Title: Fracturing Fluid Characterization Facility

Author: The University of Oklahoma

Sponsor: Gas Research Institute (GRI) and US Department of Energy (DOE)

Report Period: January -- December 1993 Annual Report


Objective: To report and discuss the progress made during the FFCF project's 1993 calendar year.

Technical Perspective: Hydraulic fracture treatment design requires a myriad of system parameters. Many of these parameters are inherent properties of the reservoir to be hydraulically fractured. The fracturing fluid's flow and particle transport characteristics are important to this design process. The observations made on this research facility will closely relate to the flow behavior expected in an actual hydraulic fracture. These same observations can also be related to the more routine, practical fluid characterization techniques used by the industry.

Results: A high-pressure, high temperature (i.e., 1200 psig, 250 degrees F, parallel plate flow cell has been designed and constructed. An instrumentation and data acquisition system has been assembled that records temperature, pressure and velocity profiles of the fluid in flow cell. A fiber optic based vision system had been incorporated. This novel system provides a low-resolution optical image of the flow field that can be digitally recorded, analyzed, and maps generated to depict proppant concentration as a function of space and time.

Experimental work was completed on impermeable facings that serve as a replaceable lining for the walls of the flow cell. These facing are currently being fabricated using sand and as epoxy resin as a bonding agent. The resin system is also used with an aggregate of silica particles to fabricate permeable facings. These permeable facings will be used in the study of fluid leaking off normal to the main direction of flow.

Experimental and numerical studies of fluid flow are reported. These studies aided in determining the minimum size requirements for fluid characterization experiments. In addition, the flow experiments coupled with analytical studies permitted the determination of the physical size of a much larger low-pressure flow apparatus necessary to adequately characterize the proppant transport properties of complex fracturing fluids.

Technical Approach: The reaction frame, or mechanical body, of the flow cell was designed and constructed by MTS, one of the project's subcontractors. The functional requirements for this design were provided by the entire project group with input from the industry advisors.

The Electrical Engineering group at OU conceived and constructed the instrumentation and data acquisition system. The high-pressure simulator (HPS) was designed to operate at a maximum pressure of 1200 psig (i.e., 12 MM lb.-force load). This required a steel superstructure that inhibits any of the desired observations. Novel techniques of burying equi-spaced optical fibers in the facings to obtain a low resolution optical image of the flow field, imbedded optical glass windows that facilitate the use of the Laser Doppler Velocimetry (LDV), and 3-D graphical representation of measured parameters such as pressure, velocity, and temperature make it possible to observe and analyze what would be impossible with conventional instrumentation.

Laboratory experiments and material property measurements all played a big part in selecting the epoxy resin as a facing material. Cement was initially thought to be the material of choice. Although it did exhibit some desirable physical properties, its mechanical integrity became uncontrollable as facings were actually fabricated.

Experimental and numerical research into turbulent flow and fluid leak-off have provided important information for understanding the application of the prototype. Limitations based on geometry are identified with these same techniques so future equipment and experiments for the FFCF can be designed and planned with clear objectives.

Project Implications: The research and development that has gone into the FFCF prototype will not only serve as the foundation for the future of this project but also provides the industry with valuable insight into some of the more fundamental aspects of fluid flow in a hydraulic fracture. These reports form the basis for advancing the state of the art in rheology research for hydraulic fracturing.

Report Contents:

GRI Report: GRI 94/0065

1.Introduction

1

Goals of the FFCF Project

1

Brief Description of the FFCF

2

The Flow Cell

2

Auxiliary Equipment

4

Instrumentation

4

Research and Development Plan for FFCF Prototype

6

2. Low Pressure, Large Scale FFCF Functional Requirements and Design Concepts

8

MTS Research Activity Summary

8

Objectives of the Low Pressure Fracture Simulator (LPS)

8

Functional Requirements

9

Proposed LPS Structural Specification

17

Discussion of Specification

18

3. Instrumentation and Data Acquisition for Fracturing Fluid Flow Measurement

24

Introduction

24

Data Acquisition and Visualization

24

Vision System

26

Laser Doppler Velociemetry Measurements

28

Particle Tracking

35

4. Operational Procedures for the FFCF High Pressure Simulator

37

Introduction

37

Fabrication and Installation of Facings

37

Facings Fabrication

37

Facing Installation

38

Operation of the MTS Hardware

39

Opening and Closing Procedures for the HPS

39

Operation of the MTS Control System

40

Operation of the Data Acquisition System

40

Honeywell Differential Pressure Transmitters

40

LDV System

42

Temperature System

42

Vision System

42

Other Data Acquisition Computers

42

5. Tests Results from the High Pressure Simulator

43

Introduction

43

Data Analysis

48

Verification Tests

51

Research Tests

62

Conclusions

74

6. Proppant Transport Modeling

77

Basics of Multiphase Mixture Theory

77

Continuum Theory, Corpuscular Theory, and Averaging Theory

77

Notation

78

Mathematical Structure

79

Balance Principles for Constituents

80

Balance Principles for the Mixture

80

Constitutive Equations

81

Restrictions on Constitutive Equations

82

Determinism of the System Equations

82

Boundary Value Problems

83

Conclusion

83

Relation of Microstructure to Constitutive Equations

83

Introduction

83

General Equations for Two-Phase Flow

85

Some Assumptions in Modeling Proppant Flows

89

Hyperbolicity Analysis of the Equations

96

An Application to Wedge Shape Fracture

98

Numerical Stability Consideration

99

Dilute Proppant Transfer

102

Introduction

102

Motion Equations

103

Constitutive Equations

106

Channel Flow

110

Approximate Analytical Solutions

111

Numerical Solutions

114

Dense Proppant Transfer

118

Kinematics and Equations of Balance

118

Constitutive Equations

121

Field Equations

123

Proppant Segregation in Poiseuille Flow

127

Numerical Results

128

Conclusion

131

7. Other Accomplishments Achieved During 1993

133

8. Proposed Work Plan for 1994 and Beyond

134

Introduction

134

Design, Fabrication, and Installation of a Low Pressure Simulator (LPS)

134

Design, Fabrication and Installation of the Computational Hardware, Instrumentation, and Data Acquisition Hardware and Software for the Low Pressure Simulator

137

Rheological and Proppant Transport Research Using the HPS

138

Convective Settling and Encapsulation Studies

139

Dynamic Fluid Loss Studies and Correlation with Laboratory Scale Experiments

139

Characterization of Crosslinked Fluid and Crosslinked Slurry Rheology

139

Investigation of Flow through Perforations

140

Preparation of a Verification Test Plan for the LPS

140

Development of a Strategy/Plan for Soliciting Future Support for the FFCF Project

140

FFCF Building Construction

141

Development of a Systematic Plan for Relocating the HPS to the New FFCF Building

141

Verification and Testing LPS

141

Summary

142