Prospects for Hydrogen Production in Oil Shale Processing Industry in Estonia: Initial Aspects of Life Cycle Analysis

Eldermann, Meelis; Siirde, Andres; Gusca, Julija

doi:10.1016/j.egypro.2016.09.081

Cited by 5 publications

(2 citation statements)

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“…Estonian oil shale processing and oil shale energy production industries are historically well-developed and provide up to 70% of the total primary energy supply of the country. Oil-shale-based liquid motor fuel plays an important role in Estonian industry . Estonian oil shale has a high oil content, which is a significant evaluation index.…”

Section: Introductionmentioning

confidence: 99%

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Characteristics of Estonian Oil Shale Kerogen and Its Pyrolysates with Thermal Bitumen as a Pyrolytic Intermediate

Jian

et al. 2017

Energy Fuels

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Preparation and collection of thermal bitumen, a pyrolytic intermediate, are key factors in elucidating the mechanism of oil shale pyrolysis. Electron paramagnetic resonance (EPR), gas chromatography, Fourier transform infrared spectrophotometry, nuclear magnetic resonance (NMR) spectrometry, distortionless enhancement by polarization transfer (DEPT), and X-ray photoelectron spectroscopy were employed to investigate the thermochemical transformation in oil shale pyrolysis. Results showed that thermal bitumen was continuously generated and decomposed during the pyrolysis process. The maximum yield of thermal bitumen at 380 °C was 11.17%. EPR analysis showed that the g factor of kerogen and the pyrolysates was slightly higher than 2 and increased as pyrolysis progressed because of the aromatization of saturates and decarboxylation. CO2 and CO were mainly generated at temperatures lower than 340 °C, and less was obtained in the subsequent pyrolysis process. In contrast, C2–C5 organic gases were mainly generated at temperatures higher than 340 °C. NMR and DEPT analyses indicated that kerogen, thermal bitumen, and shale oil were mainly composed of aliphatic structures. During the pyrolysis process, aliphatic structures were constantly transformed into aromatic compounds, which were easily retained in shale oil and semi-coke. Pyrrolic, pyridinic, and quaternary compounds constituted 80% of the nitrogen compounds in kerogen and the pyrolysates. The sulfoxide content of thermal bitumen and semi-coke was considerably higher than that of kerogen, indicating that sulfoxide compounds present better thermostability during the pyrolysis process.

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Section: Introductionmentioning

confidence: 99%

“…Oil-shalebased liquid motor fuel plays an important role in Estonian industry. 14 Estonian oil shale has a high oil content, which is a significant evaluation index. Therefore, the current study analyzed the organic evolution of kerogen derived from Estonian oil shale.…”

Section: Introductionmentioning

confidence: 99%