The effects of different intake charge diluents on the combustion and emission characteristics of a spark ignition natural gas engine

The effects of different intake charge diluents on the combustion and emission characteristics of a spark ignition natural gas engine

Accepted Manuscript The effects of different intake charge diluents on the combustion and emission characteristics of a spark ignition natural gas eng...

2MB Sizes 1 Downloads 46 Views

Accepted Manuscript The effects of different intake charge diluents on the combustion and emission characteristics of a spark ignition natural gas engine Zhuoyao He, Qijian Jing, Lei Zhu, Wugao Zhang, Zhen Huang PII:

S1359-4311(15)00631-6

DOI:

10.1016/j.applthermaleng.2015.06.072

Reference:

ATE 6765

To appear in:

Applied Thermal Engineering

Received Date: 1 November 2014 Accepted Date: 24 June 2015

Please cite this article as: Z. He, Q. Jing, L. Zhu, W. Zhang, Z. Huang, The effects of different intake charge diluents on the combustion and emission characteristics of a spark ignition natural gas engine, Applied Thermal Engineering (2015), doi: 10.1016/j.applthermaleng.2015.06.072. This is a PDF file of an unedited manuscript that has been accepted for publication. As a service to our customers we are providing this early version of the manuscript. The manuscript will undergo copyediting, typesetting, and review of the resulting proof before it is published in its final form. Please note that during the production process errors may be discovered which could affect the content, and all legal disclaimers that apply to the journal pertain.

ACCEPTED MANUSCRIPT 1

The effects of different intake charge diluents on the combustion and emission

2

characteristics of a spark ignition natural gas engine

3 4 5

Zhuoyao He, Qijian Jing, Lei Zhu*, Wugao Zhang, Zhen Huang*

6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

ABDC: after bottom dead center ATDC: after top dead center BBDC: before bottom dead center BTDC: before top dead center CAD: crank angle degree  : specific heat capacity at constant pressure for intake mixture  : specific heat capacity at constant pressure for component i

26 27 28 29 30 31 32

 : specific heat capacity at constant volume for intake mixture  : specific heat capacity at constant volume for component i ECU: electronic control unit EGR: exhaust gas recirculation EOC: end of combustion HC: hydrocarbon , : lower heating value of natural gas

33 34 35 36 37 38 39 40 41 42 43

IVO: intake valve opening k: specific heat ratio of intake mixture  : mass flow rate of natural gas

: engine speed p: cylinder pressure R: gas constant ST: spark timing TDC: top dead center THC: total hydrocarbon T: mean in-cylinder temperature  : engine torque

Corresponding authors: E-mail address: [email protected] (Lei Zhu*) E-mail address: [email protected] (Zhen Huang*)

RI PT

Key Lab. for Power machinery and Engineering of M. O. E., Shanghai Jiao Tong University, 200240 Shanghai, P R China

M AN U

SC

* Corresponding author address: Key laboratory of Power Machinery and Engineering, Ministry of Education, Shanghai Jiao Tong University, Shanghai 200240, China. Tel: +86-21-34205949 Fax: +86-21-34205949

AC C

EP

TE D

Nomenclature: :

1 / 23

58 59 60 61 62

[CO]: CO emission concentration [23 ]4 : intake oxygen concentration [52 ]: NOx emission concentration [THC]: total hydrocarbon emission concentration

SC

 : peak mean in-cylinder temperature  : exhaust manifold temperature V: cylinder volume  : mass percentage of component i  : mass fraction burnt θ: crank angle θ : crank angle for spark timing θ : crank angle for end of combustion θ ! : crank angle for 10 percent mass fraction burnt θ"!: crank angle for 90 percent mass fraction burnt ∆$% : ignition delay ∆$&% : combustion duration η : effective thermal efficiency ()*+, : net heat release rate (-

AC C

EP

TE D

M AN U

44 45 46 47 48 49 50 51 52 53 54 55 56 57

RI PT

ACCEPTED MANUSCRIPT

2 / 23

ACCEPTED MANUSCRIPT Abstract

M AN U

SC

RI PT

Exhaust gas recirculation (EGR) is the most common method to control NOx emission of internal combustion engine. The major components of EGR are CO2 and N2, which have different influences on engine combustion and pollutants formation through thermal, dilution and chemical effects. The main objective of this work is to investigate the different influences of CO2 and N2 on engine combustion and emission on a four-cylinder, turbo charged, spark ignition natural gas engine with electronically control unit, simultaneously to separate the thermal effect with the comparison with Ar. It was found that the peak in-cylinder pressure and heat release rate both decreased along with the increase of intake dilution extent regardless of the diluent’s type. For each diluent gas, NOx emission decreases while HC emission increases with the increased dilution ratio. However, CO emission firstly decreased and then increased. Results also revealed that NOx and CO emission could be simultaneously reduced by intake charge dilution at a little sacrifice of HC emission. The effects of three diluents are different compared with each other. Among these three diluents, it can be found that CO2 is the most effective on reducing NOx and CO emission followed by N2. However, both CO2 and N2 dilution deteriorates the thermal efficiency while Ar dilution improved it. Besides, when NOx emission was reduced to the same level, the thermal efficiency is the highest and CO emission is the lowest for Ar dilution.

EP

TE D

Key words: Intake charge dilution, Natural gas engine, Combustion, Emission

AC C

63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82

3 / 23

ACCEPTED MANUSCRIPT 83

1. Introduction With the increasing price of crude oil, demand for energy provision and the tightening of emission

85

regulations, nowadays, seeking for an alternative fuel for oil is getting more and more urgent. Among many

86

alternative fuels, natural gas is found to be the most promising and attractive for its strong sustainability and

87

cleanliness. The application of natural gas also contributes to the reduction of CO2 emission for its high

88

hydrogen-carbon ratio. However, natural gas engine is also encountered with substantial conventional

89

emissions like NOx, hydrocarbon (HC) and CO.

SC

RI PT

84

In order to solve the aforementioned problems in spark ignition natural gas engine, numerous studies have

91

been conducted by a series of researchers. Jiao Deng et al. [1] suggested that HC and CO emission could be

92

lowered by blending a portion of hydrogen with natural gas at little sacrifice of increasing NOx emission.

93

Antonio Mariani et al. [2] found that hydrogen addition into natural gas drastically accelerated the in-cylinder

94

combustion process and improved engine operating thermal efficiency, moreover, it also contributed a lot to

95

lowering the cyclic variation of the engine.

TE D

M AN U

90

Some other researchers like Arvind Thiruvengadam et al.[3] adopted after-treatment to handle the

97

conventional emissions of natural gas engine and gained encouraging achievements. Be that as it may, the

98

adoption of catalyst entailed a complex controlling system and was expensive. The most promising way for

99

controlling conventional emissions, especially NOx emission, under middle and low load for engines was EGR

100

for its simplicity and high controllability, which has been investigated by several researchers. Amr Ibrahim et

101

al.[4] found that the application of EGR on a spark ignition natural gas engine substantially reduced NOx

102

emission through experimental and simulative study in 2009. Moreover, Amr Ibrahim et al.[5] also declared

103

that not only NOx emission could be decreased, but also the thermal efficiency of the engine could be

104

improved through EGR strategy at EGR rate of approximately 5% in 2010. Actually, EGR contains high

AC C

EP

96

4 / 23

ACCEPTED MANUSCRIPT 105

specific heat capacity gases like N2, CO2 and H2O(g), these gases intrinsically act as diluents which affect the

106

combustion process of engine thermally and chemically[6]. To obtain deeper understanding about EGR, some researchers focused on the independent effect of the

108

main components, CO2 and N2 and H2O, of EGR. N. Ladommatos et al.[7-10] conducted a series of

109

experiments on diesel engine to investigate the effects of intake charge diluents like EGR, CO2 and N2 and

110

H2O on the emissions of the engine. Results showed that intake charge dilution lowered the NOx emission

111

significantly, especially for diluents CO2 and H2O. Lei Zhu[11] and coworkers investigated the effect of CO2

112

on the gaseous and particulate emissions of a diesel engine fueled with biodiesel and biodiesel blended with

113

methanol and ethanol. He found that CO, HC and particulate emission all increased while NOx emission

114

decreased evidently by CO2 intake dilution. In diesel engine, diffusion combustion dominates the combustion

115

process. While, in spark ignition engine, stoichiometric air-fuel mixture is inducted into the cylinder

116

homogeneously thus premixed combustion dominates the combustion process. Thus, the effect of intake

117

dilution on the combustion and emission in spark ignition engine may be different from that in diesel engine.

118

So far, such intake charge dilution experiments on spark ignition engine have been conducted by a few

119

researchers. V. Subramanian et al.[12] conducted intake charge dilution experiments on a hydrogen fueled

120

spark ignition engine with CO2, N2 and EGR being diluents, and pointed out that intake charge dilution

121

lowered NOx emission. Nevertheless, the impact of intake charge dilution on the formation of HC and CO

122

emission was not evaluated as hydrogen was not a carbonaceous fuel. Zhongshu Wang et al.[13] conducted

123

intake charge dilution with N2 being diluents on a spark ignition natural gas engine, results indicated that N2

124

dilution could substantially decrease NOx emission in spite of increasing CO and HC emission. In addition to

125

N2 and CO2, Ar, which is monotonic gas exists in air with a small amount (0.93% vol.), was also used for such

126

fundamental studies in engines. Hany A. Moneib[14] and coworkers investigated the effect of Ar intake

AC C

EP

TE D

M AN U

SC

RI PT

107

5 / 23

ACCEPTED MANUSCRIPT dilution on the engine performances and found that Ar dilution could effectively reduce NOx emission and

128

improve thermal efficiency at the same time. WeiFeng Li and coworkers[15] assessed the dilution and thermal

129

effect of CO2 and N2 by comparing with Ar dilution and and the following conclusions were drown: 1) CO2

130

had greater effects on NOx formation than N2 at the same dilution ratio, 2) Ar dilution improved thermal

131

efficiency of the engine. Still, the effect of the diluents CO2, N2, and Ar on combustion and emission were not

132

comprehensively compared in the above mentioned works.

RI PT

127

The main components of EGR are CO2 and N2, which have different effects on engine combustion and

134

emission formation [6]. In one hand, both N2 and CO2 in combustion chamber would introduce higher heat

135

capacity into the engine cylinder, and then affect the engine combustion and emission (thermal effect). In

136

another hand, CO2 was believed to decompose and involve in a complex chemical reaction during the

137

combustion process (chemical effect). The main objective of this work is to investigate the different influences

138

of CO2 and N2 on engine combustion and emission, simultaneously to separate the thermal effect with

139

comparison of Ar .

140

2. Experimental setup and methodology

TE D

M AN U

SC

133

In this research, experiments have been carried out on a four-cylinder, water cooled, turbo-charged,

142

four-stroke, spark ignition natural gas engine. The displacement of this engine was 5.3L and the compression

143

ratio was 11. The specification of the test engine is shown in Table 1. An eddy current dynamometer was used

144

to control the engine speed and torque. The schematic diagram of this test system is shown in Fig1. Natural gas

145

was supplied to the natural gas injection assembly, on which six natural gas injectors were mounted, via a

146

pressure reducer from CNG bottles. The amount of natural gas fuel was controlled by ECU and recorded. The

147

main component of the natural gas used in this study was 96% methane with some other impurities. The

148

diluents, CO2, N2 and Ar, with purity of 99.99%, were supplied to the intake pipe of the engine from gas

AC C

EP

141

6 / 23

ACCEPTED MANUSCRIPT bottles via a pressure regulator as shown in Fig. 1. A mixer was installed on the inlet pipe before the

150

compressor to assist the mixing between inlet air and diluent gas. The oxygen concentration in the inlet pipe

151

was used as an indicator to evaluate the extent of dilution in this test. As shown by Fig. 1, the inlet mixture was

152

sampled to NIDR analyzer after being filtered and dehumidified for oxygen concentration measurement.

RI PT

149

In this study, in-cylinder pressure of the second cylinder was measured with Kistler piezoelectric

154

transducer (type 6118BFD35 Q03A41) for combustion analysis. The resolution of the transducer was 10 Pa.

155

After being amplified by Kistler charge amplifier (type 5015), cylinder pressure was supplied to combustion

156

analyzer (D2T Evolution 3) along with crank angle signal and recorded by computer. The crank angle signal

157

was generated by a 60-teeth gear with a single missing tooth and sensed by a magneto-electric tachometric

158

transducer. The cylinder pressure was recorded every 0.5 crank angle degree. CO emission was measured by

159

non-dispersive infra-red analyzer (NIDR CAI 602P). Total hydrocarbon (THC) and NOx emission were

160

measured by heated flame ionization detector (HFID CAI 600) and heat chemiluminescent analyzer (HCLD

161

CAI 600) respectively. A self-developed procedure with Labview Software was used for emission data

162

acquisition.

TE D

M AN U

SC

153

Based on the first law of thermal dynamics and ideal gas assumption, a zero dimensional model, which

164

neglected the leakage through the piston ring and assumed specific heat of each intake component to be

165

constant, was used to make combustion analysis[16]. Net heat release rate

166

temperature T(θ) were determined through the followings equations:

168 169 170

AC C

167

EP

163

789:; (=) 7?

A

= AB p(θ)

7C(?) 7?

T(θ) =

+ AB V(θ)

7E(?) 7?

(?)F(?)

k=

&I

R =  − 

7?

and mean in-cylinder

(a)

(b)

G &H

789:; (=)

(c) (d) 7 / 23

ACCEPTED MANUSCRIPT 171

 = ∑  

(e)

172

 = ∑  

(f)

where p(θ) was measured cylinder pressure (Pa) and θ was crank angle (CAD), R,  ,  and k were gas

174

constant (kJ/(kg·K)), specific heat capacity at constant pressure (kJ/(kg·K)), specific heat capacity at constant

175

volume (kJ/(kg·K)) and the specific heat ratio of intake mixture, respectively.  was the mass percentage of

176

component i in the intake mixture,  and  were the specific heat at constant pressure (kJ/(kg·K)) and at

177

constant volume (kJ/(kg·K)) of component i in the intake charge. The end of combustion(EOC) was detected

178

through the method developed by Brunt et al.[17], which considered the crank angle at which pV1.15 peaked as

179

the end of combustion. Burn rate (mass fraction burnt)  (θ) is caculated through equation (g). Crank angle

180

for 10 percent and 90 percent mass fraction burnt, θ

181

equation (i), respectively.

M AN U

SC

RI PT

173

!

and θ"!, are obtained by solving equation (h) and

-

 ($) =

185 186

EP

184

(g)

 ($) = 0.1

(h)

 ($) = 0.9

(i)

Effective thermal efficiency η is calculated through the following equation:

AC C

183

()*+, %= MN (-OPQ ()*+, %= L(MN

L-

TE D

182

 ∗4∗3W/Y!

η = Z [\, ]^__

∗`a,[\ ∗ !!!

(j)

187

where  , n,  and , were engine torque (Nm), engine speed (rpm), mass flow rate (kg/h) and lower

188

heating value (kJ/kg) of natural gas, respectively.

189

The maximum torque of the engine was 645Nm and its corresponding rotating speed, 1500rpm, was

190

chosen to be the tested speed in this study. The tested conditions in this study were 45%, 50%, 65% of the

191

maximum load. Under a specific load condition, diluent gases were added gradually through the inlet pipe until

192

the engine running was unstable. For all the tests, the spark ignition advance was fixed at 20 crank angle 8 / 23

ACCEPTED MANUSCRIPT degree before top dead center (BTDC) and equivalence ratio was fixed at 0.73. Engine coolant and lubrication

194

oil temperature were controlled to be 78~80℃ and 80~85℃, respectively. All data were recorded when the

195

engine running reached its steady state. Cylinder pressure of 200 consecutive cycles were saved and averaged

196

to make combustion analysis. In this study, firstly, CO2 was inducted as intake charge diluent under different

197

loads to study its effect on the combustion and emission characteristics. Secondly, experiments were carried

198

out with N2 and Ar being intake charge diluents under a single load and the comparison between these different

199

diluents was made.

SC

RI PT

193

M AN U

200 201

3. Results and Discussion

202

3.1 Combustion characteristics

203

3.1.1 Effects of CO2 as an intake charge diluent on combustion characteristics In this study, dilution test was firstly carried out for diluent CO2 under three loads, namely 35%, 50%, 65%

TE D

204

of the maximum load, to investigate the effects of intake charge dilution on the combustion and emission

206

characteristics. Generally, the induction of CO2 restrains the combustion temperature and slows down the

207

flame propagation speed of the air-fuel mixture. This is supported by the investigation conducted by Halter, F.

208

et al.[18]. He suggested that the existence of CO2 slowed down the combustion process in two ways: firstly,

209

the addition of CO2 increased the heat capacity of the intake charge mixture and lowered the adiabatic

210

combustion temperature. Secondly, the dissociation process of CO2 also contributed to worsening the

211

combustion process. These two effects were concluded as thermal and chemical effects by N. Ladommatos et

212

al.[6] and they suggested that the dissociation of CO2 may somehow be involved in combustion reactions. So,

213

as shown by Fig. 2, the peak pressure decreases with the increase of intake dilution extent ignoring its load

214

condition and the peak pressure occurs further away from TDC with increased intake dilution. In addition, the

AC C

EP

205

9 / 23

ACCEPTED MANUSCRIPT heat release process is elongated and the peak value of heat release rate is decreased and retarded. All these

216

implies that the existence of CO2 reduces the flame speed and slows down the heat release process, which is in

217

accordance with results of Halter, F. et al.[18]. The possible result of prolonged and retarded heat release

218

process is the decrease of degree of constant volume[19], and it could be concluded that the brake thermal

219

efficiency of the engine also decreases with the increase of dilution extent. In order to maintain a constant load,

220

more fuel-air mixture should be inducted under higher dilution extent. This is one of the reasons that the

221

in-cylinder pressure shows a slight increasing trend with the increased dilution in Fig.2. Another reason for this

222

phenomenon is that the increasing amount of diluents, along with the increasing of dilution extent, itself would

223

contribute to increase the bulk volume intake charge. This phenomenon is in accordance with the experiments

224

done by Zhongshu Wang and coworkers[13]. In this paper, ignition delay (∆$% ) and combustion duration

225

(∆$&% ) are calculated through equation (k) and equation (l), respectively.

M AN U

SC

RI PT

215

∆$% = $

!

TE D

226

− $

∆$&% = $"! − $

227

!

(k) (l)

Due to the elongated ignition delay, lengthened combustion process and lowered adiabatic flame

229

temperature by CO2 dilution, the peak mean in-cylinder temperature drops monotonously along with the

230

increase of CO2 dilution extent as shown in Fig. 3. Moreover, the elongated ignition delay and combustion

231

process also results in more energy released further away from TDC during the expansion stroke. Therefore,

232

the exhaust manifold temperature ( ) increases monotonously along with the increase of intake dilution

233

extent.

AC C

EP

228

234 235

3.1.2 Comparison between the effects of CO2, N2, Ar as intake charge diluents on combustion

236

characteristics 10 / 23

ACCEPTED MANUSCRIPT The effects of different intake charge diluents, CO2, N2 and Ar, on the combustion characteristics have

238

been displayed in Fig. 4. Compared with the case of no dilution, the peak pressures for all these three dilution

239

cases are comparatively lower. Under the same dilution extent, i.e. intake charge O2 concentration being 19.7%,

240

CO2 behaves the strongest impact on combustion process followed by N2 and then Ar. The ignition delay and

241

combustion duration are remarkably affected by intake dilution and increase with the increased dilution, as

242

shown by Fig. 5. According to Williams’[20] theory, it is easy to conclude that the initiation of flame would be

243

more difficult for deeper diluted mixtures under a fixed ignition energy as dilution restrains the adiabatic

244

temperature of the flame. So, as shown by Fig. 5(a), ignition delay increases with dilution extent whatever the

245

diluent is. As shown in table 2, the specific heat capacity is the highest for CO2 and lowest for Ar. Thus, under

246

the same intake dilution extent, the ignition delay for Ar dilution is the shortest, for CO2 dilution is the longest

247

and lies between for N2 dilution. Moreover, these differences in ignition delay become more pronounced with

248

the increased dilution.

TE D

M AN U

SC

RI PT

237

The flame speed is reduced by decreased flame temperature when dilution gases are added. As shown in

250

Fig. 5 (b), deeper dilution results in lower flame speed and longer combustion duration. This is in good

251

agreement with C. Prathap’s[21] research that dilution gas lowers the flame temperature and flame velocity

252

evidently, and the flame speed decreases along with the increase of dilution extent. Among these three dilution

253

cases, argon dilution yields the highest flame temperature owing to its lowest specific heat capacity thus its

254

combustion duration is always the shortest as shown in Fig. 5 (b). This phenomenon becomes more remarkable

255

under higher dilution extent.

AC C

EP

249

256

The peak mean in-cylinder temperature variation along with intake oxygen concentration is shown in Fig.

257

6 (a). It can be seen that the peak mean in-cylinder temperature drops along with the increase of dilution extent

258

for all these three diluents and that it is the highest for Ar dilution and lowest for CO2 dilution. The variations 11 / 23

ACCEPTED MANUSCRIPT of the exhaust manifold temperature along with intake oxygen concentration for these three diluents show

260

different trends as shown in Fig. 6 (b). Exhaust manifold temperature increases for CO2 dilution and decreases

261

for Ar dilution with the increasing dilution extent. However, it exhibits a down-up trend for N2 dilution. In

262

comparison, exhaust manifold temperature is always the highest for CO2 dilution case followed by N2 dilution

263

and then Ar dilution, which is contrary to the situation for peak mean in-cylinder temperature. Lower exhaust

264

manifold temperature indicates less heat loss through exhaust and and thus thermal efficiency may tend to be

265

higher. This is verified by Fig. 7. The thermal efficiency increases slightly when the intake oxygen

266

concentration is above 19.5 and then decreases slowly with the increase of Ar dilution in spite of a decrease in

267

peak mean in-cylinder temperature. While, for both CO2 and N2 dilution, the thermal efficiency drops

268

remarkably along with the increase of dilution extent.

M AN U

SC

RI PT

259

269 3.2 Emission Characteristics

271

3.2.1 Effects of CO2 as an intake charge diluent on emission characteristics

TE D

270

The variation of CO emission along with the intake charge oxygen content under different loads is shown

273

in Fig. 8. It can be clearly seen that CO emission firstly decreases to some extent and increases along with the

274

increase of dilution extent irrespective of the load condition.

AC C

EP

272

275

In spark ignition engine, it is believed that CO concentration is close to equilibrium in the immediate post

276

flame zone at the condition peak cycle temperature (about 2800K) and pressure (about 15 to 40bar)[22], which

277

means that higher temperature leads to higher concentration of CO because of the existence of chemical

278

equilibrium between CO and CO2 through an endothermic equation (m)[23]. However, CO deviates from its

279

equilibrium when the burnt gases cools down in the expansion stroke and undergoes kinetically controlled

280

oxidization process[22]. 12 / 23

ACCEPTED MANUSCRIPT CO3 ⇌ CO + O3

281

(m)

At the first, the immediate post flame zone temperature is suppressed due to the increased heat capacity of

283

the intake charge when slight amount of CO2 is inducted. Thus, CO concentration in the burnt gas is reduced in

284

the post flame zone. Besides, the increased temperature during the expansion stroke, which could be

285

demonstrated by the exhaust manifold temperature variation in Fig. 3 (b), favors the oxidation process of CO.

286

The above two factors bring about a decreasing trend for CO emission when slight dilution is taken as shown

287

in Fig. 8 (a). However, when dilution extent further increases, the immediate post flame zone temperature

288

drops remarkably so that CO concentration no longer reaches its equilibrium and stays very high level.

289

Therefore, CO emission increases along with the increased CO2 dilution.

M AN U

SC

RI PT

282

The main HC formation mechanisms are suggested as the followings: (1) flame quenching at the

291

combustion chamber wall, (2) crevice volume originated HC emission, (3) oil layer absorption of fuel, (4)

292

incomplete combustion[22], among which quenching and crevice effect are considered to be the key factors in

293

this study. With load increases, the mean in-cylinder temperature during the combustion process is enhanced

294

and the cylinder wall temperature is improved thus lead to a shorter quenching distance[24]. In addition, as

295

indicated by Fig. 3, the boosted exhaust temperature for higher loads favors the post oxidization process of

296

unburnt HC component. So, HC emission is lower for higher load condition as revealed by Fig. 8 (b). However,

297

HC emission increases monotonously along with the increase of CO2 dilution extent. This should be ascribed

298

to the following two reasons: 1) the inducted CO2 suppresses the combustion temperature, causing lower

299

laminar flame speed as well as larger quenching distance[24], 2) the elongated combustion process renders

300

fuel-air mixture staying in the crevice for longer time and at last escapes the primary combustion process.

301

These two key factors jointly induce the increasing trend of HC emission with the increased dilution.

302

AC C

EP

TE D

290

The NOx emission of the engine along with varying dilution extent under high, middle and low load is 13 / 23

ACCEPTED MANUSCRIPT shown in Fig. 8 (c). The NOx emission shows a decreasing trend with the increased dilution extent

304

monotonously regardless of the load conditions. Ordinarily, the formation of NOx in the combustion of air-fuel

305

mixture entails the following requests: high temperature, high O2 concentration and long time duration. In this

306

study, the equivalence ratio and the engine speed is fixed at 0.73 and 1500rpm, respectively. The dominant

307

factor that affects the formation of NOx is the maximum combustion temperature. This is verified by the

308

approximate linear relationship between ln(NOx) value and the peak mean in-cylinder temperature (Tmax)

309

indicated by Fig. 8 (c). As previously discussed, diluent CO2 suppresses combustion temperature thus restrains

310

the formation of NOx.

M AN U

SC

RI PT

303

Throughout Fig. 8, the effect of CO2 dilution on HC emission is not distinct when intake oxygen content

312

is above 20.3%, while NOx and CO emission drop evidently along with the increased of dilution. At middle

313

load, when intake oxygen content changed from 20.93% (no dilution) to 20.3%, both CO and NOx emissions

314

are lowered by 28.2% and 81.9%, while HC emission increases slightly. In conclusion, with slight intake

315

dilution (intake O2 concentration changed from 20.93 to 20.3), NOx emission could be decreased significantly

316

at a little sacrifice of HC emission regardless of the loads. At the same time, CO emission decreased evidently.

TE D

311

EP

317

3.2.2 Comparison of the effects between CO2, N2, Ar as intake charge diluents on emission

319

characteristics

AC C

318

320

The effects of CO2, N2 and Ar on emission characteristics are shown in Fig. 9. The effects of all three

321

diluents on CO emission characteristic are very similar as indicated by Fig. 9 (a). CO emission exhibits a

322

downward-upward trend with varying dilution. However, the point that minimum CO emission is achieved for

323

CO2 dilution case occurs under the lightest dilution extent followed by N2 and then Ar dilution case. Before

324

these points, CO2 behaves the strongest effect on reducing CO emission. When intake oxygen concentration is 14 / 23

ACCEPTED MANUSCRIPT 325

diluted to be 20.3%, CO concentration was lowered by 25.8%, 13.5%, 7.8% for CO2, N2 and Ar dilution,

326

respectively. However, the minimum CO emission value could be reached by Ar dilution is the lowest followed

327

by N2 dilution and then CO2 dilution. There seems to be no very remarkable differences between the effects of these three diluents on HC

329

emission before the points that minimum CO emission values are achieved and HC emission increases slowly

330

along with the increased dilution. When too more diluent gas is inducted, the combustion process would be

331

influenced (flame speed being slowed, flame propagation being seriously interfered), which is proved by the

332

peak mean in-cylinder temperature from Fig. 9 (c), thus brought about a rapid increase in HC emission as

333

indicated in Fig. 9 (b).

M AN U

SC

RI PT

328

The NOx emission decreases along with the increase of dilution extent regardless of the diluents. Among

335

these three diluents, CO2 is the most effective for reducing NOx emission while Ar is the least effective one.

336

When oxygen concentration was diluted to be 20.3%, NOx emission was reduced by 80.5%, 51.6% and 33.2%

337

for CO2, N2 and Ar dilution, respectively as shown in Fig. 9 (c). It was considered that both thermal and

338

chemical interaction should be responsible for the NOx reduction, among which thermal effect was considered

339

to be the primary factor[25]. Both N2 and Ar were inert gases thus wouldn’t involve chemical effect[6]. The

340

heat capacity is higher for N2 as shown in Table 2. Therefore, the results of thermal impact on NOx emission

341

could be described by comparing Ar dilution and N2 dilution as shown in Fig. 9 (c). It is obvious that thermal

342

effect is the dominant factor on lowering NOx emission. As has been discussed in section 3.2.1, NOx emission

343

is highly dependent on combustion temperature. So, owing to the comparatively higher specific heat capacity,

344

CO2 shows more effective impact on lowing the combustion temperature and this is demonstrated by the peak

345

mean in-cylinder temperature along with dilution extent shown in Fig. 9. Moreover, it was also suggested that

346

hydrocarbon radical reacts with NOx and lead to the formation of hydrogen cyanide, which ultimately lead to

AC C

EP

TE D

334

15 / 23

ACCEPTED MANUSCRIPT 347

the formation of N2, thus help to reduce NOx emission[8]. Under high dilution extent, HC emission is found to

348

be high, thus the possible reaction between HC and NOx in the post-flame and exhaust would help to restrain

349

NOx in the exhaust. So, ultimately, extreme low NOx emission is obtained. Throughout the comparison between these three diluents in terms of the combustion and emission

351

characteristics, it could be found that both CO2 and N2 could lower NOx emission effectively, while, thermal

352

efficiency decreases noticeably. However, Ar dilution almost does not worsen thermal efficiency while lowers

353

NOx emission. Actually, for Ar dilution, thermal efficiency increases at first and then decreases along with the

354

increased dilution as shown in Fig. 7. When NOx is lowered to the same level (100ppm, for example, shown in

355

Fig. 9, points A, B and C), it can be clearly found that the thermal efficiency is the highest for Ar dilution

356

followed by CO2 and then N2 as shown in Fig. 7. Besides, CO emission is the highest for CO2 dilution and

357

lowest for Ar dilution as indicated by Fig. 9 (a).

M AN U

SC

RI PT

350

359

4. Conclusions

TE D

358

In this paper, the effects of intake charge diluents, CO2, N2 and Ar, on the combustion and emission

361

characteristics of a spark ignition natural gas engine have been investigated and the comparison between these

362

three diluents has been carried out. It was found that intake charge dilution had an evident effect on the

363

combustion process and the emission of the spark ignition natural gas engine. Under a fixed load condition,

364

with the increase of dilution extent, the peak in-cylinder pressure and the maximum value of heat release rate

365

decreases and their corresponding crank angle shifts further away from the crank angle for spark timing.

366

Moreover, the ignition delay and combustion duration both are prolonged by intake charge dilution. However,

367

among the three diluents, CO2 shows its strongest effect on the combustion processes followed by N2 and then

368

Ar.

AC C

EP

360

16 / 23

ACCEPTED MANUSCRIPT With the increasing dilution extent, NOx emission decreases while HC emission increases regardless of

370

the diluents. However, CO emission exhibits a down-up trend. Reducing NOx and CO emission simultaneously

371

could be achieved when appropriate dilution extent is chosen at a little sacrifice of HC emission for all these

372

three diluents. In comparison, CO2 is the most effective for reducing NOx and CO emission followed by N2

373

and then Ar. However, both CO2 and N2 dilution lower thermal efficiency while Ar dilution improves thermal

374

efficiency. When NOx is lowered to the same level, the thermal efficiency is the highest and CO emission is the

375

lowest for Ar dilution.

SC

RI PT

369

With the comparison between N2 and Ar, the thermal effect on combustion and NOx emission is separated

377

in Fig. 9 (c). It could be found that thermal effect helps to lowering NOx emission remarkably. Similar analysis

378

on combustion is given in Fig. 4 and results show that thermal effect lowers peak in-cylinder pressure as well

379

as peak heat release rate.

M AN U

376

381

Acknowledgements

TE D

380

The author would like to thank National Science Foundation of China (Project No. 51306117; 51436005),

383

Ministry of Science and Technology (MOST) of China (Project No.2012BAD47B04) and Foundation of

384

Shanghai Jiao Tong University to support this research.

AC C

385

EP

382

17 / 23

ACCEPTED MANUSCRIPT 386

References

387 388 389 390 391 392 393 394 395 396 397 398 399 400 401 402 403 404 405 406 407 408 409 410 411 412 413 414 415 416 417 418 419 420 421 422 423 424 425 426 427 428

[1] J. Deng, F. Ma, S. Li, Y. He, M. Wang, L. Jiang, S. Zhao, Experimental study on combustion and emission characteristics of a hydrogen-enriched compressed natural gas engine under idling condition, International Journal of Hydrogen Energy, 36 (2011) 13150-13157. [2] A. Mariani, M.V. Prati, A. Unich, B. Morrone, Combustion analysis of a spark ignition i. c. engine fuelled 1616-1623.

RI PT

alternatively with natural gas and hydrogen-natural gas blends, International Journal of Hydrogen Energy, 38 (2013) [3] A. Thiruvengadam, D.K. Carder, M. Krishnamurthy, A. Oshinuga, M. Gautam, Effect of an economical oxidation catalyst formulation on regulated and unregulated pollutants from natural gas fueled heavy duty transit buses, Transportation Research Part D: Transport and Environment, 16 (2011) 469-473.

[4] A. Ibrahim, S. Bari, A comparison between EGR and lean-burn strategies employed in a natural gas SI engine using a two-zone combustion model, Energy Conversion and Management, 50 (2009) 3129-3139.

SC

[5] A. Ibrahim, S. Bari, An experimental investigation on the use of EGR in a supercharged natural gas SI engine, Fuel, 89 (2010) 1721-1730.

[6] N. Ladommatos, S. Abdelhalim, H. Zhao, Control of oxides of nitrogen from diesel engines using diluents while

M AN U

minimising the impact on particulate pollutants, Applied Thermal Engineering, 18 (1998) 963-980. [7] N. Ladommatos, S. Abdelhalim, H. Zhao, Z. Hu, The dilution, chemical, and thermal effects of exhaust gas recirculation on diesel engine emissions-part 1: Effect of reducing inlet charge oxygen, in, SAE Technical Paper, 1996.

[8] N. Ladommatos, S.M. Abdelhalim, H. Zhao, Z. Hu, 97/02332 The dilution, chemical, and thermal effects of exhaust gas recirculation on diesel engine emissions. Part 2: Effects of carbon dioxide, Fuel and Energy Abstracts, 38 (1997) 186.

TE D

[9] N. Ladommatos, S.M. Abdelhalim, H. Zhao, Z. Hu, The Dilution, Chemical, and Thermal Effects of Exhaust Gas Recirculation on Disesel Engine Emissions-Part 4: Effects of Carbon Dioxide and Water Vapour, in, SAE Technical Paper, 1997.

[10] N. Ladommatos, S.M. Abdelhalim, H. Zhao, Z. Hu, The dilution, chemical, and thermal effects of exhaust gas recirculation on diesel engine emissions-Part 3: effects of water vapour, in, SAE Technical Paper, 1997.

EP

[11] L. Zhu, C. Cheung, W. Zhang, Z. Huang, Effect of charge dilution on gaseous and particulate emissions from a diesel engine fueled with biodiesel and biodiesel blended with methanol and ethanol, Applied Thermal Engineering, 31 (2011) 2271-2278.

AC C

[12] V. Subramanian, J.M. Mallikarjuna, A. Ramesh, Intake charge dilution effects on control of nitric oxide emission in a hydrogen fueled SI engine, International Journal of Hydrogen Energy, 32 (2007) 2043-2056. [13] Z. Wang, H. Zuo, Z. Liu, W. Li, H. Dou, Impact of N2 dilution on combustion and emissions in a spark ignition CNG engine, Energy Conversion and Management, 85 (2014) 354-360. [14] H.A. Moneib, M. Abdelaal, M.Y.E. Selim, O.A. Abdallah, NOx emission control in SI engine by adding argon inert gas to intake mixture, Energy Conversion and Management, 50 (2009) 2699-2708. [15] W. Li, Z. Liu, Z. Wang, Y. Xu, Experimental investigation of the thermal and diluent effects of EGR components on combustion and NOx emissions of a turbocharged natural gas SI engine, Energy Conversion and Management, 88 (2014) 1041-1050. [16] R. Krieger, G.L. Borman, Computation of apparent heat release for internal combustion engines, in: MECHANICAL ENGINEERING, Vol. 89, ASME-AMER SOC MECHANICAL ENG 345 E 47TH ST, NEW YORK, NY 10017, 1967, pp. 59-&. [17] M.F. Brunt, A.L. Emtage, Evaluation of burn rate routines and analysis errors, in, SAE Technical Paper, 1997. 18 / 23

ACCEPTED MANUSCRIPT [18] F. Halter, F. Foucher, L. Landry, C. Mounaïm-Rousselle, Effect of Dilution by Nitrogen and/or Carbon Dioxide on Methane and Iso-Octane Air Flames, Combustion Science and Technology, 181 (2009) 813-827. [19] T. Shudo, Improving thermal efficiency by reducing cooling losses in hydrogen combustion engines, International Journal of Hydrogen Energy, 32 (2007) 4285-4293. [20] G. Williams, Combustion theory, (1985). [21] C. Prathap, A. Ray, M.R. Ravi, Investigation of nitrogen dilution effects on the laminar burning velocity and flame stability of syngas fuel at atmospheric condition, Combustion and Flame, 155 (2008) 145-160. [23] S.R. Turns, An introduction to combustion, McGraw-hill New York, 1996. [24] S.R. Turns, An introduction to combustion, McGraw-hill New York, 1996.

RI PT

[22] J.B. Heywood, Internal combustion engine fundamentals, Mcgraw-hill New York, 1988.

[25] A.A. Quader, Why intake charge dilution decreases nitric oxide emission from spark ignition engines, in, SAE Technical Paper, 1971.

SC

429 430 431 432 433 434 435 436 437 438 439 440 441 442

AC C

EP

TE D

M AN U

443

19 / 23

ACCEPTED MANUSCRIPT 444

Table Captions

445 Table 1. Engine specifications

447

Table 2. The specific heat capacity at constant pressure of the diluents at standard condition

RI PT

446

448

AC C

EP

TE D

M AN U

SC

449

20 / 23

ACCEPTED MANUSCRIPT 450 Table 1. Engine specifications Number of cylinders

4

Number of strokes

4

Displacement/L

5.3

Intake valve opening/CAD BTDC

22.5

Bore/mm

114

Intake valve closing/ CAD ABDC

34.5

Connecting rod length/mm

130

Exhaust valve opening/ CAD BBDC

67.5

Compression ratio

11

Exhaust valve closing/ CAD ATDC

25.5

RI PT

451

AC C

EP

TE D

M AN U

SC

452 453

21 / 23

ACCEPTED MANUSCRIPT 454 455

Table 2. The specific heat capacity at constant pressure of the diluents at standard condition Diluents

CO2

N2

Ar

Cp/kJ/(kmol·K)

37.198

29.071

20.785

AC C

EP

TE D

M AN U

SC

RI PT

456 457

22 / 23

ACCEPTED MANUSCRIPT 458

Figure Captions

459 Fig. 1. The schematic layout of the experimental setup

461

Fig. 2. Cylinder pressure and net heat release rate along with crank angle under 35, 50, 65% load for CO2

462

dilution

RI PT

460

Fig. 3. The peak mean in-cylinder temperature and exhaust manifold temperature variation along with intake

464

O2 concentration under 35%, 50%, 65% load for CO2 dilution

465

Fig. 4. Cylinder pressure and neat heat release rate along with crank angle under 50% load for CO2, N2 and Ar

466

dilution when intake oxygen concentration is 19.7%

467

Fig. 5. The ignition delay and combustion duration variation along with intake O2 concentration under 50%

468

load for CO2, N2 and Ar dilution

469

Fig. 6. The peak mean in-cylinder temperature and exhaust manifold temperature variation along with intake

470

O2 concentration for CO2, N2 and Ar dilution under 50% load

471

Fig. 7. Effective thermal efficiency variation along with intake oxygen concentration for CO2, N2 and Ar

472

dilution under 50% load (points A, B and C correspond to [52 ] = 100ppm)

473

Fig. 8. CO, HC and NOx emission variation along with intake O2 concentration for CO2 dilution under

474

different loads

475

Fig. 9. CO, HC and NOx emission variation along with intake O2 concentration for CO2, N2 and Ar dilution

476

under 50% load (points A, B and C correspond to [52 ] = 100ppm, points A, D and E correspond to

477

[23 ]4 = 20.3%)

AC C

EP

TE D

M AN U

SC

463

478

23 / 23

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

ACCEPTED MANUSCRIPT

ACCEPTED MANUSCRIPT

AC C

EP

TE D

M AN U

SC

RI PT

1, CO2 is the most effective on reducing NOx and CO emission followed by N2 and then Ar. 2, NOx and CO emission could be simultaneously reduced by intake charge dilution regardless of the diluents when appropriate dilution extent is chosen. 3, Both CO2 and N2 dilution worsen while Ar dilution improves thermal efficiency. 4, Thermal effect is a dominant factor for reducing NOx emission.