
Phosphate ; as PO43- 20 20 - 40 20 - 40 5. - 15
Hydrazine ; as N2 H4 0.1 - 0.3 0.1 - 0.4 0.1 - 0.5
ก ก F
2531 5 ก
ก F
19. RAW WATER
FILTERING
FILTERED WATER
SOFTENING RO
DEMINERALIZATION
MAKE - UP WATER
THERMAL
DEAERATION
20. THERMAL CONDENSATE
DEAERATION POLISHING
FEED
WATER
ADDITTIVE
INJECTION
CONDENSATE
160°C BOILER
WATER STEAM
BLOW - DOWN
IJT
21. Water Flow Path
ก (Circulation) boiler F 2 ก
ก ก ก supply F ก
Fก
ก F F boiler furnace ก
ก waterwalls F ก ก ก
F ก overheat ก
22. F F กก F กF Fก steam
F F ก F F carbon steel F
482 °c steam/water mixture F F
260 °c superheater steam F 500 °c
gas ก F >1,000 °c superheater F 600 °c
steam flow F F ก F Fก (Limit) F
23. ก Start-up F Steam Flow กก vent drain
superheat F ก F F superheat
Fก superheater steam F firing
F F furnace gas temp. ก 537°c กF ก
c load steam
flow F F superheater ก F superheater metal temperature
กF F F( 600°c )
F firing rate ก F superheater metal
temperature ก F F F กF F F
steam F F F F steam F
26. ก (Circulation)
F superheater F F
fluid ( ) F F F F
ก F F F ก F safe limit F F F
ก F F fluid ก F F F F ก (overheat)
ก F water walls F ก 3
Natural circulation
Forced circulation
circulating pump F ก
Once through F
29. F acidity F F ( F ก )
acidity F pH
F pH =7 F ก
F pH กF 7 ก
F pH กF 7 F
F F F F ก ก ก กF F F F ก
30. Acid Attcak F pH กF 7 ก
ก ก ก ก F F
Caustic Attack F pH ก F 7 ก F
F กก F F F ก
ก ก corrosion F F pH ก กF
31. scale
ก F F F
F F ก overheat ก
Scale ก ก F ก F
(suspended solids)
(dissolved solids)
ก , , ก ก F ก ก ก F clarifier
ก F F F F กF silica
(Sio2- ก ก F) ก ก ก,
ก
32. F ก ก F ก ก steam drum
F ก ก ก F F F F F
( ก ก F F กF ก )
F F F F ก ก ก F steam drum
ก F F F ก
F ก กก ก ก F ก
concentration ( F F ) F continuous blowdown
33. ก (phosphate) F
F F ก F ก ก F F
ก F ก Sludge
( , ก )
ก ก ก hard scale ( ก )
ก continuous blowdown
ก F F F ก
F F
34. ก ก
F F F F
silica , phosphate , total solids ( F ) pH