Heavy oil upgrading in the presence of high density water: Basic study

被引:118
作者
Watanabe, Masaru [1 ]
Kato, Shin-nosuke [1 ]
Ishizeki, Satoshi [1 ]
Inomata, Hiroshi [1 ]
Smith, Richard Lee, Jr. [1 ]
机构
[1] Tohoku Univ, Res Ctr Supercrit Fluid Technol, Aoba Ku, Sendai, Miyagi 9808579, Japan
关键词
Bitumen; Asphaltene; Upgrading; Supercritical water; Coke formation; Phase separation kinetic model; SEM; Phase behaviour; SUPERCRITICAL WATER; COKE FORMATION; HYDROTHERMAL VISBREAKING; PHASE-SEPARATION; ASPHALTENES; PYROLYSIS; BITUMEN; PRESSURES; BEHAVIOR; CRACKING;
D O I
10.1016/j.supflu.2009.11.013
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Heavy oil (Canada oil sand bitumen) upgrading in high density water (100 and 200 kg/m(3)) at 723 K was performed by a batch reactor. Yields of asphaltene, maltene, and coke were evaluated. With increasing water density, the rate of coke formation was promoted. To get some hints of coke formation mechanism, the formed coke was observed by scanning electron microscope (SEM). The most part of the coke formed st neat pyrolysis (pyrolysis in the absence of high density water) was coalescent structure of some small coke particles, while that at pyrolysis in the presence of water (200 kg/m(3) of water density) was porous structure that indicated occurrence of phase inversion of coke precursors. Based on the results, the reaction mechanism of the heavy oil upgrading was considered: lighter oil was extracted in high density water and the concentration of light hydrocarbon decreased in a heavier oil phase, while the concentration of heavier oil in the oil phase increased. Thus, the lighter oil decomposed further in high density water phase and the heavier oil in the oil phase combined together to form coke due to its higher concentration. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:48 / 52
页数:5
相关论文
共 13 条
[1]   FLUID MIXTURES AT HIGH-PRESSURES .9. PHASE-SEPARATION AND CRITICAL PHENOMENA IN 23 (NORMAL-ALKANE + WATER) MIXTURES [J].
BRUNNER, E .
JOURNAL OF CHEMICAL THERMODYNAMICS, 1990, 22 (04) :335-353
[2]   Thermal cracking of Athabasca bitumen: Influence of steam on reaction chemistry [J].
Dutta, RP ;
McCaffrey, WC ;
Gray, MR ;
Muehlenbachs, K .
ENERGY & FUELS, 2000, 14 (03) :671-676
[3]   Modelling of the pyrolysis of tert-butylbenzene in supercritical water [J].
Ederer, HJ ;
Kruse, A ;
Mas, C ;
Ebert, KH .
JOURNAL OF SUPERCRITICAL FLUIDS, 1999, 15 (03) :191-204
[4]   Consistency of asphaltene chemical structures with pyrolysis and coking behavior [J].
Gray, MR .
ENERGY & FUELS, 2003, 17 (06) :1566-1569
[5]   Upgrading of bitumen by hydrothermal visbreaking in supercritical water with alkali [J].
Kishita, A ;
Takahashi, S ;
Kamimura, H ;
Miki, M ;
Moriya, T ;
Enomoto, H .
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2003, 46 (04) :215-221
[6]   Hydrothermal visbreaking of bitumen in supercritical water with alkali [J].
Kishita, A ;
Takahashi, S ;
Kamimura, H ;
Miki, M ;
Moriya, T ;
Enomoto, H .
JOURNAL OF THE JAPAN PETROLEUM INSTITUTE, 2002, 45 (06) :361-367
[7]   Liquid-phase behavior during the cracking of asphaltenes [J].
Rahmani, S ;
McCaffrey, W ;
Elliott, JAW ;
Gray, MR .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (17) :4101-4108
[8]   Kinetics of solvent interactions with asphaltenes during coke formation [J].
Rahmani, S ;
McCaffrey, W ;
Gray, MR .
ENERGY & FUELS, 2002, 16 (01) :148-154
[9]   Quantitative molecular representation and sequential optimization of athabasca asphaltenes [J].
Sheremata, JM ;
Gray, MR ;
Dettman, HD ;
McCaffrey, WC .
ENERGY & FUELS, 2004, 18 (05) :1377-1384
[10]   FLUID-PHASE EQUILIBRIA AND CRITICAL PHENOMENA FOR THE DODECANE-WATER AND SQUALANE-WATER SYSTEMS AT ELEVATED-TEMPERATURES AND PRESSURES [J].
STEVENSON, RL ;
LABRACIO, DS ;
BEATON, TA ;
THIES, MC .
FLUID PHASE EQUILIBRIA, 1994, 93 :317-336