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Hydraulic Fracturing Stimulation in Unconventional Reservoirs: The Recent Advanced Technology in
Hydraulic Fracturing Fluids
Presented By:
Abdulaziz Ellafi, Ph.D. Candidate at UND
▪ Research Assistant/Reservoir Engineer, Energy & Environmental Research Center (EERC), 2020
▪ Graduate Research and Teaching Assistant, Petroleum Eng. Department at UND, 2018
▪ Master’s Degree from Missouri University of Science and Technology, MO, USA, 2018
▪ Bachelor’s Degree from University of Tripoli, Libya, 2011
Contact Information:
Email: [email protected]
LinkedIn: https://www.linkedin.com/in/abdulaziz-ellafi-767275138/
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Presentation Outline
▪ Overview of Unconventional Reservoirs
▪ Bakken Petroleum System (BPS), Williston Basin
▪ Problem Statement
▪ Challenges Related to High Water Production in the Bakken
▪ Water Management Options
▪ Experimental and Simulation Studies
▪ Conclusions
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Overview of Unconventional Reservoirs
3
Daily crude oil production in Eagle Ford and Bakken Petroleum System (U.S. Energy Information
Administration , 2020)
Bakken Formation, Williston Basin
4
Modern Horizontal Drilling and Multi-Stage Hydraulic Fracturing
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Problem Statement
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Features of Produced Water
Produced waters salinity range in the United States (Otton and Mercier, 2015).
FW PW1
Specific Gravity 1.00 1.20
pH 8.07 4.83
Chloride (ppm) 50-630 163,637
Sulfate (ppm) 11 40
Aluminum (ppm) 0 1.42
Boron (ppm) 0 20.30
Barium (ppm) 0 5.69
Calcium (ppm) 304 29,222
Iron (ppm) 0 34.60
Potassium (ppm) 0 1,660
Magnesium (ppm) 30 4,347
Sodium (ppm) 4 70,342
Strontium (ppm) 0 2,204
TDS (ppm) 237-988 267,588
Hardness (ppm) 328 >20
Table 1: Chemical composition of the produced water analysis from Permian Basin.
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Challenges Related to High Water Production in the Bakken
The change in water cut over time in the U.S shale plays (Male, 2019).
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Water Management Options
Schematic of the process (Miller, 2003).
Schematic of MSF process (Miller, 2003).
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Water Disposal Methods
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0
Flowback water Treatment
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Fontenelle et al., 2013 introduced smart water treatment using electrochemical process for flowback and produced
waters, which does not remove dissolved ions. This technology separate colloidal organic and inorganic materials.
FW PW1 PW2 PW3
PW3 after treated
water
Specific Gravity 1.00 1.20 1.10 1.20 1.10
pH 8.07 4.83 6.21 5.3 7.5
Chloride (ppm) 50-630 163,637 118,000 166,014 166,152
Sulfate (ppm) 11 40 N/D 12 17
Aluminum (ppm) 0 1.42 N/D 1 1
Boron (ppm) 0 20.30 N/D 23.3 28
Barium (ppm) 0 5.69 N/D 8 8
Calcium (ppm) 304 29,222 9,480 29,755 29,875
Iron (ppm) 0 34.60 5.1 13 4
Potassium (ppm) 0 1,660 N/D 1,692 1,705
Magnesium (ppm) 30 4,347 N/D 4,629 4,452
Sodium (ppm) 4 70,342 N/D 74,562 76,427
Strontium (ppm) 0 2,204 N/D 1,777 1,791
TDS (ppm) 237-988 267,588 125,300 275,053 277,095
Hardness (ppm) 328 >20 12,740 36 18
Economic Analysis
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Cost Analysis ($/bbl) Freshwater Wastewater
Supply $ 0.25 - $ 3 $ 0.0 - $ 0.5
Transport $ 0.65 - $ 5.0 $ 2.0 - $ 9.0
Storage - $ 2.0 - $ 4.0
Disposal - $ 0.5 - $ 1.75
Bakken Well Performance
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Bakken Formation Characterization and Produced Water
Mineral analysis results of the Middle Bakken Formation samples.
Constituents Produced Water
Aluminum(ppm) 0.42
Barium(ppm) 33
Bromide(ppm) 816
Calcium(ppm) 22,400
Bicarbonates(ppm) 61
Chloride(ppm) 189800
Conductivity (µS/cm) 257
Dissolved Oxygen 8.24
Fluorine(ppm) 33
Iron(ppm) 34.60
Lithium(ppm) 60
Magnesium(ppm) 1430
Nitrate(ppm) 64
pH 2.94
Potassium(ppm) 7400
Sodium(ppm) 89500
Specific gravity 1.20
Strontium(ppm) 1540
Sulfate(ppm) 197
TDS (mg/L) 268,588
TPH (ppm) >20
TSS (mg/L) 10,623
Turbidity (NTU) 182
Table 2. Chemical composition of the Bakken Formation produced water.
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Fracture Treatment Fluids in Past and Present
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Type of FRs Chemical Name Chemical Structure
Non-ionic PAM Polyacrylamide
Anionic PAM
Polyacrylamide-co-acrylic acid,
hydrolyzed polyacrylamide
Poly-acrylamido-2-
methylpropane sulfonate
Cationic PAM Poly (acrylamide-co-N,N,N-
trimethyl-2-((1-oxo-2-propenyl)oxy))
Table 2. Types and chemical structures of friction reduces (FRs) (Xiong et al., 2018).
Anionic HVFRs in High TDS Environment
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Viscosity Profile
Ba Geri et al., 2019
Ba Geri et al., 2019
Cationic HVFRs have been successfully used in up to 100% produced water. However, this fluid can not be
compatible with formation rocks, such Bakken formation due to negatively charged that might cause formation
damage. On the other hand, anionic HVFRs tend to have minimum formation damage, but can’t tolerate high TDS
level of salt water.
The viscosity and elasticity (n’ & k’) are crucial factors to develop better fracturing fluids
Enhancing Anionic HVFRs in High TDS Environment
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The work of Seymour et al., 2018 showed that the addition of suitable surfactants can improve
performance and extend the salt tolerance of HVFRs. Also, study of Gu et al., 2019 concluded a
surfactant–polymer mixture has the advantages of strong shear resistance, drag reduction polymer to
mechanical and thermal degradation and the micelle structure’s critical concentration is reduced.
Seymour et al., 2018
Pressure reduction using friction loop
Gu et al., 2019
Bead model of the surfactant–polymer mixture
HVFR Viscosity Profiles Measurement
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Dilution
(%)TDS (ppm)
Hardness
(ppm)pH Iron (ppm)
Sulfate
(ppm)
Chloride
(ppm)
Bakken
Produced
Water
173,00022,400,00
0 2.9 152000 816000 189800
Grand
Forks Tap
Water
277 - 7.9 - - -
90%
FW/10%
PW
31,300 2,240,000 6.7 15200 81600 18980
70%
FW/30%
PW
84,300 6,720,000 6.2 45600 244800 56940
50%
FW/50%
PW
91,200 1,120,000 6.1 76000 408000 94900
Table 3. Summary of HVFRs fluids characterization case scenarios
HVFR Viscosity Profiles Measurement
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HVFRs samples at different levels of produced water.
Base Case Case#1 Case#2 Case#3
Dilution Ratios 100%FW 90%FW/10%PW 70%FW/30%PW 50%FW/50%PW
Dosage 0.25 to 8.0gpt 0.25 to 8.0gpt 6gpt & 8gpt 8gpt
Experiment
Temperature70⁰F and 150⁰F 70⁰F and 150⁰F 70⁰F and 150⁰F 70⁰F and 150⁰F
Table 4. Summary of HVFRs fluids characterization case scenarios.
HVFR Viscosity Profiles Measurement
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Viscosity Profile of HVFR Fracturing Fluid blend at 100% Bakken Tap Water at 70⁰F (right) and 50%
Bakken Produced Water at 70 ⁰F and 150 ⁰F.
Implementation Simulation Test
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Reservoir Simulation Model
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Reservoir Simulation Model
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Case Study: Middle Bakken Formation
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Treatment Cases(#)
Type of Fluids(Name)
Pump Rate(bpm)
Final Proppant Concentration
(Ibm/gal)
Proppant Size(mesh)
Case Study #1 Slickwater 50 2 40/70
Case Study #2 Linear Gel 50 2 40/70
Case Study #3 HVFR-PR 50 2 40/70
Case Study #4 HVFR-PRS 50 2 40/70
Table 5. Summary of re-stimulation case scenarios.
Pre-Re-fracturing Simulation Well Flow Behaviors
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Results and Analysis
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Case Study #1
Results and Analysis
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Case Study #2
Results and Analysis
28
Case Study #3
Results and Analysis
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Effect of Fracturing Fluid Types on Bakken Oil Well Production
Conclusions
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In this study, a comprehensive study was employed for the application of produced water with fracturing fluids in
unconventional shale plays, such as the Bakken Formation. The research findings point out the following:
▪ The freshwater availability has decreased with increasing associated costs, which leads to impacts on human
health, agriculture, livestock, and wildlife. The water treatment process can help to reduce contaminate
groundwater resources and toxic air emissions due to transportation and disposal operations.
▪ The research outcomes could contribute to practices in other countries that have unconventional resources,
such as Saudi Arabia, Russia, China, Argentina, and Libya, especially some of these nations already face
challenges of availability of clean water.
▪ The separation process of the organic and inorganic materials from the flowback water may be the best option
to treat produced water with low cost and effective application that would be successfully used with fracturing
fluids, such as crosslinked and friction reducers fluids.
Conclusions Cont.
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▪ The common type of HVFRs is anionic fluid due to its lower cost and better drag reduction. Although anionic
HVFRs tend to have minimum formation damage but cannot tolerate a high TDS level of saltwater and more
sensitive to Iron constituent.
▪ Cationic HVFRs have been successfully used in up to 100% produced water with the lower-cost operation, but
cationic HVFRs may not be compatible with formations that contain a high amount of quartz and/or clay
(Bakken Formation).
▪ This paper enhanced the ability of anionic HVFRs in Bakken produced water condition by using dilute water (for
example 10% to 50% instead of using the water treatment and freshwater). The research outcomes concluded
that increasing in HVFRs dosage (8 gpt) can extend the performance of frac-fluids when 50% of produced water
is used.
Conclusions Cont.
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▪ The simulation results showed the surfactant as additives modified the rheological properties of HVFRs in harsh
conditions by preventing degradation, reducing viscosity, expanding fluid viscoelasticity, and extending the flow
behavior index (n’) and flow consistency index (k’) performance of the fracturing fluids to be able to carry
proppant deeper into secondary and tertiary fractures. Surfactant might be a good candidate to enhance the
unfolding time anionic HVFRs in high TDS conditions and cold water as well as improving oil recovery from
unconventional shale plays.
Publications
▪ Ellafi, A., Ba Geri, M., Bubach, B., & Jabbari, H. (2019a, August 28). Formation Evaluation and Hydraulic Fracture Modeling of
Unconventional Reservoirs: Sab'atayn Basin Case Study. American Rock Mechanics Association.
▪ Ellafi, A., Jabbari, H., Ba Geri, M., & Alkamil, E. (2019b, November 11). Can HVFRs Increase the Oil Recovery in Hydraulic
Fractures Applications? Society of Petroleum Engineers. doi:10.2118/197744-MS
▪ Ellafi, A., Jabbari, H., Wan, X., Rasouli, V., Ba Geri, M., & Al-Bazzaz, W. (2020a). How Does HVFRs in High TDS Environment
Enhance Reservoir Stimulation Volume? International Petroleum Technology Conference (IPTC) 2020 IPTC-20138
▪ Ellafi, A., Jabbari, H., Tomomewo, O., Mann, M., and Ba Geri, M. (2020b) ‘Future of Hydraulic Fracturing Application in Terms of
Water Management and Environmental Issues: A Critical Review ', Society of Petroleum Engineers (SPE), (SPE-199993-MS)
▪ Ba Geri, Noles, J., Kim, S., & Ellafi, A. (2020). New Developed Mathematical Model for Predicting Viscosity Profile and Proppant
Transport Utilizing HVFRs Dosage with Produced Water. Society of Petroleum Engineers. doi:10.2118/ 201433-MS
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Acknowledgment
▪ The authors would like to acknowledge the North Dakota Industrial Commission (NDIC), Petroleum
Research Fund for their financial support of this work, through the contract NDIC G-045-89. The financial
support of the North Dakota Industrial Commission (NDIC) is highly appreciated.
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Thank You for your attention!
Questions?
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