Ameen A. Al-Muntaser

Dr. Ameen A. Al-Muntaser

orcid

Research Focus & Metrics

Academic Career Length

10Years (2017-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 January 2020 in Journal of Petroleum Science and Engineering
Verified
Journal Article
Closed access
AAAmeen A. Al-Muntaser
Ameen A. Al-Muntaser
MVMikhail A. Varfolomeev
Mikhail A. Varfolomeev
MSMuneer A. Suwaid
Muneer A. Suwaid
Chengdong YuanChengdong Yuan
Chengdong Yuan
ACArtem E. Chemodanov
Artem E. Chemodanov
MAMarat I. Amerkhanov
Marat I. Amerkhanov

1 September 2018 in Journal of Petroleum Science and Engineering
Verified
Journal Article
Closed access
IRI.Z. Rakhmatullin
I.Z. Rakhmatullin
Sergey V. EfimovSergey V. Efimov
Sergey V. Efimov
VTV.A. Tyurin
V.A. Tyurin
AAAmeen A. Al-Muntaser
Ameen A. Al-Muntaser
AKA.E. Klimovitskii
A.E. Klimovitskii
VKV.V. Klochkov
V.V. Klochkov

1 December 2021 in Journal of Petroleum Science and Engineering
Verified
Journal Article
Closed access
MVMikhail A. Varfolomeev
Mikhail A. Varfolomeev
Chengdong YuanChengdong Yuan
Chengdong Yuan
ABAlexander V. Bolotov
Alexander V. Bolotov
IMIlgiz F. Minkhanov
Ilgiz F. Minkhanov
SMSeyedsaeed Mehrabi-Kalajahi
Seyedsaeed Mehrabi-Kalajahi
DSDamir K. Shaihutdinov
Damir K. Shaihutdinov

1 January 2020 in Fuel
Verified
Journal Article
Closed access
Chengdong YuanChengdong Yuan
Chengdong Yuan
KSKamil Sadikov
Kamil Sadikov
Mikhail A. VarfolomeevMikhail A. Varfolomeev
Mikhail A. Varfolomeev
RKRamil Khaliullin
Ramil Khaliullin
WPWanfen Pu
Wanfen Pu
SMSeyed Saeed Mehrabi-Kalajahi
Seyed Saeed Mehrabi-Kalajahi

1 August 2018 in Applied Catalysis A: General
Verified
Journal Article
Closed access
Chengdong YuanChengdong Yuan
Chengdong Yuan
Mikhail A. VarfolomeevMikhail A. Varfolomeev
Mikhail A. Varfolomeev
DEDmitrii Anatolevich Emelianov
Dmitrii Anatolevich Emelianov
MSMuneer A. Suwaid
Muneer A. Suwaid
AKArtashes A. Khachatrian
Artashes A. Khachatrian
AAAmeen A. Al-Muntaser
Ameen A. Al-Muntaser

27 September 2022 in Catalysts
Verified
Journal Article
Open access
PDF file
OAOmar F. Al-Mishaal
Omar F. Al-Mishaal
MSMuneer A. Suwaid
Muneer A. Suwaid
AAAmeen A. Al-Muntaser
Ameen A. Al-Muntaser
Mohammed Amine KhelkhalMohammed Amine Khelkhal
Mohammed Amine Khelkhal
Mikhail A. VarfolomeevMikhail A. Varfolomeev
Mikhail A. Varfolomeev
MHMohammed Hail Hakimi
Mohammed Hail Hakimi
Heavy oil resources are attracting considerable interest in terms of sustaining energy demand. However, the exploitation of such resources requires deeper understanding of the processes occurring during their development. Promising methods currently used for enhancing heavy oil recovery are steam injection methods, which are based on aquathermolysis of heavy oil at higher temperatures. Regardless of its efficiency in the field of in situ upgrading of heavy oil, this technique still suffers from energy consumption and inefficient heat transfer for deeper reservoirs. During this study, we have developed a molybdenum-based catalyst for improving the process of heavy oil upgrading at higher temperature in the presence of water. The obtained catalyst has been characterized by a set of physico-chemical methods and was then applied for heavy oil hydrothermal processing in a high-pressure reactor at 200, 250 and 300 °C. The comparative study between heavy oil hydrothermal upgrading in the presence and absence of the obtained molybdenum-based oil soluble catalysts has pointed toward its potential application for heavy oil in situ upgrading techniques. In other words, the used catalyst was able to reduce heavy oil viscosity by more than 63% at 300 °C. Moreover, our results have demonstrated the efficiency of a molybdenum-based catalyst in improving saturates and light hydrocarbon content in the upgraded oil compared to the same quantity of these fractions in the initial oil and in the non-catalytically upgraded oil at similar temperatures. This has been explained by the significant role played by the used catalyst in destructing asphaltenes and resins as shown by XRD, elemental analysis, and gas chromatography, which confirmed the presence of molybdenum sulfur particles in the reaction medium at higher temperatures, especially at 300 °C. These particles contributed to stimulating hydrodesulphurization, cracking and hydrogenation reactions by breaking down the C-heteroatom bonds and consequently by destructing sphaltenes and resins into smaller fractions, leading to higher mobility and quality of the upgraded oil. Our results add to the growing body of literature on the catalytic upgrading of heavy oil in the presence of transition metal particles.