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Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982

RESEARCH ARTICLE

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OPEN ACCESS

Design, Fabrication and Performance Evaluation of a Shea Butter
(Vitellaria Paradoxa) Clarifying System
Gbabo Agidi1, J.T Liberty2, T.O Fakayode1 and G.Y Olanrele1
Department of Agricultural and Bioresources Engineering, Federal University of Technology, Minna, Niger
State1
Department of Agricultural and Bioresources Engineering, University of Nigeria, Nsukka, Enugu State, Nigeria2

ABSTRACTS
This work was aimed at the design, fabrication and performance evaluation of a Shea butter clarifying machine.
It consists of two units and each unit of the system was made up of three tanks. The inner tank houses the oil to
be clarified; second tank holds the water meant for generating steam to melt the oil in the inner tank while the
external (third) tank provides insulation needed to minimize heat loss. The first unit of the system was designed
to clarify the Shea butter even as the second unit concentrates the oil. A pump was located between the two units
to help force the clarified oil from the first unit into the second unit. The designed system had capacity to clarify
170litres of oil in an hour in a single batch operation. When the oil was gently stirred by the stirrer welded to a
shaft, impurities in the oil settles down at the conical section of the inner tank due to difference in densities and
the action of reagents added. The impurities can easily be separated out while the cleaned oil floats at the top
and pumped into the second tank. Power was generated from a 0.5hp (373W) electric motor for shaft rotation
through gear motors which also assisted to reduced the motor speed from 1450rpm to the selected speed of
45rpm. The test result indicated that the clarifying system functioned properly. About 80litres of Shea butter
was used to test-run the machine. Sodium hydroxide (NaOH) and activated carbon were used as reagent to assist
in the oil clarification. After the test, approximately 70litres of clarified Shea butter was recovered.
Keywords: Clarified, design, fabricate, performance evaluation, Shea butter

I.

INTRODUCTION

Nigeria and many other Africa countries is
making great effort to boost her economy by limiting
imports and promote exports which has resulted to
intense research into possibility of obtaining a wide
range of products from locally available agricultural
products. Food and agricultural processing, extraction
of liquids from solid raw materials has been an area
of interest to many researchers.
Recently, research and development in Shea
butter extraction enterprise has become an essential
task in vegetable oil extraction industry in Nigeria as
it’s being used as raw material for food, soap,
cosmetics, pharmaceutical, medical, cooking oil, and
metal cutting fluids and as a substitute for cocoa
butter in chocolate and confectionary industries.
These products have high potential for export
(Olaoye, 1994).
The traditional method of Shea butter
clarification and purification involves stirring the
butter extracted vigorously in a heating chamber,
while the oil which floats up is then ladled off the top
of the pot with the slurry settling down at the bottom
of the pot. This however, despite the human effort
exerted does not give a clear and pure Shear butter.
Also, Shea butter produced by traditional method of
or by the use of oil expeller contains physical
impurities, high free fatty acid and other natural
triglycerides. It is therefore imperative to have an
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efficient and effective clarifier that will produce a
pure Shea butter, reduce human drudgery and requires
less skills and strength to operate.
Therefore, this work is aimed at the:
i.
Design of Shea butter clarifying system
ii.
Fabricate a Shea butter clarifier
iii.
Performance evaluation of the Shea butter
clarifying system
iv.
Produce a Shea butter void of any physical
impurity and reduced free fatty acid (FFA)
content

II.

MATERIALS AND METHODS

Design Parameters
The design parameters considered for design
of the clarification system include availability of
material, thermal conductivity of material, versatility,
durability strength, efficiency, ease of maintenance,
ease of operation, cost of materials, ergonomics and
the technological status of the intended users.
Materials Selection
Some of the factors considered in choosing
materials for this fabrication work include; thermal
conductivity of the materials, fabrication cost,
operation and maintenance cost, availability of
material, strength and rigidity.

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Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982
Physical Properties Determination of Shea Butter
Melting point: This is the point at which Shea butter
exist as oil. According to Alander (2002), Shea butter
melts at approximately 30oC – 35oC depending on the
variety and quality of the nut from which the oil was
extracted.
Viscosity: The more viscous a vegetable is, the better
it is as lubricant. According to Olaniyan and Oje
(2007), Shea butter has an optimum viscosity of about
100cp when the heating temperature is 700-900C.
Moisture Content: Moisture content of oil must be
made minimal as possible. This is because oils with
high moisture content are susceptible to
recontamination or rancidity. According to Olaniyan
and Oje (2007), moisture content reduces as the
temperature increases.
Colour Intensity: Yellow is the dominant colour of
Shea butter at all heating temperature. Heating above
900C will results in darkening of the oil.
Rancidity Index: As the heating temperature
increases, there is an increase in the rancidity index as
indicated by the darkening of the oil. Rancidity index
indicates the degree of deterioration of fats and oil.
Rancidity index sets in at 90oC (Olaniyan and Oje
(2007).

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Hollow Pipe: Helps convert the refined oil into the
second unit (tank) for concentration of the oil and it
was connected through an electric pump.
Electric Pump: Assists to force the oil under
pressure through pipes into the second tank for
concentration of the oil.
Description of the Machine
The Shea butter clarification system
designed was made of two main units. The two units
(tanks) were made of same material and volume. Both
units consist of three compartments (tanks). The first
(inner) tank houses the stirrer and the oil to be
clarified. A hollow pipe extends from one edge of the
tank (at different levels of oil) to the other, without
passing through the centre of the tank so as not to
impede the rotation of the stirrer. The hollow pipes
serve to increase the rate of heat transfer into the oil
by conveying the steam generated from the second
tank into and through the first tank. The major task of
the first tank was to clarify the oil. The second tank
was meant to boil water so as to generate steam to
melt oil in the inner tank (first tank). It had a
boiler/heating element attached to it for boiling water
while the third tank (external) provides insulation for
the entire system hereby minimizes heat loss to the
environment.

Components of the Machine
Tank: is the main component of the clarification
system. They contain the oil to be clarified, water to
generate steam and the insulating material.
Shaft: is the rotating component used to transmit
power from electric motor to the stirrer/agitator.
Power was delivered to the shaft by some tangential
force and the resultant torque set up within the shaft
permits power to be transferred to various parts linked
to it. Members such as gears were mounted on the
shaft in order for it to transfer power.
Stirrer/Agitator: this is the component used for
gentle stirring of the oil. It was made up of stainless
steel sheet attached welded to the shaft.

Fig.1: the two units of the Shea butter Clarifier

Worm Gear: transmits power at high velocity ratios
between non-intersecting shafts that are generally but
necessarily at right angle. The worm gear is widely
used as speed reducer, which consist of worm and a
worm wheel or gear.
Electric Motor: Converts electric energy into
mechanical energy. It provides the rotational motion
and power needed to rotate the shaft through the gear
system.
Fig.2: A cross section through the Shea butter
Clarifying System
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Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982

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(b) Second tank
Capacity of the second tank = 250litres =
0.25m3
A capacity of 250litres was designed so as to have
enough space for the water needed to generate steam
An allowance of 0.1m was allowed between inner
tank and second tank. Therefore, the diameter of the
second tank is;

D  0.4  0.1  0.1  0.6m

d  0.6m; r  0.3m; V  r 2 h
0.25
0.25m 3  x0.3 2 xh;  h 
x0.3 2
 0.884m  0.9m
Fig3: Orthographic View of the Clarifier
Design Calculations of Major Components
1. Design of the Tank
(a)
Inner tank
Capacity = 85litres = 0.085m3
The capacity was divided between the three sections
of the tank;
i.
Upper cylinder
Capacity = 75litres = 0.075m3

V  r 2 h

A diameter of 0.4m was assumed for the inner tank to
allow for easy rotation of the shaft
D = 0.4m, r = 0.2m

0.075  x0.2 2 xh,  h 

0.075
 0.59  0.6m
x0.2 2

ii. Frustum of cone
Capacity = 9.8litres =0.0098m3



V 1
3h R 2  Rr   r 2



The same diameter of the upper tank was transferred
as the top diameter of the frustum of the cone.
A diameter of 4cm (0.04m) was selected for the
bottom diameter of the cone.
Therefore, if D = 0.4m; d = 0.04m; r = 0.02m;
R = 0.2m

0.0098  1
Hence,



3h 0.2 2  0.2 x0.2  0.022
3x0.0098
h
 0.21m  0.2m
0.0444x



iii. Lower cylinder for discharge of slurry
Capacity = 0.002m3 (0.2litres)
The bottom diameter of the frustum of the cone was
the same diameter of hollow pipe for discharge of
slurry
d = 0.04m; r = 0.02m; V  2r h
2

0.0002  x0.02 2 xh;  h 

0.0002
x0.02

(c) Third tank (external)
Capacity of tank = 350litres = 0.35m3
An allowance of 0.05m (5cm) was also given between
the second and the external tank. Therefore,

d  0.6  0.05  0.05  0.6  0.1  0.7m; r  0.35m

V  r 2 h; 0.35  x0.35 2 xh
0.35
 0.909m  0.9m
x0.35 2

h

(d) Volume of the space to be filled with water
Volume of space to be filled with water =
volume of second tank-volume of inner tank
Let volume of the second tank be = V2
Volume of second tank = V1
Volume of space between the two tanks be = V3
V3 = V 2 – V1
V2 = 0.2m3; V1= 0.085m3
V3= 0.2 – 0.085 = 0.115m3 = 115litres
Hence, the volume of the space to be filled with water
was 115litres. Now assuming this space was 1/3 filled
with water, then;

V

1
x0.115  0.038m 3  38.33litres
3

Therefore, volume of water required to fill the space
when it is 1/3 filled with water was 38.33litres
Since volume of water is known, the mass of the
water was calculated thus;

mass
volume
 Mass  DensityxVolume
Density 

Density of water at 40C is 1000kg/m3 (Douglas, 2005)
Volume = 0.038m3

 Mass  1000x0.038  38.33kg
2.

Design of the Shaft
For a shaft with little or no axial load, the
diameter may be obtained using the American Society
of Mechanical Engineers (ASME) code equation
given as;

 0.1521m  0.15m
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979 | P a g e
Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982

 16
d 
 S
 a

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1

K b M b 

2

 K t M t 

2

3




Where,
d = diameter of the shaft
Mb = bending moment
Mt = torsional moment
Kb= combined shock and fatigue applied to bending
moment
Kt = combined shock and fatigue factor applied to
torsional moment
Sa = allowable stress
For rotating shaft when load is suddenly applied
(minor shock) (Khurmi and Gupta, 20050;
Kb = 1.5 to 2.0; Kt = 1.0 to 1.5
For shaft without keyway, allowable stress Sa =
55MN/m2
For shaft with keyway allowable stress Sa = 40MN/m2
Determination of Maximum Torsional Moment

kWx1000x60 9550xkW
Mt 

(Hall et al.
2rev / min
rev / min
1981)

0.2m

0.2m

0.2m

0.6m
Fig. 4: Free body diagram of Shaft

W1  W2  W3  W4
Taking moment at A

M



 W2 x0.2  W4 x0.2

 0.77x0.2  0.77x0.2  0.154  0.154  0

Taking moment at B

M



 W3 x0.2  W1 x0.2

 0.77x0.2  0.77x0.2  0.154  0.154  0

Taking moment about C

M



 W1 x0.4  W2 x0.2  W3 x0.4  W4 x0.2

 0.77 x0.4  0.77 x0.2  0.7 x0.4  0.77 x0.4
 0.308  0.154  0.308  0.154  0

Power  3hp; SpeedN  1450rpm

Therefore bending moment = 0

1hp  746W ; 3hp  2238W  2.238kW
9550x2.238
Mt 
 14.74 Nm
1450

 16
d 
 S
 a

Determination of the Bending Moment
Load distributed on shaft;
W2
0.2m

W1
0.2m

W4

0.2m
W3

0.6m
Fig. 3: Free body diagram of Shaft

W1  W2  W3  W4
W1 = weight of blade on shaft
To calculate the weight of the blade;
mass
Density 
; mass  densityxvolume
volume
Volume  Areaxthickness; Thickness  2mm  0.002 m

Length  10cm  0.1m; Breadth  5cm  0.05m
Area  0.1x0.05  5 x10 3 m 2
Volume  5 x10 3 x0.002  1x10 5 m 3
Density of steel material  7850kg / m 3
Mass  7850x1x10

5

 0.0785kg

K b M b 

2

 K t M t 

2






1

3

K b  2.0; K t  1.5; M b  0; M t  14 .74 Nm; S a  40 MN / m 2

16

d3  
6
 x40 x10

2.0 x0  14.74x1.5 


2

16

2 

0 2  22.11 
6
 x40 x10

16


6
 x40 x10
 16353.76 


 125663706.1 

22.11 


2

1

3



1

1



1

3

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1

3

 0.014m  14.18mm  15mm

3. Design of the Stirrer
The stirrer consists of three pairs of blade
with equal dimensions, spaced equally on the three
shaft rod. Each pair was made of two blades and each
blade was welded on opposite side of the shaft.
Length of stirrer = 10cm = 0.1m
Breadth of stirrer = 5cm = 0.05m
Thickness = 2mm = 0.002m

Density 

mass
Volume areaxthickness ;
volume

Area = L x B

Weigth  massxacceleration due to gravity
W  0.0785x9.81  0.77 N

3

3

 16353.76 

6 
 x 40 x10 

3

 2.815x10 6

1

2

Volume  LxBxthickn  0.1x0.05x0.002
ess
 1.0 x10 5 m 3

Density of steel material = 7850kg/m3

980 | P a g e
Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982

Mass  7850 x1.0 x10 5  0.0785 kg

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separating out at the conical section of the tank after
agitation of the oil.

Therefore the mass of each stirrer was 0.0785kg
Since there were six blades of the stirrer,

b.

Total mass  0.0785x6  0.471kg
Weight  massxacceleration due to gravity

 0.471x9.81  4.62 N
Fabrication and Evaluation of the Machine
Fabrication: All parts of the Shea butter clarifying
system were fabricated from metals except the
insulator made of a good insulting material,
Rockwool. The inner and second tanks were
fabricated from stainless steel while the external tank
was fabricated from mild steel. The choice of
stainless steel for the inner and second tank was
because of the food material involved (Shea butter)
and water which could cause corrosion of the metals
and subsequent contamination of the food material.
The shaft was made of steel rod while the
stirrers-stainless steel sheet. Also, the pipes in the
inner tank designed for better heat circulation in the
oil, were made of stainless steel material and the
pipes for conveying the clarified oil into the second
tank was made of galvanize steel because of the high
temperature of the flowing fluid.
For this design, the shaft obtained power
from the motor for rotation through the gear motor
which eliminates completely attachments such as
pulleys and the belt system thereby eliminating the
problem of belt slipping off the pulley during rotation.
The tanks were fabricated using 2mm thick metal
material. The support for the motor was fabricated
using 4mm thick angle iron while the tank-stand was
also fabricated with 4mm thick angle iron. The pipe
in the inner tank was made of 1 1 inch diameter pipe
2
while the pipe for oil transfer into the second tank
was made of 3 inch. The gate valve was a brass
4
material while the pressure relief valve was also 1 1

Bleaching agent
Activated carbon was used as the bleaching
agent. 1kg of activated carbon was added to the
80litres of Shea butter to be clarified. The quantity of
bleaching agent added depended on the end colour
desired. The more the amount added toa certain level,
the brighter the colour of the oil produced, because
there will be more of the agent to absorb all the
colouring pigment. The activated carbon reacted with
the colur pigment present in the oil it thus,
discolouring the oil.

Plate1: Sample of the Crude Shea Butter

2

inch in diameter.
Testing: An evaluation was done to ascertain whether
the constructed clarifying system functions properly.
80litres of Shea butter was used to test-run the
machine alongside some reagents. The stirrer gently
rotates as designed while the water in the second tank
also boiled at the designed time, 30minutes.
Reagent Used;
a. Caustic soda (NaOH)
0.1M of NaOH solution was prepared in 250cm3 of
distilled water.
Preparation: 4g of NaOH dissolved in 1000cm3 of
distilled water to give 0.1M of NaOH solution.
Therefore, 1g of NaOH dissolved in 250cm3 of
distilled water to give 0.1M of NaOH solution. The
caustic soda reacts with Free Fatty Acids present in
the oil and neutralized it to form soap which can be
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Plate2: Sample of the Clarified Shea Butter

III.

RESULTS OBTAINED

Volume of Crude Shea butter = 80litres
Colour of crude Shea butter = Dark Yellow
Volume of Caustic Soda (NaOH) = 250cm3
Mass of Activated Carbon = 1kg
Time = 60minutes
The water in the tank was allowed to boil to
generate the required heat to melt the oil completely
before adding the reagents. Caustic soda was added
first and the soap stock formed as result of the
reaction between the NAOH and the free fatty acid
was separated out first before adding the bleaching
agent to remove the colouring pigment. The soap
stock formed had to be removed first before adding
981 | P a g e
Gbabo Agidi et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982

www.ijera.com

the bleaching agent so as not to impede the action of
the bleaching agent.
Volume of Clarified Shea Butter = 70litres
Colour of Clarified Shea Butter =Yellow
Volume of Slurry Obtained  10litres.

IV.

CONCLUSION AND
RECOMMENDATION

The clarifying system developed will help
improve the quality of Shea butter hence, make it
more attractive and appealing to buyers.The results
obtained from the performance evaluation showed
that the clarifying system functioned properly as
expected. Using 80litres of oil to test the machine
while adding 0.1M of 500ml of sodium hydroxide
(caustic soda) and 1kg of activated carbon as a
bleaching agent, a golden yellow coloured Shea butter
was obtained and approximately 10litres of slurry was
also separated out. Visual inspection of the clarified
Shea butter indicated that there was no visible
evidence of any physical impurity present.
However, a filter bed should be introduced at
the point of oil flow from the first unit into the second
unit to further help trap finer particles and some other
colouring pigment present in the oil. Also, a
temperature sensor should be introduced into the oil
to determine at any instant the temperature of the oil
in order to avoid over heating of the oil.

REFERNCES
[1]

[2]

[3]

[4]

[5]

Alander, J., Anderson, JA.C. (2002). The
Lipex shea butter family. The complete
emollient range for cosmetic formulations.
Chemical Engineering Department, Lund
University, Sweden.
Hall, S.A, Holowenko, R.A and Lauglin,
G.H.
(1989). Thetheory and problems of
Machine design. Schaum’s Outline Series.
S.I (metric) edition
Khurmi, R.S, Gupta, J.K (2005). Machine
Design. Eurasia publishing house (PVT)
Ltd,
Nagar, New Delhi.
Olaoye, J.O (1994). Oil Recovery Process
from
Shea butter Nut through modified
Clarification. M.Eng Thesis. Department of
Agricultural Engineeering, University of
Ilorin, Nigeria.
Olaniyan,
A.M,
Oje,
K.
(2007).
Development of Mechanical
Expression
Rig for dry extraction of Shea butter
fromshea Kernel. Nigeria J. Food Sci.
Technology.

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  • 1. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982 RESEARCH ARTICLE www.ijera.com OPEN ACCESS Design, Fabrication and Performance Evaluation of a Shea Butter (Vitellaria Paradoxa) Clarifying System Gbabo Agidi1, J.T Liberty2, T.O Fakayode1 and G.Y Olanrele1 Department of Agricultural and Bioresources Engineering, Federal University of Technology, Minna, Niger State1 Department of Agricultural and Bioresources Engineering, University of Nigeria, Nsukka, Enugu State, Nigeria2 ABSTRACTS This work was aimed at the design, fabrication and performance evaluation of a Shea butter clarifying machine. It consists of two units and each unit of the system was made up of three tanks. The inner tank houses the oil to be clarified; second tank holds the water meant for generating steam to melt the oil in the inner tank while the external (third) tank provides insulation needed to minimize heat loss. The first unit of the system was designed to clarify the Shea butter even as the second unit concentrates the oil. A pump was located between the two units to help force the clarified oil from the first unit into the second unit. The designed system had capacity to clarify 170litres of oil in an hour in a single batch operation. When the oil was gently stirred by the stirrer welded to a shaft, impurities in the oil settles down at the conical section of the inner tank due to difference in densities and the action of reagents added. The impurities can easily be separated out while the cleaned oil floats at the top and pumped into the second tank. Power was generated from a 0.5hp (373W) electric motor for shaft rotation through gear motors which also assisted to reduced the motor speed from 1450rpm to the selected speed of 45rpm. The test result indicated that the clarifying system functioned properly. About 80litres of Shea butter was used to test-run the machine. Sodium hydroxide (NaOH) and activated carbon were used as reagent to assist in the oil clarification. After the test, approximately 70litres of clarified Shea butter was recovered. Keywords: Clarified, design, fabricate, performance evaluation, Shea butter I. INTRODUCTION Nigeria and many other Africa countries is making great effort to boost her economy by limiting imports and promote exports which has resulted to intense research into possibility of obtaining a wide range of products from locally available agricultural products. Food and agricultural processing, extraction of liquids from solid raw materials has been an area of interest to many researchers. Recently, research and development in Shea butter extraction enterprise has become an essential task in vegetable oil extraction industry in Nigeria as it’s being used as raw material for food, soap, cosmetics, pharmaceutical, medical, cooking oil, and metal cutting fluids and as a substitute for cocoa butter in chocolate and confectionary industries. These products have high potential for export (Olaoye, 1994). The traditional method of Shea butter clarification and purification involves stirring the butter extracted vigorously in a heating chamber, while the oil which floats up is then ladled off the top of the pot with the slurry settling down at the bottom of the pot. This however, despite the human effort exerted does not give a clear and pure Shear butter. Also, Shea butter produced by traditional method of or by the use of oil expeller contains physical impurities, high free fatty acid and other natural triglycerides. It is therefore imperative to have an www.ijera.com efficient and effective clarifier that will produce a pure Shea butter, reduce human drudgery and requires less skills and strength to operate. Therefore, this work is aimed at the: i. Design of Shea butter clarifying system ii. Fabricate a Shea butter clarifier iii. Performance evaluation of the Shea butter clarifying system iv. Produce a Shea butter void of any physical impurity and reduced free fatty acid (FFA) content II. MATERIALS AND METHODS Design Parameters The design parameters considered for design of the clarification system include availability of material, thermal conductivity of material, versatility, durability strength, efficiency, ease of maintenance, ease of operation, cost of materials, ergonomics and the technological status of the intended users. Materials Selection Some of the factors considered in choosing materials for this fabrication work include; thermal conductivity of the materials, fabrication cost, operation and maintenance cost, availability of material, strength and rigidity. 977 | P a g e
  • 2. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982 Physical Properties Determination of Shea Butter Melting point: This is the point at which Shea butter exist as oil. According to Alander (2002), Shea butter melts at approximately 30oC – 35oC depending on the variety and quality of the nut from which the oil was extracted. Viscosity: The more viscous a vegetable is, the better it is as lubricant. According to Olaniyan and Oje (2007), Shea butter has an optimum viscosity of about 100cp when the heating temperature is 700-900C. Moisture Content: Moisture content of oil must be made minimal as possible. This is because oils with high moisture content are susceptible to recontamination or rancidity. According to Olaniyan and Oje (2007), moisture content reduces as the temperature increases. Colour Intensity: Yellow is the dominant colour of Shea butter at all heating temperature. Heating above 900C will results in darkening of the oil. Rancidity Index: As the heating temperature increases, there is an increase in the rancidity index as indicated by the darkening of the oil. Rancidity index indicates the degree of deterioration of fats and oil. Rancidity index sets in at 90oC (Olaniyan and Oje (2007). www.ijera.com Hollow Pipe: Helps convert the refined oil into the second unit (tank) for concentration of the oil and it was connected through an electric pump. Electric Pump: Assists to force the oil under pressure through pipes into the second tank for concentration of the oil. Description of the Machine The Shea butter clarification system designed was made of two main units. The two units (tanks) were made of same material and volume. Both units consist of three compartments (tanks). The first (inner) tank houses the stirrer and the oil to be clarified. A hollow pipe extends from one edge of the tank (at different levels of oil) to the other, without passing through the centre of the tank so as not to impede the rotation of the stirrer. The hollow pipes serve to increase the rate of heat transfer into the oil by conveying the steam generated from the second tank into and through the first tank. The major task of the first tank was to clarify the oil. The second tank was meant to boil water so as to generate steam to melt oil in the inner tank (first tank). It had a boiler/heating element attached to it for boiling water while the third tank (external) provides insulation for the entire system hereby minimizes heat loss to the environment. Components of the Machine Tank: is the main component of the clarification system. They contain the oil to be clarified, water to generate steam and the insulating material. Shaft: is the rotating component used to transmit power from electric motor to the stirrer/agitator. Power was delivered to the shaft by some tangential force and the resultant torque set up within the shaft permits power to be transferred to various parts linked to it. Members such as gears were mounted on the shaft in order for it to transfer power. Stirrer/Agitator: this is the component used for gentle stirring of the oil. It was made up of stainless steel sheet attached welded to the shaft. Fig.1: the two units of the Shea butter Clarifier Worm Gear: transmits power at high velocity ratios between non-intersecting shafts that are generally but necessarily at right angle. The worm gear is widely used as speed reducer, which consist of worm and a worm wheel or gear. Electric Motor: Converts electric energy into mechanical energy. It provides the rotational motion and power needed to rotate the shaft through the gear system. Fig.2: A cross section through the Shea butter Clarifying System www.ijera.com 978 | P a g e
  • 3. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982 www.ijera.com (b) Second tank Capacity of the second tank = 250litres = 0.25m3 A capacity of 250litres was designed so as to have enough space for the water needed to generate steam An allowance of 0.1m was allowed between inner tank and second tank. Therefore, the diameter of the second tank is; D  0.4  0.1  0.1  0.6m d  0.6m; r  0.3m; V  r 2 h 0.25 0.25m 3  x0.3 2 xh;  h  x0.3 2  0.884m  0.9m Fig3: Orthographic View of the Clarifier Design Calculations of Major Components 1. Design of the Tank (a) Inner tank Capacity = 85litres = 0.085m3 The capacity was divided between the three sections of the tank; i. Upper cylinder Capacity = 75litres = 0.075m3 V  r 2 h A diameter of 0.4m was assumed for the inner tank to allow for easy rotation of the shaft D = 0.4m, r = 0.2m 0.075  x0.2 2 xh,  h  0.075  0.59  0.6m x0.2 2 ii. Frustum of cone Capacity = 9.8litres =0.0098m3  V 1 3h R 2  Rr   r 2  The same diameter of the upper tank was transferred as the top diameter of the frustum of the cone. A diameter of 4cm (0.04m) was selected for the bottom diameter of the cone. Therefore, if D = 0.4m; d = 0.04m; r = 0.02m; R = 0.2m 0.0098  1 Hence,  3h 0.2 2  0.2 x0.2  0.022 3x0.0098 h  0.21m  0.2m 0.0444x  iii. Lower cylinder for discharge of slurry Capacity = 0.002m3 (0.2litres) The bottom diameter of the frustum of the cone was the same diameter of hollow pipe for discharge of slurry d = 0.04m; r = 0.02m; V  2r h 2 0.0002  x0.02 2 xh;  h  0.0002 x0.02 (c) Third tank (external) Capacity of tank = 350litres = 0.35m3 An allowance of 0.05m (5cm) was also given between the second and the external tank. Therefore, d  0.6  0.05  0.05  0.6  0.1  0.7m; r  0.35m V  r 2 h; 0.35  x0.35 2 xh 0.35  0.909m  0.9m x0.35 2 h (d) Volume of the space to be filled with water Volume of space to be filled with water = volume of second tank-volume of inner tank Let volume of the second tank be = V2 Volume of second tank = V1 Volume of space between the two tanks be = V3 V3 = V 2 – V1 V2 = 0.2m3; V1= 0.085m3 V3= 0.2 – 0.085 = 0.115m3 = 115litres Hence, the volume of the space to be filled with water was 115litres. Now assuming this space was 1/3 filled with water, then; V 1 x0.115  0.038m 3  38.33litres 3 Therefore, volume of water required to fill the space when it is 1/3 filled with water was 38.33litres Since volume of water is known, the mass of the water was calculated thus; mass volume  Mass  DensityxVolume Density  Density of water at 40C is 1000kg/m3 (Douglas, 2005) Volume = 0.038m3  Mass  1000x0.038  38.33kg 2. Design of the Shaft For a shaft with little or no axial load, the diameter may be obtained using the American Society of Mechanical Engineers (ASME) code equation given as;  0.1521m  0.15m www.ijera.com 979 | P a g e
  • 4. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982  16 d   S  a www.ijera.com 1 K b M b  2  K t M t  2 3    Where, d = diameter of the shaft Mb = bending moment Mt = torsional moment Kb= combined shock and fatigue applied to bending moment Kt = combined shock and fatigue factor applied to torsional moment Sa = allowable stress For rotating shaft when load is suddenly applied (minor shock) (Khurmi and Gupta, 20050; Kb = 1.5 to 2.0; Kt = 1.0 to 1.5 For shaft without keyway, allowable stress Sa = 55MN/m2 For shaft with keyway allowable stress Sa = 40MN/m2 Determination of Maximum Torsional Moment kWx1000x60 9550xkW Mt   (Hall et al. 2rev / min rev / min 1981) 0.2m 0.2m 0.2m 0.6m Fig. 4: Free body diagram of Shaft W1  W2  W3  W4 Taking moment at A M   W2 x0.2  W4 x0.2  0.77x0.2  0.77x0.2  0.154  0.154  0 Taking moment at B M   W3 x0.2  W1 x0.2  0.77x0.2  0.77x0.2  0.154  0.154  0 Taking moment about C M   W1 x0.4  W2 x0.2  W3 x0.4  W4 x0.2  0.77 x0.4  0.77 x0.2  0.7 x0.4  0.77 x0.4  0.308  0.154  0.308  0.154  0 Power  3hp; SpeedN  1450rpm Therefore bending moment = 0 1hp  746W ; 3hp  2238W  2.238kW 9550x2.238 Mt   14.74 Nm 1450  16 d   S  a Determination of the Bending Moment Load distributed on shaft; W2 0.2m W1 0.2m W4 0.2m W3 0.6m Fig. 3: Free body diagram of Shaft W1  W2  W3  W4 W1 = weight of blade on shaft To calculate the weight of the blade; mass Density  ; mass  densityxvolume volume Volume  Areaxthickness; Thickness  2mm  0.002 m Length  10cm  0.1m; Breadth  5cm  0.05m Area  0.1x0.05  5 x10 3 m 2 Volume  5 x10 3 x0.002  1x10 5 m 3 Density of steel material  7850kg / m 3 Mass  7850x1x10 5  0.0785kg K b M b  2  K t M t  2     1 3 K b  2.0; K t  1.5; M b  0; M t  14 .74 Nm; S a  40 MN / m 2 16  d3   6  x40 x10 2.0 x0  14.74x1.5    2 16  2   0 2  22.11  6  x40 x10  16   6  x40 x10  16353.76     125663706.1  22.11    2 1 3  1 1  1 3 www.ijera.com 1 3  0.014m  14.18mm  15mm 3. Design of the Stirrer The stirrer consists of three pairs of blade with equal dimensions, spaced equally on the three shaft rod. Each pair was made of two blades and each blade was welded on opposite side of the shaft. Length of stirrer = 10cm = 0.1m Breadth of stirrer = 5cm = 0.05m Thickness = 2mm = 0.002m Density  mass Volume areaxthickness ; volume Area = L x B Weigth  massxacceleration due to gravity W  0.0785x9.81  0.77 N 3 3  16353.76   6   x 40 x10  3  2.815x10 6 1 2 Volume  LxBxthickn  0.1x0.05x0.002 ess  1.0 x10 5 m 3 Density of steel material = 7850kg/m3 980 | P a g e
  • 5. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982 Mass  7850 x1.0 x10 5  0.0785 kg www.ijera.com separating out at the conical section of the tank after agitation of the oil. Therefore the mass of each stirrer was 0.0785kg Since there were six blades of the stirrer, b. Total mass  0.0785x6  0.471kg Weight  massxacceleration due to gravity  0.471x9.81  4.62 N Fabrication and Evaluation of the Machine Fabrication: All parts of the Shea butter clarifying system were fabricated from metals except the insulator made of a good insulting material, Rockwool. The inner and second tanks were fabricated from stainless steel while the external tank was fabricated from mild steel. The choice of stainless steel for the inner and second tank was because of the food material involved (Shea butter) and water which could cause corrosion of the metals and subsequent contamination of the food material. The shaft was made of steel rod while the stirrers-stainless steel sheet. Also, the pipes in the inner tank designed for better heat circulation in the oil, were made of stainless steel material and the pipes for conveying the clarified oil into the second tank was made of galvanize steel because of the high temperature of the flowing fluid. For this design, the shaft obtained power from the motor for rotation through the gear motor which eliminates completely attachments such as pulleys and the belt system thereby eliminating the problem of belt slipping off the pulley during rotation. The tanks were fabricated using 2mm thick metal material. The support for the motor was fabricated using 4mm thick angle iron while the tank-stand was also fabricated with 4mm thick angle iron. The pipe in the inner tank was made of 1 1 inch diameter pipe 2 while the pipe for oil transfer into the second tank was made of 3 inch. The gate valve was a brass 4 material while the pressure relief valve was also 1 1 Bleaching agent Activated carbon was used as the bleaching agent. 1kg of activated carbon was added to the 80litres of Shea butter to be clarified. The quantity of bleaching agent added depended on the end colour desired. The more the amount added toa certain level, the brighter the colour of the oil produced, because there will be more of the agent to absorb all the colouring pigment. The activated carbon reacted with the colur pigment present in the oil it thus, discolouring the oil. Plate1: Sample of the Crude Shea Butter 2 inch in diameter. Testing: An evaluation was done to ascertain whether the constructed clarifying system functions properly. 80litres of Shea butter was used to test-run the machine alongside some reagents. The stirrer gently rotates as designed while the water in the second tank also boiled at the designed time, 30minutes. Reagent Used; a. Caustic soda (NaOH) 0.1M of NaOH solution was prepared in 250cm3 of distilled water. Preparation: 4g of NaOH dissolved in 1000cm3 of distilled water to give 0.1M of NaOH solution. Therefore, 1g of NaOH dissolved in 250cm3 of distilled water to give 0.1M of NaOH solution. The caustic soda reacts with Free Fatty Acids present in the oil and neutralized it to form soap which can be www.ijera.com Plate2: Sample of the Clarified Shea Butter III. RESULTS OBTAINED Volume of Crude Shea butter = 80litres Colour of crude Shea butter = Dark Yellow Volume of Caustic Soda (NaOH) = 250cm3 Mass of Activated Carbon = 1kg Time = 60minutes The water in the tank was allowed to boil to generate the required heat to melt the oil completely before adding the reagents. Caustic soda was added first and the soap stock formed as result of the reaction between the NAOH and the free fatty acid was separated out first before adding the bleaching agent to remove the colouring pigment. The soap stock formed had to be removed first before adding 981 | P a g e
  • 6. Gbabo Agidi et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 3, Issue 6, Nov-Dec 2013, pp.977-982 www.ijera.com the bleaching agent so as not to impede the action of the bleaching agent. Volume of Clarified Shea Butter = 70litres Colour of Clarified Shea Butter =Yellow Volume of Slurry Obtained  10litres. IV. CONCLUSION AND RECOMMENDATION The clarifying system developed will help improve the quality of Shea butter hence, make it more attractive and appealing to buyers.The results obtained from the performance evaluation showed that the clarifying system functioned properly as expected. Using 80litres of oil to test the machine while adding 0.1M of 500ml of sodium hydroxide (caustic soda) and 1kg of activated carbon as a bleaching agent, a golden yellow coloured Shea butter was obtained and approximately 10litres of slurry was also separated out. Visual inspection of the clarified Shea butter indicated that there was no visible evidence of any physical impurity present. However, a filter bed should be introduced at the point of oil flow from the first unit into the second unit to further help trap finer particles and some other colouring pigment present in the oil. Also, a temperature sensor should be introduced into the oil to determine at any instant the temperature of the oil in order to avoid over heating of the oil. REFERNCES [1] [2] [3] [4] [5] Alander, J., Anderson, JA.C. (2002). The Lipex shea butter family. The complete emollient range for cosmetic formulations. Chemical Engineering Department, Lund University, Sweden. Hall, S.A, Holowenko, R.A and Lauglin, G.H. (1989). Thetheory and problems of Machine design. Schaum’s Outline Series. S.I (metric) edition Khurmi, R.S, Gupta, J.K (2005). Machine Design. Eurasia publishing house (PVT) Ltd, Nagar, New Delhi. Olaoye, J.O (1994). Oil Recovery Process from Shea butter Nut through modified Clarification. M.Eng Thesis. Department of Agricultural Engineeering, University of Ilorin, Nigeria. Olaniyan, A.M, Oje, K. (2007). Development of Mechanical Expression Rig for dry extraction of Shea butter fromshea Kernel. Nigeria J. Food Sci. Technology. www.ijera.com 982 | P a g e