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DG-CementInternship ReportSubmitted By Aitazaz Ahsan 10-ME-04
Aitazaz AHSAN 10-ME-04 8/20/13 DG-Cement
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In the name of Allah, the most merciful,
The most beneficent
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To my beloved parents and honorable teacher
Engineer Yar Muhammad Khan.
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First of all, we are very thankful to the almighty ALLAH, the most
Beneficent and the most Merciful for his blessing to all of us.
We would like to convey our sincere gratitude to our internship advisor
Engineer Yar Muhammad Khan, who believed in me and for his kind interest
and guidance without which this endeavor would not have been materialized.
Special thanks to him for his encouragement and support.
I would like to thank all those who directly or indirectly helped me in making
this report fruitful.
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Abstract
This Report is concerned with DG-Cement manufacturing and all
the processes involved starting from raw material to the packing of
final product. It mainly describes all the mechanical components
present in DG-Cement Plant. The plant was established in 2007 at
Khairpur near Kallar Kahar and it is producing 7000tons cement
per day. It is equipped with all latest equipment required for the
production of cement and has the major role in exporting ordinary
Portland cement from Pakistan which has maximum setting strength
of about 10000Psi. The report cover all the areas which are
important from study point of view. Hope everyone will find it as a
best material to study.
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Safety Section
It is the first portion of internship in which we have learned about safety
precautions in DG-Cement. In Khairpur plant all equipment of firefighting isavailable at every place and every person is equipped with safety helmets and
jackets. Internee are also provided with security helmet to prevent any
damage. Fire alarms are attached and one main security alarm which indicates
any emergency. In case of major emergency when the alarm rings, all the
workers are advised to come out of plant and stop working till that security
team covers the danger. There is a red line spread all around the plant which
also covers tunnel area so that in case of any damage workers can even pull a
single wire and emergency can be felt. AFF is added in 3% with water which
produces foam and used in firefighting. The company has firefighting Vanwhich is of about 10Million cost. Very costly equipment is present and all the
environment is safe and sound. There is no such danger while working at DG.
Pipes are present which sprays the water on fire during working in form of
mist and thus prevent the fire fighter also they have different kind of nozzles
which exhaust water at 7Bar pressure and covers an area of 100ft. Security
buzzers are present and also they are connected through cello phones with
each other. Main firefighting or danger area is of Kiln because in this region
the temp is almost around 1600C so there is a chance of fire spreading. After
visiting the plant we can say that it has best equipment of safety and has full
security of workers working over there.
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Image showing Fire Fighting Van and All Fire Fighting Equipment.
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INTRODUCTION
General Introduction about DG-Ordinary Portland cement Manufacturing
Cement is a mixture of argillaceous and calcareous minerals and has the majorportion ofCalcium Carbonate (60-80%) and Silica (20-30%) and has the
additives Aluminum Oxide (0-10%) and Fe2O3 (0-10%).
Additives are added to perform reactions at low temperature of 1600C
otherwise 2000C temp is required to perform Kiln reactions and to
decompose Calcium Carbonate into CaO and CO2. By mixing all of the above
reactants the product formed is called clinkers which has ball like shape and
they are stored in clinker silo. They are then mixed with gypsum in proper
portion as additive (5%) to increase setting time of cement and are grinded intwo cement mills having capacity of producing 175tons cement per hour.
They are then stored in cement Silo having 22000tons capacity each (total 3).
After that they are transferred to packing plant for packing of cement into
bags. All automation is present in packing plant. Plant has designed with a
capacity of 7000Tons/day. When we talk about power supply, the plant has
33MW power units and they also have supply through wapda. The plant is
under Nishat Group of industries and a paper manufacturing shop is also
present. It has complete safe and healthy environment which has complete
control of dust. Also coal manufacturing from RDF is present. Canteen is alsopresent and it is equipped with laboratory and clinic facility also it has CCR
and other main units for meetings like admin block. All the workers are well
corporation especially Safdar Kamal& Yar Muhammad Khan sb.
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Beautiful Entrance View of Plant
First Bag Produced By DG-Cement
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Top View of Complete Plant
Canteen of DG-Cement
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The production Starts from Quarry.
Quarry Section & Crusher Section
Quarry is the place from where raw material in extracted. Drilling and blasting
is done to extract the material. A hole of about 10-15 m is drilled and
ammonium nitrate in filled as an explosive in these holes. When this explosive
is ignited the rocks are broken into pieces of different sizes. These pieces are
then loaded on the dumper trucks and conveyed to the crusher. It is located
about 3-4 Km from the plant. Drilling takes place firstly and then blasting of
calcium carbonate take place which is then feed to apron feeder and move
towards crusher. Two main crushers are present which are CaCO3 crusher
(1500-1700tons/hour and additive crusher. Both have same mechanism but
numb of hammers and their weights are different. CaCO3 Crusher is of bigger
size and comparatively hard to crush lime stone into small pieces of almost 1-
2inch.
Quarry and raw materials:
The following raw material is required in the production
process:
1. Lime stone: This raw material is company owned and is
extracted from the nearby quarry Unit. Limestone has the
highest composition in the cement product. 76% of the cement
constitutes of limestone.
2. Clay: Clay is another natural resource. This raw material is
also company owned. 24% of cement composition comprises
of clay.
3. Iron Ore, Bauxites and silica sand: Iron Ore is theonly resource that is bought from contractors. Iron Ore, Bauxites and silica
sand are added in small quantities less than one percent and it helps to
strengthen the cement.
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4. Gypsum: Gypsum acts as a retarding agent. It slows down
the hardening process which in turn gives the constructor
enough time to use it.
Limestone Crusher: (EV 200*300):
Capacity: 1500 tons/hr.
Supplier: FLSmidth
Raw material such as limestone, clay, marl and shale are dumped into hoppers
by dump trucks and entered into a hammer crusher through an apron feeder.
Inside hammer crusher there are 48 Hammers attached to four main rotor
shafts each having 12 hammers each and each having weight of 100Kg
approx. They rotate at a
speed of 1200-1300 rpm
and is capable of crushing
feed of very large sizes.
Input is through hopper
and then apron feeder
takes the lime stone
pieces to main crusher
where a rotating disk and
steel chains are present to
prevent backward
movement of broken
pieces. Lamella plates are
used for movement of raw
stones of crusher. Magnet
separator is attached to
conveyor belt to prevent metallic particles from reaching the raw mill. Whenwe talk about additive crusher it has only one shaft having 12 hammers,
smaller in size and attached to a single shaft. They are then transferred to main
storage section and then move towards raw mill through belts.
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Storage Yard:
The crushed material is stored in the form of piles in the storage yard. There
are 6 piles in the storage yard. Mixed piles are used in larger quantity where
as high grade and additive piles are used
in small quantity.
e & clay)
Stacker:
A stacker is a device which form
conical piles of the crushed material.
Feed is conveyed to the stacker through
conveyor belts. This stacker then moves
to and fro to make a pile. The stacker belt
is called Jib in engineering terms.
Now, for conveying this material from
piles to the conveyor following
equipment are used :
Side scrapper:
Side scrapper is a device which picks the crushed feed from the piles through
its feedbelt called Hoist. This belt has a number of small buckets of lowcapacity. When this belt moves, the buckets picks feed from the pile and put
it on the belt conveyor. Side scrapper in used for those piles which are required
in low quantity like bauxite and iron ore.
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Raw Mill Section
Raw mill Feed area
The raw mill feed area consists of 4
feed hoppers:
The capacity of first two hoppers is 800 tons while the other two hoppers have
a capacity of 600 tons. The feed from each pile is conveyed to the hoppers
through conveyor belts in relevant hoppers. Each hopper has 4 load cells. This
section is one of most important section of plant where the crushed material
in form of piles is transferred to bins through belts and then to Raw Mill
through rotary feeder (28rpm) which permits only raw material to fall inside
the raw mill and air is not allowed to fall.
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Main specification of Raw Mill
ATOX Raw Mill
Grinding Capacity 500Tons/Hour. Vertical Roller mill with three rollers.
Sections of Raw Mill
There are 3 sections of a raw mill.
Table:The raw feed from the belt
conveyor directly falls on
the rotating t able of the raw
mill. The table contains 3
crushing rollers. The raw fed
is crushed to fine powder
with these rollers. The
coarse particles are collected
at the bottom of raw mill and
are sent to the vibrator from
where they are sent to theraw feed belt conveyor and again recycled to the ram mill for re
crushing. The vibrator is use to handle the quantity of the material
being put on the belt.
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Separator:
At the top of the raw mill, there is separator section. Hot gases from
the kiln comes from the bottom of the raw mill and lift very fineparticles with it. A suction fan
with motor power of 4500 kw
produces suction and sends dusty
air into the cyclones at the top.
Here the dusty air rotates and
particles are separated from the
air. These particles are collected at
the bottom of the cyclone and sent
to the CF silo with the help of air
slides. The air which still contains
dust particles are separated in
Conditioning tower and Electrostatic precipitator.
Two input ducts are coming inside the raw mill which provide hot
air having temp 108C almost and there in single outlet duct which
takes material and exhaust air in form of cyclones. Id fan is attached
which is used for rapid movement of air b/w inlet and outlet ducts.
Material transfer in form of cyclones prevents the raw material from
reaching Id fan. This material is then transferred to silos four in
numb and the dusty air is transferred to conditioning tower where
foggy drops are sprayed from 30 nozzles each having 3mm dia to
decrease dusty air temp to a lower limit (80-100C) before it reaches
EP (Electrostatic Precipitators) In this section cooled dusty air ispassed between electrical plates where ionization of dust take place,
they are ionized into positive and negative plates and then stick to
respective plates. After this process hammering or shock is produced
in plates which removes dust from plates and this dust is then
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transferred through bucket elevators to the CF-silo. The same
process occurs with grinded material, they are conveyed through
duct to bucket elevators and then transferred to CF-Silo through
bucket elevators. Air from EP and exhaust air from raw mill isexhausted to the atmosphere using chimneys so that fresh air cycle
can be started again.
CF-Silo is main storage of crushed material.
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Raw Mill Closed View
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ID Fan Attached
with Raw Mill
Conditioning
Tower Bins, and
air inlet and outlet
flow through raw
mill.
Side View of Electrostatic Precipitator.
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A Complete Side view showing EP, Conditioning Tower & Preheater
Image Showing CF-Silo and Raw Mill Area
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Coal Mill is also present nearby which produces RDF and then convert
this coal into powder form before feeding it into Kiln. Coal mill has
following specifications
Coal mill grinds coal in
powder form and then feed
to pre heater which is the
next section of plant before
Kiln.
Image below is
representing main coal
storage and feed section
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KILN-ZONE
(a)Pre-Heater Section:
It is the main section before Kiln
where calciner is present, in this
section pre burning of (fuel+RDF)
takes place. Here the temp of
grinded mixtures reaches up to
850C. In this section there are
five diff zones of temp starting
from 150 and moving downtowards 850 in the final zone of
pre heater. Coal is burned in the
bottom of calciner while hot air is
sucked upward through fan and
different reactions take place as
the material falls down. Image is
shown and we can see that raw
material is feed to pre heater
through bucket elevator and the
zone is placed before
kiln.
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(b)KILN Section (Heart of Plant):In this section hot material from pre heater having temp 850C approx. is
feed to main Kiln. It is two support Kiln and is a friction drive having two
main driving wheels placed on four rollers, during combustion it keeps on
rotating to prevent any damage and a 500KV motor is driving the gear unit
of Kiln which consist of planetary and helical gears. Half sleeve bearing is
used to support Kiln shaft. Kiln has following main zones of temperature
(i) Calcining Zone(800-1200)(ii) Burning Zone(1200-1600)(iii) Cooling Zone(1600-800)
Kiln has revolution (0.2-4) according to requirement and has weight of800Tons. Kiln is made up of structured steel lined inside with refractory
material to sustain max temp.
Above pic explaining all data regarding Kiln. Kiln is not straight but
has 3.5% slope which is almost 2 for flow of paste material. When
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raw material goes to Kiln hood where remaining 40% fuel burning
take place. On the other end of the kiln, there is huge burner having
a supply of coal, furnace oil and air. The burner emits a flame which
is prolonged with high pressure air. The flame burn the material and
the product is formed and the material is converted into paste like
form. Cooling fans are attached with Kiln to decrease the surface
temp at required level as shown above. From Kiln Hood material is
transferred to Fuller or Clinker Cooler section.
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ABOVE PIC SHOWING KILN HOOD
CLINKER COOLER
The clinker cooler is used to lower the clinker temperature. There
are 10 ID fans five on each side which take fresh air from theatmosphere and send it to the cooler. At the bottom of the cooler
there are reciprocating rails which move with the help of hydraulic
motors. These rails convey the clinker forward to the clinker
crusher. In the end of cooler steel chains are present which prevent
the material from coming back after striking the crusher because
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there is a chance of refractory material due to strike of large particles
total 4 sections and coolers is purely hydraulic drive 75mm each
plate can move to and fro. They are easy to assemble and operation
is quiet safe and time saving. In clinker crusher section there aretotal 69 Hammers, 23 hammers per shaft of the rotor and having
weight of 60Kg each. After cooler section the material moves
towards main Clinker Silo having 110,000Tons capacity. The
crushed clinker is dropped on the deep pan conveyor at the bottom
of the conveyor which conveys it to the clinker storage. The clinker
from the deep pan conveyor is stored in the clinker storage. Its
capacity is 110,000 tons. Its length is 60 m and its width is 46 m.There are 3 gates at the bottom of the clinker storage from where the
clinker is sent to cement mill through belt conveyor. Besides the
main clinker storage bin, there is a temporary clinker storage hopper
with a capacity of 1400 tons. If the temporary hopper is also full
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then the clinker is removed from the hopper and dumped into clinker
storage yard.
Cement mill feed area:
There are 2 cement mills and 6 hoppers (3 for each mill) in the
cement mill feed area. The 1st hopper contains the clinker which is
major constituent of the cement. The cement contains 95 % clinker
which is conveyed through weigh feeder to the main belt conveyor
which takes it to the cement mill.
Gypsum addition:
The crushed gypsum from a separate crusher is conveyed by belt
conveyor to the cement mill. It is mixed in the clinker while
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crushing. Gypsum is added to about 45 %. Its purpose is to increase
the settling time of the cement.
Mixing of additive:
The additive which is pure limestone is also added in the cement
mill. Its added to about 2 %. Its function is to increase strength of
cement.
Metal Detector:
To protect the cement mills from damage, a metal detector is
installed which analyzes the feed and if a metal object is found itopens the dividend gate automatically and sends the feed containing
metal objects to the rejected bin, which is again recycled to the main
belt and magnetic separate removes it.
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CEMENT MILLS AREA
Cement mills specifications OK 36-4:
The feed which is free from impurities falls on
the table of cement mill which contains three
rollers. Each roller has weight of 35 tons and
the clearance between table
and rollers is 0.5 mm. These
rollers move hydraulically
using nitrogen gas as
hydraulic fluid. The rollers
crush the feed to a very fine
powder. The air slides
conveys the ground product to
the bucket elevator which liftsit to enter into the 1st storage
silo and so on.
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Separator present Inside Cement Mill.
Storage Silos:
Specifications of storage
Silos:: 22,000 tons
: 45 m
: 22.4 m
There are 3 cement storage
silos in which crushed
cement is stored up tillpacking. To convey the
cement to the other 2 silos
air slides are used. From
these silos the cement enters
air slides by air circulations
through blowers. Now these
air slides take the cement to
the packing plant.
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Schematic view of silo: The old
cement was blocking the air slides
as well as bridging preventing the
flow of cement from the silo.
Sockets installed above discharge
gates and lower air slides proved
the ideal solution to blocking of
silo and can be used whenever
there is build-ups.
Packing Plant:
The packing plant comprises of 6 packers and 12 terminals. Each
packer has a capacity of 100 tons/hr. Each Packer has 8 nozzles and
shooting of bag on these nozzles is done by shooters which are latest
techniques applied over there. Also manual installing of bags on
packing is done through workers. Alarm is attached with each
packing unit so that it can be turned on whenever there may be ademand of cement. From slide bars the cement falls to hopper
through screen to remove any impurities. There is a weight sensor
attached with each packing unit which dispose of any bag having
weight more than 50.5Kg or less than 49.5Kg. A blower is present
which removes dust present on cement bags. Nylon and paper bags
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are used according to requirement and they have valves made up on
the top side for automatic sealing.
The cement bags are attached manually to the rotating packer whichfills the cement bag. When the bag is filled up to the required weight,
it automatically falls on the conveyor belt which takes the bags to
the roller conveyor. From these rollers the bags slide to different
channels and finally cement bags are loaded on the trucks for
dispatch.
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DISPATCHING SECTION
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Some Important Installations In DG-Cement Plant For Dust Control:
Bag Filter :The dust produced by crushing process can cause damageto the equipment and may produce dust, to overcome this problem a bag
filter is employed. A fan blows air and all the dust goes to the bag filter. Inside
the bag filter a special type of canvas cloth is used. When air passes through
this filter cloth, the dust particles stick to the cloth and clean air passes
through. The dust particles are then collected and sent to the conveyor. After
sometime when the filter is choked with particles, Purging system is used
in which high pressure air is used, this air removes all particles from the
filter cloth.
Electrostatic precipitator :
The clean air from the conditioning tower still contains some particles which
have to be removed. These particles are separated from air by passing it
through the
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In Electrostatic precipitator there are 2 corona wires which are mesh like.
These wires are negatively charged. There is a positively charged electrode inthe center which is equidistant from both corona wires. Dusty air passes
through these corona wires and the particles get negatively charged. The
negatively charged particles in air are then attracted by the positively charged
electrode and the particles stick with it and clean air is exhausted from the
chimney. In order to remove particles from the electrode. A Wrapping
device is used. This device hits the electrode as a hammer and particles fall
down from it. These particles are collected and conveyed to the CF silo via
screw conveyor.
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References:
www.sick.com/.../cement/Pages/cement.aspx
www.siamrefractory.com/cement_cyclone.php
www.freepatentsonline.com
www.DGcement.com
Report Prepared By:
Aitazaz Ahsan 10-ME-04
Mechanical Engineering Department UET Taxila.
DG-Cement Internship 2013 Phase-III
Contact 03035500424
http://www.freepatentsonline.com/http://www.dgcement.com/http://www.dgcement.com/http://www.freepatentsonline.com/