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BOILER
Mae Sod Clean Energy Co., Ltd.



        IJT
B9




                       B7                     B8



           B6                         Start
                                     Normal state
      B4




B3
                       BOILER
            B5




     B2
                                        Belt size
                                B1   1000 mm.BW.x33.5 M.L.   11 kw
                                B2   1000 mm.BW.x14.7 M.L.   7.5 kw
                                B3   1000 mm.BW.x214 M.L.    30 kw
            B1
                                B4   1000 mm.BW.x14.7 M.L.   7.5 kw
                                B5   1200 mm.BW.x43 M.L.     22 kw
                                B6   900 mm.BW.x38 M.L.      11 kw
                                B7   900 mm.Bw.x73 M.L.      15 kw

           MILL                 B8   1500 mm.BW.x9 M.L.      5.5 kw
                                B9   900 mm.BW.x89 M.L.       11 kw
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
Steam Boiler
                        Cap.      : 95 TPH
                        Pres.     : 60 Bar
                        Temp. : 500°C
              DRUM      F.W.P.    : 160°C
                        Bag. feed : 4 set
                        Bag. Ext. : 13000kg/hr



    FURNACE




    STOKER




ก              , , กF                  F   IJT Boiler
Boiler                   F 2 F

         F       F       F

    F        F       F
Boiler       F   ก   4 F   F

    Air & Gas system

    Water & Steam system

    Fuel Handling system

    Ash Handling system
200 C



superheat

economizer
   800 C      160 C
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
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
ก
        F    F               F

Turbulence           ก   ก       F

Time             ก       F
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
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
F F   ก กF
WaterWalls
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
RAW WATER




    FILTERING




FILTERED WATER




    SOFTENING RO
  DEMINERALIZATION




MAKE - UP WATER




    THERMAL
   DEAERATION
THERMAL                                    CONDENSATE
DEAERATION                                   POLISHING




  FEED
 WATER
                      ADDITTIVE
                      INJECTION




                                            CONDENSATE




    160°C    BOILER
             WATER                  STEAM


                      BLOW - DOWN

                          IJT
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
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
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
ก   F   F       ( Heat Transfer )




ก               ก



                           ก   F
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
furnace
ก   ก   F
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
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
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
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
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
ก          ก
                    F            F        F   F
silica , phosphate , total solids (               F   )   pH

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  • 1. BOILER Mae Sod Clean Energy Co., Ltd. IJT
  • 2. B9 B7 B8 B6 Start Normal state B4 B3 BOILER B5 B2 Belt size B1 1000 mm.BW.x33.5 M.L. 11 kw B2 1000 mm.BW.x14.7 M.L. 7.5 kw B3 1000 mm.BW.x214 M.L. 30 kw B1 B4 1000 mm.BW.x14.7 M.L. 7.5 kw B5 1200 mm.BW.x43 M.L. 22 kw B6 900 mm.BW.x38 M.L. 11 kw B7 900 mm.Bw.x73 M.L. 15 kw MILL B8 1500 mm.BW.x9 M.L. 5.5 kw B9 900 mm.BW.x89 M.L. 11 kw
  • 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
  • 4.
  • 5. Steam Boiler Cap. : 95 TPH Pres. : 60 Bar Temp. : 500°C DRUM F.W.P. : 160°C Bag. feed : 4 set Bag. Ext. : 13000kg/hr FURNACE STOKER ก , , กF F IJT Boiler
  • 6. Boiler F 2 F F F F F F F
  • 7. Boiler F ก 4 F F Air & Gas system Water & Steam system Fuel Handling system Ash Handling system
  • 9.
  • 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
  • 12. F F F Turbulence ก ก F Time ก F
  • 13. 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
  • 15.
  • 16.
  • 17. F F ก กF WaterWalls
  • 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. 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
  • 24. F F ( Heat Transfer ) ก ก ก F
  • 25.
  • 26. (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
  • 28. ก 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. (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 F F F F silica , phosphate , total solids ( F ) pH