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Manufacturing
Process
Most
of us remain unclear of the manufacturing of sugar. Let us delve into
the intricacies involved in the manufacturing process.
a)
MANUFACTURING PROCESS
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The
manufacturing of sugar begins when harvested cane is received at
the mill gate, after which cane is weighed on the platform type
weighbridges. This has the weight recording arrangement linked to
a computer that records the gross and net weights as well as the
price payable to the farmers. Cart cane gets unloaded directly into
the cane carrier and tractor trolleys whereas truck cane is unloaded
with the help of overhead traveling cranes.
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The
sugarcane is uniformly fed to the fibrizor to prepare the same for
efficient milling. The prepared cane will then pass through the
four milling tandem for the initial grinding. The juice extracted
is strained and kush-kush separated from the juice is returned to
the mill tandem. Bagasse from the last mill is conveyed to the boilers
as fuel by means of a carrier system.
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The
mixed juice from the milling plant is mechanically screened, followed
by double sulphitation process. The juice is then heated to about
70 degree centigrade in rapid flow vertical juice heater to maintain
good co-efficient of heat transfer. The heated juice is limed and
sulphsited in a continuous juice sulphiter, and then heated to 105
degree centigrade and passed through a flash tank for the removal
of gas and air before letting it into continuous 36" dia clarifier,
where the settling of the mud floc takes place. Accumulated mud
from the mud boot is separately withdrawn by gravity flow. Clear
juice is withdrawn from the upper regions through the overflow box
for further treatment.
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Clarified
juice from the clarifier is further heated to around 15 degree centigrade
in a plate heat exchanger, before being pumped for thickening. Vapour
from the 2nd effect is used to heat the pans. A quintuple effect
evaporator is used for the final thickening of the juice into syrup.
The syrup at 60-65 degree centigrade is further bleached by passing
it through a continuous syrup sulphitation vessel and pumped to
pan supply tanks at the pan floor.
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Intensive
exhaustion takes place in the pans before crystallization. Air-cooled
crystallizers are used for proper crystallizations. After the mother
liquor in the massecuite is exhausted to the optimum limit i.e.
the maximum sugar from the mother liquor has been transferred to
sugar crystals, the two constituents are separated in the centrifugals.
The sugar is washed thoroughly with super heated wash in stages
within the centrifugal baskets.
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The
sugar discharged from centrifugals is conveyed, dried and cooled
by multi-tray hoppers. The sugar is then screened in a grader so
as to separate fine and lumps. Sugar is thereafter sack filled,
stitched and conveyed to the sugar warehouse.
b)
STEAM GENERATION
Two
bagasse fired water tube boilers are provided to meet the requirements
of the factory process. The boiler is equipped with oil burners designed
for 50% of steam capacity. The boiler is rated for an output of 70 tonnes
of steam per hour operating pressure.
c) POWER GENERATION
Three
3MW Turbo Alternators are provided for the power requirement of the
factory. In addition, one 250 KW diesel powered generation and one transformer
500 KW to trap grid power is also provided to supplement the availability
of power.
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