Saturday, March 13, 2021

B MASSECUITE DROPPING PURITY CALCULATION

 

B massecuite dropping purity calculation sheet

Grain and molasses ratio calculation for ‘B’ continuous pan

In this article explain with example for B grain purity calculation with their required quantity of molasses. B continuous pan grain and molasses flow rate requirement according to the continuous pan capacity. Finally calculate B continuous pan massecuite dropping purity and its vapour requirement.

 

Data required for B massecuite purity calculation.

S.No

Particulars

Brix

Purity

Specific Gravity

1

Syrup

60

82

1.276

2

AH molasses

75

71

1.337

4

Required B grain footing ( Before slurry feed)

86

75

1.435

5

B grain

88

?

1.435

6

B grain batch pan capacity in metric ton(MT)

60

 

 

7

Graining Volume of the batch pan

45

%

 

8

Grain &  molasses ratio 

1

3

 

9

B continuous pan capacity

30

T/hr

 

10

B massecuite Brix

95

 ?

 

Calculation part :

B Grain material purity ( For B grain taken Syrup & AH molasses as a footing material and then further fill up with AH molasses.)

S.No

Particulars

Values

UOM

Remarks

1

Solids in B Grain

52.8

MT

88 x 60 /100

2

Volume of the pan

41.8

M3

60 / 1.435

 

 

418

HL

41.8 x 10

3

Grain Volume 

188.153

HL

418 x 45 %

 

 

18.82

M3

188.15 /10

4

Weight of the grain material

27

MT

18.82 / 1.435

5

Solids in grain material

23.22

MT

27 x 86 / 100

6

Solids from Syrup for grain material

8.4

MT

8.4 x 4 / 11

7

Solids from AH for grain material

14.8

MT

23.22 – 8.4

8

Weight from Syrup for grain material

14.07

MT

8.4 x 100 / 60

9

Weight from AH for grain material

19.70

MT

19.70 x 100 / 75

10

Volume from Syrup for grain footing material

11.03

M3

C26 / 1.276

 

 

110

HL

11.03 x 10

11

Volume from AH for grain footing material

14.74

M3

19.70 / 1.337

 

 

147

HL

14.74 x 10

12

Solids from AH to further filling of the grain material

29.58

MT

52.8 – 23.22

13

Weight from AH to further filling of the grain material

39.44

MT

29.58 x 100 / 75

14

Volume from AH to further filling of the grain material

29.4989

M3

39.44 / 1.337

 

 

295

HL

29.49 x 10

15

Final B grain drooping purity

72.8

 

[ (29.58 x 71) + (23.22 x 75)] / 52.8

B grain and AH required for B Continues pan for given grain and molasses ratio and B massecuite final dropping Purity.

1

Grain Quantity

60

MT

 

2

AH molasses quantity

180

MT

60 x 3

3

B  grain solids for B m/c

52.80

MT

60 x 88 / 100

4

AH solids for B m/c

135

MT

180 x 75 / 100

5

 B M/c Production for given B grain solids

187.80

MT

52.80 + 135

 

Quantity of B massecuite

197.68

MT

187.80 x 100 / 95

6

Grain feed quantity for Continuous Pan

9.11

MT/hr

60 x 30 / 197.68

 

 

6.35

HL/hr

9.11 / 1.435

7

AH Molasses feed quantity for Continuous Pan

27.32

MT/hr

9.11 x 3

 

 

204

HL/hr

27.32 x 10 / 1.337

8

B massecuite Final purity

71.49

%

[ (52.80 x 75) + (135 x 71)] / 187.80

Steam Flow requirement for Continuous pan.

1

Evaporation rate in AH

21.05

%

((95 -75)/95)

2

Evaporation rate in B grain

7.37

%

(95 – 88)/95

 

 

6.42

T/hr

9.11 x 7.37% + 27.32 x 21.05%

3

Consider 20% extra

7.71

T/hr

6.42 x 1.2

 

Steam Flow requirement for Continuous pan

7.71

T/hr

 

 

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