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RED HERRING PROSPECTUS Dated August 24 ... - Globus Spirits

RED HERRING PROSPECTUS Dated August 24 ... - Globus Spirits

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GRAIN PROCESS<br />

LIQUEFACTION FERMENTATION AND DISTILLATION<br />

PROCESS DESCRIPTION FOR GRAIN BASED LIQUEFACTION AND FERMENTATION:<br />

FLOW DIAGRAM FOR GRAIN SPIRIT PRODUCTION:<br />

Milling<br />

Section<br />

Slurry Preparation /<br />

Liquefaction Section<br />

Consisting of<br />

i. Grain storage (20 days capacity)<br />

ii. Magnetic separator<br />

iii. Vibratory Screen<br />

iv. Chain conveyor<br />

v. Bucket elevators<br />

vi. Hopper bins<br />

vii. Hammer mill<br />

Consisting of<br />

i. Mixing tank<br />

ii. Slurry tank<br />

iii. Jet cooker<br />

iv. Holding coil<br />

v. Flash tank / holding tank<br />

vi. Liquefaction tank<br />

vii. Slurry coolers<br />

Fermentation<br />

Section<br />

Consisting of additional equipment for the<br />

Existing fermentation section like<br />

i. Fermentors<br />

ii. Wash re circulation pumps<br />

iii. Fermented wash coolers<br />

iv. Suitable modifications in piping / equipment, etc.<br />

A) MILLING AND FLOUR HANDLING:<br />

The incoming grain is first cleaned with the help of destoner and magnetic separators to<br />

remove stones and other material, which may damage the hammers during milling. The<br />

grain is fed to hammer mill in controlled manner. In milling, grain is crushed to flour of<br />

uniform size. Oversized screening rejects are segregated with the help of vibratory<br />

screen. These are taken to coarse bin before sending it to mill again. Intermediate<br />

hopper is provided for buffer capacity for flour storage. The flour addition is metered<br />

through a weigh feeder with load cell arrangement before transferring to the mixing tank<br />

for slurry preparation process.<br />

B) SLURRY PREPARATION / LIQUEFACTION:<br />

Grain flour is fed at controlled rate to mixing tank and then to agitated slurry tank where<br />

some amount of water and enzyme stabilizing chemicals is added. A portion of the<br />

liquefying enzyme is also added here. This slurry is then “cooked” in the jet cooker. The<br />

slurry is continuously pumped to a steam jet cooker where high-pressure steam at 7 bar<br />

(g) / 170 °C rapidly raises the slurry temperature. The mixture of slurry and steam is<br />

then passed through the holding coil which has several “U” bends in series and sufficient<br />

capacity to provide the desired retention time at a given flow rate. The cooked mash is<br />

discharged to a flash tank. The cooking process, accomplished in the above manner,<br />

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