Analysis of the Effect on the Mechanical Injection Engine Using Doped Diesel Fuel by Ethanol and Bio-Oil

2015 ◽  
Vol 9 (2) ◽  
pp. 124 ◽  
Author(s):  
Nattan Roberto Caetano ◽  
R. Cataluña ◽  
H. A. Vielmo
2021 ◽  
pp. 146808742110477
Author(s):  
Mebin Samuel Panithasan ◽  
Gnanamoorthi Venkadesan

In the search for an alternative energy source with lesser pollution for transportation needs, bio-oil, a denser and viscous fuel that needs a transesterification process, have been widely considered for diesel engines. However, these problems are solved by using low viscous biofuel, but this improvement also significantly leads to increased NOx emission. Hence this present study investigates the usage of a low viscous biofuel in the CRDI engine with measures to reduce NOx emission through water injection technique. The low viscous bio-oil was used in this study along with an ignition enhancer (di-tert-butyl-peroxide), non-metallic nano additive (rice husk). They were tested in a constant speed, single-cylinder, diesel engine for various loads. Considering the brake thermal efficiency (BTE), 2% and 150 ppm were selected as the optimum value after testing five ratios (1%, 1.5%, 2%, 2.5% and 3%) of di tert butyl peroxide (DTBP) and four ratios (50, 100, 150 and 200 ppm) of rice husk (RH). The lemon peel oil (LPO) with the optimum additive ratio produced 30.69% BTE, which was 4.7% lesser than diesel fuel. A considerable decrease in fuel consumption and emissions except for nitrogen oxides (NOx) is recorded. NOx emission increased by 17.3% for the biofuel blend containing RH and DTBP. To control NOx emission, 2% of water was injected into the intake manifold with the fresh intake air. Two percent by vol. was finalised after experimenting four ratios (1%, 2%, 3% and 4%) of water addition. This 2% water reduces 11% of NOx emission and affects the other outputs, denoted with the 8.9% reduced BTE value compared with diesel fuel. Thus, the LPOC combination proved to operate well in the CRDI engine and produces lower NOx emissions than other LPO blends.


2017 ◽  
Vol 32 (1) ◽  
pp. 542-553 ◽  
Author(s):  
Michael D. Kass ◽  
Christopher J. Janke ◽  
Raynella M. Connatser ◽  
Samuel A. Lewis ◽  
James R. Keiser ◽  
...  
Keyword(s):  

2019 ◽  
Vol 231 ◽  
pp. 694-700 ◽  
Author(s):  
Abid Farooq ◽  
Hoda Shafaghat ◽  
Jungho Jae ◽  
Sang-Chul Jung ◽  
Young-Kwon Park

Energy ◽  
2015 ◽  
Vol 83 ◽  
pp. 80-88 ◽  
Author(s):  
Yufu Xu ◽  
Yubin Peng ◽  
Xiaojing Zheng ◽  
Karl D. Dearn ◽  
Hongming Xu ◽  
...  

2018 ◽  
Vol 67 ◽  
pp. 02030 ◽  
Author(s):  
Dijan Supramono ◽  
Justin Edgar ◽  
Setiadi ◽  
Mohammad Nasikin

Bio-diesel was synthesized by hydrogenating the non-polar fraction of the bio-oil produced from the co-pyrolysis between corncobs and polypropylene. Co-pyrolysis of corn cobs and polypropylene was conducted in a stirred tank reactor at heating rate of 5°C/min and maximum temperature of 500°C to attain synergetic effect in non-polar fraction yield where polypropylene served as a hydrogen donor and oxygen sequester so that the oxygenate content in the biofuel product reduced. Stirred tank reactor configuration allowed phase separation between non-polar and polar (oxygenate) compounds in the bio-oil. Hydrogenation reaction of the separated non-polar phase, which contained alkenes, was carried out in a pressured stirred tank reactor using a NiMo/C catalyst in order to reduce the alkene content in the bio-oil. The aim of the present work is to reduce the alkene content in the separated non-polar fraction of bio-oil by catalytic hydrogenation to obtain biofuel with low alkene content and viscosity approaching to that of diesel fuel. To quantify effect of the pressure on the alkene composition, the experiment was done at H2 initial pressures of 4, 7, 10, and 13 bar and at corresponding saturation temperatures of octane. The biofuel products were characterized using GC-MS, LC-MS, FTIR spectroscopy, H-NMR, Higher heating values (HHV) and viscometer for comparison with those of commercial diesel fuel. Analysis of the lower molecular weight fractions of biofuels by GC-MS found that the hydrogenation reactor at pressures at 4 and 7 bar produced biofuels with predominant hydrocarbon contents of cycloalkanes and alkanes, while that at 10 and 13 bar produced biofuels with predominant contents of alkanes and alkenes. In comparison, diesel fuel contains mostly alkanes and aromatics. However, analysis over the whole content of bio-oil by H-NMR found that different pressures of reactor hydrogenation did not reduce alkene compositions in biofuels appreciably from alkene composition in bio-oil feed. In comparison, diesel fuel contained mostly alkanes with aromatic composition about 4% and no alkene content. Various data suggest that alkene content in the biofuels be reduced to approach their viscosity to that of diesel fuel. Modification of the hydrogenation reactor is required by improving convective momentum of hydrogen gas into the bio-oil to enhance contact of solid catalyst, hydrogen gas and bio-oil.


2013 ◽  
Vol 27 (11) ◽  
pp. 6831-6838 ◽  
Author(s):  
Renato Cataluña ◽  
Pedro M. Kuamoto ◽  
Cesar L. Petzhold ◽  
Elina B. Caramão ◽  
Maria E. Machado ◽  
...  

Energy ◽  
2010 ◽  
Vol 35 (1) ◽  
pp. 283-287 ◽  
Author(s):  
Yufu Xu ◽  
Qiongjie Wang ◽  
Xianguo Hu ◽  
Chuan Li ◽  
Xifeng Zhu

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