Submitted:
22 August 2024
Posted:
23 August 2024
You are already at the latest version
Abstract
Keywords:
1. Introduction
2. Ultrasound in Oil Recovery and Processing
3. Ultrasounic Treatment of Coal
4. Ultrasonic treatment of oil shale
5. Conclusion
Supporting Information:
Conflict of Interest:
Acknowledgements
References
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| Ultrasound frequency | Ultrasound intensity |
Exposure time | The effect of exposure | Reference |
| 40 kHz | 150, 300, 500 W |
3-90 min | Injection of water and surfactants using ultrasound improves oil recovery by 11% and 12%, respectively. With increased ultrasonic intensity, oil recovery improves from 61.1% (150 W) to 67.4% (500 W) | [10] |
| 20 kHz | 300 W | 3-10 min | Ultrasound changes the morphology of the carbonate rock by forming microcracks. Sandstone particles exfoliated more strongly than dolomite particles. | [11] |
| 30 kHz | 100 W | - | Improved mobility and oil percolation depending on the viscosity and pore geometry of the rock. The effect of ultrasound was stronger for light oils. | [12] |
| 25-125 kHz | 120-300 W | 15-120 min | The completeness of oil recovery was mainly influenced by the intensity of ultrasound and the sludge’s hydrophilicity (the maximum recovery level - 92% was achieved for hydrophilic sludge with an ultrasound intensity of 240 W). | [13] |
| 18, 20, 25 kHz | 1000 W | 10-100 min | When using ultrasound and hydrogen peroxide together, the permeability increased to 40.90%. | [14] |
| 15-28 kHz | - | - | Ultrasound with a frequency of 20 kHz caused the formation of microcracks in the cores. The viscosity of oil and the surface tension between oil and water have also decreased. | [15] |
| 40 kHz | 200 W | 8 h | The oil recovery rate increased by 11.7%. The oil viscosity at 60 °C decreased by 32%, the content of resins and asphaltenes decreased by 49% and 37%, respectively. | [16] |
| 42, 46 kHz | 35-50 W | 8 min | Ultrasonic irradiation reduced the number of asphaltene clusters in the oil. Ultrasound of 50 W and 46 kHz during 8 minutes reduced the viscosity of the heated oil to 40%, and of the cooled oil by 10%. | [17] |
| 21.7; 41.9; 98.0; 123.0 kHz | 0.5-0.7 W/sm2 |
5-35 min | The efficiency of oil recovery from sludge increases with processing time, increased intensity and decreased frequency of ultrasound. | [18] |
| 50 kHz | 10 kW/m2 | 0-200 h | Improved recovery of low-maturity shale oil was achieved by expanding the pores of the reservoir and increasing the mobility of oil. With an ultrasonic treatment duration of less than 150 hours, the diameter, surface and total pore volume increased slightly with increasing treatment time. With longer processing (200 h), these pore parameters increased significantly. | [19] |
| 50 kHz | 30, 60, 100 W | 2-18 min | The combined use of ultrasound and solvent (n-heptane) led to the greatest decrease of the viscosity of heavy asphaltene oil. | [20] |
| 40 kHz | 150, 500 W/sm2 | 15-60 min | The extraction of paraffin (as the heavier oil) and kerosene (as the lighter oil) from a 2D micro-model of a porous medium has been studied. Short-term and intermittent ultrasound can recover more oil compared to continuous ultrasound for a longer time. With an increase of ultrasound intensity, oil extraction increased. When using paraffin, extraction was 74%, and kerosene - 82% at 500 W/cm2 intensity with intermittent ultrasound. |
[21] |
| - | 80, 100, 120 W | 1-3 min | Ultrasonic and thermal treatment of heavy oil samples leads to an decrease in viscosity by 20% and by 2.3 times for two oil samples. Thermal and ultrasonic treatment showed the same effect. | [22] |
| 18, 24, 35 kHz | - | - | The viscosity of heavy oil samples decreases by 5.3-12.1%, average oil by 37%, and bio-oil by 2 times. | [23] |
| 22 kHz | 1000 W | 80 min | Ultrasound increases the permeability of low-permeability cores to 80, 42, 87 and 81% and removes inorganic deposits. | [24] |
| 20 kHz 40 kHz |
60 W | 0-99 min | The water-oil emulsions were treated with ultrasound, then surfactants or biosurfactants produced by aerobic microorganisms were added to them. Emulsions with biosurfactants were more stable, their injection increased oil recovery to 86.9% | [25] |
| Country | Process Parameters | Obtained results | Reference |
| Kazakhstan | Solvents: benzol, kerosene, hexane, hexyl alcohol, diesel fuel and white spirit in ratios from 5:1 to 1:5 Flocculant: “Uniflok” (hydrolyzed polyacrylonitrile derivatives) Ultrasonic treatment Process time: 2-3 min to 6 hours. |
It has been established that the rate of separation of organic components depends not only on ultrasonic treatment, but also on the solvents used. When kerosene and white spirit are used as solvents, as well as at a concentration of flocculant 0.1%, the maximum separation of the organic part is achieved within 10 minutes. | [54] |
| China | Solution: surfactant including SDBS, NAOL, NaLA Frequency: 28 kHz, dual-frequency combined ultrasounds (28/68), (28/80), (68/80), and tri-frequency combined ultrasounds (28/68/80) |
Multi-frequency ultrasound treatment results in faster oil separation than single-frequency ultrasound treatment. Optimal separation was achieved using three-frequency ultrasound at a temperature of 20-30 °C, a surfactant concentration of 1.5 g/l for 10-15 minutes. | [59] |
| China | Frequency: 28 kHz Intensity: 200W The mass ratio of the agent (YSFL) and oil sand: 1:1 Temperature: 70°C |
The oil product yield is 94.2% in 13 minutes. The optimal process temperature is 60°C. The optimal mass ratio agent:oil sand is 0.8:1. | [60] |
| Russia | Solution: Na2SiO3 Frequency: 22 kHz Intensity: 1000W Temperature: 30°C and 75°C. Solution pH: >7 |
94% bitumen is separated at 60°C during 8 minutes at concentration of Na2SiO3 6%. | [61] |
| Russia | Solution: Sodium silicate (Na2O·SiO2), Na2CO3 (sodium carbonate) and sodium hydroxide (NaOH). Frequency: 28 kHz and 200 kHz. Intensity: 60-200 W Temperature: 30°C and 75°C. Process time: 15 min |
It has been found that the high intensity of ultrasound separates more bitumen. Purification using an alkaline solution recommended only for mixtures with particle sizes of at least 10 µm. |
[62] |
| Kazakhstan | Solution: alkaline medium of sodium silicate and sodium carbonate Frequency: 22 kHz Intensity: 400W Process time: 8-15 min |
At the optimal concentration of the solution, Na2SiO3 – 0,5 mol/l, Na2СO3 – 1,1 mol/l, a high degree of bitumen separation was achieved 94-96%. | [58] |
| Russia | Solution: Sodium silicate (Na2O·SiO2), Na2CO3 (sodium carbonate) and sodium hydroxide (NaOH). Temperature: 300-350 K (27-77°C) Intensity: 100 W Frequency: 22 kHz |
With a sufficiently high alkalinity (more than 3-5% by weight), the bitumen separation increases by about 95%. The rate of separation of bitumen from oil sands increases with increasing temperature. | [56] |
| China | Solution: surfactant SDBS Frequency: For single frequency: 28 kHz or 68 kHz, for dual- frequency: frequencies of 28 kHz and 68 kHz simultaneously Intensity: 75W Process time: 30 min |
The dual-frequency ultrasound treatment technology increases the level of oil production from oil sands to 95%, reduces the temperature by 40 °C, the concentration of surfactants in solution by 60%, water consumption by 20%, and also reduces the process time by 66%. | [8] |
| Canada | Combined treatment by ultrasonic and freeze/thaw. Solution: bio-surfactant (rhamnolipid), NaCl Frequency 20 kHz Intensity: 66 W Process time: 10 min |
Ultrasound treatment with an intensity of 66 W for 10 minutes, an oil sludge/water ratio of 1:2 and without the addition of bio-surfactant and salt, the degree of oil recovery was 80%. As a result of the combined treatment, oil recovery was 64.2%. Ultrasound helps to separate oil from solid particles, and freezing/thawing promotes the separation of water and oil. | [63] |
| Canada | Solution: 3% NaCl Frequency 20-40 kHz Intensity: 45, 84 W Process time: 160 min |
As a result of the work, a high degree and speed of oil extraction from sandstone was noted at a higher ultrasound frequency and a shorter distance from the ultrasonic electrode. | [64] |
| China | Solution: Surfactant SDBS Frequency: 20, 28, 40 kHz Intensity: 540 W Process time: 160 min |
It was found that at an ultrasound intensity of 4.89 W/cm2, the number of oil droplets first increases and then decreases with increasing ultrasound intensity. At an ultrasound frequency of 20 kHz, the number of oil droplets varies from 250 to 300 mµ. | [65] |
| China | Extractants: petroleum ether, toluene Solution: surfactants SDBS and Triton X-100, Na2SO4·H2O, NaOH Frequency: 21.7, 41.9, 98.0 and 123.0 kHz Intensity: 1 W/cm2 Process time: 35 min |
It has been found that with an increase in the intensity of ultrasound and processing time, the efficiency of separating oil from oil sludge increases. | [18] |
| China | LAS and AEO-9 were chosen as surfactants, and Na2CO3 and Na2SiO3 were chosen as dispersants. Frequency: 28 kHz Intensity: 500 W Process time: 10 min Temperature: 60°C Solution pH: 10 |
As a result of the experiment, the oil recovery from the oil sludge increased to 99.32%. The oil separated from the oil sludge contained 0.53% of solid particles. | [66] |
| China | Modification reagents: Sx4056: petroleum sulfonate: sodium silicate = 1:4:10 Frequency 35 kHz Intensity: up to 90 W Process time: 20 min Temperature: 60°C pH of the solution: 10 |
The oil sand with an organic content of 30.8% was pretreated with a modifying reagent under the influence of ultrasound, and then flotation extraction was performed. At a concentration of the modifying reagent of 10.0 g/l, an ultrasound frequency of 53 kHz, and a intensity of 75 W, the content of the organic part decreased to 0.66 % | [67] |
| China | Frequency 25, 50, 100 kHz Intensity: up to 300 W Process time: 120 min |
The optimal conditions for separating oil from oil sludge are the frequency of 25 kHz, the ultrasound intensity of 0.33 W/cm2 and the ratio of oil sludge:water is equal to 1:2. It has been established that the use of surfactant solution is necessary for the extraction of resinous asphaltene components from oil sludge when exposed to ultrasound | [68] |
| Japan | Frequency 28 kHz Temperature: 200°C Reagent: THF |
88% of bitumen was separated from oil sands and 42% of sulfur was removed from bitumen. | [69] |
| Japan | Frequency: 28 kHz Intensity: 11 W Process time: 0-180 min Temperature: 450°C Reagents: hydrogen peroxide and THF |
When using 3 wt% H2O2 and 60 minutes of irradiation, the degree of bitumen separation was 93%, and the degree of desulfurization was 86%. | [70] |
| Japan | Frequency: 28 kHz Intensity: 200 W The temperature: 850°C pH=13 (concentrated alkali solution) gas CO2 |
Bitumen is effectively separated from an alkaline solution using ultrasonic irradiation with CO2 injection. Bitumen recovery rate of 70% at a CO2 injection rate of 20 ml/min. | [71] |
| Canada | Jet cavitation The temperature: 5-55 °C. Process time: 10 min |
The mass of bitumen-free sand when using cavitating jets was greater than with non-cavitating jets. The cavitation effect for bitumen separation ranged from 40% to 50%. | [72] |
| Canada | Jet cavitation Cavitation σ=0.37 - 0.46 Intensity: 69-93 W The temperature: 12-23 °C Process time: 3 hours Six cavitation nozzles with a diameter of 13-17 mm have been tested |
Higher cavitation activity was observed when using a self-resonating nozzle. Cavitation jets can be used instead of hydraulic transport, thereby reducing the energy consumption of the bitumen separation process. | [73] |
| China | Jet cavitation Inlet pressure 6-14 MPa |
At an inlet pressure of 12 MPa, a temperature of 35 °C, and a hydrodynamic cavitation time of 4 s, the oil recovery coefficient from oil sludge reached 82.3 % | [74] |
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