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 |
|
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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