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Type of the Paper (Article)

1

Performance Evaluation of the Physical and

2

Combustion Properties of Briquettes Produced from

3

Agro-Wastes and Wood Residues

4

Babajide Charles Falemara1*, Victoria Ibukun Joshua2, Oluwaseyi Oluwafunmi Aina1 and Rivi

5

David Nuhu3

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1 Forestry Research Institute of Nigeria, P.M.B. 5054, Forest Hills, Jericho, Ibadan, Oyo State, Nigeria;

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[email protected]

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2 Montane Forest Research Station, Jos, Plateau State; [email protected]

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3 Federal College of Forestry, Jos, P.M.B. 2019, Jos Plateau State, Nigeria; [email protected]

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* Correspondence: [email protected]; +2348066714571

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Abstract: This study investigated the physical and combustion properties of briquettes produced

13

from agricultural wastes (groundnut shells and corn cobs), wood residues (Anogeissus leiocarpus)

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and admixtures of the particles at 15%, 20% and 25% starch levels (binder). A 6 x 3 factorial

15

experiments in a Completely Randomized Design (CRD) was adopted for the study. The briquettes

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produced were analyzed for density, volatile matter, ash content, fixed carbon and specific heat of

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combustion. The result revealed that the density ranged from 0.44g/cm3 to 0.53g/cm3, while

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briquettes produced from groundnut shells had the highest (0.53g/cm3) significant mean density.

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Mean volatile matter and ash content of the briquettes ranged from 24.35% to 34.95% and 3.37% to

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4.91%. A. leiocarpus and corn cobs particles had the lowest and highest ash content respectively. The

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briquette fixed carbon and specific heat of combustion ranged from 61.68% to 68.97% and

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7362kca/kg to 8222kca/kg respectively. Briquette produced from A. leiocarpus particles had the

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highest specific heat of combustion. In general, briquettes produced from A. leiocarpus particles and

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admixture of groundnut shell and A. leiocarpus particles at 25% starch level had better quality in

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terms of density and combustion properties and thus suitable as environmentally friendly

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alternative energy source.

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Keywords: Biomass; Briquette; Combustion; Density; Energy source

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1. Introduction

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An estimated 3 billion people in our current estimated 7.63 billion people in the world [1, 2] rely

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upon wood, kerosene, biomass and coal for domestic cooking. This led to rapid deforestation and

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loss of more than 3% of the world's forests on an annual basis. The use of wood is increasing on daily

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basis especially in the less technologically developed countries of the world [3]. With deforestation

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becoming a major problem in many parts of the developing world, there is increased scarcity of

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fuelwood for household cooking. Increase in the energy demand and use in Nigeria due to rapid

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growth in population and industry has raised concerns about the economic and environmental

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impacts of power generation based on national energy sources. Kerosene and gas are the major

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cooking fuel [4].

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Environmental and ecological problems are the major issues of concern associated with

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exploitation of these fuels. Another major challenge with these fuels is their unsustainability and

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projected depletion over the years. The use of fuel wood in the large scale without replenishing poses

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serious environmental consequences in many countries. Also population increase in countries like

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Nigeria places more demands on energy to light and heat homes, to cook food, to drive transport,

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(2)

wood for fuel energy. One of such alternative means is the use of biomass for briquette production

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through densification and manufacture of carbonized or uncarbonised processes [6]. Biomass in the

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form of wood and agricultural wastes constitute one of the third largest alternative source of

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primary energy in the world aside from coal and oil [7].

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The large quantities of agricultural residues produced in Nigeria can play a significant role in

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meeting her energy demand. However, the abundant quantities of agricultural wastes and forest

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residues are neither managed effectively, nor utilized efficiently in all developing countries. The

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common practice is to burn these residues or they are left to decompose [8]. This burning itself

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contributes to atmospheric pollution, but more than that; the burning or decomposition is a waste of

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available energy [9]. Recycling of these biomass helps to ameliorate the accumulation of greenhouse

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gases [10] and can be renewably converted into liquid, solid or gas states [11]. Briquetting provides a

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value addition, sustainable and efficient utilization of the biomass residues [12].

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The natural environment cannot continue to provide cooking fuel for the ever increasing

59

population. An alternative and sustainable fuel energy source becomes imperative. The focus of this

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study is to examine the qualities (physical and combustion properties) of briquettes produced from

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agricultural wastes (groundnut shells and corn cobs), wood residues (Anogeissus leiocarpus) and

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admixtures of the particles.

63

2. Materials and Method

64

2.1. Study Site

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The experiment was carried out in Federal College of Forestry Jos, Plateau State Nigeria. Jos is

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located in Northern Guinea savanna is situated between latitudes 80 and 30´ and 100 10 N and

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longitude 80 20´ and 90 30´E.

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2.2. Materials for the briquette production

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The materials used for the briquette production include agricultural waste from groundnut shell

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and corn cobs; and sawdust of Anogeissus leiocarpus (Plate 1a). The choice of the agricultural wastes

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was based on the relative abundance of the groundnut and corn crops in the northern parts which

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are annual crops. The A. leiocarpus was chosen also based on its relative abundance in the timber

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market.

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2.3. Sample Preparation Procedures

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Wood samples (planks) of A. leiocarpus species was obtained from the timber market at Katako.

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The wood samples were processed and converted into sawdust using circular saw machine. The

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agricultural wastes (groundnut shells and corn cobs) were sourced from surrounding farms and

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pulverized into small particles. The particles were pre-treated in hot water at 1000C for 30 minutes to

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remove extractives that may inhibits the binding ability of the particles and cassava starch. They were

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thereafter sundried for 7 days so as to reduce the moisture content (Plate 1a & 1b). The particles were

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sieved using 80µm wire mesh, so as to reduce the particles size into fine particles [13].

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The starch binder at different levels of 15%, 20% and 25% [14, 15] was prepared with 250ml

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boiled water, stirred and mixed with measured (Plate 1d) grams of separate particles singly and

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combined (at a mixing proportion of 50:50). The homogenously mixed stock was poured into the

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fabricated briquette moulder (Plate 1e) and compressed using hydraulic jack (Plate 1f). The briquettes

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were then removed and air dried for 30days. Proximate analysis was thereafter carried out for

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properties investigation.

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2.4. Experimental Design

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The experimental design for the study was 6 x 3 factorial experiments in a Completely

95

Randomized Design (CRD). The factors consist of six (6) particle types (A. leiocarpus sawdust only

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(T1), groundnut shell only (T2), corn cobs only (T3), A. leiocarpus sawdust (T4) + Groundnut shell, A.

97

leiocarpus sawdust + Corn Cobs treatment combination (T5) and A. leiocarpus sawdust + Groundnut

98

shell + Corn Cobs treatment combination (T6) and three starch levels (15%, 20% and 25% starch

99

levels). This gave18 treatment combination replicated four times (Plates 2a, 2a, 3a-3f).

100

101

102

103

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105

106

107

108

109

110

111

112

113

114

115

116

117

118

119

120

121

122

123

124

125

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Plate 1. Materials used for the production of the briquette and production process. (a) Particle types and starch;

127

(b) Pre-treatment in hot water (1000C); (c) Drying of the particles; (d) Weighing of the materials (particle and

128

starch); (e) Fabricated briquette hydraulic moulder; (f) Compression, hydraulic pressing and moulding of the

129

briquette.

130

131

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133

134

135

136

137

138

139

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(f)

(a) (b) (c)

(4)

143

144

145

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147

148

149

150

151

152

153

154

155

156

157

Plate 2. (a) Briquettes produced based on particle types; (b) Briquettes produced based on particle types and

158

starch levels

159

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161

162

163

164

165

166

167

168

169

170

171

172

173

174

175

176

177

178

179

180

181

182

183

184

185

186

Plate 3. Briquettes produced from different particle types. (a) Anogenssus leiocarpus briquette (T1);

187

(b) Groundnut Shell briquette (T2); (c) Corn Cobs briquette (T3); (d) Admixture of T1 + T2 briquette;

188

(e) Admixture of T1 + T3 briquette; (f) Admixture of T1 + T2 + T3 briquette.

189

2.5. Variables Assessed

190

The following parameters were determined on each of the sample briquettes [14, 16].

191

 Relaxed density: The relaxed density was determined according to the weight and the volume of

192

each briquette block which depends on its shape. The volume (V=πr2h) was be based on direct

193

(a) (b) (c)

(e)

(d) (f)

G ro u n d n u t sh el l p a rt ic le A . l ei oc ar p u s p a rt ic le C o rn c o b s p a rt ic le G ro u n d n u t sh el l + A . le io ca rp u s p a rt ic les C o rn c o b s + A . l ei oc ar p u s p a rt ic les G ro u n d n u t sh el l+ C o rn co b s+ A . l ei oc ar p u s p a rt ic les

(a) (b)

15% starch level

20% starch level

25% starch level

(5)

measurement of radius and height (m) and the weight (g) using digital weigh balance. The

194

density of each briquette sample was calculated using the formula in equation 1;

195

= ( )

( ) ………...Equation 1

196

 Volatile matter (%Vm): The percentage volatile matter was determined by placing the crucible

197

containing the oven dry weight (w2) in the furnace for 10 minute at 5500C to obtain weight (w3)

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after which the volatile matter in it must have escaped. The percentage volatile matter (%Vm)

199

was calculated using the formula as shown in equation 2;

200

(%) =( ( ) – ( ) .

( )

201

………Equation 2

202

 Ash content (%Ash): 2g of oven dry pulverized briquette was placed in a crucible (w2). The

203

crucible was placed in the furnace for 4 hours at 550C to obtain the ash weight (w4). Percentage

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ash content was calculated using equation 3;

205

ℎ (%) = ( )

( ) ……….Equation 3

206

 Fixed carbon (%FC): The percentage fixed carbon was calculated by subtracting the sum of

207

percentage volatile matter and percentage ash content from 100% (Equation 4).

208

(%) = 100% − (% + % ℎ) ……...Equation 4

209

 Specific Heat of Combustion (Hc): The specific heat of combustion (Hc) was calculated from the

210

formula as shown in equation 5;

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Specific Heat of Combustion (Hc) = 0.35 (147.6 x %FC) + (144 x %VM) + (%Ash)

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…..……...Equation 5

213

2.6. Statistical Analysis

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Analysis of variance (ANOVA) resulting from 18 treatment combinations and four replicates

215

was carried out to evaluate the performance of each of the treatments. Where significant differences

216

existed, Duncan’s Multiple Range Test (DRMT) was used for mean separation to determine the

217

magnitude of differences.

218

3. Results

219

3.1. Effect of Treatments and Starch Levels on Relaxed Density of the Briquette

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The relaxed density of the briquettes ranged between 0.46g/cm3 and 0.53g/cm3 (Figure 1)

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Briquette made with groundnut shell particles had the highest relaxed density (0.53g/cm3), while

222

briquette produced with the three combinations of A. leiocarpus, groundnut shell and corn cobs

223

particles had the lowest (0.46g/cm3) mean briquette density. The statistical analysis revealed that

224

groundnut shell had significantly higher effect on the relaxed density of the briquette, while the other

225

particle treatments and treatment combinations were not significantly different from each other

226

(p≥0.05).

227

The effect of starch levels on briquette relaxed density (Figure 2) indicated that briquettes

228

produced at 20% starch level had the highest relaxed density (0.49g/cm3), while briquette produced

229

at the lowest starch level (15%) had the lowest density (0.46g/cm3). The effects of the three starch

230

levels on briquette relaxed density were not significantly different (p≥0.05) from each other, as there

231

were little variations in the relaxed density of the briquettes produced from the three starch levels.

232

233

(6)

236

Figure 1. Mean Effect of Treatments on Density (g/cm3) of Briquette

237

Means in the same bar having the same superscript are not significantly different (p≥0.05)

238

239

240

241

242

Figure 2. Mean Effect of Treatments on Density (g/cm3) of Briquette

243

Means in the same bar having the same superscript are not significantly different (p≥0.05)

244

245

3.2. Effect of particle types on combustion properties of the briquettes

246

The volatile matter (Figure 3) ranged between 26.4% and 34.9%. Briquettes made with A.

247

leiocarpus and mixture of groundnut shell and A. leiocarpus had the highest (34.9%) and lowest

248

(26.4%) volatile matter respectively. The statistical analysis revealed that the effects of all particle

249

types excluding A. leiocarpus wood particle on volatile matter were not significantly different

250

(p≥0.05) from each other. The volatile matter of briquettes produced from mixture of agricultural

251

residues (A+gnut shell (26.4), A+corn cobs (28.5%) and A+G+C (28.4%) and wood particle were lower

252

than briquettes produced from unmixed/uncombined particle types (A. leiocarpus (34.9%),

253

groundnut shell (29.8%) and corn cobs (31.2%). Ash content (Figure 3) of the briquettes ranged

254

between 3.4% and 4.9%. The ash content of the briquettes were not significantly different from each

255

other, though corn cob briquette had the highest ash content (4.9%) while briquette from Anogeissus

256

0.47b 0.53

a

0.44b 0.46b 0.48b 0.46b

0.00 0.10 0.20 0.30 0.40 0.50

A. leiocarpus particle

Groundnut Shell Corn cobs Groundnut shell + A.leiocarpus

Corn cobs + A. leiocarpus

A.leiocarpus + Groundnut shell

+ Corn cobs

R

e

lax

e

d

D

e

n

si

ty

(g/

c

m

3)

Particle Type

0.46

a

0.49

a

0.47

a

0.44 0.45 0.45 0.46 0.46 0.47 0.47 0.48 0.48 0.49 0.49 0.50

15%SL

20%SL

25%SL

R

el

ax

ed

d

en

si

ty

(g/

cm

3

)

(7)

leiocarpus particle had the lowest ash content (3.4%). Mixture of agricultural residues (gnut shell and

257

corn cobs) and wood particles had the same ash content.

258

The specific heat of combustion and fixed carbon ranged from 7362kca/kg to 8222kca/kg and

259

61.7% to 69% respectively (Figure 4). As similarly observed for volatile matter, the specific heat of

260

combustion of the briquettes produced from mixed particles (groundnut shell and A. leiocarpus

261

(7362kca/kg); corn cobs and A. leiocarpus (7561kca/kg), A. leiocarpus, groundnut shell and corn cobs

262

(7589kca/kg)) were lower than the specific heat of combustion of briquettes produced from unmixed

263

A. leiocarpus (8222kca/kg), groundnut shell (7677 kca/kg) and corn cobs (7882kca/kg) particles. On

264

the other hand, the fixed carbon of briquettes produced from mixed particles (groundnut shell and

265

A. leiocarpus (69%); corn cobs and A. leiocarpus (66.8%), A. leiocarpus, groundnut shell and corn

266

cobs (67.7%)) were higher than the fixed carbon of unmixed particle types (A. leiocarpus (61.7%),

267

groundnut shell (65.4%) and corn cobs (63%) particles). Briquette produced from mixture of

268

groundnut shell and Anogeissus leiocarpus particles had the lowest specific heat of combustion

269

(7362kca/kg) and highest fixed carbon content (69%). The specific heat of combustion and fixed

270

carbon were not significantly different from each other (p≥0.05).

271

272

273

Figure 3. Effect of particle types on percentage volatile matter (%VM) and Ash content (%) of the

274

briquette

275

Means in the same bar having the same superscript are not significantly different (p≥0.05)

276

277

34.9a

29.8bc 32.1ab

26.4c 28.5bc 28.4bc

3.4a

4.8a 4.9a

4.7a 4.7a

3.9a

0.0 1.0 2.0 3.0 4.0 5.0 6.0

0.0 5.0 10.0 15.0 20.0 25.0 30.0 35.0 40.0

Anogeissus leiocarpus

Groundnut Shell Corn cobs Gnut shell + A. leiocarpus

Corn cobs + A. leiocarpus

A. leiocarpus + Gnut shell + Cobs

A

sh

(%

)

V

o

lati

le

m

atte

r

(%

)

Particle Types

(8)

278

Figure 4. Effect of particle types on specific heat of combustion (SHC) and fixed carbon (%FC) of the

279

briquette

280

Means in the same bar having the same superscript are not significantly different (p≥0.05)

281

282

283

3.3. Effect of starch levels on combustion properties of the briquettes

284

The result of findings as shown in Figures 5 and 6 revealed that briquettes produced at 20%

285

starch level had the lowest volatile matter (24.2%) and specific heat of combustion (7165Kca/kg),

286

while 25% starch level produced briquettes with the highest volatile matter (33.5%) and specific heat

287

of combustion (8051Kca/kg). On the other hand, briquettes produced at 20% starch level had the

288

highest ash content (4.7%) and fixed carbon (71.1%), while 25% starch level produced briquettes

289

having the lowest ash content (4.1%) and fixed carbon (62.4%). In addition, the volatile matter of

290

briquettes produced at 15% and 25% starch levels were not significantly different from each other as

291

similarly observed for specific heat of combustion and fixed carbon. The effects of the three starch

292

levels (15%, 20% and 25%) on ash content of the briquettes were not significantly different from each

293

other (p≥0.05). The effects of 20% starch level on fixed carbon and specific heat of combustion was

294

significantly (p≤0.05) higher and lower respectively from the other starch levels (15% and 25%).

295

296

Figure 5: Effect of Starch levels on percentage volatile matter (%VM) and Ash (%) of the briquette

297

Means in the same bar having the same superscript are not significantly different (p≥0.05)

298

8222a 7677bc 7882ab 7362bc 7561c 7589bc

61.7c

65.4abc

63.0bc

66.8ab

67.7a

58.0 60.0 62.0 64.0 66.0 68.0

6800 7000 7200 7400 7600 7800 8000 8200

Anogeissus leiocarpus

Groundnut Shell Corn cobs Gnut shell + A. leiocarpus

Corn cobs + A. leiocarpus

A. leiocarpus + Gnut shell + Cobs

F

ix

e

d

C

ar

b

o

n

(%

)

S

H

C

(K

c

a/

k

g)

Particle Types

SHC (Kca/kg) %FC

32.4

a

24.2

b

33.5

a

4.4

a

4.7

a

4.1

a

3.8

3.9

4.0

4.1

4.2

4.3

4.4

4.5

4.6

4.7

4.8

0.0

5.0

10.0

15.0

20.0

25.0

30.0

35.0

40.0

15%SL

20%SL

25%SL

%

A

sh

%

V

ol

at

il

e

M

at

te

r

Starch Levels

%Volatile Matter

(9)

299

300

301

Figure 6: Effect of Starch levels on percentage specific heat of combustion (Kca/kg) and fixed carbon

302

(%FC) of the briquette

303

Means in the same bar having the same superscript are not significantly different (p≥0.05)

304

305

4. Discussion

306

4.1. Relaxed Density

307

The briquette produced from groundnut shell had poor compaction and agglomeration at

308

higher starch level which contributed to its higher significant effect on density (Figure 1). This

309

assertion contradicts the report of Egbewole et al. [14] on poor agglomeration of briquette at lower

310

starch levels of 10% and 15% for wood sawdust. The implication of this is that particle sizes and type

311

have great influence on density of briquettes as similarly observed by Aina et al. [17]. Quality of the

312

mixture composition and technological characteristics of the bio-raw material have a very important

313

influence on the particle agglomeration during the pressing process [18]. In collaboration with the

314

findings of Tembe et al. [15] on comparative analysis of combustion properties of briquettes from

315

groundnut shell and rice husk, the starch level had no significant effect on the briquette density. The

316

relaxed density obtained in the study is within the range of values as obtained by Ige et al. [19] and

317

Onuegbu et al. [20] who reported a relaxed density range between 0.319g/cm3 and 0.590g/cm3. In

318

addition, high density is an indication of longer burning time, as such briquettes produced from

319

groundnut shell (0.53g/cm3); admixture of corn cobs and A. leiocarpus (0.48g/cm3); and A. leoicarpus

320

(0.47g/cm3) particles will tend to burn for a longer time compare to others.

321

4.2. Volatile Matter

322

The range of values for volatile matter (24.2% and 34.95%) of briquettes produced in this study

323

(Figures 3 and 5) is lower than 43% to 49% obtained by Adegoke et al. [13] from mixed sawdust

324

briquettes of tropical hardwood species, 72.33% to 77.44% of briquettes produced from three

325

hardwood species as reported by Emerhi [21] and 68% stated by Ige et al. [18]. Adetogun et al. [22] in

326

their study on briquettes from maize cobs reported a higher volatile matter ranging between 57.82%

327

and 62.91% compared to a lower value of 31.2% and 33.5% for briquettes made from maize cob in

328

this present study (Figures 3 and 5). Conversely, Egbewole et al. [14] and Sotannde et al. [23] reported

329

a lower volatile matter for briquettes made from wood sawdust (13.89% to 19.33%) and neem-wood

330

residues (10% to 13%) respectively.

331

Volatile matter which is a mixture of short and long chain hydrocarbons, aromatic

332

7931

a

7165

b

8051

a

63.2

b

71.1

a

62.4

b

58.0

60.0

62.0

64.0

66.0

68.0

70.0

72.0

15%SL

20%SL

25%SL

6600

6800

7000

7200

7400

7600

7800

8000

8200

F

ix

ed

C

ar

b

on

(

%

)

Starch Level

S

H

C

(

K

ca/

k

g)

(10)

influences secondary air requirement and distribution aspects. Lower volatile matter is an indication

335

that the briquettes might not be easy to ignite, but once ignited they will burn smoothly with clean

336

flame without smoke, while high volatile matter results in high combustibility at low ash content

337

[24]. In contrast, the higher the volatile matter of a briquettes, the higher the amount of emissions

338

during burning. This implies that low volatile matter is required for good quality briquette and it

339

typically range between 20 and 35%. The volatile matter values obtained in this study is with the

340

acceptable quality values required for fuelwood.

341

4.3. Ash Content

342

The low ash content as observed in this study (Figure 3 and 5) is a reflection of the high specific

343

heat of combustion/heating value (Figures 4 and 6) which is an indication that the briquette does not

344

contain high mineral (non-combustible) matters. As posited by Sotannde et al. [23] ash content

345

normally causes an increase in the combustion remnant, thereby lowering the heating effect. The

346

briquettes produced at 25% starch level had the lowest ash content (Figure 5) thus indicating its

347

suitability in briquette production. The low ash content as observed in this study corroborates the

348

findings of Akowuah et al. [25], Adetogun et al. [22] and Sotannde et al. [23] who all reported a lower

349

ash content of 2.6%, 1.06% to 1.23% and 3.50% to 5.75% respectively. On the contrary, higher ash

350

content ranging from 19.07% to 21.72%; 10.44% to 42.33%; 18.67% to 22.06%; and 18% were reported

351

by Emerhi [21], Ogbuagu et al. [26], Ikelle and Anyigor [27], and Ige et al. [19] respectively. Lower

352

ash content is an indication of good quality briquette and generally range between 5% and 20% [28].

353

Ash is an impurity that will not burn. Higher ash content in a fuel usually leads to higher dust

354

emissions, air pollution and affects the combustion volume and efficiency of combustion [29].

355

Consequently, the lower ash content as observed in this study validates the high quality and

356

improved efficiency of the briquettes.

357

4.4. Specific heat of combustion

358

The specific heat of combustion values ranging between 7362kcal/kg and 8222kcal/kg (Figures

359

4 and 6) as obtained in this study is within the range of values (7500kcal/kg and 8000kcal/kg) as

360

similarly reported by Bamiyo [30]. However, Egbewole et al. [14] and Tembe et al. [15] in their

361

findings reported a lower specific heat of combustion ranging from 4908.52kcal/kg to 5257.66kcal/kg

362

and 3284kcal/kg to 3980kcal/kg respectively.

363

4.5. Fixed Carbon

364

Fixed carbon gives an indication of the proportion of char that remains after the devolitization

365

phase or after volatile matter is distilled off. It gives a rough estimate of the heating value of a fuel

366

and acts as the main heat generator during burning [25]. The fixed carbon as observed in this study

367

(Figures 4 and 6) is close to the high fixed carbon content of briquette obtained by Sotannde et al. [23]

368

and Egbewole et al. [14] of 85.25% and 85.95% respectively. According to Sotannde et al. [23], it is

369

expected that the high fixed carbon and its smokeless flame will enhance the heat value and

370

combustion duration of briquette. However, the fixed carbon as reported in this study is relatively

371

higher than 9.06% to 11.46% obtained by Adegoke et al. [13] 5.75% to 8.28% stated by Emerhi [21],

372

16.80% - 20.90% quantified by Adetogun et al. [22] and 15% fixed carbon estimated by Ige et al. [19].

373

A good quality and efficient fuel briquette is dependent on lower volatile matter and ash content with

374

a higher fixed carbon content [31] in collaboration with result of findings of this study.

375

5. Conclusion

376

The study examined the physical and combustion properties of briquettes produced from

377

agricultural wastes (groundnut shells and corn cobs) and wood residues (Anogeissus leiocarpus) as

378

well as homogenous combination of the particles. The study affirmed that briquettes produced from

379

(11)

25% starch level had better quality in terms of density, agglomeration, compaction and combustion

381

properties with respect to high volatile matter, low ash content, high fixed carbon and high specific

382

heat of combustion. There were little variations in the quality of the briquette produced from these

383

two particle types compared to other homogeneous and heterogeneous particle types. This study has

384

been able to confirm that agricultural wastes alongside wood waste can be utilized in producing

385

quality briquettes. As such, wood wastes from A. leiocarpus and a combination of groundnut shell

386

and A. leiocarpus particle type using 25% starch level are suitable for briquette production due to

387

better combustion performance.

388

Subsequently, the briquettes will provide better and efficient environmentally friendly

389

alternatives to other forms of energy source, help to solve agricultural and wood wastes management

390

issues, help in the restoration of already destroyed forests by proving alternative fuel wood. It could

391

also enhance market diversification, rural economic empowerment and job opportunities.

392

393

Author Contributions: The first author conceived the research idea, adopted and designed the fabricated

394

briquette moulder, wrote the original draft manuscript, analyzed the data and review and editing of the

395

manuscript. The second author participated in the investigation and production process, reviewed and edited

396

the manuscript. The third author conducted the laboratory analysis and contributed to manuscript preparation

397

and review. The fourth author sourced and fabricated the materials used for the methodology, participated in

398

the investigation and production process as well as contributed to manuscript preparation.

399

Funding: This research received no external funding.

400

Conflicts of Interest: The authors declare no conflicts of interest.

401

402

6. References

403

1. World Health Organization. Household air pollution and health. Fact Sheet 2018. Accessed on the 4th of

404

July 2018 from http://www.who.int/news-room/fact-sheets/detail/household-air-pollution-and-health

405

2. Worldometers. Current World Population. Retrieved on the 4th of July 2018 from

406

http://www.worldometers.info/world-population/?

407

3. Aremu, M.O.; Agarry, S.E. Enhanced Biogas Production from Poultry Droppings using Corn Cob and Waste

408

Paper as Co-Substrates, International Journal of Engineering Science and Technology. 2013. 5, 2, 247-253

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4. Frank. O.O.; Akhihiero T.E. Fuel Briquettes from Water Hyacinth-Cow Dung Mixture as Alternative Energy

410

for Domestic and Agro-Industrial Applications. Journal of Energy Technologies and Policy. 2011. 3, 6, 56 –

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61

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5. Ismaila A.; Zakari I.Y.; Nasiru R.; Tijjani B.I.; Abdullahi I.; Garba N.N. Investigation on biomass briquettes

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as energy source in relation to their calorific values and measurement of their total carbon and elemental

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contents for efficient biofuel utilization. Advances in Applied Science Research. 2013. 4, 4, 303-309

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6. International Tropical Timber Organization. Tropical Forest Update, 15, 1, 2005. International Tropical

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Timber Organization (ITTO), Yokohama, Japan. 2005. 32pp.

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7. Chen, L.; Xing, L.; Han, L. Renewable energy from agro-residues in China: Solid biofuels and biomass

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briquetting technology. Renew. Sustain. Energy Rev. 2009, 13, 2689–2695.

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8. Oladeji, J.T. Utilization of Potential of Melon Shells for Pyrolysis as Biomass Fuels. World Rural Observation.

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2012, 4, 2, 60-64

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9. Oladeji, J.T.; Ogunsola, A.D. Pyrolysis of Sawdust into Medium-Grade Fuels and Chemical Preservatives.

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Proceedings of 2nd Engineering Conference of the School of Engineering; Federal Polytechnic, Offa, July

13-423

15, 2010. 64-67

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10. Havrland, B.; Ivanova, T.; Łapczyńska-Kordon, B.; Kolarikova, M. Comparative analysis of bio-raw

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materials and biofuels. 12th International Scientific Conference on Engineering for Rural Development –

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Proceedings, Latvia University of Agriculture Faculty of Engineering. 2013, T. 12, 541-544.

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11. Kambo, H.S.; Dutta, A. A comparative review of biochar and hydrochar in terms of production,

physical-428

chemical properties and applications. Renewable and Sustainable Energy Reviews. 2015, 45, 359-378. DOI:

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10.1016/j.rser.2015.01.050

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12. Li, Y.; Liu, H. High-pressure Densification of Wood Residues to Form an Upgraded Fuel” Biomass and

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of briquette produced from mixed sawdust of tropical wood species. Climate Change and Forest Resources

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Management: The Way Forward. In; Proceedings of the 2nd Biennial National Conference of the Forests

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and Forest Products Society. 2010. 368 – 371

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14. Egbewole, Z.T.; Alao, J.S.; Ogunsanwo, O.Y.; Sotunde, O.A; Aina K.S.; Akinyemi, O. Potential use of wood

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production. An Alternative for energy Generation. PAT Journal. 2009. 5, 1, 181-195.

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15. Tembe, E.T.; Adeogun, A.C.; Elaigwu, V.O. Comparative Analysis of Combustion Properties of Briquettes

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from Groundnut shell and rice husk. 36th Annual Conference of the Forestry Association of Nigeria. 2011.

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389 - 394

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16. Fuwape, J. A.; Sobanke, A.O. Combustion characteristics of wood briquettes produced from sawdust

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National Conference of Nigerian Society of Agricultural Engineering, 1998. 1- 11, 8 – 11th September, 1998.

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17. Aina, K.S.; Baiyewu, R.A.; Ogunleye, M.B.; Adegoke, I.A.; Adesope, A.S.; Fatade, B.O. Evaluation of

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Combustion properties of briquette produced from Cedrella odorata, Terminalia superba and Cordia

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millenii. Climate Change and Forest Resources Management: The Way Forward. In; Proceedings of the 2nd

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Biennial National Conference of the Forests and Forest Products Society. 2010. 395 – 400

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18. Alexandru, M.; Tatiana, I.; Bohumil, H.; Victor P.; Vasile, V. Particularities of bio-raw material particle

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agglomeration during solid fuel pressing process. Engineering for Rural Development. 2013. 499 - 503

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19. Ige, A.R.; Elinge, C.M.; Hassan, L.G.; Adegoke, I.A.; Ogala, H. Effect of Binder on Physicochemical

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Properties of Fuel Briquettes Produced from Watermelon Peels. AASCIT Journal of Energy. 2018, 5, 2,

23-451

27.

452

20. Onuegbu, T.U. Improving Fuel wood Efficiency in Rural Nigeria: A case for Briquette Technology, National

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Magazine of the CSN. 2010, 5, 4, 35-39.

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21. Emerhi, E.A. Physical and combustion properties of briquettes produced from sawdust of three hardwood

455

species and different organic binders. Advances in Applied Science Research. 2011. 2, 6, 236-246

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22. Adetogun, A.C.; Ogunjobi, K.M.; Are, D.B. Combustion properties of briquettes produced from maize cob

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of different particle sizes. Journal of Research in Forestry, Wildlife and Environmental. 2014. 6, 1, 28-38

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23. Sotannde, O.A.; Oluyege, A.O.; Abah, G.B. Physical and combustion properties of charcoal briquettes from

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neem wood residues. Int. Agrophysics, 2010, 24, 189-194

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24. Maninder, R.; Singh, K.; Grover, S. Using agricultural residues as a Biomass Briquetting: An Alternative

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source of energy. Journal of electrical and electronic Engineering. 2012, 1, 5, 11-15.

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25. Akowuah, O.J.; Kermausuor, F.; Mitchual, J.S. Physicochemical characteristics and market potential of

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sawdust charcoal briquette, International Journal of Energy and Environmental Engineering. 2012, 3, 20,

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26.

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26. Ogbuagu, J.; Onuegbu, T.; Ikelle I.I.; Chimezie O.; Anyigor, C. Production and analysis of the heating

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properties of coal and Rice husk briquettes using CaSO4 as a binder. Journal of Physical Science and

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Innovation. 2013. 1, 5, 35 – 44

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27. Ikelle, I.I.; Anyigor, C. Comparative Thermal Analysis of the Properties of Coal and Corn Cob Briquettes.

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IOSR Journal of Applied Chemistry (IOSR-JAC). 2014. 7, 6, I. 93-97

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28. Garcia, R.; Pizarro, C.; Lavin, A.V.; Bueno J.L. Characterization of Spanish biomass wastes for energy use,

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Bioresource Technol. 2012, 103, 249-258. doi:10.1016/j.biortech.2011.10.004

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29. Katimbo, A.; Nicholas, K.; Simon, K.; Hussein, B.K.; Peter, T. Potential of densification of mango waste and

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effect of binders on produced briquettes. Agric. Eng. Intl. CIGR Journal. 2014, 16, 4, 146-155.

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30. Bamiyo, F. Briquette: Alternative Energy Source. 2004. File://:\Briquette.htm. Pp 1-5

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31. Asamoah, B.; Nikiema, J.; Gebrezgabher, S.; Odonkor, E.; Njenga, M. A review on production, marketing

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and use of fuel briquettes. Colombo, Sri Lanka: International Water Management Institute (IWMI). CGIAR

477

Research Program on Water, Land and Ecosystems (WLE). 2016, 51p. (Resource Recovery and Reuse Series

478

7). doi: 10.5337/2017.200

479

Figure

Figure 1. Mean Effect of Treatments on Density (g/cm3) of Briquette Means in the same bar having the same superscript are not significantly different (p≥0.05)
Figure 3. Effect of particle types on percentage volatile matter (%VM) and Ash content (%) of the briquette
Figure 4. Effect of particle types on specific heat of combustion (SHC) and fixed carbon (%FC) of the briquette
Figure 6: Effect of Starch levels on percentage specific heat of combustion (Kca/kg) and fixed carbon (%FC) of the briquette

References

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