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Effects of using ethyl acetate as a surprising additive in SI engine pertaining to an environmental perspective

  • Original Paper
  • Published:
International Journal of Environmental Science and Technology Aims and scope Submit manuscript

Abstract

Blending oxygenated fuels with gasoline improve exhaust emissions. In this study, tests were performed in a single-cylinder spark-ignition engine at a constant speed of 1600 rpm for different loads (8, 10, 12, and 14 kg) and compression ratios (8:1, 9:1, and 10:1), and carbon monoxide, hydrocarbon, nitrogen monoxide, and carbon dioxide emissions were determined. Ethyl acetate was mixed with gasoline at 4%, 8%, and 12% by volume and used as alternative fuels in the experiments. The performance of ethyl acetate blends compared to gasoline was investigated by energy, exergy, and exergoeconomic analyses. Carbon monoxide, hydrocarbon, and nitrogen monoxide occurring in the engine were lower for ethyl acetate blends than gasoline. When the load is 14 kg and the compression ratio is 10:1, hydrocarbon emissions in 12% ethyl acetate blend and gasoline are 128.66 ppm and 161 ppm, respectively. According to the data obtained from energy analysis, the difference between the thermal efficiency of 12% ethyl acetate blend and gasoline fuels is a maximum of 5%. This difference decreases even more at low engine loads. When the load is 14 kg and the compression ratio is 10:1 in 12% ethyl acetate blend and gasoline, the exergy efficiency is 34.27% and 37.17%, respectively. According to the exergoeconomic analysis, the engine power cost varies according to different loads and compression ratios and is higher by 20–27% in 12% ethyl acetate blend than gasoline. In case pump prices of ethyl acetate are reduced, fuel blends with gasoline can be used as an alternative fuel.

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Availability of data and material

The data used and/or analyzed throughout the present study are available from the authors on reasonable request.

Code availability

Not applicable.

Abbreviations

BTE:

Brake thermal efficiency

C8H18 :

Gasoline

C4H8O2 :

Ethyl acetate

CO:

Carbon monoxide

CO2 :

Carbon dioxide

EA4:

4% Ethyl acetate and 96% gasoline blend

EA8:

8% Ethyl acetate and 92% gasoline blend

EA12:

12% Ethyl acetate and 88% gasoline blend

HC:

Hydrocarbon

NO:

Nitrogen oxide

NOX :

Nitrogen oxides

O2 :

Oxygen

RON:

Research octane number

RVP:

Reid vapor pressure

C:

Cost flow rate ($/h)

c:

Specific exergy cost ($/MJ)

CRF:

Capital recovery factor (-)

Cp:

Specific heat capacity (kJ/kgK)

\(\dot{E}x\) :

Exergy rate (kW)

E fuel :

Energy of fuel (kW)

EF:

Exergoeconomic factor (%)

h :

Enthalpy (kJ)

Hu:

Heat value of fuel (kJ/kg)

i :

Interest rate (%)

M f :

Maintenance factor ( −)

\(\dot{m}\) :

Mass flow rate (kg/s)

N :

System lifetime (year)

n :

Engine speed (rpm)

P:

Pressure (kPa)

P0 :

Pressure of the environment (kPa)

\(\dot{Q}\) :

Heat transfer rate (kW)

\({\overline{\text{R}}}\) :

Universal gas constant (8.314 J mol/K)

R :

Gas constant (kJ/kgK)

RCD:

Relative cost difference (-)

t year :

Annual working hours (h)

T :

Torque (Nm)

T 0 :

Temperature of the environment (K)

T :

Temperature (K)

rpm:

Revolutions per minute

S gen :

Entropy produced (kW/K)

s :

Entropy (kJ/kg K)

y e :

Component mole fraction (%)

\(\dot{W}\) :

Work (kW)

Z :

Engine cost ($)

\(\dot{Z}\) :

Capital investment cost rate ($/h

ε:

Flow exergy

φ:

Fuel exergy factor

µ :

Gas viscosity

η:

Thermal efficiency

a:

Air

chem:

Chemical

cw:

Cooling water

CI:

Compression ignition

DI:

Direct injection

dest:

Destruction

ex:

Exhaust

heat:

Heat transfer

in:

Inlet

out:

Outlet

p:

Potential

phy:

Physical

ref:

Reference

s:

Source

w:

Work

0:

Environmental conditions

References

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Acknowledgements

The authors wish to acknowledge all who assisted in performing this experimental study. The authors would also like to thank the Editor and anonymous reviewers for helping us to present a balanced account of our research.

Funding

This work was supported by Scientific Research Projects Coordination Unit of Kırıkkale University. Project number: 2018/067.

Author information

Authors and Affiliations

Authors

Contributions

MKY has contributed to the definition of research objectives, hypotheses, results interpretation, and validation of results. DE has contributed to the designing of the graphs and validation of results. HY has contributed to the definition of research objectives, data analysis plan, and validation of results. BD has contributed to the definition of research objectives, hypotheses, data analysis plan, and validation of results. MKY and HY performed conceptualization and investigation. All authors were responsible for article writing, revision/proofreading, and final approval.

Corresponding author

Correspondence to M. K. Yeşilyurt.

Ethics declarations

Conflict of interest

The authors declare that they have no conflict of interest. The authors acknowledge that no financial interest or benefit has been raised from the direct applications of their research.

Ethical approval

This article does not contain any studies with human participants or animals performed by any of the authors.

Consent to participate

All authors agree to submit the present manuscript to the highly reputed International Journal of Environmental Science and Technology.

Consent for publication

This paper is original. It has not been published previously by any of the authors and is even not under the consideration in any other journal at the time of submission.

Additional information

Editorial Responsibility: Senthil Kumar Ponnusamy.

Electronic supplementary material

Below is the link to the electronic supplementary material.

Supplementary file1 (DOCX 15 kb)

Appendix

Appendix

The uncertainty values of the measured characteristics are as follows: load (∆m) and engine speed (∆N) are considered as ± 0.1 kg and 1 rpm, respectively. For the fuel samples, the uncertainty of the volume (∆f) is taken as ± 0.1 cc and the uncertainty of the time (∆t) is accepted as ± 0.2 s, respectively. A sample calculation of the uncertainty analysis at the load of 14 kg operating condition is presented underneath (Table 11).

Table 11 The engine parameters and their values
$$\frac{\Delta N}{N} = \frac{1}{1600} = 0.0625 \%$$
(28)
$$\frac{\Delta m}{m} = \frac{0.1}{{14}} = 0.7143 \%$$
(29)
  1. 1.

    Uncertainty in brake power (BP)

    $$BP = \frac{2\pi NT}{{60. 1000}} = \frac{2\pi Nmgl}{{60000}} = \frac{2 x 3.14 x 1600 x 14 x 9.81 x 0.230 }{{60000}} = 5.2927 kW$$
    (30)
    $$\frac{\partial BP}{{\partial N}} = \frac{2\pi mgl}{{60000}} = \frac{2 x 3.14 x 14 x 9.81 x 0.230}{{60000}} = 0.00330791$$
    (31)
    $$\frac{\partial BP}{{\partial m}} = \frac{2\pi Ngl}{{60000}} = \frac{2 x 3.14 x 1600 x 9.81 x 0.230}{{60000}} = 0.3780467$$
    (32)
    $$\Delta BP = \sqrt {\left( {\Delta N\frac{\partial BP}{{\partial N}}} \right)^{2} + \left( {\Delta m\frac{\partial BP}{{\partial m}}} \right)^{2} }$$
    (33)
    $$\Delta BP = \sqrt {\left( {1 x 0.00330791} \right)^{2} + \left( {0.1 x 0.3780467} \right)^{2} }$$
    (34)
    $$\Delta BP = 0.037949115 kW$$
    (35)
    $$\frac{\Delta BP}{{BP}} = \frac{0.037949115}{{5.2927}} = 0.717\%$$
    (36)

2.Uncertainty in mass of the fuel consumption (MFC)

$$MFC = \frac{f x 3600 x \rho }{{t x 1000}} = \frac{25.00 x 3600 x 0.715}{{60 x 1000}} = 1.0725 \frac{kg}{h}$$
(37)
$$\frac{\partial MFC}{{\partial t}} = - \frac{f x 3600 x \rho }{{\left( t \right)^{2} x 1000}} = - \frac{25.00 x 3600 x 0.715}{{60 x 60 x 1000}} = - 0.017875$$
(38)
$$\frac{\partial MFC}{{\partial f}} = \frac{3600 x \rho }{{t x 1000}} = \frac{3600 x 0.715}{{60 x 1000}} = 0.04290$$
(39)
$$\Delta MFC = \sqrt {\left( {\Delta t\frac{\partial MFC}{{\partial t}}} \right)^{2} + \left( {\Delta f\frac{\partial MFC}{{\partial f}}} \right)^{2} }$$
(40)
$$\Delta MFC = \sqrt {\left( {0.2 x - 0.017875} \right)^{2} + \left( {0.1 x 0.04290 } \right)^{2} }$$
(41)
$$\Delta MFC = 0.005584329 \frac{kg}{{kWh}}$$
(42)
$$\frac{\Delta MFC}{{MFC}} = \frac{0.005584329}{{1.0725}} = 0.521\%$$
(43)

3.Uncertainty in brake specific fuel consumption (BSFC)

$$BSFC = \frac{MFC}{{BP}} = \frac{1.0725 }{{5.2927}} = 0.202637595 \frac{kg}{{kWh}}$$
(44)
$$\frac{\partial BSFC}{{\partial BP}} = - \frac{MFC}{{\left( {BP} \right)^{2} }} = - \frac{1.0725}{{\left( {5.2927} \right)^{2} }} = - 0.038286242$$
(45)
$$\frac{\partial BSFC}{{\partial MFC}} = \frac{1}{BP} = \frac{1}{5.2927} = 0.188939482$$
(46)
$$\Delta BSFC = \sqrt {\left( {\Delta BP\frac{\partial BSFC}{{\partial BP}}} \right)^{2} + \left( {\Delta MFC\frac{\partial BSFC}{{\partial MFC}}} \right)^{2} }$$
(47)
$$\Delta BSFC = \sqrt {\left( {0.037949115 x - 0.038286242} \right)^{2} + \left( {0.005584329 x - 0.188939482} \right)^{2} }$$
(48)
$$\Delta BSFC = 0.001795617 \frac{kg}{{kWh}}$$
(49)
$$\frac{\Delta BSFC}{{BSFC}} = \frac{0.001795617}{{0.202637595}} = 0.886\%$$
(50)

4.Uncertainty in brake thermal efficiency (BTE)

$$BTE = \frac{BP x 3600 x 100}{{MFC x LHV}} = \frac{5.2927 x 3600 x 100}{{1.0725 x 44250}} = 40.14849\%$$
(51)
$$\frac{\partial BTE}{{\partial BP}} = \frac{3600 x 100}{{MFC x LHV}} = \frac{3600 x 100}{{1.0725 x 44250}} = 7.585635$$
(52)
$$\frac{\partial BTE}{{\partial MFC}} = - \frac{BP x 3600 x 100}{{\left( {MFC} \right)^{2} x LHV}} = - \frac{5.2927 x 3600 x 100}{{\left( {1.0725} \right)^{2} x 44250}} = - 37.43449$$
(53)
$$\Delta BTE = \sqrt {\left( {\Delta BP\frac{\partial BTE}{{\partial BP}}} \right)^{2} + \left( {\Delta MFC\frac{\partial BTE}{{\partial MFC}}} \right)^{2} }$$
(54)
$$\Delta BTE = \sqrt {\left( {0.037949115 x 7.585635 } \right)^{2} + \left( {0.005584329 x - 37.43449} \right)^{2} }$$
(55)
$$\Delta BTE = 0.355764677\%$$
(56)
$$\frac{\Delta BTE}{{BTE}} = \frac{0.355764677}{{40.14849}} = 0.886\%$$
(57)

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Yeşilyurt, M.K., Erol, D., Yaman, H. et al. Effects of using ethyl acetate as a surprising additive in SI engine pertaining to an environmental perspective. Int. J. Environ. Sci. Technol. 19, 9427–9456 (2022). https://doi.org/10.1007/s13762-021-03706-3

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  • DOI: https://doi.org/10.1007/s13762-021-03706-3

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