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FINAL INDUSTRIAL INTERNSHIP REPORT [Wonji/Shoa Sugar Factory] 1
CHAPTER 1
1. INTODUCTION
1.1 Location and Foundation of WSSF
Wonji/shoa sugar factory is located at southeast of the country and far from Addis Ababa
110km at Adama-Asalla road. This company is founded by kaizen in 2011. But wonji/shoa
sugar factory produce sugar at the wonji town that is the upper reach of Awash Ethiopia
112km southeast of Addis Ababa after taking the land of nomads in 1951, Ethiopia
government granted a concession of 5,000 hectares. For increasing demand of sugar in
Ethiopia, the wonji estate expanded to include an addition of 1,600 hectares of land from
shoa, about seven km from wonji town. The wonji/shoa sugar factory started sugar
production in 1962.
The late king Haile-selassie described this large-scale commercial investment in Ethiopia that
could very well make Ethiopia self sufficient in sugar production and exports to its
neighbouring countries. Emperor Haile-silassie further claimed that with the crushing
capacity of 1600 tonnes of canes per day. Wonji/Shoa sugar factory started as joint venture
between the Dutch, Handlers-Vereeniging Amsterdam (HVA) firm and the Ethiopian
government. The HVA owned about 90 percent of sugar plantation and while sugar factory
owned only 10 percent. Also in its operation of sugar factory, HVA remitted 10 percent of the
invested capital and 15 percent of the annual profits to its headquarters.
With the change of government in 1974, under pro-clamination No 31 of 1975, all the sugar
factory in Ethiopia became nationalized and administered under the centralized bureaucratic
administration of the new military government. Though; the Wonji Company was very
productive until the 1980’s, It eventually stagnated because of the atrocities and red terror
committed by the military government causing competent and effective workers to leave the
factory and run for their lives.
Finally, in 1991 as the ensuing civil war completely devastated the authoritarian apparatus of
the military administration in Ethiopia, the sugar corporation was dissolved by law and all
existing factory were re-established as public enterprise to be run by the Ethiopia sugar
development agency starting in 1992. To revive the sugar industry, the Ethiopia sugar
development agency was formed as a share company of the development bank of Ethiopia,
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Ethiopian insurance company and then the existing of three sugar factories (i.e. Wonji, shoa
and metehara) in 1998. Furthermore, under the Council of Regulation Minister’s (No.
192/2010), in 2010. The current Ethiopian sugar corporation was then formed replacing the
sugar development agency.
1.2 Purpose of establishing sugar factory
The most conspicuous reasons for the establishing of sugar Corporation were to:
Grow sugarcane and other yielding crop
To fulfil social need of sugar in the country
Process and produce sugar, sugar products and sugar by products
Sell the products and by-products in domestic and export market
Encourage and supports the sugarcane grower who supply their cane
Cooperate with educational institutions to produce the required type, number and
quality of trained man power for the sugar industry (sugar corporations and Ethiopian
sugar industry profile March 12, 2013).
1.3 Relation of WSSF factory with other sugar factory
The Wonji/shoa sugar factory Corporation is currently carrying out expansion projects within
the existing sugar factory at Metehara, Finchaa, Tendaho and other additional sugar factories
like Beles in the centre of Amhara region, Wolkait in northern Tigray area, Kesem in the
north-eastern of Afar regional state, and six more factories in the south omo zone of the
southeast Nation nationalities and peoples’ region.
1.4 New wonji/shoa sugar factory
This factory to become self-sufficient in sugar production by the end of 2013 and diversify
the products of sugar cane into ethanol, electrical power, fertilizers, and build tissue culture
laboratories, the corporation is visualizing creating the sugar industries to be competitive
enough to maintain a sustainable growth pattern at the international level. In order to develop
trained and disciplined employees the Ethiopian sugar corporation is instructing its
employees in the use of Japanese philosophy of continuous improvement by applying
kaizen’s processes and technology to improve the company’s production culture and
leadership. Kaizen corporate culture is a continuum off resolving cycles of continual,
dynamic and self-motivated practice in the quest of recreation of self-disciplined and self-
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innovation organizations. It also is conductive to realization of human potential of all
members of the organization (Minister of Industry, 2011).
To implement kaizen, about 7,537 members of leadership at various levels and staffs of the
corporation and sugar factory have been trained on kaizen, quality control circle (QCC), the
seven types of waste , their causes and their preventive measures and their application
methods. The country plan to increase the sugar production of sugar from 314,000 tons in
2009 to 2.25 million tons in 2015 and 1.25 million tons of sugar and sugar related factory are
to be exported (Minster of Industry , June 2011).
1.5 Main products or service of WSSF
Wonji/shoa sugar factory is mainly depends on agricultural of sugar cane as raw materials
and produces output likes;
White sugar,
Final bagasse,
Electric power and
Final molasses.
This the main supply from the factory, but there are many by-products which is use for
different uses. Example from bagasse, it produces steam in boiler, writing paper, fiber board,
newsprint produced in other factories.
1.6 Main customers or end user from WSSF
Wonji/shoa sugar factory have different plants whose have own purpose; like milling house
plant (input of sugarcane, output of final bagasse and raw juice), clarification and evaporation
house plant (input of raw juice and steam, output of syrups), steam generation house plant
(input of treated water and final bagasse, output of steam,) power generation house plant
(input of dry steam, output of electric current) and pan house plant (input of steam and
syrups, output of sugar and molasses). Those output from different plants have their own
costumers like;
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Customers of white sugar (from pan house product)
East Africa (coca cola company)
Moha soft drink factory (Pepsi company)
FAO (food and agricultural organization) the united nation
MEWIT (JINAD) which distribute white sugar to the whole market
of the country.
Customers of molasses (from pan house product)
Belazaf alcohol and liquors factory
Desta alcohol factory
National liquor and alcohol factory
Customers of final bagasse (from mill house)
Tendaho sugar factory for boiler
Customers of electric current (from power generation)
Ethiopian Electric power associated (EELP)
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1.7 Overall organization and work flow
Fig. 1: overall organizational work flow
Management
board
General Manager Internal audit
Executive assistant
to general manager
Public relation estate
and environmental
service
Project implementation
and productivity
improvement
Legal service
Management and improvement
service productivity
Commercial
department
Factory and
logistics
division
manager
Agricultural
operation
manager
Finance and
Human
Resource
Manager
Wonji technical
Wonji process
Shoa technical
Shoa process
Logistics department
Confectionery works
Plantation
Dept
LPCD Dept’
Harvesting
dept
Field
equipment
service Dept
Civil eng.Dept
Finance Dept’
Human
resource
department
Medical
department
Secretary
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CHAPTER 2
2. OVERALL INTERNSHIP EXEPRIENCE
2.1. How we get in to WSSF
Fig 2: company profile vew
During the end of 3rd year, we collect the internship paper from the department and taking to
wonji/shoa sugar factory at a summary vacation. Wonji/shoa sugar factory confirming our
internship letters request and appreciation to learn during staying in company by dividing
students into different plants, day to day follow up, activities of industries like operation,
maintenance and repair. This helps as by increasing our knowledge and identifying the
problem with appropriate solution.
2.2. Section/plants we allowed to learn in WSSF
In our staying in the WSSF for internship duration, we work on the whole company that are
related to our field and supporting to our project design. But the factory supervisor is
restricted to four plants for four months. Those are:
Juice extraction (milling) plant
Clarification and evaporation plant
Steam generation and power generation plant and
Pan and centrifugal plant
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Fig 3: processes take place in sugar factory
2.2.1 Juice extraction (milling) plant
The main purpose of juice extraction plant is well extraction of raw juice by mill and separate
from final bagasse. This final bagasse has no content of sugar.
Also in this plant there are many machines that are use for different purpose from preparation
of cane to raw juice and final bagasse produce. Those are like;
Cane trucks: this is by lifting the whole vehicle on a tipping platform with the rear gate of
the truck swinging open to allow the cane to discharge into a feeder carrier
Spiller tables: cane is often discharge from large vehicles into elevated feed conveyors
which are wide as the length of the truck or trailers.
Kicker or tumbler: is usually fitted at the top of the feeder table before the cane discharge to
cane conveyor. This consists of a slowly rotating shaft that the cane fails smoothly off the
discharge end avoiding a heavy fall of a large mass of cane.
Cane conveyors: there are many types of cane carries like apron, belt, chain and slot
carriers. They are used to conveyor the cane from the feeder tables to mill.
Magnets: it used almost impossible to prevent the entry of tramp iron into the system.
Removal of tramp iron in this way pays for itself very quickly, since the damage caused to
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cane preparation equipment and mill roll can be severe leading to increased downtime and
reduce recovery.
Cane knives: it is driven by electric motor that is used to reduce the height or size of the
piece of cane to the size suitable for handling in the extraction process.
Mill conventional: refers to mill feed and discharge rolls at a common level and vertically
floating top cells. Although some variations was proved successful.
Head stocks: is to maintain the working element particularly the roll in their desired
orientation.
Mill roll: are usually constructed of a shaft of steel, on to which is shrunk a cast iron shell.
Fig 4: mill roll
Mill bearings: the majority of mill bearing are of hollow (ported) construction, either cast
entirely of bronze or comprising a steel housing with a bronze using.
Lubrication: the maximum permissible bearing pressure for bronze bearing is usually 9 to
11mpa, depending on the design and lubrication.Roller bearings: alternatively to bronze
bearing is spherical roller bearings;
low friction
no cooling water needed
no wear of roller journals
reduced roll length between centre (lower bending stress)
Tolerant of small misalignments.
Mill drives: power absorbed by a mill depend on many factory
The crushing rate (power and fibber throughout)
The mill speed (power and fibber x torque)
Mill configuration (no, size and arrangement of roll)
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Power lost in bearing
Mill feed method
Mill setting and the hydraulic load on the top of roll
Rotary juice screen: wedge bar type rotary screen for screening unstrained containing 50%
suspended solid/fine cush cush particles. Rotary drum juice collect trough and other parts in
contact with juice shall be SS304. Rotary juice screen shall have auto cleaning system with
water and steam periodically.
Sprockets and supports: if the inter carrier is also to serve as a mill feed roller, the slats will
generally required additional support around the head pulley.
Fig 5: sprocket and the chain
Chevrons: are notches cut into top of mill to assist feeding the bagasse through the mill.
Donnelly chutes: Donnelly observed that the angle of the bagasse feed plate into a mill has a
marked effect on the pressure and hence on the friction grip of the bagasse on the feed roll.
Pusher feeders: are mechanical device designed to forced bagasse into a mill. They are drive
by an electric and have a reciprocating action.
Imbibitions: in order to extract as much as possible of the sugar which it retains, it is
therefore necessary to restore to an artifice, since this moisture contents cannot be made to
replace by water the juice comprising it.
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Fig 6: juice returning, screening and imbibitions process
Bagasse conveying:
a) Bagasse belt conveyors: the most convenient and cost effective means to convey
bagasse is by conventional troughed belt conveyors. This belt is used to elevate
bagasse at inclinations of up to 23o from the horizontal, provided that the feed
arrangements are suitable.
b) Bagasse chain conveyors: for bagasse conveyance, chain and slat conveyors are more
costly initially and in maintenance than are belt conveyors of equivalent capacity.
Their use is usually confined to applications where belts are not suitable. Example
are:
Where elevations steeper than 23o are required.
Where multiple off takes are required.
Where bagasse is transported in both direction.
For feeding bagasse in to boiler chutes.
Bagasse feeding to boiling: for satisfactory boiler performance, bagasse must be fed reliable
at high rate into narrow enclosed chutes, keeping them full without chocking or generation
excessive dust.
Juice recycling: apart from the first mill, the juice from the first extraction stage of a mill
(e.g. from the pressure feeder of a pressure fed mill or the first roll of a four roll mill) is
generally of lower brix than the average for the mill. Recycling can be usually be taken to
saturation of the feed materials, which is a wetness level of 500% to 600% on fiber, beyond
which there is no benefit to be gained.
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2.2.2 Clarification and evaporation plant
The aims of clarification are;
To form floes to trap all suspended matter which can be at satisfactory rate
To produce clarified juice of high quality with a minimum turbidity, colour, and a low
calcium contents.
The aim of evaporation also;
To remove water from juice up to desired brix and to thick juice or syrup without any
change in sugar and reducing sugar.
To maintain clarified juice PH around (7±1)
Some machines used in these plants are:
Juice mass flow measurement: it is commonly practice to employ batch scales to measure
the mass of raw juice produced. Because of most other metering device do not approach the
same accuracy.
Batch scales: a batch scale system consists of supply tank above a weight hopper, which
accept batch of juice and records the mass before discharging. The weight hopper is tarred
before accepting a new batch. This weight hopper is supported on three or four load cells to
record the mass.
Juice pumping: raw juice contains some sand and fibrous bagasse particles and is abrasive
and corrosion. To specify the pump duty, it is necessary to know the average and maximum
flow rate to be pumped including filtrate return, as well as the head on the pump under both
conditions.
Fig 7: juice pumping
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Pump selection: the total pump head required is made up of the following.
The difference between liquid levels on suction and discharging sides.
Any difference between vacuum and/or pressire on the inlet and outlet side liquid free
surface
friction i.e. the head required to overcome resistance to follow through pipe and
fitting
pressure drop across the control valve
head loss through equipment such as heaters in the system
The velocity head at final discharge.
Plate heater: the plate heater is a pack of thin plates arranged in a frame so that the space
between each alternative plate is open to the same fluid.
Flashing: the purpose of flashing is to force outlet the air presents in the juice, to cause the
bagacious particles to burst and then sink with the flock and to insure constant flashed juice
temperature. A practical check on flashing is to observe the vapour coming out of the flashing
tank vent, if there is no vapour than flashing is not taking place.
Filtration: the clarification process separates the juice in to two layers;
The clear juice, which rise to the surface.
The mud which collects at the bottom.
The clear juice goes to manufacture that is direct to evaporation. But the mud has first to be
filtered, in order to separate from the juice the suspended matter which it contains, with the
absolute salts formed and the fine bagasse entrained with them.
Flocculated mud settles in the clarification process in the lower layer and the under flow is
removed at a steady rate. The mud has then to be filtered to recover the juice from the soil
and mud solids, mostly with the addition of fine bagasse particles, known as bagacillo, as a
filtration aid. Filtrate is returned to the juice heating system.
The operation of the mud withdrawal from the clarified compartment is regulated by the
operator to keep the mud upper level in the clarifier close to a desired target. Various aids to
the operators have been used. These involve variable speed mud pumps, and draining off the
mud for timed periods, combined with maintaining a constant level in a mud-receiving tank.
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The advantage of filtering is only mud derived from weak juices: hence also the advantage of
substituting water for the juice in the cake, by washing, and by carrying the washing as far as
possible.
The disadvantage of this type of filter is overload the clarification station. When the latter is
working near the limit of its capacity, it is undesirable to increase the volume of the jiuces,
and consequently their speedof circulation in the clarifier, by a fraction which represents
approxmately.
Fig 8: Oliver campbell
Evaporation:
The clarification process has given a clear juice. This consists of sugar dissolved in water,
together with certain impurities. Now that we have removed the impurities as far as possible
it remains to remove water.
Pre-evaporators: refers to an evaporator that is dedicated to vapour bleeding. Juice
from the pre-evaporation feed the first effects that use exhaust steam for evaporation.
Optimum operating condition: the best performance from an evaporator set is
obtained when it is run as steadily as possible. This is generally achieved through the
use of automatic controls.
Effect of superheat: if the superheat is excessive, it is possible for the heat transfer
rate to be affected adversely. In this case a significant proportion of the heat transfer
has to take place from the vapour phase to the tube surface, rather than by the far
more rapid form of heat transfer in condensation.
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Flash pots: if vapour flashing is to be practiced, the condensate is usually collected in
a receiver or flash pot, which has to be sized to permit the flashing to occur without
re-entraining too much liquid.
Syrup pumping: because syrup is extracted from the last effect at its boiling point,
the NPSH (net positive suction head) available on the pumps may be low. In addition
is common to install a strainer on the pump station, which, if it blocks; introduces a
suction line pressure drop that makes the situation worse.
2.2.3 Steam and power generation plant
The aim of steam generation is;
To produce steam from boiler by burning of dry bagasse in furnace and heating
treated water in boiler.
The aim of power generation is;
To produce electric power by steam that is produced in steam generation plant in case
rotating turbine for the factory and for other customers like ELPA.
Steam generation plant
The amount of steam generated from bagasse depends on the efficiency of the boiler. The
pressure at which the is generated and the calorific value (determine by moisture and ash
contents) of the bagasse.
The amount of bagasse lost in the raw juice and the filters depends on whether milling or
diffusion is being practiced.
Some machines used in this plant are;
Bagasse distributors: because of its low density and high drag coefficient bagasse is best
distributed pneumatically rather than mechanically in to furnace.
Fans: a boiler to operate successfully it must have enough grates to allow the fuel to be
burned efficiently and enough fan capacity to provide the air required to complete
combustion and exhaust the products of combustion from the unit. Four types of fans:
o Primary air fan: supply hot air to the underside of the grate
o Over fire air (OFA) fan: supplies the additional air required to combustion.
o Induced draft (ID) fan: exhausts the products of combustion from the boiler to
atmosphere
o Distribution air fan: used to convey the bagasse in to the furnace
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Furnace: has to be equipped with a fuel feeding system, an air distribution system and an ash
removal system.
The grate: in step grates, combustion takes place on the steps. The dead plate which
precedes them serves to remove the excess moisture from the bagasse before it comes to the
grate. The ash grate which follows the steps grate serves to complete the combustion and
utilise the heat transmitted by radiation from the incandescent bagasse the ashes are dropped
in to the ash pit.
Heating surface: the heating surface comprises that of the boilers tube and the tube of water
walls, when these are provided. The total heating system/surface has no great signification in
modern boilers, an account of the difference in rate of heat transfer existing between the
difference components of the boiler units.
Boiler bank: the steam drum and boiler drum are connected by a set of tube are called bank
tubes. The boiler bank is almost a convection heat transfer section.
Air pre-heater: air heater can be successfully employed to recover heat from flue gas at
lower temperature level than is possible with economizer. The heater rejected chimney can be
reduced to higher extent thus increase the efficient of the boiler.
Deaerator: the solubility of oxygen, air and carbon dioxide in water is a function of the
water temperature. Deaerators use steam for clear water for boiler.
Feed water treatment: dosing should take place as far upstream as possible to protect the
pre-heater system as well.
Steam usage: process steam usage of the cane mill depends on such factors as cane crush rate,
number of evaporator effects target sucrose extraction and hence imbibitions % fiber and use
downstream evaporator vapour for pan and juice heating.
Power generation plant
To optimize mill electricity generation, the following parameters must be considered:
process steam demand
bagasse availability for fuel
factory electrical demand
irrigation power requirements
electricity sale price
cost of supplementary fuel
emergency power sources
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Steam turbines: steam turbines take in steam at relatively high pressure and temperatures
and exhaust the steam either to process, or in some cause to a condenser operating under sub-
atmosphere pressure. For a constant Steam flow through the turbine (i.e. no steam bleeding),
the difference in total heat per unit mass (specific enthalpy, KJ/Kg) at the steam inlet and the
outlet of the turbine. Represents the energy extracted from the steam in the form of
mechanical work, used either to drive a mechanical load, or to drive a rotating alternating
current generator.
Impulse or impulse-reaction turbines: steam turbines are either “impulse” or “impulse-
reaction”. There are no pure reaction turbines.
In an impulse turbine, the steam pressure is caused to drop across stationary nozzles,
generating high steam velocity with increased kinetic energy. This high steam
velocity steam impinges on moving blades which extract the energy by reducing the
velocity. There is no pressure drop across the blade moving. This turbine is simpler
and cheaper because there no pressure sealing across the moving blades. The
efficiency of this turbine is around 84%.
In an impulse-reaction turbine, which is always multi-stage, there is a steam pressure
drop across both the fixed and moving blades. This turbine is more efficient because
there are more stages of steam pressure drop, each of which has fewer losses. The
efficiency of this turbine is around 78%.
Transformers: transformers transform electrical power from one supply voltage to another,
with high efficiencies, typically 98 to 99%. Transformer must be operating within their
design limits as regards current, voltage and operating temperatures. Maintenance of
transformers also include elimination of oil leaks, maintenance of breather desiccant,
ensuring adequate cooling and most important, regulate oil quality checks followed by oil
drying and filtering.
Use for bagasse: excess bagasse may find very profitable use as,
Raw material for the manufacture of fire proofed insulating boards used for building
purpose
Raw material for the fabrication of paper pulp
Raw material for the manufacture of various solvents utilised in industry.
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2.2.4 Pan and centrifugal plants
The objective of centrifugal is also to separate massecuite from the surround molasses or
matter liquids.
The objective of pan house is also to obtain maximum amount of sugar syrup through
crystallization by concentration under vacuum in vessels. The crystallization stage in a sugar
house involves crystallizing as much as possible from evaporator syrup.
Crystallization in a vacuum pan continues until the point is reached where further
crystallization would result in a massecuite that stops circulating or that cannot be discharged
from pan. Massecuite leaving a vacuum pan is supersaturated and hot, in the range 63 or
75oc.
Feed tanks: syrup A and B molasses are usually stored in tanks on the ground floor, with
small feed tanks provides on the pan floor, from which the feed passes to the pans.
Vacuum seed receivers: are often provided on the pan floor provide flexibility in pan floor
operation. These vessels are normally cylindrical in shape, insulated, and with a horizontal
stirrer rotating at about 1min that scrapes close to the internal surfaces.
Strike receivers: these U-shaped horizontal troughs fitted with horizontal rotating stirrers.
The receive massecuite from batch pans on strike, and provide a buffer between the bath pans
and continuous crystallizers or centrifugals.
Centrifugal separation: after crystallization, the sugar crystals are separated from the
massecuite by centrifuging. Because of the nature of the mother liquor, particularly the high
dissolved solids content and high consistency, centrifugal forces need to be high, requiring
high speed machines.
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Fig 9: centrifugal separation
Centrifugal drives: is machines were driven by fixed speed motors or pole-changing motors
to accommodate the different speeds required for spinning, feeding and discharging.
Feed mixers: a horizontal feed mixer is usually installed close to the centrifugals, which are
fed from the mixer through one or more valves.
Washing: this is achieved by addition of water and steam. Because of the short time the
machine crystal dissolution is low. The extent to which the water and steam mix with the
mother liquor to reduce its viscosity and the extent to which the water and steam actually
wash the molasses film off the crystal is know.
Seed growing pan: the basic material used in the pan boiling is syrup of 50 to 65 % brix and
80-85% purity. The PH is also between 5-5.4. The brix of the sugar is assumed as 100%. As a
result the concentration of syrup to massecuite is from 60-100% brix. This is achieved by two
ways as below
o Concentration of 60 to 100% brix
o Formation of sugar crystal
Rotary cascade drier: is which has comprises a cylindrical drum, rotating at a slight slope to
the horizontal, running on steel rollers or cradles. The holdup of a rotary drier varies with the
feed rate, the number of flights, the shell diameter and the air rate.
Rotary louver driers: unlike the cascade variant, little design information has been
published on rotary louver driers, perhaps because they are designed by relatively few
suppliers, and the information is regarded as proprietary.
Screw conveyors: these devises comprise a central shaft running along the axis of a U-
shaped trough, with a screw or helical ribbon attached to the shaft. The greatest disadvantage
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of this type conveyor is that the sugar crystals may be ground between the screw and the
shell.
Vibrator conveyors: this operates on the same principle bit using high frequency vibration.
These can be enclosed (dust-free) but consume more power and certainly classify the sugar.
Twin conveyors: overcome the vibration problem of a grasshopper by oscillating two
identical units 180o out of phase.
Slip-stick conveyors; are a recent innovation, operating by means of a slow forward stroke
followed by a rapid return stroke. They rely on the sugar slipping on the return stroke to
advance the sugar along the conveyor.
Belt conveyors: are continuous belts consisting of several plies of fabric impregnated,
bonded and coated with rubber. These run on idler, spaced at intervals of about 1 to 1.5m for
the top, load-carrying strand and much larger spacing’s for the lower, empty strand. Belt
conveyors may inclined, does not recommend more than 22.5o for dry sugar. Prefers a limit
of 20o and recommends 16o. Belt speeds of 1.2 to 1.6 m/s are common, except for ship-
loading conveyors which can run at around 2.9 m/s.
Fig 10: sugar conveying belt
Bagging and packaging: sugar packaged into sack, bags and packages ranging in size from a
few grams to 1000kg. Bags for commercial customers are usually 25kg, 50kg and 100kg.
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2.3. The piece of work we have been executing
During the internship period, we were working in the preparatory section and loom shed. In
this group, we were working maintenance of different parts of the machines. The term
maintaining can be defined as something to repair or to bring functional which were non-
functional due to many problems. In this time, we were able to know different machine parts,
which we learned in the last seven semesters of our educations. In addition, we know how to
maintain machine parts and we can see the integration of mechanical and electrical machine
parts.
2.4 Procedures we have been using during performing our work tasks
The procedures we were following during our internship practice are-
First, we understand how the machines operate.
Then we ask the operators and maintenance workers how the work is to
be executed
And after that we try to do the jobs ourselves and if we get problems
which need further
explanation and something we don’t know we write down them and
discuss at our break
time and discussion time with our supervisor and try to know more
There were many textile activities, which are not concerned under
mechanical, and these terms were difficult to understand for us.
2.5 How we was good in performing our work tasks
As our supervisor told us and comparing, what we do with what we learn and with what the
other workers do, we were very nice. We were also punctual and well enter acted with the
workers. And the other thing that makes us to say we were very nice is we were not only
asking for our supervisor to know more but also we were referring different books and web
sites related to the department we have been working.
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2.6 Challenge we faced while performing our work
During the training in the company, we faced many challenges that influence our work. This
includes:
Number of student increase at one place
Sound of some machine can be disturbed
Load capacity on the supervisor
No internet coverage in the company
Environmental is also very hot
Some other student limitation of language
2.7 measures we take in order to solve the challenge
In order to solve those challenges we take some measure
Following day to day
Active participating
Gather information by interview and observation about machine in whole plant
Asking experienced technical documentary room
Referring manual document from different room
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CHAPTER 3
3. OVERALL BENEFIT OF THE INTERNSSHIP
After completing the training we gained many benefit from this internship program like the
following:
Improving practical skills
Upgrading theoretical knowledge
Improving its interpersonal communication skills
Improving team playing skills
Improving leadership skills
Understanding about work ethics related issue
Entrepreneurship skill
3.1. Improving practical skills
Wonji/shoa sugar factory is a huge company in our country that produce sugar for the
costumers. So it goes in different process and plants. Due to this complex process there is
some linkage, broken of machine, corrosion, bending and disassembling are occurred.
Therefore, to solving this problem there are many ways taking like welding, assembling,
engaging and disengaging of the gear, valve, pump, pipe and tanks. Also how hydraulic and
pneumatic system is worked.
So, we really understanding by seeing, sharing aid with the operators of that place and also
working with them practically. This encourages as increasing our confidence to operate the
machine by itself.
3.2. Upgrading theoretical knowledge
Theoretical knowledge is prerequisite for practical provision of recommendation for
maintenance activities. For examples,
Pump selection: the total pump head required is made up of the following;
o The difference between liquid levels on suction and discharge sides
o Any difference between vacuum and/or pressure on the inlet and outlet side liquid
free surfaces
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o Friction, i.e. the head required to overcome resistance to flow through pipes and
fittings
o Pressure drop across the control valve
o Head loss through equipment such as heaters in the system
o The velocity head at final discharge
Bearing selection: the following consideration takes place for selection of bearing
o Low friction
o Minimum lubrication use and no contamination of juice
o No cooling water needed and no wear of roller journals
o Tolerant of small misalignments
o Reduced roll length between centres (lower bending stress)
Valve selection: to select the exact valve for replace or change must to know
o Valve weight
o Valve stroke
o Valve opening orifice area (A0)
o Valve cross section area (Av)
o Friction loss at delivery and waste valve
If pump is stop working it should be replacing by other pump. During replacing some
consideration should also take place like, pressure of suction side and discharging side, types
of pump we selects, speed of rotation and number of impellers and size of the pumps.
Therefore upgrading theoretical knowledge we applied our skill at real world practices
without any confusion.
3.3. Improving interpersonal communication skills
Wonji/shoa sugar factory has different plants from cane transporting to sugar story house.
This is done by its group of workers in different plants. During their team works they are
communicating to each others, putting idea if some problem was occurred and supporting
their idea for solving the problem.
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Communicating to each other’s is facilitating their jobs and increasing the productive of the
sugar supplying for their customers. Therefore we can also gained many wisdom from
company worker by asking and changing idea to each other.
3.4. Improving team playing skills
Working with group is the one which facilitate the productivity of the factory. So we improve
the team working skills by discussion with our supervisor and his colleagues in different
action and solving problems. This team playing skill is that necessary in all anyway, because
one support others to increase their productivity in all case. So we can improve the team
playing skills by decision making in group where some problem are exists.
3.5. Improving leadership skills
In WSSF there are many work flow in different plant from company manager to the last
labour that decrease the load on someone and this increase the company profited. From this
we ensure the following improvement:
Ability to solve problem quickly
Understand behaviour of the worker and manage them properly
Facilitate the new idea from this colleagues and making decision
3.6. Understanding about work related issues
To fulfil of the goal one product, ethics has its own advantage. Because, in any company if
there is environmental health, work division, enough material and no corruption the
productivity and supply of the company is increase. We also gain this work ethics during us
staying in WSSF. Therefore we also some work ethics like
Punctuality
Keeping rule and regulation of the factory
Safety first
Honesty
Accountability and transparency
Responsibility
Polite communication with manager and colleagues
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3.7. Entrepreneurship skill acquired
Entrepreneurship is the process of creating something new with value by devoting the
necessary time and effort, assuming the accompanying financial, psychics and social risks
and receiving the result reward of Monetary and personal satisfaction of independency. This
is gained by the following characteristics.
Low fear of failure
Self-confidence
Use of feed back
Use of resource
Clear goal setting
Internal locus of control
Long term plan
Therefore from the above characteristics we acquired the concept of the entrepreneurship for
putting idea of new creation or modifying the existing material for increasing the capital of
the individual and members.
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CHAPTER 4
4. PROJECT DESIGN
4.1 PROBLEM IDENTIFICATION AND THEIR PROPOSED
SOLUTION
In WSSF, the corporation between the worker is solve more problem occurred in the
company. But some problem occurs at different place/plants. We are also identified at least
four problems that is available in this factory:
Steam pipe: This problem is occurred in steam generation plant. The pipe use in this
plant is not well give function. Because of pressure drop across the pipe, steam was
leaved pipe. The longer distance has flow, the lower velocity we shall choose for the
steam, so as to avoid excessive pressure drop.
Bulk pile storage of bagasse: In wonji/shoa sugar factory, this problem is occurred at
final bagasse storage area which discharged from mill plant, Because of the large area
involved this usually means storage in open air. Pile management of the company
becomes important in maintaining sloping piles and ensuring that no dams from
which can catch and hold water.
Conveying problem: In the company material/product are conveyed by the belt at
many areas. This belt is repeatedly failed and material is stored for long time without
giving function. So we have an idea to change this conveying by chain that has long
life without any fail.
Ash conveying belt: This problem is occurred in steam generation plant that after
bagasse is burned in furnace and the waste of bagasse ash and smoke gas are to be
discharged. Smoke gas is taking to chimney to release the gas to outside or
environment. But ash is taking to discharge by means of belt. This belt is usually out
of function because of the burned bagasse has maximum temperature. So the
concerned company manager take to solve this problem by take the minimum
reduction with belt to fall and increase the belt quality to resist heat of ash.
So from the above problem those occurred in the WSSF, we select “design of roller
conveying chain” to solve the problem of material conveying from one place to other place.
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4.2 PROBLEM SELECTED (ROLLER CONVEYING CHAIN)
4.2.1 Introduction
Roller conveying chain is mostly preferred in sugar factory to transport goods like sugar by
sack. This roller conveying chain is to solve the problem occurred in the factory that the
sugar sack is conveying to the sugar storage area..
Belt conveying has the following problem:
It has more linkage
Has maximum slip due to smooth surface
Fails under high temperature
Low carrying capacity i.e. convey only 50kg per meter length
Therefore roller conveying chain we design has the following advantage over belt conveying:
Carry heavy load i.e. 100kg per meter length
Discharging rate is maximum
Required low human power and low cost
Operate at high temperature
Reduce the labour and time of convey/transport
Low maintain
Long life
Has no linkage, slip and failure like a belt
4.4.2 Design analysis
Drive end: Apply driving power to the discharge end of a conveyor so that only the
carrying run is under maximum tension. Apply power to the head sprocket through
another chain and sprocket.
Pre-tension and take-ups: Provide take-ups in all conveyor installations to ensure
slack for installation and maintenance and to compensate for elongation due to wear.
Install the catenary take-ups at the head end of the conveyor; install all other take-ups
at the foot or loading end of the conveyor.
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Points to consideration
1. Ensure that chains always engaged with at least three sprocket teeth
2. For long conveyors use take-up devices to eliminate chain slack. Take-up
stroke = (c*0.02) =S
Where: c = center distance between sprockes
S = catenary sag allowance
But this equation is for conveyors longer than 50ft.
Long shaft centre distances: For unusually long shaft centers, either use two
conveyors with a transfer point or use bearing roller chain.
Return chain supports: On chain conveyors more than fifteen feet long, support
the return strand on a track or guide to minimize pulsation and whip and to prevent
the sagging chain striking obstacles
Operating temperatures: Standard conveyor chain can be operated normally in
ambient temperature between 150F and 1400F. Select the appropriate chain for
condition out of this range, including operation in freezing chambers or heat-treatment
ovens.
4.2.3 Material selection
The material selection for our design has the following consideration:
Availability of material
Low cost
Suitability of the material
Easy replaced/maintain
We take material selection from appendixes table 1.
The frame:
The frame is the basic component on which all the other component is tight on it. It used for
supporting the overall weight of the machine. This frame is 10m in length and 1m in width.
This frame is carry the weigth of the sugar conveyed up to 10 quintal of sack and the weigth
of the chain, sprocket, slat and motor up to It is made up of rectangular steel bar that
structure is shown as below.
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Fig 11: supporting bar
Slats:
The slats are where the product is carried on it. This slat is made up of light metal which is
resist the friction, rust and corrosion. This is shown below
Fig 12: slat
Nut and bolt:
Bolt and nut are used to tight the component of the machine together for have same rotation
and reduce sliding. Bolt and nut are shown as fig below
Fig 13: bolt and nut
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4.3 DESIGN AND CALCULATION
4.3.1 Design of chains
In the design of chain, some consideration takes place
No slip takes place during chain drive
It gives high transmission efficiency (up to 98%)
It transmits more power
It transmit horizontal convey
To simplify the design process, the following assumptions are made depending on the desired
geometry and shape of the machine.
Module, m =4mm
Diameter of sprocket 1 = sprocket 2 = sprocket 3 = sprocket 4 =650mm
Velocity ratio of the chain drive and sprocket is 1
Appropriate center distance for pitch diameter of 250mm, x = 10000mm
Rotational speed of the motor, N = 900 rpm
Rotational speed of the shaft sprocket N =60rpm
Power transmitted by the driven pulley is 12KW
Roller type chain
From these values, we calculate
Number of teeth for each sprockets, T1 =T2 =T3 = T4
T = ∏*D/p
T = ∏*650/250 = 8.16
T =8
To calculate the length of chain and number of chain
The length of one side chain, L = B*P, where B = number of chain of one side
To calculate the total length of the chain
L = 2*length of travelled + 2 (½ ∏*diameter of the sprocket)
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Diameter of the sprocket is Ds = P*cosec(180/T)
Where T = number of the teeth
P= pitch
Ds = diameter of the sprocket
Ds = 250mm*cosec (180/8)
Ds = 650mm
Therefore L = 2* 10000mm + ∏*(650)
L = 22041mm
We also calculate the number of chain
B = L/P
B = 22041mm/250mm
B = 88
From the appendix table 2; For roller type chain with the speed of the sprocket 60rpm, the
factory of safety for chain can be taken as, n = 7
Pitch line velocity of sprocket; V=∏*Ds*Ns/60=∏*0.65m*60rpm/60=2.04m/s
Load on chain W = rated power/pitch line velocity = P/V
W = 12KW/2.04m/s
W = 5.88kN
The total load of the chain, W =��
� ,
n = safety factory = 7
Therefore the breaking load on the chain is calculated as
Wb = W*n = 5.88KN*7
Wb= 41.16KN
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4.3.2 Design of sprockets
In the conveyor two chains and four sprockets are employed it is nprmal practice to keyway
the driving sprocket to the shaft as a pair. The teeth should be in line to ensure equal load
sharing. When a pair of sprockets is mounted on a shaft the long bosses of the sprockets
should be assembled so as to face each other, i.e. towards the shaft midpoint. This allows the
sprockets to lie close to the shaft bearing, giving maximum support to the load, while at the
same time required only the minimum width of conveyor structure.
Fig 14: sprocket
For the pitch diameter of 250mm and number of teeth is 8
The diameter of the sprocket is D = PT/∏
D = 250mm*8/∏
D = 636.9mm
Therefore from standard table we take diameter of each four sprocket is D =650mm
The torque applied on the tooth of sprocket is
Torque = chain pull x radius of the sprocket
Torque = W*r = 5.88kN*0.325m
Torque = 1.911kNm
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4.3.3 Design of shaft
Shaft is a rotating member, usually of circular cross-section, used to transmit power or
motion from one point to the other. It provides the axis of rotation or oscillation of elements
such as gear, pulley, flywheel, cranks, sprockets and the like. An axle is a non-rotating
member which carries no torque and is used to support rotating wheels, pulley, and the likes.
Types of shaft
Shafts are classified as follows according to their industrial application.
Line spindle: It is a shaft which transmits power to several machine elements.
Spindle: A spindle is a short revolving shaft. Example: head stock spindle, drill press spindle
etc
Stub shaft: a shaft that is integral with an engine, motor or prime mover.
Counter shaft: A short shaft that connects a prime mover to a line shaft of a machine
According to the application, shafts may be divided in to two types
Transmission shafts: these shafts transmit between the source and the machines adsorbing
power. Counter shaft and line shafts, over head shafts and all factory shaft are transmission
shafts. Since these shafts carry machine parts such as pulleys, gears etc. Therefore they are
subjected to bending in addition to twisting.
Machine shaft: these shafts form an integral part of the machine itself. Example: crank shaft,
stub shaft.
Shaft material: When greater strength is required, as in high-speed machinery, such as
nickel, or chrome vanadium steels are used. When resistance to corrosion is desired, some
copper alloys are used. The material used for shafts should be have the following properties
It should have high strength
It should have good machinability
It should have low notch sensitivity factory
It should have good heat treatment properties
It should have high wear resistant properties
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For calculation of design of shaft we select the plain carbon steel C-30 for all shafts from
appendixes table 1.
Having selected the size of conveyor chain required for a system, another important is the
diameter of the sprocket shafts. The head shaft takes the greatest stress and attention for
design.
We select two shaft one for drive and other for driver
i. Design for drive/head shaft
This shaft is subjected to two supporting bearing, force applied on the sprocket and also force
applied by transmission drive motor pulley.
Fig 15: Schematic diagram of drive shaft
For roller conveying chain the weight applied by sprocket is the summation of:
Weight of the total conveying sugar sack for 10m are 10 quintals per unit length i.e.
Wp = 10x100kgx10m/s2 = 10000N. But this weight is equal disturbed on four
sprockets equally, for each spocket weight = 10000N/4 = 2500N
The pulley shaft drive force by is 500N
Calculation of maximum bending moment
The maximum bending moment induced in the conveyor head shaft. From the diagram the
arrangement of two conveyor sprockets are located equidistant from the respective nearby
shaft bearing (40mm), whilst the transmission chain sprockets on the overhanging shaft, that
distant from the one end of the bearing (50mm).
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FP=500N 140mm FSC = 2500N FSD =2500N
A B C D E
FRB 100mm 900mm 100mm FRE
To calculate the maximum bending moment on the shaft, first calculate the reaction force.
Therefore to calculate the reaction force at point E we take the summation of moment at point
B is zero.
∑MB= 0
-500Nx140mm + (2500Nx100mm) + (2500Nx1000mm) - FRE*1100mm = 0
FRE = 2436N
To calculate the reaction force at point B, the summation of force along y-axis is zero
∑FY = 0
-500 + FRB -2500 – 2500 + 2436 = 0
FRB = 3064N
Therefore to calculate the maximum bending moment, for each section
Section AB
140mm ∑MB = 0
A B FV MB = 500Nx140mm
MB = 70000Nmm
The shearing force at point b is
∑FY = 0,
-500N + FV = 0,
FV = 500N
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Section AC
500N 140mm FV
A B C
3064N 100mm
∑MC =0
-500Nx240mm + 3064Nx100mm - MC =0
MC = 186400Nmm
The shearing force at point C is also
∑FY = 0
-500N + 3064N – FV =0
FV = 2564N
Section DE
∑MD = 0
MD -2436Nx100mm = 0
MD = 243600Nmm
FV D E The shearing stress along y-axis is zero
100mm ∑FY =0, -FV + 2436N = 0
2436N FV = 2436N
At point A and E the bending moment of the shaft is equal to zero and the maximum bending
moment is at point D that is 243600Nmm. So from the above data we draw bending moment
diagram
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500N 2500N 2500 N
A B C D E
3064N 2436N
243.6Nm
186.4kNm
Mb
70Nm
0
Shaft length in mm
Bending moment for driven shaft
Therefore the above diagram the maximum bending is Mmax = 243.6KN
Calculation of twisting moment (TORQUE)
Torque on the shaft is calculated as
T = 60P/2∏N = 60*12kW/2∏*60
T = 1910Nm
From equivalent bending moment
Meq = √(kbMb)2+(ktT)2 where kb and kt is 1 for stationary load applied
Meq = √(243.6KNm)2 +(1.91KNm)2
Meq = 243.6KNm
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From appendix table 7; Ultimate tensile strength for material we selected plain carbon steels
of C-30 is 550N/mm2 and yield strength is 300N/mm2
For the safety factory of 7
We know that the allowable tensile stress
���� = �����/� = 550mpa/7
���� = 78.57mpa
Therefore ���� = 32Meq/∏d3
d3 = (32Meq/ ∏����
d3 = (32x243.6Nm/∏*78.57*106N/mm2)
d = 0.0318m
d = 31.8mm
From the standard of the shaft diameter it take, d = 38mm
From equivalent twisting moment
The maximum torsion stress occurred is
���� =��
���x Te where � = shearing stress, Te = equivalent torque
d = diameter of the shaft
The torque transmitted by the shaft
T = Px60/2∏N = 12X60X103/2∏*60, T =1910Nm
The allowable shearing stress is equal to
���� = ��/2
���� = 300���/2
���� = 150Mpa
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From this the diameter of the shaft is calculated as
d3 = 16Te/∏ ����
d3 = 16*1910Nm/∏*150*106N/m2
d = 0.0401m
d = 40.1mm
From the standard shaft diameter we select, d =44mm
Therefore from the two equivalent moments the maximum shaft diameter is allowed. So the
shaft diameter for drive is d =44mm
ii. Design for driven shaft
This shaft is subjected to bearing supporting at both side and two sprocket that is equal
distance from bearing.
Fig 15: Schematic diagram of the driven shaft
This shaft is applied force by two sprocket (each of weight of 10kg * acceleration due
to gravity 10m/s2), F1 = F2 = 2500N
Also it is supported by two bearing that located by pins located from sprockets by
140mm distance apart.
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Calculation for maximum bending moment
FSB=2500n 900mm FSC=2500N
A B C D
140mm 140 mm
FRA FRD
The force applied at point B is 2500N by sprocket, so to calculate the reaction at D we taking
a moment at point A is equal to zero.
∑MA = 0
(2500N*140mm) + (2500N*1040mm) - (FRD*1180mm) = 0
FRD*1180mm = 53000Nmm
FRD = 2500Nmm
To get the bearing reaction at point A, we calculate the summation of all force along y-axis is
zero
∑FY = 0
FRA – 2500N -2500N + FRD = 0
FRA – 2500N -2500N + 2500N = 0
FRA = 2500N
To calculate the maximum bending moment for each point, it is calculate for each section.
For section AB
140mm FV ∑MB =0
A B MB -2500N*140mm = 0
FRA = 2500N MB = 35,0000Nmm
To calculate the shearing force, summation of force along y-axis is zero,
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FV –FRA =0
FV = 2500N
For section CD
FV ∑MC = 0, MC – 2500N*140mm = 0
1 40mm MC = 350,000Nmm
C D FD = 2500N
To calculate the shearing force along y-axis the summation of force is zero.
FV – 2500N = 0
FV = 2500N
Therefore the maximum bending moment is obtained at point B and C is 350000Nmm and
the minimum bending is at point A and D will be zero. From the above data we draw the
maximum bending moment diagram.
A B C D
Mb 350000Nmm
0
Length of the shaft in mm
Therefore the maximum bending moment is obtain at point B and C are Mmax =350Nm
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The torque due to sprocket on the shaft is,
T = F sprocket * radius of the sprocket
T = 5000* 325mm
T = 1625000Nmm
From the maximum bending moment and torque produced, we calculate the equivalent
moment,
M eq = �(�t�)� + (����)�
From the appendixes table 5; we select kt for torsion and kb for moment that is applied load at
stationary. Therefore, kt = kb = 1
Meq = �(�t�)� + (����)�
Meq = √(1625000)2 +(350000)2
Meq = 1662265Nmm
Calculation for twisting moment (TORQUE)
For the driven shaft rotate at similar to drive shaft by 60rpm and the power of 12KW, the
torque applied on the shaft is calculated as
T = 60P/2∏N
T = 60*12X103/2∏*60
T =1.91KNm
From equivalent bending moment
Meq = �(�t�)� + (����)�
Meq = √(1625000)2 +(1910)2
Meq = 1662265Nmm
For the shaft material of plain carbon steel C-30, the ultimate tensile strength is 550N/mm2
and yield strength is 300N/mm2, The safety factor of 7
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The allowable tensile stress is calculate as
���� = �����/� = 550mpa/7
���� = 78.57mpa
Therefore to calculate the diameter of shaft
���� = 32Mmax/∏d3
d3 = 32����/∏����
d3 = 32x1662.265Nm/∏*78.57x106N/m2
d = 0.05995m
d = 59.9mm
From the standard shaft table we take d= 65mm
4.3.4 Design of the key
Key is piece of mild steel inserted between the shaft and sprocket to connect these together in
order to prevent relative motion between them. Key is used as temporary fastening are
subjected to considerable crushing and shearing stresses.
Types of key
Sunk keys
Saddle key
Tangent keys
Round key
Spline key
From the above key, key that we select is rectangular sunk key. The usual proportions of this
key are
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For driver shaft,
For the d =44mm
T = 1910Nm
���� = 150Mpa
Width of the key, w = d/4 = 45mm/4 = 11.25mm
Thickness of the key, t = 2w/3 = d/6 =45mm/6 = 7.5mm
Length of the key,
T = F*d/2 =�*w*l*d/2
L = 2T/ �*w*d = 2*1910Nm/150*106N/m2*0.01125m*0.044m
L =0.0514m
L = 51.4mm
For driven shaft
For the d =65mm
T = 1910Nm
���� = 150Mpa
Width of the key, w =d/4 = 65mm/4 = 16.25mm
Thickness of the key, t = 2w/3 = d/6 = 65mm/6 = 5.4mm
Length of the key,
T = F*d/2 =�*w*l*d/2
L = 2T/ �*w*d = 2*1910Nm/150*106*0.01626m*0.065m
L = 0.0237m
L = 23.7mm
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4.3.5 Bearing selection
A bearing is machine elements which support another moving machine element. It permits a
relative motion between the contact surfaces of the members, while carrying load. A little
consideration will show that due to relative motion between the contact surfaces, a certain
amount of the wasted in overcoming frictional resistance and if the rubbing surfaces are in
direct contact, there will be rapid wear. In order to reduce frictional resistance, wear and in
some cases to carry away the heat generation.
Roller conveying chain has used bearing at shaft supporting end. This bearing we selected
has the following consider
Low starting and running friction
Ability to withstand momentary shock
Accuracy of shaft alignment
Low cost of maintenance
Small overall dimensions
Reliability of service
Easy to mount and erect
Cleanliness
Lubrication of bearing
Bearing are lubricated for the following purposes:
To reduce friction and wear between the sliding parts of the bearing,
To prevent rusting or corrosion of the bearing surfaces
To protect the bearing from water, dirt, etc., and
To dissipate the heat.
For driver shaft of the diameter of 45mm we select the bearing number 209 are selected and
also for the driven shaft of the diameter of 65mm bearing number 313 is selected from
appendix table 3.
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4.4 Cost analysis
The overall cost that we design for conveying purpose is as follow
Component Dimension material Quantity Price (in
birr)
Chain 22.04m Mild steel 2 2200
Sprocket Dia 650mm Mild steel 4 500
Shaft Dia 45x 1240mm
Dia 65x 1100mm
Mild steel 5 650
Bearing 209-
313-
Carbon
chromium
steel
10 1750
Key 11.25mmx7.5mmx51.4mm
16.25mmx5.4mmx23.7mm
Mild steel 6 300
Slats 250mmx1100mm Light metal 88 8800
Frame body 0.02x0.02x32m Cast iron
steel
1 1300
Nut and bolt M24 Mild steel 372 1116
Total cost 16616
Table 6: cost analysis of the project
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Fig 16: roller conveying chain
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Conclusions
After we joined in to wonji//shoa sugar factory for four months, we have gained many benefit
that concerning to our field what we have been learn in the class theoretically by seeing,
asking and operating some machine and part of increase our skill in many ways. So this
university-industrial linkage was prepared or conducting by department for engineering
student after taking some course will be bring student self relief and confidence to know what
they learn by theory and also opportunity to know what industry look like. When student join
in to factory and finding some problem occurred in the factory and give their proposed
solution for that problem was increase high quality productivity and give student to bring the
new idea and appreciate to discover the new machine. Therefore this course or internship is
important for student in term of student increase to link their theoretically knowledge with
practically.
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Recommendation
Wonji/shoa sugar factory was the first sugar factory in Ethiopia that produce raw sugar, sugar
product and sugar by product for internal market and for export. This factory produces sugar
in high quality and also produces electric power from steam by itself. But we recommend
that, the WSSF factory is to
Produce steam by two pair of boiler rather than single boiler to increase power
generation
Decrease by air pollution by reducing the amount smoke released from the boiler
Increase the productivity per day as much as possible
Increase the efficiency of the turbine that produce electricity to 32MW
Give pocket money for student during internship
Additional plant like ethanol, work shop, i.e. and
Decrease the wastage of the steam by increase the efficiency of pipe flow.
Decrease the extravagance of lime during uptake from the land during for mixing.
Avoid improper ash drop in steam generation plant by increasing size of ash
conveying belt and making its coverage through which the ash is dropped.
Minimize bursting of steam pipe by using a pipe which can stand with high pressure
and temperature.
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References
1) Hand book of cane sugar engineering. 3rd completely revised, edition
2) Cane sugar engineering, Peter Rein
3) Machine design –R_S_khurmi,kGupta text book
4) Strength of materials 4th. By Ferdinand l. Singer_Andrew Pytel
5) Shingley_s mechanical engineering design 8th edition
6) Fundamental of material science and engineering
7) Www. Roller conveying chain
8) Wonji/shoa sugar factory manual
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Appendixes
Table 1 material selection
Component Material
Chain Mild steel
Sprockets Mild steel
Shaft Mild steel ( C-30)
Bearing Tin-based alloy
Supporting bar Mild steel
Nut and bolt Mild steel
Slat Light metal
Table 2: factor of safety (n) for roller and silent chains
Type
of
chain
Pitch
of
chain
in
mm
Speed of sprocket
50 200 400 600 800 1000 1200 1600 2000
Bush
roller
chain
2012-
15-25
7 7.8 8.55 9.35 10.2 11 11.7 13.2 14.5
30-35 7 8.2 9.35 10.3 11.7 12.9 14 16.3 -
30-35 7 8.5 10.2 13.2 14.8 16.5 19.5 - -
Silent
chain
12,7-
15.87
20 22.2 24.4 29 29 31.0 33.4 37.8 42.0
19.5-
25.4
20 23.4 26.7 30 33.4 36.8 40.0 46.5 53.5
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Table 3: bearing selection
Bearing No. Bore (mm) Outside diameter (mm) Width
(mm)
206
306
406
30
62
72
90
16
19
23
207
307
407
35 72
80
110
17
21
25
208
308
408
40 80
90
110
18
23
27
209
309
409
45 85
100
120
19
25
29
210
310
410
50 90
110
130
20
27
31
211
311
411
55 100
120
140
21
29
33
212
312
412
60 110
130
150
21
29
33
213
313
413
65 120
140
160
22
31
35
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Table 4: ultimate tensile strength and yield strength
Material Ultimate tensile
Strength, N/mm2
Yield strength,
N/mm2
Plain carbon steels
C 07
C 10
C15
C20
C25
C30
C40
C45
C50
40 Ni 3
30 Ni4 Crl
40 Cr 3 Mol V20
40 Crl
320 - 400
340 - 420
370 - 490
440 - 520
460 - 550
500 - 600
580 - 680
600 - 750
660 - 780
750 - 1050
1000 - 1150
1350
700 – 850
200
210
240
260
280
300
330
380
380
600
600
1120
540
Table 5: The recommended value of the kb and kt
Nature of loading Kb Kt
Stationary shaft
Stationary applied load
Suddenly applied load
Revolving shaft
Suddenly applied load
Minor shock load
Heavy shock load
1
1.5-2.0
1.5
1.5-2.0
2.0-3.0
1
1.5-2.0
1
1-1.5
1.5-3.0