Fabrication And Performance Evaluation Of An Improved Biomass Cook Stove

DOI : 10.17577/IJERTV2IS3485

Download Full-Text PDF Cite this Publication

Text Only Version

Fabrication And Performance Evaluation Of An Improved Biomass Cook Stove

Fabrication And Performance Evaluation Of An Improved Biomass Cook Stove

1Dept. of Mechanical Engg., Ambrose Alli University, PMB 14, Ekpoma- Nigeria

2Delta State Polytechnic, Otefe Oghara-Nigeria

3Dept. of Production Engg.,Ambrose Alli University,PMB14,Ekpoma-Nigeria

ABSTRACT

The design, fabrication and testing of an improved biomass cook stove was undertaken in the work. The design improvement of the stove entail improvement in the following areas. Provision of insulation around the combustion chamber to reduce conduction of heat loss across the walls of the chamber, provision of a pot skirt for increasing heat transfer efficiency, establishing the same cross sectional area everywhere as well as the provision of insulated short chimney right above the fire to ensure sufficient draft for good combustion and provision of a graft or fuel tray for complete combustion of a variety of biofuels. Performance test on fuel types reveal sawdust is the most economical in specific fuel consumption as well as giving the least smoking time of the fuel types.

Keywords;Biomass,Duncan multiple test,Fuel consumption,Smoked time

INTRODUCTION

In rural areas, cooking is one of the largest energy consuming activities in less developed countries. In fact, about half of the total population cooks with bio fuels. Firewood and charcoal from forests has been the major source of this energy (ERG, 1986) with the advent of coal gas the cooking ranges became somewhat less elaborate and the designs and the designs concentrated more on the efficient utilization of heat. About the middle of the first half of the 20th century interest in gas fired ranges began to develop in the United states and England while these revolution in cooking methods and cooking ranges was taking place in most of Europe and America, majority of countries in Africa was still using the primitive methods of open wood fires for cooking, even today this is the principal method of cooking food in the villages of sahel and Sudan zones of Africa. In sharp contrast to the situation that existed in primitive times in Europe or even in these zones of Africa in the last century, ample supplies of wood for cooking is scare and where it must be brought accounts for 10 to 20 percent of income of a typical family;A state of the art survey final report, (1977) . In addition, and more seriously, the use of wood in these agreed is resulting in deforestation and decalcification; a critical global

problem. Considering the problems of the less developed countries Nigeria inclusive a significant reduction in the use of fuel wood for cooking could be realized Stout et al,( 2001). Wherever stick-wood is plentiful and at a low cost, conventional improved cook stoves are attractive options. In the ever-increasing areas where charcoal and firewood are becoming a scarce and/or an expensive commodity, there arises a need to develop an option to cleanly burn alternative biomass fuels It is in the light of the foregoing that this work entails to bridge by developing a simple improved biomass stove and performing a series of test to evaluated the best biomass fuels in terms of their fuel consumption and level of emission reduction on the basis of the smoking time.

DESIGN DESCRIPTION

The biomass cook stove is circular in section and consists of a combustion chamber, top section and the base. The hearth of the combustion chamber is made of ceramic the outside of which is lined with fibreglass and encased in a mild steel casing. The top of the stove consists of the pot seat and the pot skirt with specified channel gaps that increase heat transfer efficiency. The base made up of a grate into which the unburned fuel is placed and from where it feeds into the the fuel magazine or firebox which leads to the combustion chamber. The opening of the firebox, the size of the channel gaps within the stove through which hot air flow and the chimney were all made the size sizes to maintain constant cross sectional area. The chimney which is also a part of the base is vertical placed above the combustion chamber to provide updraft needed to maintain the fire. The principle of operation of this stove is simple. As fire burns within the combustion chamber, air is drawn into the combustion chamber from below by convection, ensuring that any smoke from smouldering wood near the fire is also draw into the fire and chimney. The heat from the combustion chamber rises and impinges directly on the base of the cooking pot.

In addition exhaust gases from the fired travelling in the annulus between the cooking pot and pot skirt also transfer heat into the sides of the pot. As a result the efficient use of energy from the fire is greatly enhanced resulting in quick cooking times and a reduction in the quantity of fuel used. The advantage of the stove is that very small sizes off wood can be used, which reduced fuel consumption when compared to traditional open fires.

DESIGN ANALYSIS AND CALCULATIONS

Based on the choice of a family sized cooking stove, the following parameter, are chosen for the design; Height of the combustion chamber 30cm: internal radius of combustion chamber r1= 60mm, internal radius of insulation lining r2=100mm; internal radius of mild steel casing r3= 120mm; external radius of mild steel casing r4= 122mm; external diameter of pot Seat =250mm. Thermal conductivity of ceramic K1=180w/mk; thermal

conductivity of fiberglass, K2=0.037w/mk; Internal conductivity of mild steel K3= 39w/mk; measured external temp of combustion chamber T0= 35oC ;measured Internal temp of combustion chamber Ti =550oC

DETERMINATION OF AREA UNDER THE POT

Maintaining a constant cross sectional area under the pot entails the determination of the channel gaps that measure heat transfer efficiency.

The following channel gaps as shown in fig 1 below are calculated; based on Winiaski method

GapA=

= 3 ..(1 )

Where area of feed chamber = 2 =113.1cm2

The following channel gaps. Gap A, gap B, gap C And gap D were calculated to be 3cm, 1.06cm, 1.2cm and 0.9cm respectively employing the Winiarskis method.

www.ijert.org 2

Heat Loss across the Cylindrical Walls of the Heating Chamber

The radial conduction heat flow for a hollow cylinder is expressed by the Fouriers law as:

=

.. (1)

where: K is the thermal conductivity of the cylinder material; A is the area of the walls of the cylinder heating chamber across which heat transfer occurs; and dT/dr is the radial temperature gradient across the walls.

r4 r3

r2

r1

Figure 3. A composite hollow cylinder

For a composite cylinder (see Fig. 3) with known inside and outside surface temperatures and having n layers of different materials the form of Eq. (1) becomes

= 1 +1

.. (2) (Kumar 2007)

1 +1 /1

=12 1

For the composite hollow cylinder consisting of three layers of materials: ceramic surrounding the combustion

chamber, insulating fiberglass and a steel casing, Eq. (2) becomes

=

1 +1

.(3)

1 21 2 1 + 1 22 3 2 + 1 23 4 3

Substituting for the various parameters gives Q=61.44W

Therefore, the heat transfer through the wall of the stove per second is determined to be 61 W.

FEED CHAMBER

In order to provide for proper combustion of fuel, provision was made for adequae ventilation within the stove. A 12cm diameter feed chamber and of length 5cm was provided.

THE STOVE STAND

These are three 50 mm high metallic structured located at equal distances around the circumferences of the bottom part of the stove. These were provided to prevent rusting and heat losses through leakage occasioned by direct contact between the stove bottom and the ground surface.

THE COMBUSTION CHAMBER

This consists of 565.5cm3 capacity of insulating ceramic surrounded by a mild steel casing enclosure designed to accommodate any biomass material as fuel. A grate or fuel tray at height of 50 mm above the ground is provided at its base to allow for free air intake by updraft and the passage of ashes during combustion.

EXPERIMENTAL PROCEDURE AND PERFORMANCE EVALUATION

The test conducted on the biomass stove included a fuel consumption test and a emission reduction test involving the determination of the smoking time. The apparatus were three big size aluminium pots, a weighing balance, three mercury-in-glass thermometers, a stopwatch, water, rice, bean, matches and fuel consisting of weighed amounts of coal,charcoal,sawdust and wood respectively. These test were carried out to simulate or match the cooking method commonly adopted in rural committees in Africa.The relative humidity and temperature were recorded as 320C and 50% respectively

The initial temperature of the water was recorded using a mercury-in-glass thermometer before the pot were placed on the stove. The charcoal was sprinkled with 10ml of kerosene and then ignited with a match. The subsequent changed in temperature up to the boiling point were recorded at 2-minute intervals with the thermometer permanently inserted in the opened pots. During the boiling of water the smoked emitted was recorded. At boiling the pots were removed from the stoves and weighed. Also the fire was put out immediately

and the remaining fuel was weighed. This procedure was carried similarly for coal, charcoal and sawdust respectively.

CONTROLLED COOKING TEST (CCT)

Controlled Cooking Test (CCT) was conducted out-doors on a cool morning to simulate traditional approach to cooking in rural areas of African and to compare the fuel consumption rate and time spent in cooking a meal of rice on the stove. Equal quantities (0.2kg) of rice were placed in the two aluminium pots procured each containing 2 litres of water. The stove was charged with the given quantity of fuel and the pot was placed on the lit stove. Stopwatches were set to monitor cooking duration and at the end of cooking, the time taken as well as quantity of fuel were noted and recorded. The smoke emission time was recorded. These tested was done taking water, bean and rice as treatment, while the blocks were taking as the fuel consisting of wood, charcaol,coal and sawdust respectively.

ANALYSIS OF RESULTS.

A two way analysis of variance (ANOVA) for fuel consumption and smoking time are shown in the following tables below employing fuels as blocks, while types of food as treatment

Table 1:ANOVA for Fuel consumption (Grammes)

Wood

Charcoal

SAWDUST

COAL

Xi

BEANS

1217

947

457

1134

481

772

460

1135

1220

402

450

1135.5

Xij.

2918

2121

1367

3405.5

9809.5

RICE

1393

588

614

937

1400

580

614

904

1450

582

750

920.5

4243

1750

1978

2761.5

10732.5

WATER

650

411

457

1003

650

350

468

1004

764

400

577

1003.5

Xij.

2064

1161

1502

3010.5

7737.5

Xi.

9225

5032

4847

9175

28279.5

x. 28279.5

Table 2 shown below is Anova summary table for fuel consumption

Table 2: ANOVA SUMMARY TABLE:

Source

df

SS

MS

F ratio

Block

3

2019147.549

673049.193

29.266

Treatment

2

392087.169

196043.845

8.525

Interaction

6

706343.93

117722.887

5.199

Error

24

551934.5

22997.271

Total

35

36699513.18

Block: Fcal > Fj-1 (k-1)

Treatment: Fcal > F1-1, IJ (k-1) Interaction: Fcal > F(1-1) (J-I), IJK (k-1) In this case, = 0.05

Table 3;Anova table for smoking time

Block Treatment

WOOD

CHARCOAL

SAWDUST

COAL

Xj..

BEANS

4.03

2.83

2.17

15.05

3.17

3.17

2.08

14.37

3.83

3.08

3.08

14.77

Xij

11.03

9.08

7.33

44.19

71.63

RICE

5.17

3.17

2.83

13.87

5.83

3.08

2.67

14.10

4.17

2.80

3.17

13.97

Xij

15.17

9.05

8.67

41.94

74.83

WATER

5.00

3.43

2.17

15.83

4.83

3.83

2.00

16.53

3.17

3.17

3.17

16.18

Xij

13.00

10.43

7.34

48.54

79.31

X.j.

39.20

28.56

23.34

134.67

225.77

X. = 225.77

In this computation = 0.05

In table 3.5, I = 3,J = 4, K = 3

Table 4Shown below is the ANOVA summary table for smoking time

Table 4: ANOVA Summary Table

Source

df

SS

MS

Ratio

Block

3

921.118

307.039

1176.395

Treatment

2

2.481

1.241

4.775

Interaction

6

8.693

p>1.449

5.552

Error

24

6.253

0.261

Total

35

938.545

Block Fcal FjI ,IJ ( K 1), Treatment: Fcal Fj I ,IJ ( K 1), Interaction: Fcal FJ 1, IJ ( K 1),

DUNCAN MULTIPLE TEST

Employing the duncan multiple test on data matrix table 1 and table 2 develop for fuel consumption ,the following analysis was carrying out.

Standard error for column means, Sx =

MSE

=

IK

22997.21

3×3

= 50.550

S MSE 22997.21

Standard error for row means, x =

JK

4×3

= 43.777

Column Means Difference Test:

x1 = 538.556 x2 = 559.111, x1 = 1019.500 and x1 = 1025.000

Using 0.005, n2 24 and q values 2,3,4 the corresponding values for r from the Duncan table are as tabulated below.

Tables 5: r Values Table

q

2

3

4

r

2.93

3.08

3.16

S

S

TABLE 6:The least significant range (LSR) is obtained by multiply r values by x

q

2

3

4

LSR

148.112

155.694

159.738

The tests for difference are as follows:

q = 4 : x4 – x1 = 1025 538.556 = 486.444 > 159.738 (Significant)

q = 3 : x4 – x2 = 1025 559.111 = 465.889 > 155.694 (Significant)

x3 – x1 = 1019 538.556 = 480.444 > 155.694 (Significant)

q = 2: x4 – x3 = 1025 1019 = 6 < 148.112

x3 – x2 = 1019 559.111 = 459 > 148.112 (Significant)

x2 – x1 = 559.111 528.556 = 20.555 < 148.112

Row Means Difference Test:

x1 = 644.792, x2 = 817.458 and x3 = 894.375

Using = 0.05, n2 = 24 and q values 2,3: r and LSR values are obtained and tabulated as below:

Table 7: r and LSR Values

q

2

3

r

2.93

3.08

LSR

128.267

134.833

The best for difference:

q = 3 : x3 – x2 = 894.375-644.792 = 249.583> 134.8333 (Significant)

q = 2: x3 – x2 = 894.375 817.458 = < 128.267

x2 – x1 = 817.458 644.792 = 172.666 > 128.267 (Significant)

Duncan Multiple Test for Smoking Time

Employing the duncan multiple test on data matrix table 3 and table 4 develop for smoking time ,the following analysis was carrying out.

S

S

Column: =

x

MSR

=

JK

0.261

3×3

= 0.029

S

S

Row: =

x

MSR

=

JK

0.261

4×3

= 0.022

Column Means Difference Test:

x1 = 2.593, x2 = 3.173, x3 = 4.356 and x4 = 14.963

Apply = 0.05, n2 = 24 and q values 2,3,4 r and LSR are obtained as earlier discussed.

Table 8: r and LSR Values Table

q

2

3

4

r

2.93

3.08

3.16

LSR

0.085

0.089

0.092

q = 4: x4 – x1 = 14.963 2.593 = 12.370> 0.092 (Significant)

q = 3: x4 – x2 = 14.963 3.173 = 11.790> 0.0927 (Significant)

x3 – x1 = 4.356 2.593 = 1.763 > 0.089 (Significant)

q = 3: x4 – x3 = 14.963 – 4.356 = 10.60 > 0.085 (Significant)

x3 – x2 = 4.356 3.173 = 1.183 > 0.085 (Significant)

x2 – x1 = 3.173 2.593 = 0.58 > 0.08 (Significant)

Row Means Difference Test:

x1 = 5.969, x2 = 6236, x3 =6.069

Using = 0.05, n2 = 24 and q values 2,3. Then the values of r and LSR values are obtained as shown in table 9

Table 9: r and LSR Values

q

2

3

r

2.93

3.08

LSR

0.064

0.068

q = 3: x3 – x1 = 6.609 5.969 = 0.640 > 0.068 (Significant)

q = 2: x3 – x2 = 6.609 6.236 = 0.373 > 0.064 (Significant)

x2 – x1 = 6.623 5.969 0.654 > 0.068 (Significant)

RESULT AND DISCUSSION

Result and Discussion on Fuel Consumption

The fuel type i.e wood, charcoal, sawdust and coal were taken as blocks and the food items on which the observations were made were regard as treatments. Refering to table 2.

FB =

F1 =

MSA MSE MSB

MSE

673049.193

=

22997.271

196043.845

=

22997.271

29.266

8.525

F1 =

MSAB 117722.887

= 8.119

MSE

j = 0, i

respectively.

22997.271

= 0 and ( ) ij = 0 implies no column effect, no row effect and no interaction effect

Rejection: Fcal > Ftable

BLOCK

Fcal = 29.666

Ftable = 3.01

Since fcal > ftable we have no evidence to accept the null hypothesis and we conclude that the fuel types have significantly different effects on heat generated by the wood stove.

TREATMENT

fcal = 8.525

ftable = 3.40

since fcal > ftable we reject the null hypothesis and conclude that in cooking/boiling the food items consume different amounts of fuel.

INTERACTION

fcal = 5.119

ftable = 2.51 Since fcal > ftable

We reject the null hypothesis and support the argument that there is interaction effect among the fuel types and food items. The meaning of this statistical inference is that the amount of fuel utilized is dependent of the nature of food items and fuel types.

Result and Discussion on smoking time

FB =

MSA MSE

307.039

=

0.261

MSB

= 1176.395

0.241

FT =

MSE

=

0.261

= 4.755

FT =

MSAB 1.449

= 5.552

MSE

Rejection: fcal > ftable

BLOCK

0.261

Fcal = 1176.395

Ftable = 3.01

We fail to accept the null hypothesis because Fcal = 176.395 > Ftable = 3.01. This conveys the argument that the smoking time is significantly influenced by the fuel type.

TREATMENT

Fcal = 4.755

Ftable = 3.40

We have no sufficient evidence to accept the null hypothesis since fcal = 4.755 > ftable = 3.40

INTERACTION

Fcal = 5.552

Ftable = 2.51

Since fcal > ftable we have no evidence to reject the alternative hypothesis. This implies that there is interaction effect.

Duncan multiple range test

Further evaluation was undertaken on the data analysis since the overall tests of means, for block, treatment and interaction fall into rejection region. In this case, the Duncan multiple range test was employed. Assumption: equal sample sizes exists for both variables. Considering Table 2, Table 4, and their respective r and LSR Tables for column and row.

FUEL UTILIZED

Table 7: r and LSR and Table6: for column means

q

2

3

4

R

2.93

3.08

3.16

LSR

148.112

155.694

159.738

Sx =

MSE

=

IK

22997.271

3×3

= 50.550

x1 = 538.556, x2 = 559.111, x3 = 1019, x4 = 1025

q = 4: x4 x1 159.738

q = 3: x4 x2 155.694

q2 = 2 : x4 x3 148.112

x3 x2 148.112

x2 x1 148.112

xi sawdust, x2 charcoal, x3 coal, x4 wood

The implication of this is as follows;Between wood and sawdust the differencein their ability to generate heat is very significant.

The difference in the heating ability obtained between coal and wood is not significant.

x1 x2 x3 x4

Their specific fuel consumption is of the following ascending order.

Saw dust charcoal coal wood Hence, sawdust is the most economical of the four fuel types.

SMOKING TIME

Table 8:r and LSR and Table9: for Column Means

q

2

3

4

R

2.93

3.08

3.16

LSR

0.085

0.89

0.092

Sx = 0.305

x x1 = 2.593, x 2 = 3.173, x3 = 4.356 and x 4 = 14.963

q = 4: x 4 – x1 > 0.092

q = 3: x3 – x1 > 0.089

q = 2: x 4 – x3 > 0.085

x3 – x 2 > 0.085

x 2 – x1 > 0.085

x1 = Sawdust,

x 2 = Charcoal,

x3 Wood x 4 = Coal.

The statistical inference here is that there exists significant difference among the smoking time of the four fuel types, but the least difference occurs between charcoal and sawdust.

x1 x2 x3 x4

Thus the smoking time of the fuel types is arranged in ascending order as follows: SAWDUST CHARCOAL WOOD COAL

Sawdust gives the smallest smoking time.

CONCLUSION

The World Health Organization has documented the significant number of deaths caused by smoke from home fires. The negative impacts can be reduced by using improved cook stoves, improved fuels (e.g. biogas, or kerosene instead of dung), changes to the environment (e.g. use of a chimney), and changes to user behaviour (e.g. drying fuel wood before use). Based on these underlying facts an improved biomass cooking stove was fabricated and the results of performance analysis employing various biomass fuel such wood, coal, charcoal and sawdust as blocks showed that sawdust has the lowest fuel co(nsumption rate. Considering pollution emission level sawdust among the fuel type reveal the least smoking time. Having achieved these goals we do believe that this improved biomass cooking stove is more efficient, meaning that the stove's users is afforded the choice of using an alternative fuel like sawdust which is majorly considered as waste product , suffer less emphysema and other lung diseases prevalent in smoke-filled homes, while reducing deforestation and air pollution.

REFERENCES

1 Amitova .H. and Walton J.D (1977).A State of The Art Survey of Solar Powered Irrigation Pumps, Solar Cookers And Wood Burning Stoves For Use In Sub-Sahara Africa Final Report . Retrieved August 24,2012, from books.google.com/…/A_State_of_the_Art_Survey_of_Solar_Power.html?id

  1. Baldwin S.F.(1987). Biomass Stoves: Engineering Design, Development and Dissemination. Princeton,NJ Volunteers in Technical Assistance.Retrieved September 20,2012,from http//www.aprovecho.org/lab/images/stories/camp08/BiomassStoves.pdf

  2. Bryden,M., Still. D., Scott. P., Hoffa.G., Ogle.D. and Goyer.K.(2008). Design Principles for Wood Burning Cook Stoves.Retrieved August 20,2012,from http//www.unep.org/…/fourth%20of%20the%20series%20of%204%20Surya%20papers.pdf

  3. Erg, (1986). Energy Research: directions and issues for developing countries,IDRC-250e,Energy Research Group, International Development Research Centre, Ottawa, Ont. Canada

  4. Kumar,D.S.( 2010).Heat And Mass Transfer , 7th ed. New Delhi:S.K Kataria And Sons , pp45-175 .

  5. Montgomery, D.C.(2001).Design and Analysis of Experiments. New York.5th Ed: John Wiley And Sons Inc,pp61-130

  6. World Health Organization Fact sheets(2005). Indoor air pollution and health, Retrieved July 20, 2012 from http//www.who.int/entity/mediacentre/factsheets/en/

  7. Stout, B. A and Best.G.( 2001). Effective energy use and climate change: Needs of rural areas in developing countries. Invited overview. Vol. III.

Leave a Reply