Selective extraction of aromatics from residual oil with subcritical water

被引:1
|
作者
Zhu, Meng-Han [1 ]
Liu, Yin-Dong [2 ]
Wang, Li-Tao [2 ]
Huang, Zi-Bin [1 ,3 ]
Yuan, Pei-Qing [1 ]
机构
[1] East China Univ Sci & Technol, Sch Chem Engn, State Key Lab Chem Engn, Shanghai 200237, Peoples R China
[2] Petrochina Petrochem Res Inst, Beijing 102249, Peoples R China
[3] East China Univ Sci & Technol, State Key Lab Chem Engn, 130 Meilong Rd, Shanghai 200237, Peoples R China
来源
CHEMICAL ENGINEERING RESEARCH & DESIGN | 2024年 / 202卷
关键词
Subcritical water; Extraction; Aromatics; Heavy oil; Hansen solubility parameters; SUPERCRITICAL WATER; SOLUBILITY PARAMETERS;
D O I
10.1016/j.cherd.2024.01.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Based on theoretical calculations and experimental characterizations, the extraction of heavy oil components using subcritical water (Sub-CW) as an extraction solvent was studied in the temperature range of 250-325( degrees)C. According to theoretical calculations, small-scale polycyclic aromatic hydrocarbons (PAHs) are preferentially dissolved in Sub-CW. Meanwhile, the dissolution of heavy oil molecules with large-scale aromatic structures and heterocyclic rings in Sub-CW is hindered. The increase in temperature reduces the hydrogen bonding force between water molecules and the van der Waals repulsion between Sub-CW and PAHs, promoting the dissolution of PAHs in Sub-CW. Extraction experiments applied in a semi-continuous device confirm that Sub-CW selectively extracts aromatic hydrocarbons from heavy oil. Increasing extraction temperature increases the yield of the extract. The aromatic hydrocarbon content in the extract at 325 C reaches 80 wt%, which is 27 wt% higher than feedstock value. In addition, the asphaltene content in the extract is reduced from the feedstock value of 14 wt% to 2 wt%.
引用
收藏
页码:444 / 454
页数:11
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