Refinery bitumen and domestic unconventional heavy oil upgrading in supercritical water

被引:24
作者
Caniaz, Ramazan Oguz [1 ,2 ]
Arca, Serhat [3 ]
Yasar, Muzaffer [4 ]
Erkey, Can [1 ,2 ]
机构
[1] Koc Univ, Dept Chem & Biol Engn, TR-34450 Istanbul, Turkey
[2] Koc Univ, Kop Univ TUPRAS Energy Ctr KUTEM, TR-34450 Istanbul, Turkey
[3] Turkish Petr Refineries Corp, R&D Prod Dev Dept, TR-41780 Izmit, Turkey
[4] Istanbul Univ, Chem Engn Dept, TR-34820 Istanbul, Turkey
关键词
Supercritical water; Heavy oil; Upgrading; Refinery; Tar sand; Bitumen; PROCESS INTENSIFICATION; OXIDE NANOPARTICLES; PETROLEUM RESIDUE; EXTRACTION; PYROLYSIS; ASPHALTENES; CRACKING;
D O I
10.1016/j.supflu.2019.104569
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
Upgrading of three different bitumens from bottom of crude oil distillation columns, a type of bitumen from side stream of a propane deasphalting (PDA) unit and bitumen extracted from domestic tar sand samples was investigated in supercritical water (SCW). Coke suppression was highest for tar sand bitumens. Low vacuum residue (VR), high amounts of lighter ends, low aromatics and lower viscosity of the feed decreased coke yields even if there were high amounts of asphaltenes in the feed. At long reaction times, yields and selectivities were similar for different feeds. Red mud, Fluid Catalytic Cracking (FCC) spent catalyst, FeSO4, Fe2O3 and a blend of FCC spent and FeSO4 were investigated as catalytic additives. The coke yield was lowest with the FCC spent catalysts. Highest liquid yield was obtained using red mud. For all feeds, shot type cokes were obtained. (C) 2019 Elsevier B.V. All rights reserved.
引用
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页数:10
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