An experimental study on the carbon conversion efficiency and emission indices of air and steam co-flow diffusion jet flames

Fuel ◽  
2021 ◽  
Vol 287 ◽  
pp. 119534
Author(s):  
M. Zamani ◽  
E. Abbasi-Atibeh ◽  
S. Mobaseri ◽  
H. Ahsan ◽  
A. Ahsan ◽  
...  
Fuel ◽  
2016 ◽  
Vol 183 ◽  
pp. 164-169 ◽  
Author(s):  
C.F. Tao ◽  
Y. Shen ◽  
R.W. Zong ◽  
F. Tang

1992 ◽  
Vol 10 (4) ◽  
pp. 753-758 ◽  
Author(s):  
V. A. Bolotin ◽  
I. N. Burdonskii ◽  
V. V. Gavrilov ◽  
A. Yu. Gol'tsov ◽  
S. V. Zavyalets ◽  
...  

X-ray emission from planar targets irradiated by 1.054-μm laser pulses was observed with temporal, spatial, and spectral resolution. The main purpose of these measurements was the investigation of energy transfer in multilayer targets and X-ray conversion efficiency. A mass ablation rate was determined from temporal analysis of multicharged ion line emission and a key role of corona X-ray emission in accelerated material preheating was established.


2018 ◽  
Vol 225 ◽  
pp. 06009 ◽  
Author(s):  
Muddasser Inayat ◽  
Shaharin A. Sulaiman ◽  
Tham W. Hung ◽  
Fiseha M. Guangul ◽  
Firdaus Basrawi

Biomass energy via gasification is an attractive substitute of fossil fuels. The distribution of biomass on the earth is scattered, so transportation and collection of biomass complicates the supply of biomass especially when the gasification rely on one type of biomass. Therefore, cogasification of different biomass is proposed as a potential solution for interruption-free gasification. Beside, unwanted by-products such as tar that cause blockage in downstream equipment can be minimized through the use of catalyst in gasification to accelerate tar reforming process. In this study, catalytic co-gasification of blended feedstock of 70% wood chips and 30% coconut fronds was carried out in a downdraft gasifier using limestone as primary catalyst. The effects of catalyst loading (0%, 30%, 50%, and 70% w/w) on syngas composition, gas yield, carbon conversion efficiency and heating value of syngas were investigated. The results showed that at 50% biomass to catalyst ratio, maximum H2 content of 11.39%, CO of 17.88%, carbon conversion efficiency of 69.49%, gas yield of 1.68 Nm3/kg and higher heating value of syngas 5.11 MJ/Nm3 were achieved. Higher catalyst loading (70%) blocked the air passage, which caused poor gasification. No more than 50% catalyst suggested for stable co-gasification operation.


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