scholarly journals Dynamic imaging of oil shale pyrolysis using synchrotron X-ray microtomography

2016 ◽  
Vol 43 (13) ◽  
pp. 6799-6807 ◽  
Author(s):  
Tarik Saif ◽  
Qingyang Lin ◽  
Kamaljit Singh ◽  
Branko Bijeljic ◽  
Martin J. Blunt

2017 ◽  
Vol 202 ◽  
pp. 628-647 ◽  
Author(s):  
Tarik Saif ◽  
Qingyang Lin ◽  
Alan R. Butcher ◽  
Branko Bijeljic ◽  
Martin J. Blunt


2019 ◽  
Vol 235 ◽  
pp. 1468-1475 ◽  
Author(s):  
Tarik Saif ◽  
Qingyang Lin ◽  
Ying Gao ◽  
Yousef Al-Khulaifi ◽  
Federica Marone ◽  
...  
Keyword(s):  
X Ray ◽  


2009 ◽  
Vol 131 (1) ◽  
Author(s):  
Omar S. Al-Ayed ◽  
Moh’d Matouq

Oil shale samples from the Ellajjun area south of Jordan were pyrolyzed in different conditions and environments. Sulfur of shale oil was determined using x-ray fluorescence (XRF). Generated products swept from the retort by several sweeping media; they include nitrogen, water vapor, hydrogen, and mixture of nitrogen and water vapor. Other conditions are 2–11 mm particle size, 1 atm operating pressure, and 410–550°C temperature range. The sulfur content of shale oil was found to be 12 wt % for hydrogen pyrolysis, while water vapor at 1 atm decreased this value to 7 wt %. Hydrogenation of oil shale resulted in 12 wt %. the sulfur content of shale oil being at 420°C, and then reduced to 10.3 wt % at temperatures higher than 470°C. When water vapor is added to nitrogen, the sulfur in the oil shale is increased by 4 wt %. Water vapor sweeping gas increased the sulfur of the shale oil from 6.5 wt % to 8.1 wt % compared with a nitrogen pyrolyzing medium. Retorted shale analysis showed 44 wt %, and 31 wt % is left in the retorted shale of the original 4.5 wt %. Sulfur found in the raw oil shale is unretorted for nitrogen and hydrogen sweeping gases. On the other hand, increasing particle size from 2 mm to 11 mm did not have any significant influence on the sulfur content of the produced shale oil.



Fuel ◽  
1989 ◽  
Vol 68 (2) ◽  
pp. 168-173 ◽  
Author(s):  
Dejan Skala ◽  
Heinz Kopsen ◽  
Milorad Sokić ◽  
Hans-Joachim Neumann ◽  
Jovan Jovanović


2016 ◽  
Vol 30 (9) ◽  
pp. 7236-7240 ◽  
Author(s):  
Zhi Q. Lu ◽  
Xiao Q. Hai ◽  
Jian X. Wei ◽  
Ri M. Bao


2012 ◽  
Vol 9 (3) ◽  
pp. 1373-1388 ◽  
Author(s):  
A. Hamadi ◽  
K. Nabih

Timahdit oil shale was subjected to firing transformation via ceramics processing followed by alkali activation to synthesis a materials combining the mechanical properties of ceramics and Zeolites. The mineralogical transformations during firing oil shale have been studied. The main crystalline phases found in oil shale ash (OSA) were wollastonite, gehlenite and augite. Modified oil shale ash (MOSA) was obtained with HNO3acid-leaching in the aim to diminish Ca content. Our experimental approach required a NaOH alkaline activating solution with different concentrations (0.5; 1; 2; 4; 6 and 8M). In our study, X-ray diffraction (XDR), Fourier transform infrared (FTIR) and SEM/EDS analysis were used to evaluate the effect of alkali activation on the structural arrangement of the starting materials (OSA and MOSA) in our study. The quantity and the type of the produced zeolites depended critically on the starting materials and on the NaOH concentration.



1989 ◽  
Vol 154 (2) ◽  
pp. 355-365 ◽  
Author(s):  
Ming-Shing Shen ◽  
Lawrence J. Shadle ◽  
John J. Kovach ◽  
Guo-Qing Zhang ◽  
Richard A. Bajura




2019 ◽  
Vol 8 (5) ◽  
pp. 372-379 ◽  
Author(s):  
Laila Makouki ◽  
Meriem Tarbaoui ◽  
Samia Glissi ◽  
Said Mansouri ◽  
Hassan Hannache ◽  
...  

The present article aims to optimize the decarbonization of Timahdit oil shale layer Y by removing carbonates from the raw rock using acetic acid. The response surface methodology “central composite design (CCD)” has been used as a method of optimization to study the 3 factors of the process. The factors studied are the concentration of the acid, the processing time, and the ratio (liquid/solid). The optimal conditions with 68.17% of residue rate are obtained with 2 mol/l as concentration, 120 min as a time of treatment and 10.02 for the ratio.The raw (Y) and optimized materials (YO) were characterized by Scanning Electron Microscopy (SEM), X-ray fluorescence (XRF) and X-ray diffraction (XRD). The results showed that the acetic acid used to remove carbonates affects the chemical composition and the texture evolution of the residues.



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