Sugar
Seed Slurry Requirement Calculation for B and C massecuite
Sugar Seed Slurry in pan boiling of Crystallization
The sugar crystallization(pan boiling) is one
of the important section in sugar
industry. In crystallization process follows different
techniques to form sugar crystals nuclei (grain
techniques).
Generally true seeding method is one of the best method of graining in pan boiling scheme. In this method sugar seed
slurry used for
crystal formation.
In true seeding method, the liquor is
concentrate upto it will reaches metastable zone. Then
Crystallization is initiated by admitting some very fine sugar seed in the form of a slurry, which provides the nuclei to start the crystallization.
The slurry having mixer
of organic solvent and very finely ground sugar particles.( 3 to 5micron size sugar nuclei).
The basic requirements of organic solvents to
be used for sugar seed
slurry preparation are as
follow
a) Boiling point of organic solvent be lower
than water.So that after introduction of slurry in pans all organic solvent
gets evaporated and crystal get spread well.
b) Solubility of sucrose in such organic
solvent should be minimum or negligible.
c) Solubility should not give any odor to
sugar.
Various methods are using in preparing the
seed slurry. Usually the seed
slurry prepared in precipitation method and ball milling of refined sugar in
alcohol for a period of time.
The magma or seed used as a footing into the
batch pan or continuous pans. The size and quality of the magma have
placed a significant role on final
crystal size and exhaustion of the massecuite. The uniform size of crystal with correct estimated
quantity of sugar seed slurry dosing is very
essential to get good quality of magma.
Now the estimation of sugar seed slurry to
the pan depended upon following parameters.
a) Generally Grain prepared in batch pan and
its magma feed to continuous pan.
b) According to dropped magma in batch pan,
estimate total production of massecuite from continuous pan.
c) Requirement of crystal size in final
dropping massecuite. ( Generally
For B
massecuite the
average crystal size having 250±20 microns and for C
massecute having 180±10
microns.)
d) Requirement crystal percent in
final dropping massecuite. ( Generally
For B
massecuite the
average crystal percent having 42±3% and for C
massecute having 32±3%)
e) Sugar seed quantity in given slurry per
liter. ( generally its having 250 to 400 grams per
liter of seed slurry)
f) Average size of sugar nuclei in
sugar seed slurry. (generally its having 3 to
5 microns)
g) The crystal axes ratio is in the following
proportion,
1.2595: 1: 0.8782
Though sugar crystal is not perfectly cubical
nature, consider it as a cubical
nature for simplification of calculation. So take volume of
crystal = 1.2595
x 1 x 0.8782 = 1.106 (unit) 3 = 1.11 (unit) 3
Now take examples for calculation of required
quantity of seed slurry to admitted to grain preparation in batch pan (magma
preparation)
Example 1 : Grain prepared
in batch pan and its material (magma) feed to continuous pan
Required Data For
calculation
S.No |
Particulars |
Values |
UOM |
1 |
Volume of
crystal |
1.11 (unit) 3 |
|
2 |
Grain Batch pan
capacity (Dropping magma) |
60 |
MT |
3 |
Continuous pan
Capacity |
35 |
MT/hr |
4 |
Grain &
Molasses ratio to continuous pan |
1 : 2 |
|
5 |
Grain feed Brix
to Cont. pan |
88 |
|
6 |
Liquor feed
brix to cont.pan |
75 |
|
7 |
Final Dropping
massecuite Brix |
95 |
|
8 |
Sugar nuclei
size in slurry |
5 |
micron |
9 |
Crystal size in
final dropping massecuite |
220 |
microns |
10 |
Crystal percent
in final dropping massecuite |
43 |
% |
11 |
Density of
crystalline sucrose |
1.5879 |
gm/cm3 |
12 |
Sugar seed
quantity in slurry |
380 |
gm/liter |
Calculation Part:
S.No |
Particulars |
Values |
UOM |
Remarks |
1 |
Magma Quantity
drooped in batch pan |
60 |
MT |
Grain pan capacity |
2 |
Molasses
required for dropped magma |
120 |
MT |
60 x 3 |
3 |
Total
massecuite production |
150.3 |
MT |
[(60 x88) + (75
x 120)]/95 |
4 |
Weight of the
crystals in massecuite |
64.64 |
MT |
150.3 x 43% |
5 |
Volume of the
single crystal in slurry |
138.75 x 10-9 |
mm3 |
0.005 x 0.005 x
0.005 x 1.11 |
|
|
138.75 x 10-12 |
cm3 |
138.75 x
10-9 /
1000 |
6 |
Weight of the
Single crystal in slurry |
220.32 x 10-12 |
gm |
138.75
x 10-12 x
1.5879 |
7 |
Volume of the
single crystal in massecuite |
0.01181928 |
mm3 |
0.220 x 0.220 x
0.220 x 1.11 |
|
|
1.18193 x 10-5 |
cm3 |
0.01181928
/ 1000 |
8 |
Weight of the
Single crystal in massecuite |
1.87678 x 10-5 |
gm |
1.18193 x
10-5 x
1.5879 |
9 |
Number of
crystals in massecuite |
3.44397 x 1012 |
|
64.64 x 106/ 1.87678 x 10-5 |
10 |
Weight of the
slurry crystals for that number of crystals in massecuite |
759 |
Grams |
3.44397 x
1012 x
220.32 x 10-12 |
11 |
Weight of the
sugar in slurry per metric ton of massecuite |
5.05 |
gm/ MT of
massecuite |
|
12 |
Volume of
the slurry required |
1.997 |
Liters |
759 / 380 |
In the above calculation crystal size
in seed slurry have
influenced very high in slurry dosing. suppose if we take crystal size 4
micron instead of 5 microns in the above calculation, the final answer will be
come as follow as
Weight of the
slurry crystals for that number of crystals in massecuite |
388 |
Grams |
|
Weight of the
sugar in slurry per metric ton of massecuite |
2.58 |
gm/ MT of
massecuite |
|
Volume of
the slurry required |
1.022 |
Ltrs |
|
So uniformity of sugar nuclei is very essential
in sugar seed slurry.
Example 2 : Grain prepared
in batch pan and its material dropped as 3 pans in same batch pan.
Required Data For
calculation
S.No |
Particulars |
Values |
UOM |
1 |
Grain Batch pan
capacity (Dropping magma) |
60 |
MT |
2 |
Grain pan
consider for massecuite dropping |
3 |
pans |
3 |
Sugar nuclei
size in slurry |
5 |
micron |
4 |
Crystal percent
in final dropping massecuite |
180 |
microns |
5 |
Crystal size in
final dropping massecuite |
35 |
% |
6 |
Density of
crystalline sucrose |
1.5879 |
gm/cm3 |
Calculation Part:
S.No |
Particulars |
Values |
UOM |
Remarks |
1 |
Total
massecuite production |
180.0 |
MT |
60 x 3 |
2 |
Weight of the
crystals in massecuite |
63.00 |
MT |
180 x 35% |
3 |
Volume of the
single crystal in slurry |
138.75 x 10-9 |
mm3 |
0.005 x 0.005 x
0.005 x 1.11 |
4 |
|
138.75 x 10-12 |
cm3 |
138.75 x 10-9 /
1000 |
5 |
Weight of the
Single crystal in slurry |
220.32 x 10-12 |
gm |
138.75
x 10-12 x
1.5879 |
6 |
Volume of the
single crystal in massecuite |
0.00647352 |
mm3 |
0.180 x 0.180 x
0.180 x 1.11 |
7 |
|
6.47352x 10-6 |
cm3 |
0.00647352
/ 1000 |
8 |
Weight of the
Single crystal in massecuite |
1.02793 x 10-5 |
gm |
6.47352x
10-6 x
x 1.5879 |
9 |
Number of
crystals in massecuite |
6.12882 x 1012 |
|
63 x 106/ 1.02793
x 10-5 |
10 |
Weight of the
slurry crystals for that number of crystals in massecuite |
1350 |
Grams |
220.32 x
10-12 x
6.12882 x 1012 |
11 |
Weight of the
sugar in slurry per metric ton of massecuite |
7.50 |
gm/ MT of
massecuite |
|
|
|
3.553 |
Ltrs |
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