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High Pressure and efficient Boilers for Cogeneration applications ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
[object Object],[object Object],[object Object],[object Object],[object Object]
The Major advantage of Co- Gen power is ;- ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
CO-GENERATION in SUGAR MILLS
How Cogeneration Saves Energy
COGENERATION PLANT LAYOUT Feed water PRDS BOILER ALTERNATOR TURBINE TO PROCESS TO PROCESS Fuel Air TO POWER SUPPLY CONDENSER TO COOLING TOWER
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],Benefits of cogeneration
Steps for conservation 1.Government of India enforced the energy conservation act 2001 with effect from 1.3.2002. 2.The initial phase of 5 years would be implementation of the act .  3.The act provides mainly for efficient use of energy and its conservation. 4.Industry using
Mandatory Requirement of Act ,[object Object],[object Object]
Energy Saving potential areas in sugar industries 1.Convertion from low Pressure to HP  Boilers 2.Steam Boilers (Reducing moisture percentage  in Bagasse) 3.Crushing section 4.Evaporator section
[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],FEASIBILITY STUDY (TYPICAL STEPS)
CASE STUDIES ,[object Object],[object Object],[object Object],[object Object]
RETROFITTING ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Case Studies ,[object Object]
Comparison of performance during various seasns from 1998 to 2002 40.7 4.84 7.06 11.9 11.9 8.96 11.23 10.3 7.06 % Lost % on Available Hours 14 53.7 59.3 51.08 110 51-05 110-25 109-25 97-15 97-10 Hrs-Mts   General Cleaning 13 94.3 66 4 70 70-00 24-25 4.-00 53-55 11.-10 Hrs-Mts   Electrical 12 97.5 176 4.5 181 180-45 24-55 4.-30 59-30 64-35 Hrs-Mts   Mechanical 11         204-10 154-55 142-15 57-50 6.-00 Hrs-Mts   No Cane 10 Rs 51.57 lakhs per season                     DOWN TIME ANALYSIS   4.19 1.08 24.68 25.8     25.18 25.46 24.68 KWH   Power / Ton of Cane 9         49.74 49.45 48.75 50.71 48.76 %   Steam % Cane 8 2.32 1.19 50.11 51.3 51.3 50.4 50.11 50.56 50.66 %   Bagasse Moisture 7         8.187 9.23 9.758 9.11 9.51 %   Recovery 6         3918.42 4247.98 4063.22 3857 4217.33 MT   Crop Day Average 5         4614.77 4783.32 4576.34 4311.12 4541.39 MT   Crushing Rate/24 hours 4         4230.29 4385.11 4194.98 3951 4162.95 MT   Crushing Rate/22 hours 3         188 165 159 191 173     No. of Crop Days 2         736663 700916 646051 736838 729598 MT   Cane Crushed 1         Actual Actual Actual Actual Actual UOM   PARTICULARS SL NO. % Saving scope Diff Min Max 1998-99 1999-00 2000-01 2001-02 2002-03      
Coomparison of performance with best two seasons       6173-40 3816-33 4148-39 HRS Total Available Hours 15         80-120 90to130 % Sugar quality ICUMSA 14       1.73 1.78 1.86 % Pol % Bagasse 13       50.52 50.11 50.66 % Bagasse Moisture 12           78.18 % Cane Preparatory Index 11       31.22 30.32 29.56 % Bagasse % Cane 10       4.415 4.449 4.52 % Molasses % Cane 9       0.037 0.049 0.1 % d)Unknown Loss         0.99 1.211 1.27 % c)Final Molasses         0.05 0.07 0.08 % b)Filter Cake         0.54 0.541 0.55 % a)Bagasse         1.617 1.871 2 % Total Losses 8       10.963 11.618 11.5 % Pol in Cane 7       9.357 9.758 9.51 %   Recovery 6       2796.416 4063.216 4217.3 MT Crop Day Average 5       3076.152 4576.344 4541.4 MT Crushing Rate / 24 hours 4       2819.806 4149.982 4162.9 MT Crushing Rate / 22 hours 3       258 159 173   No. of Crop Days 2       721475.5 646051.4 729598 MT Cane Crushed 1                           2500 5000 5000 MT Plant Sanctioned Capacity                       %saving scope Min  Max 1994-95 2000-01 2002-03 UOM   PARTICULAR SL NO
  Possible increased in crushing of cane per season= 24220 MT/season   Remarks:Possible saving of running hours =128 hours     128 hours 213.8 341.8                     694.65 1477.49 2325 Qtls   Process Stock-Brown Sugar 30       8.82 11.23 7.06 %   Lost % on Avaible Hours 29 33.17 112.166 167.83 168-45 167-50 112-10 HRS   Others 28 11.2 97.16 109.416 164-00 109-25 97-10 HRS   General Cleaning 27       5.-30 4.-00 11.-10 HRS   Electrical 26 93 4.5 64.58 152-15 4.-30 64-35 HRS   Mechanical 25       54-15 142-15 6.-00 HRS   No Cane 24                 DOWN TIME ANALYSIS         9.83 9.923 9.68 % Peak Period Recovery 23 Rs 21.62 lakhs/season       25.18 24.68 KWH Power / Ton of Cane 22 2.77 47.41 48.76 47.41 48.75 48.76 % Steam % Cane 21       93.43 91.66 91.27 % Reduced B.House Extraction 20       95.89 96.02 95.73 % Reduced Mill Extraction 19       3.69 3.78 4.12   Milling Loss 18       295.62 293.58 259.14 % Imbibition% Fiber 17       544-45 428-25 292-55 HRS Down Time Hours 16
      75-45 10.-20 21-35 12.-40 20-45 5.-55 5.-00 0-00 HRs b)Engineering(Mech&Elec)         6.-00 0-00 0-00 0-00 0-00 0-00 6.-00 0-00 HRs a)Want of Cane         292-55 19-35 51-50 43-45 38-15 35-25 102-20 1.-45 HRs Stoppage Hours 8       3855-44 172-28 692-10 676-15 705-45 636-35 641-40 330-51 HRs Total Working Hours 7       4148-39 192-03 744-00 720-00 744-00 672-00 744-00 332-36 HRs Total Available Hours 6       167 8 31 29 31 27 27 14 Days Season Days-Crushing Day 5       173 8 31 30 31 28 31 14 Days Season Days-Crop Day 4       696220 25397 114975 13123.3 14747 13227.5 113875 3100 Qtls Sugar Production 3       9.61 6.68 8.75 10.14 10.66 10.06 8.84 8.05 %   Recovery 2       729598 21860 128072.4 127097 140288 134980 128742 48558.3 MT Cane Crushed 1                               %saving Min Max TOTAL JUNE.03 MAY.03 APL.03 MAR.03 FEB.03 JAN.03 DEC.02 UOM   PARTICULARS SL NO ANALYSIS OF PERFORMANCE FOR THE SEASON 2002-2003(MONTH WISE)
Remarks: Saving of power in terms of money will be Rs 77.15 lakhs /month. @Rs 5.00/KWH 32.2 23.27 34.3 24.63 34.3 25.57 25.13 24.69 23.27 23.61 23.61 Units Power per Ton of Cane 23       48.76 70.91 48.18 47.96 48.37 47.62 47.69 49.47 % Steam % Cane 22       4.52 4.93 4.85 4.66 4.61 4.37 4.17 4.26 % Molasses % Cane 21       31.35 34.15 31.55 31.51 31.71 30.99 30.45 29.6 % Final Molasses Purity 20       29.56 31.63 30.75 30.19 29.42 29.06 28.82 27.53 % Bagasse % Cane 19       1.86 1.9 1.84 1.84 1.85 1.86 1.88 1.89 % Pol % Bagasse 18       91.27 90.46 91.14 91.19 91.15 91.39 91.49 91.66 % Reduced BH. Extraction 17       95.73 94.48 95.64 96.02 96.12 95.88 95.31 94.79 % Reduced Mill Extraction 16       0.1 0.288 0.263 0.06 0.058 0.057 0.062 0.069 % d)Unknown         0.08 0.105 0.087 0.08 0.084 0.083 0.081 0.08 % c)Filter Cake         0.55 0.6 0.57 0.56 0.545 0.54 0.543 0.521 % b)Bagasse         1.27 1.45 1.369 1.31 1.306 1.218 1.143 1.13 % a)Final Molasses         2 2.443 2.284 2.01 1.993 1.898 1.828 1.8 % Total Losses 15       11.5 9.11 11.025 12.14 12.627 11.947 10.656 9.844 % Pol % Cane 14       4368.85 2732.5 4131.368 4382.66 4525.41 4999.27 4768.2 3468.45 MTs Crushing Day Average 13       4217.33 2732.5 4131.368 4236.57 4525.41 4820.73 4153 3468.45 MTs Crop Day Average 12       4541.39 2731.8 5037.504 4510.66 4771 5088.96 4815.3 3522.43 MTs Crushing Rate / 24 hours 11       4162.95 2504.2 4617.712 4134.77 4373.12 4664.88 4414 3228.9 MTs Crushing Rate / 22 hours 10       7.06 10.-20 6.97 6.08 5.14 5.27 13.75 0.53 % Down Time % Available 9       112-10 9.-15 30.15 1.-50 17-00 3.-15 48-50 1.-45 HRs   e)Others         97-10 0-00 0-00 29-15 0-00 26-15 41-40 0-00 HRs d)General Cleaning         1.-20 0-00 0-00 0-00 0-30 0-00 0-50 0-00 HRs   c)Process  
 
 
 
BY Technological Up gradation ,[object Object],[object Object],[object Object],[object Object],[object Object]
Acquire Best Available Technology in New Projects ,[object Object],[object Object],[object Object],[object Object],[object Object]
KCP Boiler 70 TPH, 43.4ata & 400 ºC TBW Boiler 70 TPH, 67ata & 485 ºC 9.74   MW, 70 tph TG Comparison Prevailing System Proposed System Multi fuel Boiler 105ata, 525 º C, 88% Topping up TG set 18.6 MW, 61 tph TG GEC Turbine SIEMENS Turbine C C 11 KV BUS 9.74   MW, 70 tph TG 18.6 MW, 61 tph TG C C GEC Turbine SIEMENS Turbine 67ata & 485 ºC 42ata & 400 ºC
Actual Thermal Efficiency of existing power plant on date Heat value of KPC boiler  ≈ 767 Kcal/kg (from steam table) (at 43.4 ata and 400ºC) Then net heat value of KPC boiler  ≈ 767 – 105 ≈ 662 Kcal/kg. Thermal efficiency of KPC boiler = η th  = (Net heat value * Total Steam generation) / (CV of  the bagasse * total bagasse consumption)   η th  = (662 * 122759) / (2277 * 61672)   = 57.99% ≈ 58% ( against 69% of design)  Heat value of TBW boiler = 807.7 Kcal/kg (From steam table) (at 67 ata and 485 ºC) Then net heat value of TBW boiler ≈ 807.7 – 105 ≈ 702.7 Kcal/kg GCV of coal = (CV of coal * total coal consumption) / Total fuel consumption   = (5500 * 4622) / 56213 = 452.22 Kcal/kg GCV of Bagasse = (CV of bagasse * total bagasse consumption) / Total fuel consumption   = (2277 * 51591) / 56213 = 2089.77 Kcal/kg Then net GCV = 452.22 + 2089.77 = 2542 Kcal/kg
Then net heat gain = heat gain * steam required for cane * efficiency of Topping TG set   = 13.8 * 125*10 3  * 0.9   = 1552.5 Kcal/kg Total power generation = 1552.5/860 = 1.8 MW Transfer rate = 1800 * 24 * 330 * 1.96 =  2.79  crore.
Thermal efficiency of TBW boiler = η th  = (Net heat value * Total Steam generation) /    (Net GCV * total fuel consumption)   = (702.7 * 129399) * 100 / (2542 * 56213)   η th  =  63 % (against  71.75 % of design) Average thermal efficiency of KPC & TBW boiler = (58+63) / 2 =  60.5 %
Expected direct efficiency of multifuel boiler = 84% Then fuel saving = 84 – 60.5 = 23.5% Cost of fuel saving = Actual cane crushed * % of fuel caned * % fuel save for 02-03  = 729598 * 0.3 * 0.235   = Rs. 51436.65 Then total saving of bagasse = 51437 * 500   = Rs. 2,57,815   =  2.57  crore Net gain in power = 2.79 crore Net gain in fuel save = 2.57 crore Then total gain = 2.79+2.57 =  5.36  crore
Heat value of AFBC boiler = 821.5 Kcal/kg (from steam table) (at 515 º C and 105 kg/cm 2 ) Then net heat gain = 821.5 – 807.7   = 13.8 Kcal/kg From data Budgeted crane crushed/year = 775000 M.T Actual crane crushed/year = 72598.401 M.T No. of crop days = 170 days % Steam required for crane = 48% % of bagasse in cane = 30% Then steam required for cane/hr. = (budgeted cane crushed * %steam reqd. for cane) /   (No. of days * 24)   = (775000 * 0.48) / (170*24)   = 91.176 tph   ≈ 100 tph For maximum efficiency steam required for cane/hr = 100/0.80 = 125 tph
The Major advantage of Co- Gen power is ;- ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
STEPS FOOR SAVINGS ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

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13 b shukla

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  • 6. COGENERATION PLANT LAYOUT Feed water PRDS BOILER ALTERNATOR TURBINE TO PROCESS TO PROCESS Fuel Air TO POWER SUPPLY CONDENSER TO COOLING TOWER
  • 7.
  • 8. Steps for conservation 1.Government of India enforced the energy conservation act 2001 with effect from 1.3.2002. 2.The initial phase of 5 years would be implementation of the act . 3.The act provides mainly for efficient use of energy and its conservation. 4.Industry using
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  • 10. Energy Saving potential areas in sugar industries 1.Convertion from low Pressure to HP Boilers 2.Steam Boilers (Reducing moisture percentage in Bagasse) 3.Crushing section 4.Evaporator section
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  • 15. Comparison of performance during various seasns from 1998 to 2002 40.7 4.84 7.06 11.9 11.9 8.96 11.23 10.3 7.06 % Lost % on Available Hours 14 53.7 59.3 51.08 110 51-05 110-25 109-25 97-15 97-10 Hrs-Mts   General Cleaning 13 94.3 66 4 70 70-00 24-25 4.-00 53-55 11.-10 Hrs-Mts   Electrical 12 97.5 176 4.5 181 180-45 24-55 4.-30 59-30 64-35 Hrs-Mts   Mechanical 11         204-10 154-55 142-15 57-50 6.-00 Hrs-Mts   No Cane 10 Rs 51.57 lakhs per season                     DOWN TIME ANALYSIS   4.19 1.08 24.68 25.8     25.18 25.46 24.68 KWH   Power / Ton of Cane 9         49.74 49.45 48.75 50.71 48.76 %   Steam % Cane 8 2.32 1.19 50.11 51.3 51.3 50.4 50.11 50.56 50.66 %   Bagasse Moisture 7         8.187 9.23 9.758 9.11 9.51 %   Recovery 6         3918.42 4247.98 4063.22 3857 4217.33 MT   Crop Day Average 5         4614.77 4783.32 4576.34 4311.12 4541.39 MT   Crushing Rate/24 hours 4         4230.29 4385.11 4194.98 3951 4162.95 MT   Crushing Rate/22 hours 3         188 165 159 191 173     No. of Crop Days 2         736663 700916 646051 736838 729598 MT   Cane Crushed 1         Actual Actual Actual Actual Actual UOM   PARTICULARS SL NO. % Saving scope Diff Min Max 1998-99 1999-00 2000-01 2001-02 2002-03      
  • 16. Coomparison of performance with best two seasons       6173-40 3816-33 4148-39 HRS Total Available Hours 15         80-120 90to130 % Sugar quality ICUMSA 14       1.73 1.78 1.86 % Pol % Bagasse 13       50.52 50.11 50.66 % Bagasse Moisture 12           78.18 % Cane Preparatory Index 11       31.22 30.32 29.56 % Bagasse % Cane 10       4.415 4.449 4.52 % Molasses % Cane 9       0.037 0.049 0.1 % d)Unknown Loss         0.99 1.211 1.27 % c)Final Molasses         0.05 0.07 0.08 % b)Filter Cake         0.54 0.541 0.55 % a)Bagasse         1.617 1.871 2 % Total Losses 8       10.963 11.618 11.5 % Pol in Cane 7       9.357 9.758 9.51 %   Recovery 6       2796.416 4063.216 4217.3 MT Crop Day Average 5       3076.152 4576.344 4541.4 MT Crushing Rate / 24 hours 4       2819.806 4149.982 4162.9 MT Crushing Rate / 22 hours 3       258 159 173   No. of Crop Days 2       721475.5 646051.4 729598 MT Cane Crushed 1                           2500 5000 5000 MT Plant Sanctioned Capacity                       %saving scope Min Max 1994-95 2000-01 2002-03 UOM   PARTICULAR SL NO
  • 17.   Possible increased in crushing of cane per season= 24220 MT/season   Remarks:Possible saving of running hours =128 hours     128 hours 213.8 341.8                     694.65 1477.49 2325 Qtls   Process Stock-Brown Sugar 30       8.82 11.23 7.06 %   Lost % on Avaible Hours 29 33.17 112.166 167.83 168-45 167-50 112-10 HRS   Others 28 11.2 97.16 109.416 164-00 109-25 97-10 HRS   General Cleaning 27       5.-30 4.-00 11.-10 HRS   Electrical 26 93 4.5 64.58 152-15 4.-30 64-35 HRS   Mechanical 25       54-15 142-15 6.-00 HRS   No Cane 24                 DOWN TIME ANALYSIS         9.83 9.923 9.68 % Peak Period Recovery 23 Rs 21.62 lakhs/season       25.18 24.68 KWH Power / Ton of Cane 22 2.77 47.41 48.76 47.41 48.75 48.76 % Steam % Cane 21       93.43 91.66 91.27 % Reduced B.House Extraction 20       95.89 96.02 95.73 % Reduced Mill Extraction 19       3.69 3.78 4.12   Milling Loss 18       295.62 293.58 259.14 % Imbibition% Fiber 17       544-45 428-25 292-55 HRS Down Time Hours 16
  • 18.       75-45 10.-20 21-35 12.-40 20-45 5.-55 5.-00 0-00 HRs b)Engineering(Mech&Elec)         6.-00 0-00 0-00 0-00 0-00 0-00 6.-00 0-00 HRs a)Want of Cane         292-55 19-35 51-50 43-45 38-15 35-25 102-20 1.-45 HRs Stoppage Hours 8       3855-44 172-28 692-10 676-15 705-45 636-35 641-40 330-51 HRs Total Working Hours 7       4148-39 192-03 744-00 720-00 744-00 672-00 744-00 332-36 HRs Total Available Hours 6       167 8 31 29 31 27 27 14 Days Season Days-Crushing Day 5       173 8 31 30 31 28 31 14 Days Season Days-Crop Day 4       696220 25397 114975 13123.3 14747 13227.5 113875 3100 Qtls Sugar Production 3       9.61 6.68 8.75 10.14 10.66 10.06 8.84 8.05 %   Recovery 2       729598 21860 128072.4 127097 140288 134980 128742 48558.3 MT Cane Crushed 1                               %saving Min Max TOTAL JUNE.03 MAY.03 APL.03 MAR.03 FEB.03 JAN.03 DEC.02 UOM   PARTICULARS SL NO ANALYSIS OF PERFORMANCE FOR THE SEASON 2002-2003(MONTH WISE)
  • 19. Remarks: Saving of power in terms of money will be Rs 77.15 lakhs /month. @Rs 5.00/KWH 32.2 23.27 34.3 24.63 34.3 25.57 25.13 24.69 23.27 23.61 23.61 Units Power per Ton of Cane 23       48.76 70.91 48.18 47.96 48.37 47.62 47.69 49.47 % Steam % Cane 22       4.52 4.93 4.85 4.66 4.61 4.37 4.17 4.26 % Molasses % Cane 21       31.35 34.15 31.55 31.51 31.71 30.99 30.45 29.6 % Final Molasses Purity 20       29.56 31.63 30.75 30.19 29.42 29.06 28.82 27.53 % Bagasse % Cane 19       1.86 1.9 1.84 1.84 1.85 1.86 1.88 1.89 % Pol % Bagasse 18       91.27 90.46 91.14 91.19 91.15 91.39 91.49 91.66 % Reduced BH. Extraction 17       95.73 94.48 95.64 96.02 96.12 95.88 95.31 94.79 % Reduced Mill Extraction 16       0.1 0.288 0.263 0.06 0.058 0.057 0.062 0.069 % d)Unknown         0.08 0.105 0.087 0.08 0.084 0.083 0.081 0.08 % c)Filter Cake         0.55 0.6 0.57 0.56 0.545 0.54 0.543 0.521 % b)Bagasse         1.27 1.45 1.369 1.31 1.306 1.218 1.143 1.13 % a)Final Molasses         2 2.443 2.284 2.01 1.993 1.898 1.828 1.8 % Total Losses 15       11.5 9.11 11.025 12.14 12.627 11.947 10.656 9.844 % Pol % Cane 14       4368.85 2732.5 4131.368 4382.66 4525.41 4999.27 4768.2 3468.45 MTs Crushing Day Average 13       4217.33 2732.5 4131.368 4236.57 4525.41 4820.73 4153 3468.45 MTs Crop Day Average 12       4541.39 2731.8 5037.504 4510.66 4771 5088.96 4815.3 3522.43 MTs Crushing Rate / 24 hours 11       4162.95 2504.2 4617.712 4134.77 4373.12 4664.88 4414 3228.9 MTs Crushing Rate / 22 hours 10       7.06 10.-20 6.97 6.08 5.14 5.27 13.75 0.53 % Down Time % Available 9       112-10 9.-15 30.15 1.-50 17-00 3.-15 48-50 1.-45 HRs   e)Others         97-10 0-00 0-00 29-15 0-00 26-15 41-40 0-00 HRs d)General Cleaning         1.-20 0-00 0-00 0-00 0-30 0-00 0-50 0-00 HRs   c)Process  
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  • 25. KCP Boiler 70 TPH, 43.4ata & 400 ºC TBW Boiler 70 TPH, 67ata & 485 ºC 9.74 MW, 70 tph TG Comparison Prevailing System Proposed System Multi fuel Boiler 105ata, 525 º C, 88% Topping up TG set 18.6 MW, 61 tph TG GEC Turbine SIEMENS Turbine C C 11 KV BUS 9.74 MW, 70 tph TG 18.6 MW, 61 tph TG C C GEC Turbine SIEMENS Turbine 67ata & 485 ºC 42ata & 400 ºC
  • 26. Actual Thermal Efficiency of existing power plant on date Heat value of KPC boiler ≈ 767 Kcal/kg (from steam table) (at 43.4 ata and 400ºC) Then net heat value of KPC boiler ≈ 767 – 105 ≈ 662 Kcal/kg. Thermal efficiency of KPC boiler = η th = (Net heat value * Total Steam generation) / (CV of the bagasse * total bagasse consumption) η th = (662 * 122759) / (2277 * 61672) = 57.99% ≈ 58% ( against 69% of design) Heat value of TBW boiler = 807.7 Kcal/kg (From steam table) (at 67 ata and 485 ºC) Then net heat value of TBW boiler ≈ 807.7 – 105 ≈ 702.7 Kcal/kg GCV of coal = (CV of coal * total coal consumption) / Total fuel consumption = (5500 * 4622) / 56213 = 452.22 Kcal/kg GCV of Bagasse = (CV of bagasse * total bagasse consumption) / Total fuel consumption = (2277 * 51591) / 56213 = 2089.77 Kcal/kg Then net GCV = 452.22 + 2089.77 = 2542 Kcal/kg
  • 27. Then net heat gain = heat gain * steam required for cane * efficiency of Topping TG set = 13.8 * 125*10 3 * 0.9 = 1552.5 Kcal/kg Total power generation = 1552.5/860 = 1.8 MW Transfer rate = 1800 * 24 * 330 * 1.96 = 2.79 crore.
  • 28. Thermal efficiency of TBW boiler = η th = (Net heat value * Total Steam generation) / (Net GCV * total fuel consumption) = (702.7 * 129399) * 100 / (2542 * 56213) η th = 63 % (against 71.75 % of design) Average thermal efficiency of KPC & TBW boiler = (58+63) / 2 = 60.5 %
  • 29. Expected direct efficiency of multifuel boiler = 84% Then fuel saving = 84 – 60.5 = 23.5% Cost of fuel saving = Actual cane crushed * % of fuel caned * % fuel save for 02-03 = 729598 * 0.3 * 0.235 = Rs. 51436.65 Then total saving of bagasse = 51437 * 500 = Rs. 2,57,815 = 2.57 crore Net gain in power = 2.79 crore Net gain in fuel save = 2.57 crore Then total gain = 2.79+2.57 = 5.36 crore
  • 30. Heat value of AFBC boiler = 821.5 Kcal/kg (from steam table) (at 515 º C and 105 kg/cm 2 ) Then net heat gain = 821.5 – 807.7 = 13.8 Kcal/kg From data Budgeted crane crushed/year = 775000 M.T Actual crane crushed/year = 72598.401 M.T No. of crop days = 170 days % Steam required for crane = 48% % of bagasse in cane = 30% Then steam required for cane/hr. = (budgeted cane crushed * %steam reqd. for cane) / (No. of days * 24) = (775000 * 0.48) / (170*24) = 91.176 tph ≈ 100 tph For maximum efficiency steam required for cane/hr = 100/0.80 = 125 tph
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