Impact of internals on oil shale pyrolysis in fixed bed reactor

2014 ◽  
Vol 44 (3) ◽  
pp. 395-402
Author(s):  
RongCheng WU ◽  
Chun ZHANG ◽  
ZhengKang DUAN ◽  
GuangWen XU ◽  
HongJuan LI
Oil Shale ◽  
2009 ◽  
Vol 26 (2) ◽  
pp. 139 ◽  
Author(s):  
O S AL-AYED ◽  
A AL-HARAHSHEH ◽  
A M KHALEEL ◽  
M AL-HARAHSHEH

Energies ◽  
2018 ◽  
Vol 11 (11) ◽  
pp. 3195 ◽  
Author(s):  
Kathleen Dupre ◽  
Emily Ryan ◽  
Azat Suleimenov ◽  
Jillian Goldfarb

The volatility of crude oil prices incentivizes the use of domestic alternative fossil fuel sources such as oil shale. For ex situ oil shale retorting to be economically and environmentally viable, we must convert the copious amounts of semi-coke waste to an environmentally benign, useable by-product. Using acid and acid + base treatments, we increased the surface area of the semi-coke samples from 15 m2/g (pyrolyzed semi-coke) to upwards of 150 m2/g for hydrochloric acid washed semi-coke. This enhancement in porosity and surface area is accomplished without high temperature treatment, which lowers the overall energy required for such a conversion. XRD analysis confirms that chemical treatments removed the majority of dolomite while retaining other carbonate minerals and maintaining carbon contents of approximately 10%, which is greater than many fly ashes that are commonly used as sorbent materials. SO2 gas adsorption isotherm analysis determined that a double HCl treatment of semi-coke produces sorbents for flue gas treatment with higher SO2 capacities than commonly used fly ash adsorbents. Computational fluid dynamics modeling indicates that the sorbent material could be used in a fixed bed reactor to efficiently remove SO2 from the gas stream.


RSC Advances ◽  
2017 ◽  
Vol 7 (35) ◽  
pp. 21467-21474 ◽  
Author(s):  
Lanxin Lin ◽  
Dengguo Lai ◽  
Zhen Shi ◽  
Zhennan Han ◽  
Guangwen Xu

Variation of chemical species from pyrolysis with temperature, with light oil/diesel and VGO dominant at temperatures below 450 °C and above 300 °C.


Geofluids ◽  
2021 ◽  
Vol 2021 ◽  
pp. 1-11
Author(s):  
Wei Wang ◽  
Yue Ma ◽  
Shuyuan Li ◽  
Changtao Yue ◽  
Jiancun Gao

Oil shale samples from Longkou City, Shandong Province, China, were pyrolyzed in a fixed bed reactor at retorting temperature varied from 400 to 550°C under nitrogen atmosphere with heating rate of 15°C/min. The influence of retorting temperature on the yield and characteristics of shale oil and retorting gases were determined. It was observed that the oil yield increased to the maximum value, 15.68 wt%, as the retorting temperature increased from 440 to 550°C. And increasing retorting temperature improved also gas yields, but reduced the char yield. The contents of H2, CO2, and CH4 in the retorting gas increased with the rising of retorting temperature. The ratio of alkane/alkene hydrocarbon (C1-C5) decreased because of the secondary cracking reactions of gas phase in the high temperature. The carbon and nitrogen contents of shale oil increased with increasing retorting temperature, while those of hydrogen and oxygen decreased. The sulfur content was not significantly affected by the retorting temperature. In addition, the shale oil obtained from 550°C had the lowest aromatic content, 25.12 wt%, and the highest saturate content, 50.03 wt%, compared to the other retorting temperatures due to the cracking of aliphatic compounds. The alkanes with 8-34 carbons and alkenes with 8-27 carbons were detected in the shale oil. The concentration more than 20 mg/goil was C23-C30 in the range of 400-550°C. The total content of n-alkanes decreased to 369.25 mg g-1oil, and that of n-alkene reached the maximum value at 550°C, 181.62 mg/goil, with the rise of retorting temperature. It was demonstrated that the higher temperature was beneficial to promoting the reaction of aromatization, dehydrogenation, fraction, and other reactions in the pyrolysis process.


2016 ◽  
Vol 148 ◽  
pp. 248-255 ◽  
Author(s):  
Somprasong Siramard ◽  
Lanxin Lin ◽  
Chun Zhang ◽  
Dengguo Lai ◽  
Shuai Cheng ◽  
...  

2014 ◽  
Vol 521 ◽  
pp. 666-670
Author(s):  
Yun Xia Bian ◽  
De Min He ◽  
Guo Zhu Kuang ◽  
Qiu Min Zhang

Proximate analysis, ultimate analysis and CO2of carbonate were determinated for the aboveground oil shale in Daqing exploratory area. The experiments of pyrolysis of Daqing oil shale were carried out in a fixed-bed reactor in order to study the influence of the pyrolysis temperature and the constant temperature time on oil shale pyrolysis characteristics. The results show that the effect of the pyrolysis is optimal under the conditions of 500°C and the constant temperature time for 20 min, with the yield of shale oil for 28.78% (the yield based on kerogen, similarly hereinafter). The mechanism of the oil shale pyrolysis was discussed. The pyrolysis reaction kinetics of oil shale was studied combining the experimental results of fixed-bed pyrolysis. The reaction activation energy is 28.92 kJ/mol during generating the shale oil process, while the reaction activation energy is 11.21 kJ/mol during generating char process. The yield curve of shale oil changing with the temperature was fitted to compare with the measured value with the constant temperature time for 20 min according to the pyrolysis kinetic parameters.


Fuel ◽  
2016 ◽  
Vol 163 ◽  
pp. 48-55 ◽  
Author(s):  
Lanxin Lin ◽  
Dengguo Lai ◽  
Erwei Guo ◽  
Chun Zhang ◽  
Guangwen Xu

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