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BOILER EFFICIENCY & FUEL ECONOMY
 
TECHNICAL INFORMATION
 

      I.   MOST IMPORTANT TECHNICAL THINGS TO KNOW

 

EQUIVALENT  % CO 2

 

% Oxygen

% Excess Air

Gas

Oil

Coal

1

5

11.3

14.7

17.1

2

10

10.8

14.0

16.3

3

17

10.2

13.3

15.4

4

23

9.6

12.5

14.6

5

31

9.0

11.8

13.7

6

40

8.5

11.1

12.8

7

50

7.9

10.3

12.0

8

61

7.4

9.6

11.1

9

75

6.8

8.8

10.3

10

91

6.2

8.1

9.4

11

110

5.7

7.4

8.6

12

133

5.1

6.6

7.7

13

162

4.5

5.9

6.8

14

200

3.9

5.2

6.0

15

250

3.4

4.4

5.1

16

320

2.8

3.7

4.2

 

II.    TO RUN BOILER SMOOTHLY & TO ATTAIN OPTIMUM STEAM FUEL RATIO

 

CONTINUOUS & REGULAR DOSAGE OF “HEATER AID”, STICKS.

 
MONITORING OF AIR DRAFT IN FURNACE
 
III.       FEW DATA REGARDING BIO MASS
 
DETAIL OF STEAM COSTING & FUEL EFFECIENCY
 

DESCRIPTION

UNIT

R.HUSK

M.STALK

P.FIBER

P.WASTE

SC.CHIPS

P.STRAW

Ambient Temp.

DEG C

13.00

13.00

13.00

13.00

13.00

13.00

Ambient Temp.

DEG F

55.40

55.40

55.40

55.40

55.40

55.40

Outlet Temp.

DEG C

190.00

190.00

190.00

190.00

190.00

190.00

Outlet Temp.

DEG F

374.00

374.00

374.00

374.00

374.00

374.00

Engy.req.to 1 kg. water va.

BTU/lb

1207.60

1207.60

1207.60

1207.60

1207.60

1207.60

Net enthalpy of steam blr.

BTU/lb

1194.21

1194.21

1194.21

1194.21

1194.21

1194.21

Hydrogen in fuel

%

5.00

5.12

5.68

4.99

5.00

5.00

Dry gas per kg. fuel

lb

7.01

6.13

7.42

6.72

4.48

6.66

Water from by H/kg fuel

lb

0.45

0.46

0.51

0.45

0.45

0.45

Ash in fuel

%

16.46

7.97

1.18

16.77

4.00

16.48

Fuel input ratio

%

100.00

100.00

100.00

100.00

100.00

100.00

Dust in fuel

%

1.00

6.00

0.50

6.00

5.00

1.00

Avg. moisture in fuel

%

11.50

18.47

6.75

10.60

41.00

15.97

G.C. value of fuel O.D.base.

Kcal/kg

3750.00

3187.50

3901.00

3375.00

4500.00

2625.00

G.C. value of fuel (Dry)

BTU/lb

6750

5737.50

7021.80

6075.00

8100.00

4725.00

G.C. value of fuel (As such)

BTU/lb

5914.01

4397.12

6515.09

5105.19

4540.05

3930.71

Moisture in air per kg of air

lb

0.15

0.13

0.11

0.14

0.07

0.14

Total Moisture in air

lb

0.71

0.77

0.69

0.70

0.93

0.75

Wet air

lb

7.61

6.72

8.05

7.31

5.00

7.24

Wet flue gas

lb

8.44

7.64

9.03

8.15

5.96

8.08

Dry gas

lb

7.73

6.87

8.34

7.45

5.03

7.33

Dry gas losses

%

10.04

11.99

9.83

11.20

8.51

14.32

Loss due to moisture in air

%

0.19

0.23

0.13

0.22

0.12

0.28

Loss  moisture in flue gas

%

11.54

17.73

10.73

13.13

22.87

18.73

Unaccounted loss unburnt

%

6.30

6.30

5.00

6.30

6.30

15.00

Total loss

%

28.07

36.25

25.69

30.85

37.80

48.33

Thermal efficiency of fuel

%

71.93

63.75

74.31

69.15

62.20

51.67

Steam per MT of fuel

MT

3.56

2.35

4.05

2.96

2.36

1.70

Avg. cost of fuel

RS/MT

1000.00

610.00

0.00

762.00

500.00

448.04

Cost of steam

RS/MT

280.72

259.86

0.00

257.77

211.46

158.82

SULPHER

%

0.20

0.42

0.00

0.00

0.00

0.00

 
 

DESCRIPTION

UNIT

SAW DUST

BAGGASSE

COTTON

BAJARA

MOONG

W.STRAW

GUARA

Ambient Temp.

DEG C

13.00

13.00

13.00

13.00

13.00

13.00

13.00

Ambient Temp.

DEG F

55.40

55.40

55.40

55.40

55.40

55.40

55.40

Outlet Temp.

DEG C

190.00

190.00

190.00

190.00

190.00

190.00

190.00

Outlet Temp.

DEG F

374.00

374.00

374.00

374.00

374.00

374.00

374.00

Engy.req.to 1 kg. water va.

BTU/lb

1207.60

1207.60

1207.60

1207.60

1207.60

1207.60

1207.60

Net enthalpy of steam blr.

BTU/lb

1194.21

1194.21

1194.21

1194.21

1194.21

1194.21

1194.21

Hydrogen in fuel

%

5.00

6.05

5.25

6.05

6.00

5.38

5.20

Dry gas per kg. fuel

lb

5.30

4.14

4.75

6.00

7.17

6.90

6.96

Water from by H/kg fuel

lb

0.45

0.54

0.47

0.54

0.54

0.48

0.47

Ash in fuel

%

5.00

4.94

4.86

5.00

4.00

8.47

4.00

Fuel input ratio

%

100.00

100.00

100.00

100.00

100.00

100.00

100.00

Dust in fuel

%

10.00

0.50

1.00

1.00

1.00

2.00

1.00

Avg. moisture in fuel

%

26.44

48.00

40.00

12.22

9.42

12.00

9.81

G.C. value of fuel O.D.base.

Kcal/kg

4500.00

4500.00

4500.00

3600.00

3750.00

3750.00

3850.00

G.C. value of fuel (Dry)

BTU/lb

8100.00

8100.00

8100.00

6480.00

6750.00

6750.00

6930.00

G.C. value of fuel (As such)

BTU/lb

5362.52

4190.94

4811.40

5631.26

6053.01

5821.20

6187.67

Moisture in air per kg of air

lb

0.08

0.07

0.07

0.11

0.15

0.14

0.15

Total Moisture in air

lb

0.79

1.10

0.94

0.77

0.78

0.75

0.71

Wet air

lb

5.83

4.76

5.30

6.65

7.86

7.53

7.57

Wet flue gas

lb

6.78

5.71

6.25

7.60

8.82

6.44

8.53

Dry gas

lb

5.98

4.61

5.30

6.83

8.04

7.69

7.82

Dry gas losses

%

8.57

8.45

8.46

9.31

10.20

10.15

9.71

Loss due to moisture in air

%

0.12

0.14

0.12

0.15

0.19

0.19

0.18

Loss  moisture in flue gas

%

16.09

29.52

21.90

14.30

12.65

12.53

11.05

Unaccounted loss unburnt

%

6.30

6.30

5.50

9.00

5.00

12.00

7.50

Total loss

%

31.07

44.41

35.98

32.76

28.05

34.88

28.44

Thermal efficiency of fuel

%

68.93

55.59

64.02

67.24

71.95

65.12

71.56

Steam per MT of fuel

MT

3.10

1.95

2.58

3.17

3.65

3.17

3.71

Avg. cost of fuel

RS/MT

941.00

600.00

610.00

700.00

700.00

762.00

750.00

Cost of steam

RS/MT

304.01

307.53

236.49

220.76

191.93

240.05

202.27

SULPHER

%

0.00

0.00

0.00

0.00

0.00

0.00

0.00

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