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Maize Flour Mill
PROCESS DESCRIPTION
The maize Milling process is a Mechanical process and consists
of cleaning , De germination, grinding and sieving operations.
After each sieving operations, product of a particular quality
is drawn and the residue is recycled for further grinding
or Milling .
A maize mill can be broadly divided into three section, i.e.
a) Ceaning section.
b) Degermination section.
c) Milling section.
The Cleaning section
In this Section elaborate arrangement are made for through
cleaning of the whole maize . The maize that is procured in
bags contain numerous impurities such as sand and grit, metal
pieces, mud limps, chaff, gunny pieces, full maize corns,
husk and dirt. Old stocks of maize also contain other impurities
such as insects and half eaten dead maize. The presence of
the above impurities is harmful to human health. The whole
of the cleaning section is devoted to the removal of these
impurities and conditioning the maize to make it suitable
for milling. The whole process of cleaning is an automatic
process and consists of addition of water, primary sieving
for removal of large sized impurities and dust particles,
Removal of stones and mud ball by Destoner. Removal of metal
impurities by passing the maize through a series of magnets.
At the end of the cleaning operation, the clean maize suitable
for the milling operation is stored in very large grain silos.
The grain should be kept in the silos for several hours for
conditioning before milling.
The Primary two objectives of conditioning are as
follows :
a) To prepare the maize so that the milling process is most
efficiently performed. This depends on the even distribution
of moisture in maize.
b) To modify the Germ characteristic of maize
To elaborate on the first objective the following
points should be mentioned:
I) The maize should be dry enough for :
- easy separation of endosperm from bran.,
- accurate and easy sifting on the plan sifter
II) The maize should be also be wet enough for:
- The bran to be sufficiently tough to avoid break in up.
The two conditions are contradictory to one another. But
in practice it is not hard to make a compromise. Maize form
different parts of the country vary considerably in physical
condition and moisture content. Hence the maize must be brought
to a physical state in which the endosperm can most efficiently
be separated from the bran. For uniform distribution of moisture,
it is stored.
Maize
| The whole maize can be divided into three major parts: |
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a) The Bran
b) The Germ
c) the Endosperm
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| a) The Bran |
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This constitutes 10% of the
total maize and has several parts like Epidermis,
Epicarp, Endo-Carp, Testa, Nucellar layer
and the a lurone. The Bran should be removed
from the maize as big as possible to get quality
Grit . Presence of Bran spoils the colour
of the Grit & flour. |
| b) The Germ: |
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This constitutes 16% of the total maize
and is ritch with oil and fats. The Germ should
be removed from the maize as much as possible
to get quality Grit . Presence of Germ increases
fat and reduces shelf lie of grit |
| c) The Endosperm |
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This constitutes 74% of the total maize.
It is this portion that is milled for Grit
& flour. The first objective of milling
therefore is to remove the Bran and germ from
the endosperm..
In the Degermination & milling section
the clean and conditioned maize is passed
through a series of grinding and sieving
operations. At the end of each sieving operation
the ground maize is separated according
to the different particle sizes. The large
particles are fed to the subsequent grinders
whereas the smaller particles which are
already suitable for finished product are
collected as a marketable products. |
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0.1 CLEANING PROCESS
The bagged maize brought in Trucks will be stored in silos
and will be conveyed to the cleaning of maize section of the
plant by bucket elevators.
0.2 DRUM SIEVE
To start with the maize is FED into a hexagonal reel. As
a Pre-cleaning machine the Drum sieve is very versatile and
is used above all in the intake section It sieves to separate
coarse impurities such as straw particles, string, paper pieces
of wood, etc. in order to relieve down stream and conveyors.
A horizontal overhung sieve drum is rotated in an enclosed
casing. The product (Maize) is fed via the inlet spout into
the interior of the Drum and is revolved so that the fines
drop through the sieve, where as the rolling motion causes
the coarse impurities to move to the outlet channel below
the inlet. The drum if divided into three sections having
different size of perforated sieve on it. The first sieve
has perforations slightly smaller than the average size of
maize is to separate dust and fines. The other two sieve have
perforations slightly larger than the average size of grain
and it separate out the impurities larger in size like stones,
string, wooden pieces.
0.3 SEPARATOR
From the Drum sieve machine the grain is fed into a separator.
This machine basically consists of two perforated sieves.
The top sieve having perforations Slightly bigger than the
average size of the grain and lower sieve having perforations
slightly smaller than the average size of the grain. The sieves
are given an vibrating motion by two unbalanced vibro motors.
Material to be separated falls freely through the inlet onto
the top coarse screen, which removes such coarse impurities
as string, straw and stones. Troughs of the top sieve falls
on the bottom sieve which can also be called as sand sieve
which removes broken kernels, sand and other fine impurities.
Tailings from the lower sieve layer consists of cleaned grain
which pass to the outlet.
The vibrating movement of the sieves facilitates an increase
of the capacity on a given sieve surface and also an increase
of the sieve effect. At the discharge end the grains are subjected
to aspiration by an aspiration chancel. The aspiration lifts
with it light impurities such as chaff, husks, etc.
0.4 DRY STONER
This unit is used for the continuous removal of stones having
the same size of grain from the stream of granular material.
The function of this machine is based on a combination of
micro projectile motion & wind sifter working on a vibro
pneumatic principal. The product is gravity fed though an
air shut off gate on to a preliminary separation screen maize,where
it passes onto an inclined oscillating deck or table. This
deck is designed as screen through which an upward current
of air is passed fluidizing the product. Due to their different
specific gravities, the heavy particles such as stones/metal
go down while the lighter particles, supported by the caution
of air float on top. The oscillating action of the screen
causes the heavy particles to work their way to the upper
end of the deck.
0.5 (INTENSIVE DAMPENING UNIT)
Maize, after being cleaned by different dry processes is
fed to a intensive dampening. The maize is carried out into
the machine in a stream of water and is rapidly sluiced around
at high speed. As the maize is charged into the worm and conveyed
through water heavier particles like stones, flints, etc.
settle at the bottom of the through. Maize is conveyed by
the worm in the trough to a whizzer which is a vertical rotating
shaft at the centre with beaters. The beaters, while lifting
the maize form the bottom to the top trash the maize on the
surface of the drum to remove extra water sticking on to the
maize, adhering dirt and some branny material. In this machine
the maize is treated with water for conditioning before being
taken for milling operation.
0.6 MAGENETS
Magnets are used in the process of maize conveying at different
stages. The complete removal of iron is very important not
only to avoid damaging the mill machinery but also to prevent
any possibility of nail or metal washer striking a spark during
later stager of the process and taus igniting a dust cloud,
which is highly explosive.
0.7 CONVEYING
Conveying of maize is done with the help of bucket elevators.
The belt bucket elevator is the ideal type of conveyor for
vertical handling or granular materials. The entire housing
is made of steel shee
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Dehusker
The Cleaned maize is fed to Dehusker .The conical dehusker
–degerminatior works by friction, dehusking and
degerminating the kernel in conical chamber runing on
roller bearings inside this conical chamber is a rotor
with convex protrusions on it surface.
The screen is mobile in relation to the Axis of conical
rotor, the mobility permits the adjustment of distance
between rotor and screen, which in term decide degermination
effect.
About 40 % of the stator surface is perforated screen
which enable discharge of the fines The two streams
generated this way
1) Coarse dehusked grit and germ
2) Fine grit, Germ, Bran, Flour Which has passed through
Screen
Aspirators
Fine fraction is feed to aspirator which separates
Fine flour and Bran from Remaining Grit with help of
difference in terminal velocity of products
Gravity table
Dehusked and clean maize grit free of flour is feed
to gravity table which got fluidized bed with help of
Five nos. of in built fans and adjustable inclination
in bed both from front to end and side wise helps to
sort material as per density. Which cause separation
of 80 % germ from different grits
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OBJECT OF MILLING
The objective in the milling of Grit are:
To separate, as completely as possible, the endosperm, which
is required for the Grit , from the bran and germ, which are
rejected, so that the Grit shall be free form Germ & bran
specks, and of good colour, and so that the palatability and
digestibility of the product shall be improved
To reduce the, Minimum amount of endosperm to flour fineness,
thereby obtaining the maximum extraction of Grit from the
maize.
The reduced endosperm is known as Grit , flour, and residual
adhering germ are obtained as a by product, used primarily
in animal feeding.
PROCESS OF MILLING
In order to separate the endosperm form the bran and germ
and reduce the endosperm to Gritt fineness, a particular from
of grinding has been developed which is combination of shearing
scraping and crushing, achieved by roller mills, and which
exploits the differences in mechanical properties between
the endosperm, bran and germ. It is essential to minimise
the production of fine particles of bran, and this basic requirement
is responsible for the complex arrangement of the modern flour
milling system and for the particular design of the specialised
machinery used in it.
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There are three basic
process
| Grinding |
Fragmenting the grain
or its parts with some dissociation of the anatomical
parts of the grain form the one another. |
| Sieving |
Classifying mixtures of particles
of differing particles size into fractions of narrower
particle size range. Names of particulars sieving
processes include., scalping., sieving to separate
the break stock (the coarsest particles) from the
reminder of break grind, Dusting, Bolting. |
| Dressing |
Sieving flour coarser particles |
| Grinding |
Classifying mixtures of semolina,
middling and dust into fractions of restricted particle
size range |
| Purifying |
Separating mixtures of bran and endosperm
particles according to terminal velocity, by means
of air currents. |
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GRADUL REDUCTION PROCESS
The modern roller milling process for making flour is described
as a “gradual reduction process” because the grain
and its parts are broken down in a secession of relatively
gentle grinding stage so that only the required amount of
endosperm fragmentation and bran occurs at each stage.
MILLING OPERATIONS IN BRIEF
After the maize has been conditioned ,Degerminated a succession
of grinding stages, using roller mills in each is used to
open the whole grain in the first stages, and in subsequent
stages preceding grindings.
An individual grinding stage may be light or heavy, according
to the character of its feed, in general, feeds consisting
of relatively pure endosperm can be heavily ground, whereas
these containing much bran must be lightly ground.
Each grinding stage yields a “grind” consisting
of a mixture of coarse, medium, and fine particles, including
a portion of flour. The differentiated particles are sorted
by shifting, a shifting stage therefore follows each grinding
stage. Some of the coarse particles are potentially Grit yielding,
these are conveyed to subsequent grinding stage, others can
yield no useful Grit , these are removed from the milling
system and contribute to the milling by-products.
Particles deferring widely in size (in the grind from any
one stage of roller milling) also differ in composition. Particles
of endosperm, which tend to be friable, are generally smaller
than particles of bran, , which tend to be tough and leathery.
The process of sieving, besides sorting the particles according
to size, thus to some extent separates particles of differing
composition from each other, e.g. endosperm from bran.
The BREAK SYSTEM consists generally of Two “ breaks”
on roller mill grinding stages, each followed by a sieving
stage. The system is fed with the whole grain in the first
break, and with the break stock in subsequent stages. The
objective in the first break to open the whole grain, and
in subsequent break to scrape off the endosperm from the bran
coat which owing to their fibrous structure and tough nature,
remain relatively large pieces.
BREAK ROLLER MILLS
Each of the break roller mills is equipped with a pair of
rolls, usually 10” (25.4 cm) in diameter and up to 40”
(101.6 cm) long mounted diagonally in parallel alignment along
heir whole length. The narrow gap, or “nip” between
the aligned rolls can adjusted to allow precision grinding.
The rolls rotate in opposite directions so that the surfaces
of both rolls are entering the nip on the same direction.
One of the rolls rotation at a faster speed than the other,
the speed differential between the two generally being 2 ½,
1 for break roller-mills. The break rolls are corrugated or
grooved over their entire surfaces, the corrugations (or ‘flutes’)
running along the length of the roll, but disposed at a slight
angle to their axes this angle being known as the ‘spiral’.
The effect of the speed differential between the to rolls
and the spiral arrangement of the flutes is to cause the flutes
of the fast roll to move across those of the slow roll at
the point of contract, simulating the action of scissors.
The first break grind thus consist of a mixture of particles
which differ in size and composition. The largest are the
bran.
SIEVING
Screening or bolting cloth is made of woven wire, silk or
nylon, for dressing, dusting and grading, although wire may
also be used for these purpose to be sieved is fed in at the
top and falls from sieve to sieve by gravity. A single plan
sifter may incorporate sieves of four or five different mesh
sizes thereby delivering five or six fractions of differing
particle size. A certain depth of stock on the sieving cloth
is required to obtain a satisfactory sieving effect. Owing
to the movement of the sieve, the stock resting on it becomes
stratified, the finest particles work down until they are
adjacent to the cloth, whilst the largest ride up to the surface
of the stock. The overlying layers of medium and coarse particles
thus tend to keep the finest particles in contact with the
sieve cloth and assist their passage through the sieve spertures.
PURIFYING
A purifier consists of an oscillacing sieve set at a slight
angle to the horizontal and enclosed by a hood or cover. The
sieve comprises four sections which become progressively coarser
in size of mash from head to tail. The good, divided into
sections to correspond to the sieve sections, is connected
by trunking to the section, side of a fan so that air, controlled
by valves, is drawn up through each sieve section. Stock to
be purified is fed into the head end of the sieve and is moved
down by the oscillating motion towards the tail or coarse
sieve section. Particles of endosperm, decreasing in purify
from head to tail sieve sections fall through the respective
sieves, against the direction of the air current (being relatively)
dense and having high terminal velocity, and are collected
in hoppers, light particles of free bran and bees-wing are
lifted by the air current, and are collected in trays (tins)
suspended above the sieves. Particles intermediate in density
and terminal velocity, consisting of bran loaded with endosperm,
are not lifted, more do they fall through the sieves, but
remain floating on the sieve, and are eventually discharged
as overtails. The required percentage of suji, Rava is taken
out here and the balance directed to Reduction system.
LIST OF EQUIPMENT
| 1. |
Intake hopper covered with Iron
grating. |
| 2. |
Elevator |
| 3. |
Drum sieve |
| 4. |
Rotary motion separator |
| 5. |
Aspiration channel |
| 6. |
Screw conveyor |
| 7. |
1 Aspiration System For the pre cleaning
section |
| 8. |
Cyclone |
| 9. |
ASPIRATION DUCTING FOR PRE-CLEANING |
| 10. |
GRAVITY SPOUTING CLEANING |
| 11. |
Volume Metric feeder |
| 12. |
Screw conveyor. |
| 13. |
Elevator |
| 14. |
Dry-Stoner Having the following features: |
| 15. |
Horizontal Scourers |
| 16. |
Vertical aspirators |
| 17. |
Intensive Grain Tempering Mixer |
| 18. |
Sanitary impactor |
| 19. |
Impact Degerminator |
| 20. |
Vertical aspirators |
| 21. |
Shifter |
| 22. |
Aspirators |
| 23. |
Gravity Table |
| 24. |
1 Aspiration System For the cleaning section |
| 25. |
Cyclone 1100
Cyclone 900 |
| 26. |
ASPIRATION DUCTING FOR CLEANING SECTION |
| 27. |
1 Aspiration System for the Dry stoner |
| 28. |
Cyclone type SEC/A-1100 |
| 29. |
ASPIRATION DUCTING FOR DRY STONER |
| 30. |
GRAVITY SPOUTING CLEANING |
Production Capacity : 20 TPD
RAW MATERIAL
MAIZE 50 TPD
PRODUCT
| MAIZE GRIT OR FLOOR |
30 TPD |
| GERM |
12 TPD |
| GRAN |
8 TPD |
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