Process Technologies for Heavy Oils and Residua Upgradings

A special issue of Processes (ISSN 2227-9717). This special issue belongs to the section "Energy Systems".

Deadline for manuscript submissions: 1 June 2024 | Viewed by 2003

Special Issue Editors


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Guest Editor
Petroleum Engineering School, Southwest Petroleum University, Chengdu, 610500, China
Interests: enhanced heavy oil recovery; in situ upgrading and gasification; solvent-assisted processes
Petroleum Engineering School, Southwest Petroleum University, Chengdu 610500, China
Interests: thermal methods; numerical simulation; enhanced heavy oil recovery
Special Issues, Collections and Topics in MDPI journals

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Guest Editor
Petroleum Engineering School, Southwest Petroleum University, Chengdu, 610500, China
Interests: heavy oil; petroleum engineering

Special Issue Information

Dear Colleagues,

Heavy oil, which accounts for more than 70% of the crude oil resources discovered in the world, contributes to about 10% of current global crude oil production. As the remaining reserves of conventional oil have been steadily decreasing over the years, the effective development of heavy oil resources plays important roles for future energy supplies and global economy.

Thermal methods have been proven to be the most effective for extracting heavy oil due to its high viscosity and low mobility under original reservoir conditions. Several commercial recovery processes are available and have been used for decades for the successful production of heavy oil, including cyclic steam stimulation (CSS), steam-assisted gravity drainage (SAGD), steam flooding and in situ combustion (ISC), etc. However, thermal recovery methods face challenges in meeting economic and environmental targets due to their high energy consumption and greenhouse gas emissions. More cost- and energy-efficient methods are urgently required to develop heavy oil reservoirs with lower quality, depths of more than 2000 meters, and with complicated water–oil contacts and fractures, etc.

A great deal of research has been conducted in recent years that aims to improve the thermal efficiency and reduce the water requirements and environmental impacts of heavy oil recovery processes. To develop more energy-effective recovery technologies, solvent- and NCG-aided processes, in situ upgrading and gasification, in situ generation of hydrogen and solvents, downhole steam generation and EM heating, etc., have been explored, to give some examples. This Special Issue is dedicated to studies on innovation and advancements in thermal recovery methods, mainly focused on, but not limited to, the following aspects:

  • Mechanisms of thermal enhanced recovery processes;
  • Cutting-edge hybrid methods;
  • Thermal methods applied in special types of reservoirs;
  • Follow-up and alternative recovery technologies;
  • Downhole heating and steam generation;
  • In situ upgrading and gasification of heavy oil;
  • Field cases for enhancement of thermal recovery methods.

Prof. Dr. Qi Jiang
Dr. Xiang Zhou
Dr. Siyuan Huang
Guest Editors

Manuscript Submission Information

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Keywords

  • heavy oil
  • thermal recovery
  • in situ upgrading
  • in situ gasification
  • solvent-aided process
  • down-hole heating
  • follow-up processes

Published Papers (2 papers)

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Research

23 pages, 10019 KiB  
Article
Study on Characteristics of Steam Chamber and Factors Influencing Nitrogen-Assisted Vertical–Horizontal Steam Drainage Development
by Aiping Zheng, Chunsheng Yu, Houchuan Huang, Xuan Li, Huan Liu, Tianxiu Li, Dong Song, Yili Liu, Pan Wang and Xiangjin Liang
Processes 2024, 12(4), 754; https://doi.org/10.3390/pr12040754 - 08 Apr 2024
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Abstract
With the notable achievements attained through the implementation of steam-assisted gravity drainage (SAGD), the vertical–horizontal steam drive (VHSD) emerges as a pivotal technological advancement aimed at significantly enhancing the efficiency of thin reservoir heavy oil recovery subsequent to steam cyclic stimulation. The inclusion [...] Read more.
With the notable achievements attained through the implementation of steam-assisted gravity drainage (SAGD), the vertical–horizontal steam drive (VHSD) emerges as a pivotal technological advancement aimed at significantly enhancing the efficiency of thin reservoir heavy oil recovery subsequent to steam cyclic stimulation. The inclusion of nitrogen assistance has proven effective in enhancing the efficacy of gravity drainage techniques in reservoir development. However, it is noteworthy that this method has only led to improvements in approximately 50% of the well groups within the observed field. The comprehensive evaluation index of VHSD was proposed, and as the objective function, it was determined that the greatest contribution to the VHSD technique lies in oil saturation, accounting for 40% of the overall evaluations. This differs from conventional SAGD operations, where reservoir thickness serves as the primary determinant. Building upon an enhanced physical simulation similarity criterion, two comparative injection scheme experiments were conducted to explore the impact of nitrogen injection on the performance of VHSD and the characteristics of the steam chamber. Nitrogen is distributed in the vicinity of the steam chamber, leading to the formation of a dual mechanism characterized by ‘top heat insulation and lateral traction’ on the steam chamber. The lateral traction accounts for approximately 25% of the team chamber volume. Additionally, the inducement of nitrogen causes a downward displacement of crude oil, resulting in its accumulation within the high-temperature region of the steam chamber. This, in turn, enhances the contact area between the high-temperature steam and the crude oil, ultimately leading to improvement in production efficiency. Further validation of the impact of nitrogen on steam lateral traction and interlayer steam drainage within the reservoir was confirmed using Xinjiang oilfield testing. The well temperature increased from 75 °C to 130 °C. Full article
(This article belongs to the Special Issue Process Technologies for Heavy Oils and Residua Upgradings)
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13 pages, 2348 KiB  
Article
Oxidation Kinetics Analysis of Crude Oils with Different Viscosities
by Bincheng Luo, Chunsheng Yu, Yuehao Chen, Kunhai Yue, Lifan Yue and Tao Chen
Processes 2023, 11(8), 2361; https://doi.org/10.3390/pr11082361 - 05 Aug 2023
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Abstract
In order to compare the oxidation kinetics parameters of crude oils with different properties in the process of crude oil oxidation, six different crude oil samples were selected to analyze the oxidation characteristics of crude oils with different properties. In order to study [...] Read more.
In order to compare the oxidation kinetics parameters of crude oils with different properties in the process of crude oil oxidation, six different crude oil samples were selected to analyze the oxidation characteristics of crude oils with different properties. In order to study the oxidation of crude oil, thermogravimetric analysis (TGA) and differential scanning calorimetry (DSC) synchronous analyzer were used for crude oil in the oxygen environment between 25 °C and 900 °C at a heating rate of 20 °C/min. The experimental results were based on crude oil oxidation using TGA and DTG experimental data to evaluate the oxidation mechanism of different crude oils, so as to better understand the situation in the oxidation reaction process. At the same time, the oxidation stage of crude oil was divided according to DSC data. Arrhenius method was used to analyze the oxidation kinetic parameters of crude oils with different properties, and the activation energies and pre-exponential factors of different crude oils were calculated. The experimental results show that the oxidation stage of crude oil can be divided into three stages: low-temperature oxidation, fuel deposition, and high-temperature oxidation. The low-temperature oxidation reaction begins at 280 °C, and the high-temperature oxidation reaction occurs at 400 °C. The low-temperature oxidation activation energy of an oil sample is 39.73–77.74 kJ/mol. The activation energy of the high-temperature oxidation is in the range of 106.27–264.47 kJ/mol. The activation energy of crude oil in the low-temperature oxidation stage increases with the increase of crude oil viscosity and decreases with the increase of crude oil viscosity in the high-temperature oxidation stage. Therefore, during the high-temperature oxidation stage, high-viscosity crude oil is more prone to reactions. Full article
(This article belongs to the Special Issue Process Technologies for Heavy Oils and Residua Upgradings)
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