Kinetics of coking shale oil vapour on combusted spent shale for eight Australian oil shale deposits
Data are presented on the kinetics of coking at 500 °C of shale oil vapours on combusted spent shale (shale ash) prepared from samples of oil shales from the Condor, Duaringa, Lowmead, Nagoorin, Nagoorin South, Rundle, Stuart and Yaamba deposits. The results are correlated in an equation that gives...
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Published in | Fuel (Guildford) Vol. 67; no. 10; pp. 1340 - 1343 |
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Main Authors | , |
Format | Journal Article Conference Proceeding |
Language | English |
Published |
Oxford
Elsevier Ltd
1988
Elsevier |
Subjects | |
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Abstract | Data are presented on the kinetics of coking at 500 °C of shale oil vapours on combusted spent shale (shale ash) prepared from samples of oil shales from the Condor, Duaringa, Lowmead, Nagoorin, Nagoorin South, Rundle, Stuart and Yaamba deposits. The results are correlated in an equation that gives the yields of carbon deposited on the shale ash as a function of reaction time and oil vapour concentration. Reaction coefficients that characterize the reactivities of the oils and ashes are given. Additional data that relate the yields of carbon to the other reaction products are also presented. On the bases of these data, recommendations are made for the selection of retort operating conditions to minimize oil yield losses due to coking. |
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AbstractList | Data are presented on the kinetics of coking at 500 °C of shale oil vapours on combusted spent shale (shale ash) prepared from samples of oil shales from the Condor, Duaringa, Lowmead, Nagoorin, Nagoorin South, Rundle, Stuart and Yaamba deposits. The results are correlated in an equation that gives the yields of carbon deposited on the shale ash as a function of reaction time and oil vapour concentration. Reaction coefficients that characterize the reactivities of the oils and ashes are given. Additional data that relate the yields of carbon to the other reaction products are also presented. On the bases of these data, recommendations are made for the selection of retort operating conditions to minimize oil yield losses due to coking. |
Author | Udaja, Pinky Wall, Geoffrey C. |
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CitedBy_id | crossref_primary_10_1016_0016_2361_95_00068_G crossref_primary_10_1016_j_jaap_2017_12_022 crossref_primary_10_1016_0016_2361_90_90321_G crossref_primary_10_1016_0016_2361_90_90075_2 crossref_primary_10_1016_0016_2361_90_90102_V crossref_primary_10_1016_j_petrol_2022_110623 crossref_primary_10_1016_0016_2361_90_90073_Y crossref_primary_10_1016_0016_2361_90_90069_3 crossref_primary_10_1016_0016_2361_93_90091_F crossref_primary_10_1016_0016_2361_90_90068_2 crossref_primary_10_1002_er_845 crossref_primary_10_1016_0016_2361_90_90071_W crossref_primary_10_1016_0016_2361_89_90296_2 crossref_primary_10_1016_0016_2361_94_90062_0 crossref_primary_10_1016_0016_2361_91_90225_Y crossref_primary_10_1016_0016_2361_90_90067_Z crossref_primary_10_1016_0016_2361_93_90090_O crossref_primary_10_1016_0016_2361_91_90228_3 |
Cites_doi | 10.1016/0016-2361(87)90097-4 10.1021/i260058a014 |
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Copyright | 1988 1989 INIST-CNRS |
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Keywords | shale oil kinetics coking Pyrolysis Combustion residue Fluid coking Reactivity Shale oil Loss Yield Kinetics Oil shale |
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References | Levy, Mallon, Wall (BIB4) 1986 (BIB2) 1988 Dumez, Froment (BIB5) 1976; 15 (BIB1) 1986 Duang, Wall, Kastl (BIB3) 1987; 66 Duang (10.1016/0016-2361(88)90115-9_BIB3) 1987; 66 Levy (10.1016/0016-2361(88)90115-9_BIB4) 1986 (10.1016/0016-2361(88)90115-9_BIB1) 1986 (10.1016/0016-2361(88)90115-9_BIB2) 1988 Dumez (10.1016/0016-2361(88)90115-9_BIB5) 1976; 15 |
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SubjectTerms | Applied sciences coking Crude oil, natural gas and petroleum products Energy Exact sciences and technology Fuels kinetics Processing of crude oil and oils from shales and tar sands. Processes. Equipment. Refinery and treatment units shale oil |
Title | Kinetics of coking shale oil vapour on combusted spent shale for eight Australian oil shale deposits |
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