**2. Equipment design and specifications**

The laboratory scale EGS simulation equipment consists of four main subsystems being a heated true-triaxial cell, a high pressure hydraulic injection system, a multi-component data acquisition system, and sample materials and characterization equipment.

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**Figure 1.** Layout of the true-triaxial cell.

#### **2.1. Heated true triaxial cell**

performance concrete, granite, and acrylic. Fracturing fluids used include water, brine, and

**Keywords:** Enhanced Geothermal Systems (EGS), true triaxial device, hydraulic fracturing,

The potential of Enhanced Geothermal Systems (EGS) is well documented in the MIT led study titled "The Future of Geothermal Energy" [1]. With this technology, unconventional deep Hot Dry Rock (HDR) reservoirs are engineered with drilling and stimulation techniques to create a heat mining system for base load energy production. The methods needed for enabling EGS energy production also have the ability to improve production from traditional geothermal

To provide the EGS reservoir stimulation, one of the most promising techniques is hydraulic fracturing. This method utilizes high pressure fluid injection into targeted reservoir intervals to enhance permeability and generate new flow paths through enhancing existing fractures and creating new fractures. With the installation of an injector-producer well scheme, the physical limitations of natural reservoir recharge and stored harvestable fluids may be overcome and a productive reservoir may be the end result. Hydraulic fracturing has been proven effective as a stimulation technique by the oil and gas industry since its first implementation in 1947 [2].

Currently, only a small number of EGS field trials have been performed due to the high economic risk of the procedure and the significant probability of failure. Thus, performing controlled EGS experiments in the laboratory setting may be able to provide some of the crucial data and experience needed for advanced fracture model calibration and full scale testing in the field. This is especially true considering that most hydraulic fracturing design techniques, as developed by the petroleum industry, are more dependent upon historical data than on theoretical analysis [3]. In the case of EGS development, this historical data does not yet exist

To fill the knowledge gap, laboratory scale EGS reservoir testing is being performed at the Colorado School of Mines using a heated true-triaxial apparatus. Some completed test results and observations are presented along with technical information on the equipment and procedures used. Focus is given to series of tests performed on a hydraulically fractured granite

The laboratory scale EGS simulation equipment consists of four main subsystems being a heated true-triaxial cell, a high pressure hydraulic injection system, a multi-component data

sample with a binary injector-producer borehole scheme installed.

acquisition system, and sample materials and characterization equipment.

**2. Equipment design and specifications**

Valvoline® DuraBlend® SAE 80W90 oil.

960 Effective and Sustainable Hydraulic Fracturing

scale model testing, acoustic emissions

resources which are already being utilized today.

**1. Introduction**

in sufficient quantities.

The layout of the heated true triaxial cell is shown in Figure 1. It consists of a cylindrical loading rig made of high strength steel. Flatjacks apply pressures on all six faces of a 30x30x30 cm3 block rock sample. Freyssinet 350 mm flatjacks, which are pressurized with pumps, allow independ‐ ent control of the principal stresses of up to 12.5 MPa. The flatjack pressures can be controlled to achieve triaxial stress conditions with different magnitudes of overburden stress σ v, maxi‐ mum horizontal stress σ H, and minimum horizontal stress σ h. Externally mounted flexible silicone rubber heaters with proportional-integral-derivative (PID) control allow for dualzone heating with separate set points for the lateral and vertical heating elements. The heating system allows for the simulation of an EGS reservoir with a temperature of up to 180 ºC.

Figure2showspicturesofthecompletedtruetriaxialcellwithandwithoutthedrillingrigplaced on top of the cell. An orientated rotary-hammer drill press is used to drill boreholes into the sample at user selected positions and angles while the sample is under stresses and tempera‐ ture. This procedure allows for strategic borehole installations that are specific to the test and the particular stimulated fracturing plane. Borehole damage is replicated by using percussive drilling into the loaded sample instead of the more common cast-in-place pre-drilled borehole methods[4-7].Theboreholeistypicallydrilledwithoneuppercasedsegmenthavingamaximum outside diameter of 10 mm and a second uncased fracturing interval having a typical diameter of5.6mm.Thesedimensionswereselectedtobeassmallaspossibletoallowforthemosteffective EGS reservoir simulation within the confines of the 30x30x30 cm3 cubical sample blocks.

#### **2.2. High pressure hydraulic injection system**

A programmable hydraulic injection system is used for both hydraulic fracture stimulation and post-fracture flow analysis. Precision high pressure flow is provided by a dual 65DM Teledyne Isco syringe pump system, a series of pneumatic-hydraulic automated valves, and a custom pump control program developed with LabVIEW. This system is capable of provid‐ ing pressures up to 70 MPa and precise controlled flow rates between 10 nL/min and 60

**Figure 2.** Pictures of the true triaxial cell. Left: without the drilling rig, Right: with the lid and drilling rig.

mL/min with a flow stability of ±0.3% from the set point. A diagram of the hydraulic system is provided in Figure 3.

**Figure 4.** Borehole sealing method applied with typical dimensions.

To monitor and control the equipment and system processes a multi-channel multi-function National Instruments CompactDAQ was used with 16 strain gage channels, 16 CJC thermo‐ couple channels, 8 voltage channels, 8 current channels, and 4 multi-function channels. The attached sensors included 2 Omega® PX309-10KG5V pressure transducers for monitoring the injection wellhead pressure and intermediate principal sample confining stress, 1 Omega® PX309-3KG5V pressure transducer for monitoring the minimum principal stress, 1 Omega® PX40-50mmHG pressure transducer for monitoring the production reservoir fill level and flow rate, 1 Omega® LD621-30 linear displacement transducer for auxiliary use, and 1 Humboldt HM2310.04 linear strain transducer also for auxiliary use. Omega® Type-T thermocouples, fabricated in-house, were positioned at the hydraulic temperature monitoring positions as indicated in Figure 3, inside the bottom of the injection and production boreholes, and in a high-coverage grid arrangement on the surface faces of the sample inside the cell, as shown in Figure 5. When used, strain gages were embedded onto the faces of the sample to monitor stress uniformity. Additional data was collected from the Teledyne Isco pump controller giving information about hydraulic system operation including flow rates, pressures, valve

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**2.3. Multi-component data acquisition system**

positions, and general pump status.

**Figure 3.** Diagram for the hydraulic fracturing system

1

Some of the programmable capabilities of the system include: (1) Stepwise continuous constant flow or pressure, (2) Controlled switching between clean and slurry fluid injection, and (3) Conditionally dependent operation with real time external data referencing capability. To seal the injection tubing into the borehole, threaded 316 SS tubing was grouted into a 10 mm outside diameter borehole using Loctite® Rapid Mix 5-Minute epoxy. The epoxy grout was delivered downhole using water-softened 00-size gelatin capsules to avoid the potential of bonding the casing to the true-triaxial cell's top lid. After reaching a 24 hr cure, an uncased 5.6 mm diameter interval was drilled through the bottom of the casing and into the sample. Figure 4 shows a diagram of the borehole sealing method.

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**Figure 4.** Borehole sealing method applied with typical dimensions.

#### **2.3. Multi-component data acquisition system**

mL/min with a flow stability of ±0.3% from the set point. A diagram of the hydraulic system

**Figure 2.** Pictures of the true triaxial cell. Left: without the drilling rig, Right: with the lid and drilling rig.

Some of the programmable capabilities of the system include: (1) Stepwise continuous constant flow or pressure, (2) Controlled switching between clean and slurry fluid injection, and (3) Conditionally dependent operation with real time external data referencing capability. To seal the injection tubing into the borehole, threaded 316 SS tubing was grouted into a 10 mm outside diameter borehole using Loctite® Rapid Mix 5-Minute epoxy. The epoxy grout was delivered downhole using water-softened 00-size gelatin capsules to avoid the potential of bonding the casing to the true-triaxial cell's top lid. After reaching a 24 hr cure, an uncased 5.6 mm diameter interval was drilled through the bottom of the casing and into the sample. Figure 4 shows a

(1) pneumatic actuated continuous flow valve system (2 and 5), dual high pressure syringe pumps (3 and 4), clean to slurry valve switching system (6), rotationally mixed hydraulic to hydraulic piston actuator (7), sample block (8), outflow reservoir (9), and general arrangement of select sensor systems.

is provided in Figure 3.

962 Effective and Sustainable Hydraulic Fracturing

**Figure 3.** Diagram for the hydraulic fracturing system

diagram of the borehole sealing method.

1

To monitor and control the equipment and system processes a multi-channel multi-function National Instruments CompactDAQ was used with 16 strain gage channels, 16 CJC thermo‐ couple channels, 8 voltage channels, 8 current channels, and 4 multi-function channels. The attached sensors included 2 Omega® PX309-10KG5V pressure transducers for monitoring the injection wellhead pressure and intermediate principal sample confining stress, 1 Omega® PX309-3KG5V pressure transducer for monitoring the minimum principal stress, 1 Omega® PX40-50mmHG pressure transducer for monitoring the production reservoir fill level and flow rate, 1 Omega® LD621-30 linear displacement transducer for auxiliary use, and 1 Humboldt HM2310.04 linear strain transducer also for auxiliary use. Omega® Type-T thermocouples, fabricated in-house, were positioned at the hydraulic temperature monitoring positions as indicated in Figure 3, inside the bottom of the injection and production boreholes, and in a high-coverage grid arrangement on the surface faces of the sample inside the cell, as shown in Figure 5. When used, strain gages were embedded onto the faces of the sample to monitor stress uniformity. Additional data was collected from the Teledyne Isco pump controller giving information about hydraulic system operation including flow rates, pressures, valve positions, and general pump status.

**2.4. Test materials**

Four material types were used for this project including medium strength concrete grout, ultrahigh strength low permeability concrete, locally obtained Colorado Rose Red Granite, and acrylic glass. Each of these materials was tested for a variety of mechanical, thermal, and acoustic properties to provide a reference for future field data comparison. A general summary of the measured properties for selected materials has been provided in Table 1. The uniaxial compression strength (UCS), elastic modulus (*E*), Poisson's Ratio (*v*), and indirect tensile strength (BTS) testing was performed using a specially instrumented ELE Accu-TekTM 250 concrete load frame. Thermal conductivity (*kT*) measurements were performed using a divided bar apparatus available through the Colorado Geological Survey [8]. Volumetric specific heat capacity (*CV*) was obtained using an insulated calorimeter. Acoustic compression (*VP*) and shear (*VS*) wave velocities were obtained using a piezoelectric pulse transmitter-receiver apparatus with oscilloscope monitoring. Porosity (ϕ) and matrix density (ρ*dry*) were measured

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For post-test analysis, diamond over cores and cut cross-sections were used. The over cores were taken to remove the borehole casing and observe the near wellbore fracture geometry. Next, cross-sections were cut using a 0.9 m diameter diamond table saw. An example cross section taken from an unconfined granite sample hydraulic fracturing test is shown in Figure 7. Cross sections such as these allowed for physical measurements of the fracture locations, fluid permeation depths, and verification of AE fracture location estimations. Fluid pathways and permeation depths were most visible on tests using oil as the fracturing fluid due to staining of the sample material. Compiling fracture geometry data from consecutive cross sections allows for three-dimensional imaging of entire stimulated fracture networks. As evident in Figure 7, these networks are expected to be very complex due to the heterogeneities

Using this equipment, an ongoing series of hydraulic fracturing stimulation and reservoir characterization testing is being performed to obtain new data for EGS technology advance‐ ment. While hydraulic fracturing experiments have been performed in more than 11 different boreholes and four different materials, focus will be given to a granite hydraulic fracturing test where an orientated intercept borehole was drilled to create a producing heated EGS reservoir. The results of the EGS simulation experiment can be divided into several key phases including sample preparation, primary hydraulic fracturing, drilling the fracture intercept

For this test, a block of Colorado Rose Red Granite, as documented in Figure 8, was loaded into the true-triaxial cell and slowly heated to an average internal temperature of 50 ºC over the span

using a 70% vacuum desiccator, 110ºC oven, and digital mass balance.

in natural rock and concrete samples.

**3. Test results and observations**

borehole, and fracture reopening and flow.

**3.1. Sample preparation**

**Figure 6.** AE sensor installed in a loading platen.

**Figure 5.** Diagram of surface sensor positions on a typical 30x30x30 cm3 sample.

To monitor the fracturing process and provide real-time location estimation for the generated hydraulic fractures, a 6-sensor piezoelectric Acoustic Emission (AE) monitoring system, obtained from Physical Acoustics Corporation, was installed inside the cell with sensors contacting the faces of the sample in an arrangement to achieve maximum volumetric coverage, as shown in Figure 5. Figure 6 shows an AE sensor installed into a 25 mm thick loading platen where it was protected from the high loading stresses being applied to the sample. Thin packing foam wafers were inserted between the sensor body and the steel housing to dampen external acoustic noise effects and provide a soft spring reaction for any movement that would occur during loading and unloading processes. In general, this platen serves as a movable interface between the pressurized flat jack and the sample inside the cell. During analysis, recorded AE events could readily be filtered by correlation coefficient, amplitude, or other criteria using digital post-processing of hit time and waveform data.

#### **2.4. Test materials**

Four material types were used for this project including medium strength concrete grout, ultrahigh strength low permeability concrete, locally obtained Colorado Rose Red Granite, and acrylic glass. Each of these materials was tested for a variety of mechanical, thermal, and acoustic properties to provide a reference for future field data comparison. A general summary of the measured properties for selected materials has been provided in Table 1. The uniaxial compression strength (UCS), elastic modulus (*E*), Poisson's Ratio (*v*), and indirect tensile strength (BTS) testing was performed using a specially instrumented ELE Accu-TekTM 250 concrete load frame. Thermal conductivity (*kT*) measurements were performed using a divided bar apparatus available through the Colorado Geological Survey [8]. Volumetric specific heat capacity (*CV*) was obtained using an insulated calorimeter. Acoustic compression (*VP*) and shear (*VS*) wave velocities were obtained using a piezoelectric pulse transmitter-receiver apparatus with oscilloscope monitoring. Porosity (ϕ) and matrix density (ρ*dry*) were measured using a 70% vacuum desiccator, 110ºC oven, and digital mass balance.

For post-test analysis, diamond over cores and cut cross-sections were used. The over cores were taken to remove the borehole casing and observe the near wellbore fracture geometry. Next, cross-sections were cut using a 0.9 m diameter diamond table saw. An example cross section taken from an unconfined granite sample hydraulic fracturing test is shown in Figure 7. Cross sections such as these allowed for physical measurements of the fracture locations, fluid permeation depths, and verification of AE fracture location estimations. Fluid pathways and permeation depths were most visible on tests using oil as the fracturing fluid due to staining of the sample material. Compiling fracture geometry data from consecutive cross sections allows for three-dimensional imaging of entire stimulated fracture networks. As evident in Figure 7, these networks are expected to be very complex due to the heterogeneities in natural rock and concrete samples.

#### **3. Test results and observations**

Using this equipment, an ongoing series of hydraulic fracturing stimulation and reservoir characterization testing is being performed to obtain new data for EGS technology advance‐ ment. While hydraulic fracturing experiments have been performed in more than 11 different boreholes and four different materials, focus will be given to a granite hydraulic fracturing test where an orientated intercept borehole was drilled to create a producing heated EGS reservoir. The results of the EGS simulation experiment can be divided into several key phases including sample preparation, primary hydraulic fracturing, drilling the fracture intercept borehole, and fracture reopening and flow.

#### **3.1. Sample preparation**

**Figure 5.** Diagram of surface sensor positions on a typical 30x30x30 cm3 sample.

**Figure 6.** AE sensor installed in a loading platen.

964 Effective and Sustainable Hydraulic Fracturing

To monitor the fracturing process and provide real-time location estimation for the generated hydraulic fractures, a 6-sensor piezoelectric Acoustic Emission (AE) monitoring system, obtained from Physical Acoustics Corporation, was installed inside the cell with sensors contacting the faces of the sample in an arrangement to achieve maximum volumetric coverage, as shown in Figure 5. Figure 6 shows an AE sensor installed into a 25 mm thick loading platen where it was protected from the high loading stresses being applied to the sample. Thin packing foam wafers were inserted between the sensor body and the steel housing to dampen external acoustic noise effects and provide a soft spring reaction for any movement that would occur during loading and unloading processes. In general, this platen serves as a movable interface between the pressurized flat jack and the sample inside the cell. During analysis, recorded AE events could readily be filtered by correlation coefficient, amplitude, or other criteria using digital post-processing of hit time and waveform data.

For this test, a block of Colorado Rose Red Granite, as documented in Figure 8, was loaded into the true-triaxial cell and slowly heated to an average internal temperature of 50 ºC over the span


with the layout as shown in Figure 5. Combined, both of these methods were in agreement that a top corner of the sample was subjected to some elevated stress concentrations as indicated by relatively high strains and an increase in localized AE activity at the specific corner. This observationwasusedtomodifyandimprove the loadingprocedure suchthat similarunintend‐ ed stress concentrations would be less likely to occur during future tests using this equipment. While loaded, a centered vertical borehole was drilled into the sample, a 107 mm deep casing interval was installed, and a 73 mm uncased interval was drilled for a final injection well depth of 180 mm. It is important to note that drilling the borehole while the sample is under load is a unique system capability that allows for laboratory simulation of a borehole damage zone. This process creates small fractures near the borehole, as has been clearly observed in acrylic testing [11-12], which may serve as fracture initiation locations. Simultaneously, the drilling process also fills these micro fractures with fines which are believed to have some effect on fracture self propping as well as near wellbore tortuosity and skin factor. Additional investi‐ gation may be necessary to better understand how the borehole damage zone influences

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hydraulic fracture initiation, growth and closure.

**Figure 8.** Pre-test image of the granite sample used for EGS reservoir simulation experiments.

Primary hydraulic fracture breakdown was achieved using oil injection at a constant flow rate of 0.05 mL/min. Valvoline® Durablend® SAE 80W90 gear oil was used as the fracturing fluid due to its high viscosity value and publicly available fluid properties. At the injection tem‐ perature of 50 ºC, this fluid has an approximate dynamic viscosity of 71.5 cP as estimated using

**3.2. Primary hydraulic fracturing**

**Table 1.** Test Material Properties (\*data from [9-10]).

**Figure 7.** Cross-section from an unconfined granite hydraulic fracturing test.

of four days. After the target temperature was reached, the sample was pressurized with confining stresses of 12.5, 8.3, and 4.1 MPa for the vertical, maximum horizontal, and mini‐ mum horizontal stresses, respectively. The AE monitoring system was active throughout the loadingprocesstoidentifyifanymechanicalshearingorthermalfracturingeventshadoccurred. In this case, the AE data produced a large scatter of events with no significant clustering which indicatedthatacceptablyuniformloadinghadbeenachievedandnosignificantfracturingevents had occurred. The uniformity of the sample loading was also verified using strain gage data, with the layout as shown in Figure 5. Combined, both of these methods were in agreement that a top corner of the sample was subjected to some elevated stress concentrations as indicated by relatively high strains and an increase in localized AE activity at the specific corner. This observationwasusedtomodifyandimprove the loadingprocedure suchthat similarunintend‐ ed stress concentrations would be less likely to occur during future tests using this equipment.

While loaded, a centered vertical borehole was drilled into the sample, a 107 mm deep casing interval was installed, and a 73 mm uncased interval was drilled for a final injection well depth of 180 mm. It is important to note that drilling the borehole while the sample is under load is a unique system capability that allows for laboratory simulation of a borehole damage zone. This process creates small fractures near the borehole, as has been clearly observed in acrylic testing [11-12], which may serve as fracture initiation locations. Simultaneously, the drilling process also fills these micro fractures with fines which are believed to have some effect on fracture self propping as well as near wellbore tortuosity and skin factor. Additional investi‐ gation may be necessary to better understand how the borehole damage zone influences hydraulic fracture initiation, growth and closure.

**Figure 8.** Pre-test image of the granite sample used for EGS reservoir simulation experiments.

#### **3.2. Primary hydraulic fracturing**

of four days. After the target temperature was reached, the sample was pressurized with confining stresses of 12.5, 8.3, and 4.1 MPa for the vertical, maximum horizontal, and mini‐ mum horizontal stresses, respectively. The AE monitoring system was active throughout the loadingprocesstoidentifyifanymechanicalshearingorthermalfracturingeventshadoccurred. In this case, the AE data produced a large scatter of events with no significant clustering which indicatedthatacceptablyuniformloadinghadbeenachievedandnosignificantfracturingevents had occurred. The uniformity of the sample loading was also verified using strain gage data,

**Figure 7.** Cross-section from an unconfined granite hydraulic fracturing test.

**Medium Strength Concrete**

Unconfined Compressive Strength, UCS (MPa) 50-60 123-154 152 ± 19\* Brazilian Tensile Strength, BTS (MPa) 2.2-2.7 4.0-6.0 7.5 ± 1.8\* Young's Modulus*, E* (GPa) 9.5-10.5 20-30 57\* Poisson's ratio*, v* - - 0.32\* Dry density, ρ*dry* (kg/m3) 1950 1970 2650 Thermal conductivity*, kT* (W/m-K) - 1.60 ± 0.02 3.15 ± 0.05 Heat capacity*, CV* (kJ/m3-K) 2013 ± 145 1820 ± 146 2063 ± 92 Porossity, ϕ 0.30-0.31 0.15-0.23 0.006-0.008 Shear wave velocity*, VS* (mm/μs) 2.48 2.54 2.62 Compressional wave velocity*, VP* (mm/μs) 3.41 3.89 4.45

**Ultra-High Strength Concrete**

**Colorado Rose Red Granite**

**Material Property**

966 Effective and Sustainable Hydraulic Fracturing

**Table 1.** Test Material Properties (\*data from [9-10]).

Primary hydraulic fracture breakdown was achieved using oil injection at a constant flow rate of 0.05 mL/min. Valvoline® Durablend® SAE 80W90 gear oil was used as the fracturing fluid due to its high viscosity value and publicly available fluid properties. At the injection tem‐ perature of 50 ºC, this fluid has an approximate dynamic viscosity of 71.5 cP as estimated using the published product information in conjunction with the Walther Equation specified in ASTM D341 [13]. The importance of using high viscosity fluid for laboratory hydraulic fracture experiments is well documented [5-6]. In this case, using a high viscosity fluid provided the important benefits of better fracture growth control for improved probability of containment and a more predictable fracture orientation as the propagation would be less influenced by natural heterogeneities in the granite sample.

A plot of the hydraulic data for primary breakdown is shown in Figure 9. During this test, the pump was stopped 16 seconds after breakdown in an attempt to keep the fracture fully contained as real-time AE events were observed to be approaching the edges of the sample. Continued AE activity was observed even after pumping was stopped which indicated continued fracture propagation. Therefore, to forcibly halt the fracture growth, the flow rate was reversed at -10 mL/min for a total of 6 seconds to pull fluid out of the fracture and then held in the stopped position thereafter. At this time, a significant pressure rebound was observed which may offer some insight into fracture dynamic fluid storage behavior with additional investigation. Ultimately, the observation of a negligible flow rate during postfracture constant pressure testing at 2000 kPa verified that a fully contained fracture had been generated.

of each event with dark red circles having higher correlation. The two-segment centered

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Extending the AE analysis by application of moment tensor methods [14], information was obtained about the fracturing mode for some of the recorded AE events. As shown in Table 2, only about 11% of the total number of recorded events could successfully be classified with a reasonable level of certainty. At a glance, the tensile failure mode appears to be dominant during this fracturing stage but uncertainty associated with the low percentage of classifiable events effectively reduces the confidence of any conclusions which could possibly be derived

vertical injection borehole is clearly visible on the front and side view plots.

**AE Event Category Number % Total % Classification**

Total Events Located 726 100 - Classifiable Events 81 11.2 100 Tensile Events 39 5.4 48.1 Shear Events 28 3.9 34.6 Mixed Mode Events 14 1.9 17.3

**Table 2.** Classifications of AE Events during hydraulic fracturing.

**Figure 10.** AE event source locations during primary hydraulic fracture.

from these figures.

**Figure 9.** Hydraulic data plot for primary fracture.

Analysis of the AE source location data collected during this primary hydraulic fracture test revealed that a contained and planar fracture propagated from the borehole in a direction perpendicular to the minimum horizontal confining stress. Additionally, the fracture appeared to have a single dominant wing as evident by the AE cloud being most prominent on only one side of the borehole. Figure 10 shows orthogonal plots of the three-dimensional AE event source location results for the test. This analysis used six-sensor location regression and filtered the results to only contain events with a correlation coefficient greater than 0.75 and amplitude greater than 25 dB. On this plot, the circle diameters are directly proportional to the amplitude of the corresponding event. Also, the color shading corresponds to the correlation coefficient

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**Table 2.** Classifications of AE Events during hydraulic fracturing.

the published product information in conjunction with the Walther Equation specified in ASTM D341 [13]. The importance of using high viscosity fluid for laboratory hydraulic fracture experiments is well documented [5-6]. In this case, using a high viscosity fluid provided the important benefits of better fracture growth control for improved probability of containment and a more predictable fracture orientation as the propagation would be less influenced by

A plot of the hydraulic data for primary breakdown is shown in Figure 9. During this test, the pump was stopped 16 seconds after breakdown in an attempt to keep the fracture fully contained as real-time AE events were observed to be approaching the edges of the sample. Continued AE activity was observed even after pumping was stopped which indicated continued fracture propagation. Therefore, to forcibly halt the fracture growth, the flow rate was reversed at -10 mL/min for a total of 6 seconds to pull fluid out of the fracture and then held in the stopped position thereafter. At this time, a significant pressure rebound was observed which may offer some insight into fracture dynamic fluid storage behavior with additional investigation. Ultimately, the observation of a negligible flow rate during postfracture constant pressure testing at 2000 kPa verified that a fully contained fracture had been

Analysis of the AE source location data collected during this primary hydraulic fracture test revealed that a contained and planar fracture propagated from the borehole in a direction perpendicular to the minimum horizontal confining stress. Additionally, the fracture appeared to have a single dominant wing as evident by the AE cloud being most prominent on only one side of the borehole. Figure 10 shows orthogonal plots of the three-dimensional AE event source location results for the test. This analysis used six-sensor location regression and filtered the results to only contain events with a correlation coefficient greater than 0.75 and amplitude greater than 25 dB. On this plot, the circle diameters are directly proportional to the amplitude of the corresponding event. Also, the color shading corresponds to the correlation coefficient

natural heterogeneities in the granite sample.

968 Effective and Sustainable Hydraulic Fracturing

**Figure 9.** Hydraulic data plot for primary fracture.

generated.

of each event with dark red circles having higher correlation. The two-segment centered vertical injection borehole is clearly visible on the front and side view plots.

**Figure 10.** AE event source locations during primary hydraulic fracture.

Extending the AE analysis by application of moment tensor methods [14], information was obtained about the fracturing mode for some of the recorded AE events. As shown in Table 2, only about 11% of the total number of recorded events could successfully be classified with a reasonable level of certainty. At a glance, the tensile failure mode appears to be dominant during this fracturing stage but uncertainty associated with the low percentage of classifiable events effectively reduces the confidence of any conclusions which could possibly be derived from these figures.

!

#### **3.3. Drilling the fracture intercept production borehole**

Using AE source location data, an estimate of the fracture geometry was obtained and an optimal intercept borehole position was selected as shown in Figure 11. Here, the intercept borehole trajectory, drilled at 30º from the vertical axis, can be seen penetrating through the expected fracture surface. A high-angle drilling orientation was used to maximize the proba‐ bility of achieving a successful intercept after considering AE source location uncertainty and drilling system tolerances. Also, the uncased 10 mm diameter intercept borehole was drilled deeper than the expected intercept location to further increase the probability of successful hydraulic connection. In the figure, the best estimate of the fracture plane was plotted using a smoothed cubic interpolation surface function fitted to events with both high-amplitude and high-correlation. After drilling was completed, the borehole was swabbed and positive indication of fracturing oil was recovered, thus indicating that the intercept was successful.

minimum principal stress to avoid the potential for continued fracture propagation which could occur with fracture reopening. The results from these tests demonstrated that the achievable stable flow rates with the primary hydraulic fracture geometry were negligible and thus the reservoir remained non-producing. While this information confirmed that the stimulated fracture geometry was fully contained as desired, it also indicated that the connec‐ tion between the injection and production boreholes was too tight to pass any significant amount of fluid through. It is expected that a significantly higher post-fracture hydraulic conductivity would occur if proppant had been used during the primary fracturing stage. To enhance the hydraulic connection of the binary borehole system, two fracture reopening stages were performed with stepped constant pressure injection tests executed in between for diagnostic purposes. These injection tests continued to use oil as the injection fluid as its high viscosity was favorable for generating controlled fractures. Figures 12 and 13 show plots of the hydraulic data obtained from the first and second fracture reopening stages respectively. Both of these plots clearly show classic hydraulic fracture reopening behavior [15] with a nearly linear pressure rise followed by a rapid breakdown event and pseudo-steady fracture propa‐ gation at an elevated pressure. Comparing the similar magnitude peak pressures of 18.1, 15.4, and 17.4 kPa, observed for the primary fracture, first reopening, and second reopening events respectively, suggests that fracture toughness was not a dominant factor in fracture propaga‐ tion so scaling criterion suggested in the literature (e.g. [5]) are likely to be satisfied even with

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An orientated view of the AE source location data as observed for the first reopening stage is shown in Figure 14. Comparing this figure to the results shown in Figure 10 and the data from the second reopening stage, it is apparent that most of the fracture growth occurred during the first reopening stage along the bottom and two horizontal extremities of the initial fracture plane. Additionally, the close proximity of the AE events to the boundaries of the sample

intact granite as the testing material.

**Figure 12.** First fracture reopening event.

**Figure 11.** AE generated fracture surface of initial hydraulic fracture.

#### **3.4. Fracture reopening and circulation flow**

*Student Version of MATLAB* With the completion of the simulated EGS reservoir, flow experiments were performed to characterize the hydraulic properties of the reservoir. These experiments included constant pressure steady state injection, constant flow rate injection for fracture reopening, stepped constant pressure injection, and constant flow rate injection without reopening. The results obtained from these tests ultimately verified that a hydraulic circuit was present inside of the sample connecting the injection borehole to the production borehole through the stimulated hydraulic fracture.

Initially, constant low-pressure steady-state SAE 80W90 oil injection was performed using specified pressures of 2000, 3000 or 4000 kPa. The pressures were intentionally kept below the minimum principal stress to avoid the potential for continued fracture propagation which could occur with fracture reopening. The results from these tests demonstrated that the achievable stable flow rates with the primary hydraulic fracture geometry were negligible and thus the reservoir remained non-producing. While this information confirmed that the stimulated fracture geometry was fully contained as desired, it also indicated that the connec‐ tion between the injection and production boreholes was too tight to pass any significant amount of fluid through. It is expected that a significantly higher post-fracture hydraulic conductivity would occur if proppant had been used during the primary fracturing stage.

To enhance the hydraulic connection of the binary borehole system, two fracture reopening stages were performed with stepped constant pressure injection tests executed in between for diagnostic purposes. These injection tests continued to use oil as the injection fluid as its high viscosity was favorable for generating controlled fractures. Figures 12 and 13 show plots of the hydraulic data obtained from the first and second fracture reopening stages respectively. Both of these plots clearly show classic hydraulic fracture reopening behavior [15] with a nearly linear pressure rise followed by a rapid breakdown event and pseudo-steady fracture propa‐ gation at an elevated pressure. Comparing the similar magnitude peak pressures of 18.1, 15.4, and 17.4 kPa, observed for the primary fracture, first reopening, and second reopening events respectively, suggests that fracture toughness was not a dominant factor in fracture propaga‐ tion so scaling criterion suggested in the literature (e.g. [5]) are likely to be satisfied even with intact granite as the testing material.

**Figure 12.** First fracture reopening event.

**3.3. Drilling the fracture intercept production borehole**

!

970 Effective and Sustainable Hydraulic Fracturing

Y Location (mm)

**Figure 11.** AE generated fracture surface of initial hydraulic fracture.

**3.4. Fracture reopening and circulation flow**

hydraulic fracture.

Using AE source location data, an estimate of the fracture geometry was obtained and an optimal intercept borehole position was selected as shown in Figure 11. Here, the intercept borehole trajectory, drilled at 30º from the vertical axis, can be seen penetrating through the expected fracture surface. A high-angle drilling orientation was used to maximize the proba‐ bility of achieving a successful intercept after considering AE source location uncertainty and drilling system tolerances. Also, the uncased 10 mm diameter intercept borehole was drilled deeper than the expected intercept location to further increase the probability of successful hydraulic connection. In the figure, the best estimate of the fracture plane was plotted using a smoothed cubic interpolation surface function fitted to events with both high-amplitude and high-correlation. After drilling was completed, the borehole was swabbed and positive indication of fracturing oil was recovered, thus indicating that the intercept was successful.

> X Location (mm)

With the completion of the simulated EGS reservoir, flow experiments were performed to characterize the hydraulic properties of the reservoir. These experiments included constant pressure steady state injection, constant flow rate injection for fracture reopening, stepped constant pressure injection, and constant flow rate injection without reopening. The results obtained from these tests ultimately verified that a hydraulic circuit was present inside of the sample connecting the injection borehole to the production borehole through the stimulated

Initially, constant low-pressure steady-state SAE 80W90 oil injection was performed using specified pressures of 2000, 3000 or 4000 kPa. The pressures were intentionally kept below the

*Student Version of MATLAB*

An orientated view of the AE source location data as observed for the first reopening stage is shown in Figure 14. Comparing this figure to the results shown in Figure 10 and the data from the second reopening stage, it is apparent that most of the fracture growth occurred during the first reopening stage along the bottom and two horizontal extremities of the initial fracture plane. Additionally, the close proximity of the AE events to the boundaries of the sample suggested that the stimulated fracture may no longer have been fully contained and lower fluid recovery efficiency during production could result. The propagation of the fracture to the sample boundary, while not ideal, was reminiscent of the extension of a hydraulic fracture into a faulted zone or natural high-flow fracture network. Here the relative permeability between the sample boundary and the cell's platens was expected to be much higher than that through the hydraulic fracture within the sample, just as a faulted zone would likely have a higher permeability than an artificially stimulated fracture. This situation, while not ideal, may more closely resemble high fluid loss field EGS systems such as those encountered at Hijiori, Japan, where treatments were performed within a discontinuous and naturally fractured volcanic zone [16]. For the final fracture geometry within the granite sample, as estimated with the AE source location data, the smaller wing of the initial fracture appeared to have extended to approximately match the dominant wing length, thus creating a planar bi-wing fracture.

**Figure 13.** First fracture reopening event.

Comparing the AE count frequency data with the pressure data, as shown in Figure 15, significant increases in AE activity were found to occur just after portions of the hydraulic data where the second derivative of injection pressure with time was negative. Thus, from observ‐ ing the real-time rate of slope change in the pressure data, it may be possible to anticipate a major fracture growth event before it occurs. Also, using a technique such as this allows for an improved understanding of fracture growth behavior in heterogeneous systems during the time between fracture initiation and shut-in. During this time, the second-order analysis could be used to identify distinct breakdown events occurring after the initial breakdown as could be expected with multi-wing fracture systems or the opening of intersected fissures, joints, or fault zones. In this laboratory case, the analysis was performed using an 11-second backward linear regression approach to obtain an estimate of the first pressure derivative, as could be used in real-time applications. The 11 second value was selected using a qualitative trial-anderror approach with the goal of obtaining a visually smoothed data set without sacrificing too much of the data accuracy.

**Figure 15.** First time derivative of pressure with AE hit count histogram for the first fracture reopening stage.

**Figure 14.** Three dimensional view of AE event source locations during first fracture reopening stage.

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desired.

To evaluate the effectiveness of each fracture reopening stage, stepped constant pressure oil injection tests were performed. In these tests, SAE 80W90 oil was injected into the sample with PID controlled pressure at 1000 kPa increments with 30 minute duration. An example of the hydraulic data from a step pressure test performed after the second reopening event is provided in Figure 16. For each constant pressure increment, the resulting steady state pressure and flow rate measurements are averaged to estimate the pressure dependent flow character‐ istics of the stimulated reservoir. These values were useful reference points during later controlled constant flow tests where fracture reopening and extension pressures were not Scale Model Simulation of Hydraulic Fracturing for EGS Reservoir Creation Using a Heated True-Triaxial Apparatus http://dx.doi.org/10.5772/56113 973

**Figure 14.** Three dimensional view of AE event source locations during first fracture reopening stage.

suggested that the stimulated fracture may no longer have been fully contained and lower fluid recovery efficiency during production could result. The propagation of the fracture to the sample boundary, while not ideal, was reminiscent of the extension of a hydraulic fracture into a faulted zone or natural high-flow fracture network. Here the relative permeability between the sample boundary and the cell's platens was expected to be much higher than that through the hydraulic fracture within the sample, just as a faulted zone would likely have a higher permeability than an artificially stimulated fracture. This situation, while not ideal, may more closely resemble high fluid loss field EGS systems such as those encountered at Hijiori, Japan, where treatments were performed within a discontinuous and naturally fractured volcanic zone [16]. For the final fracture geometry within the granite sample, as estimated with the AE source location data, the smaller wing of the initial fracture appeared to have extended to approximately match the dominant wing length, thus creating a planar bi-wing fracture.

Comparing the AE count frequency data with the pressure data, as shown in Figure 15, significant increases in AE activity were found to occur just after portions of the hydraulic data where the second derivative of injection pressure with time was negative. Thus, from observ‐ ing the real-time rate of slope change in the pressure data, it may be possible to anticipate a major fracture growth event before it occurs. Also, using a technique such as this allows for an improved understanding of fracture growth behavior in heterogeneous systems during the time between fracture initiation and shut-in. During this time, the second-order analysis could be used to identify distinct breakdown events occurring after the initial breakdown as could be expected with multi-wing fracture systems or the opening of intersected fissures, joints, or fault zones. In this laboratory case, the analysis was performed using an 11-second backward linear regression approach to obtain an estimate of the first pressure derivative, as could be used in real-time applications. The 11 second value was selected using a qualitative trial-anderror approach with the goal of obtaining a visually smoothed data set without sacrificing too

**Figure 13.** First fracture reopening event.

972 Effective and Sustainable Hydraulic Fracturing

much of the data accuracy.

**Figure 15.** First time derivative of pressure with AE hit count histogram for the first fracture reopening stage.

To evaluate the effectiveness of each fracture reopening stage, stepped constant pressure oil injection tests were performed. In these tests, SAE 80W90 oil was injected into the sample with PID controlled pressure at 1000 kPa increments with 30 minute duration. An example of the hydraulic data from a step pressure test performed after the second reopening event is provided in Figure 16. For each constant pressure increment, the resulting steady state pressure and flow rate measurements are averaged to estimate the pressure dependent flow character‐ istics of the stimulated reservoir. These values were useful reference points during later controlled constant flow tests where fracture reopening and extension pressures were not desired.

A comparison of the stepped constant pressure test data obtained before and after the second reopening event is shown in Figure 17. On this plot, it was evident that there was negligible flow rate dependence with pressure after the first fracture reopening stage. This suggested that the flow of the injected fluid was not dominated by stimulated fracture flow and the hydraulic connection between the injection and production boreholes was not flowing effectively if at all. To improve the inter-well connectivity, the second fracture reopening stage was performed with high success. As can be seen in Figure 17, pressure dependent flow rate characteristics were much more prominent after this second stage with a clear proportional relationship. To augment these observations, borehole swabbing was performed periodically to check for fluid production in the intercept borehole. The swab's results did not positively indicate hydraulic connection until after the second fracture reopening stage. Thus, even though the first treatment did not attain an acceptable hydraulic connection, the execution of additional fracture stimulation treatments from the same injection well was successful in creating an effective hydraulic connection

fracture geometry was stable with water flow. Additional testing is required and planned in

**Figure 17.** Averaged oil injection stepped constant pressure data before and after the second fracture reopening

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A heated true-triaxial cell has successfully been able to produce a laboratory simulation of an EGS reservoir. Preliminary experiments using granite have provided valuable resulting data as well as new observations that may bring some additional insight into the potential of EGS

order to obtain a full characterization of the laboratory simulated EGS reservoir.

**Figure 18.** Second water flow test data plot.

**4. Conclusions**

stage.

**Figure 16.** Step pressure test data taken after the second fracture reopening stage.

With a confirmed hydraulic connection between the boreholes, the injection fluid was changed to tap water for thermal flow testing and EGS reservoir characterization. Water injection was performed with two constant flow rate controlled tests to attain pressure dependent flow characteristics for the reservoir. The first test utilized a flow rate of 0.05 mL/min and the second used a higher rate of 0.10 mL/min. While these tests provide similar data to constant pressure injection, it is more easily compared to field applications where flow rate control is the standard. Periodic borehole swabbing results indicated a significant and continuous fluid production in the intercept borehole. Figure 18 provides an example of the flow rate data obtained during the second water flow test. Here, it is evident that the reduction in viscosity by changing from oil to water resulted in significantly reduced pressure losses, as expected. Also, these flow rates did not produce any significant AE activity indicating that the stimulated Scale Model Simulation of Hydraulic Fracturing for EGS Reservoir Creation Using a Heated True-Triaxial Apparatus http://dx.doi.org/10.5772/56113 975

**Figure 17.** Averaged oil injection stepped constant pressure data before and after the second fracture reopening stage.

fracture geometry was stable with water flow. Additional testing is required and planned in order to obtain a full characterization of the laboratory simulated EGS reservoir.

**Figure 18.** Second water flow test data plot.

#### **4. Conclusions**

A comparison of the stepped constant pressure test data obtained before and after the second reopening event is shown in Figure 17. On this plot, it was evident that there was negligible flow rate dependence with pressure after the first fracture reopening stage. This suggested that the flow of the injected fluid was not dominated by stimulated fracture flow and the hydraulic connection between the injection and production boreholes was not flowing effectively if at all. To improve the inter-well connectivity, the second fracture reopening stage was performed with high success. As can be seen in Figure 17, pressure dependent flow rate characteristics were much more prominent after this second stage with a clear proportional relationship. To augment these observations, borehole swabbing was performed periodically to check for fluid production in the intercept borehole. The swab's results did not positively indicate hydraulic connection until after the second fracture reopening stage. Thus, even though the first treatment did not attain an acceptable hydraulic connection, the execution of additional fracture stimulation treatments from the same injection well was successful in

creating an effective hydraulic connection

974 Effective and Sustainable Hydraulic Fracturing

**Figure 16.** Step pressure test data taken after the second fracture reopening stage.

With a confirmed hydraulic connection between the boreholes, the injection fluid was changed to tap water for thermal flow testing and EGS reservoir characterization. Water injection was performed with two constant flow rate controlled tests to attain pressure dependent flow characteristics for the reservoir. The first test utilized a flow rate of 0.05 mL/min and the second used a higher rate of 0.10 mL/min. While these tests provide similar data to constant pressure injection, it is more easily compared to field applications where flow rate control is the standard. Periodic borehole swabbing results indicated a significant and continuous fluid production in the intercept borehole. Figure 18 provides an example of the flow rate data obtained during the second water flow test. Here, it is evident that the reduction in viscosity by changing from oil to water resulted in significantly reduced pressure losses, as expected. Also, these flow rates did not produce any significant AE activity indicating that the stimulated

A heated true-triaxial cell has successfully been able to produce a laboratory simulation of an EGS reservoir. Preliminary experiments using granite have provided valuable resulting data as well as new observations that may bring some additional insight into the potential of EGS technology. Some of the most important advancements and observations that have been made include:

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[4] Behrmann, L. A, & Elbel, J. L. Effect of Perforations on Fracture Initiation. Journal of

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[6] Ishida, T, Chen, Q, Mizuta, Y, & Roegiers, J. Influence of Fluid Viscosity on the Hy‐ draulic Fracturing Mechanism. Transactions of the ASME; (2004). , 190-200.

[7] Wieland, C. W, Miskimins, J. L, Black, A. D, & Green, S. J. Results of a Laboratory Propellant Fracturing Test in a Colton Sandstone Block. Proceedings SPE Annual Technical Conference and Exhibition, September (2006). San Antonio, Texas, USA.,

[8] Macartney, H, & Morgan, P. The Potential for Geothermal Energy Recovery from En‐ hanced Geothermal Systems in the Raton Basin of Southern Colorado, USA. Proceed‐

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