Form of presentation | Articles in international journals and collections |
Year of publication | 2019 |
Язык | английский |
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Al-Muntaser Amin Akhmed Mokhammed , author
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Bibliographic description in the original language |
Al-Muntaser AA, Varfolomeev MA, Suwaid MA, Yuan C, Chemodanov AE, Feoktistov DA, Rakhmatullin IZ, Abbas M, Domínguez-Álvarez E, Akhmadiyarov AA, Klochkov VV. Hydrothermal upgrading of heavy oil in the presence of water at sub-critical, near-critical and supercritical conditions. Journal of Petroleum Science and Engineering. 2019 Oct 14:106592. |
Annotation |
In this study, the hydrothermal upgrading (HTU) of high sulfur-content heavy oil was investigated at sub-critical (Sub-CW), near-critical (NCW) and supercritical water (SCW) conditions. Products obtained after HTU, including gases, liquid, and coke (if formed), were analyzed to understand the upgrading performance at different conditions. At Sub-CW (200, 250, and 300 ?C), 250 ?C is the optimum temperature where a viscosity reduction from 2073 to 1758 mPa s was achieved with a slight removal of sulfur (mainly sulfur) and the generation of a small amount of light and non-condensable hydrocarbons in gas phase (C1–C4, isoalkanes and alkenes, H2S, CO2 and H2, etc.). At NCW (350 ?C) and SCW (400 ?C), heavy oil was upgraded into light oil with a significant removal of heteroatoms, an increase of saturates content, a reduction of aromatics, resins and asphaltenes contents, and a high yield of light gaseous hydrocarbons (mainly methane). Simultaneously, each SARA fraction was also greatly ameliorated: the content of light alkanes with low molecular weight in saturates was increased, diaromatics content in aromatics was increased with a reduction of polyaromatics content, aromatics-type carbon atoms in resins was increased with a decrease in aliphatic hydrocarbons. Moreover, MALDI-TOF measurements of asphaltenes show that the molecular weights of asphaltenes were reduced. All these results indicated that HTU at Sub-CW can be used for heavy oil pre-treatment (in-situ or ex-situ upgrading) considering its main effect of viscosity reduction with a small removal of heteroatoms, while HTU at NCW and SWC has a great potential in in-situ and ex-situ upgrading and oil refining as it can convert heavy oil into light oil.
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Keywords |
Heavy oil, Hydrothermal upgrading, Sub-critical water, Near-critical water, Supercritical water, In-situ upgrading |
The name of the journal |
Journal of Petroleum Science and Engineering
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URL |
https://www.sciencedirect.com/science/article/pii/S0920410519310137 |
Please use this ID to quote from or refer to the card |
https://repository.kpfu.ru/eng/?p_id=216352&p_lang=2 |
Full metadata record |
Field DC |
Value |
Language |
dc.contributor.author |
Al-Muntaser Amin Akhmed Mokhammed |
ru_RU |
dc.date.accessioned |
2019-01-01T00:00:00Z |
ru_RU |
dc.date.available |
2019-01-01T00:00:00Z |
ru_RU |
dc.date.issued |
2019 |
ru_RU |
dc.identifier.citation |
Al-Muntaser AA, Varfolomeev MA, Suwaid MA, Yuan C, Chemodanov AE, Feoktistov DA, Rakhmatullin IZ, Abbas M, Domínguez-Álvarez E, Akhmadiyarov AA, Klochkov VV. Hydrothermal upgrading of heavy oil in the presence of water at sub-critical, near-critical and supercritical conditions. Journal of Petroleum Science and Engineering. 2019 Oct 14:106592. |
ru_RU |
dc.identifier.uri |
https://repository.kpfu.ru/eng/?p_id=216352&p_lang=2 |
ru_RU |
dc.description.abstract |
Journal of Petroleum Science and Engineering |
ru_RU |
dc.description.abstract |
In this study, the hydrothermal upgrading (HTU) of high sulfur-content heavy oil was investigated at sub-critical (Sub-CW), near-critical (NCW) and supercritical water (SCW) conditions. Products obtained after HTU, including gases, liquid, and coke (if formed), were analyzed to understand the upgrading performance at different conditions. At Sub-CW (200, 250, and 300 ?C), 250 ?C is the optimum temperature where a viscosity reduction from 2073 to 1758 mPa s was achieved with a slight removal of sulfur (mainly sulfur) and the generation of a small amount of light and non-condensable hydrocarbons in gas phase (C1–C4, isoalkanes and alkenes, H2S, CO2 and H2, etc.). At NCW (350 ?C) and SCW (400 ?C), heavy oil was upgraded into light oil with a significant removal of heteroatoms, an increase of saturates content, a reduction of aromatics, resins and asphaltenes contents, and a high yield of light gaseous hydrocarbons (mainly methane). Simultaneously, each SARA fraction was also greatly ameliorated: the content of light alkanes with low molecular weight in saturates was increased, diaromatics content in aromatics was increased with a reduction of polyaromatics content, aromatics-type carbon atoms in resins was increased with a decrease in aliphatic hydrocarbons. Moreover, MALDI-TOF measurements of asphaltenes show that the molecular weights of asphaltenes were reduced. All these results indicated that HTU at Sub-CW can be used for heavy oil pre-treatment (in-situ or ex-situ upgrading) considering its main effect of viscosity reduction with a small removal of heteroatoms, while HTU at NCW and SWC has a great potential in in-situ and ex-situ upgrading and oil refining as it can convert heavy oil into light oil.
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ru_RU |
dc.language.iso |
ru |
ru_RU |
dc.subject |
Heavy oil |
ru_RU |
dc.subject |
Hydrothermal upgrading |
ru_RU |
dc.subject |
Sub-critical water |
ru_RU |
dc.subject |
Near-critical water |
ru_RU |
dc.subject |
Supercritical water |
ru_RU |
dc.subject |
In-situ upgrading |
ru_RU |
dc.title |
Hydrothermal upgrading of heavy oil in the presence of water at sub-critical, near-critical and supercritical conditions
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ru_RU |
dc.type |
Articles in international journals and collections |
ru_RU |
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