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Advanced Hydraulic Fracturing Technology For Unconventional Tight Gas Reservoirs Students: Pieve La Rosa, A.; Correa, J.; Kubacak, T.; Ouyang, L. and Awoleke, O. Principal Investigators: Ding Zhu and A. D. Hill

Advanced Hydraulic Fracturing Technology For Unconventional Tight Gas Reservoirs Students: Pieve La Rosa, A.; Correa, J.; Kubacak, T.; Ouyang, L. and Awoleke,

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Advanced Hydraulic Fracturing Technology For Unconventional Tight

Gas Reservoirs

Students: Pieve La Rosa, A.; Correa, J.; Kubacak, T.; Ouyang, L. and Awoleke, O.

Principal Investigators: Ding Zhu and A. D. Hill

RPSEA Unconventional Gas Conference – April 6th, 2010 2

Outline

Project Overview

Experimental Determination of Hydraulic Fracture Conductivity

Static Yield Stress Study and Gel Displacement Modeling

Tight Gas Sand (TGS) Advisory System

RPSEA Unconventional Gas Conference – April 6th, 2010 3

Dynamic Fracture Conductivity Tests(Task 4)

RPSEA Unconventional Gas Conference – April 6th, 2010 4

Introduction

Polymer damage in the fracture reduces fracture conductivity and effective fracture length

Static conductivity tests in general overestimate fracture conductivity

Dynamic conductivity test is designed to simulate filter cake buildup and gel behavior in a condition closer to field conditions

RPSEA Unconventional Gas Conference – April 6th, 2010 5

Conductivity Experiments – Schematics

Leak off Fluid

Data Acquisition and

Processing

Pressure Gauge

Metering Pump

Crosslinker

Hydraulic Load Frame

Hydraulic Load Frame

Core A

Side Piston

Core B

Side Piston

Centrifugal Pump Centrifugal Pump

Base Gel

Valve Valve

Tap water

Pressure Transmitters

Heating Tape

FracturingFluid

High-pressure Vessel

Diaphragm PumpMixer

Heating Jacket

Proppant

Valve

P-97

P-98P-99

Force

Back Pressure Regulator

Check Valve

Force

Data Acquisition and

Processing

Hydraulic Load Frame

Hydraulic Load Frame

Core Sample

Side Piston

Pressure Transmitters

Heating Jacket

Back Pressure Regulator VentMass Flow

Controller

N2

WaterChamber

Setup for Slurry Pumping Setup for Fracture Conductivity Measurements

RPSEA Unconventional Gas Conference – April 6th, 2010 6

Conductivity Experiments – Core Properties and Dimensions

• Length: 7.25 in• Width: 1.65 in• Height: 3 in• Permeability: 0.05-0.1 md

RPSEA Unconventional Gas Conference – April 6th, 2010 7

Conductivity Experiments – Conductivity Computation

y b mx

hw

q

wkqZRTL

Mhpp

f

2

22

21 1

2

2

kdL

dp

RPSEA Unconventional Gas Conference – April 6th, 2010 8

Conductivity Experiments – Summary of Previous Results

0.0

10.0

20.0

30.0

40.0

50.0

60.0

70.0

20 30 40 50 60 70

Gel Concentration (lb/Mgal)

Cle

anup E

ffic

iency

(%

)

1 Gas Rate 1 SLM

Gas Rate 0.75 SLM

Gas Rate 0.5 SLM

Gas Rate 0.2 SLM

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10.0

20.0

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60.0

70.0

0.00 10.00 20.00 30.00 40.00 50.00

Gas Flux (ft/min)

Cle

anup E

ffic

iency

(%

)

1

Gel Conc 30 lb/Mgal

Gel Conc 40 lb/Mgal

Gel Conc 50 lb/Mgal

0.0

10.0

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30.0

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Gas Flux (ft/min)

Cle

anup E

ffic

iency

(%

)

1 Gel Conc 30 lb/Mgal

Gel Conc 40 lb/MgalGel Conc 50 lb/MgalGel Conc 30 lb/Mgal No BreakerGel Conc 50 lb/Mgal No Breaker

0.0

10.0

20.0

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0.00 10.00 20.00 30.00 40.00 50.00

Gas Flux (ft/min)

Cle

anup E

ffic

iency

(%

)

1

Gel Conc 30 lb/Mgal

Static Test @ 30 lb/Mgal

Polymer concentration has a small but clear impact on clean up efficiency

Gas flux has a large effect on clean up efficiency

Presence/absence of breaker has a clear impact on clean up efficiency

Static tests will produce higher clean-up efficiencies compared to dynamic tests

RPSEA Unconventional Gas Conference – April 6th, 2010 9

Conductivity Experiments – Current Work

Addition of new equipment to previous setup• Diaphragm pump to handle solid pumping• Load frame

Accurate load control Accurate vertical displacement measurement Automatic data acquisition

RPSEA Unconventional Gas Conference – April 6th, 2010 10

Conductivity Experiments – Apparatus

RPSEA Unconventional Gas Conference – April 6th, 2010 11

Conductivity Experiments – Range of Test Variables

1. Nitrogen rate: 0.5-3 standard liter minute2. Temperature: 150-250 F⁰3. Polymer loading: 10-30 lb/Mgal4. Breaker: Presence or absence of breaker5. Closure stress: 2000-6000 psi6. Proppant concentration: 0.5-2 ppg7. Fracture fluid pumping rate: 0.7-1.5 gpm

Develop an experimental schedule based on Design of Experiments to identify the most important factors

RPSEA Unconventional Gas Conference – April 6th, 2010

Conductivity Experiments – Design of Experiments

Screening experiments in order to determine which variables

are the most important.

Two-factor / multiple factor experiments to refine

information and develop a conductivity model.

Optimization, to determine which levels of the critical variables result in the best

system performance.

Experimental Design allows us to have a more efficiently designed schedule of experiments and determine interaction between multiple and complex system variables.

RPSEA Unconventional Gas Conference – April 6th, 2010 13

Experimental Schedule based on Design of Experiments

No. N2 rate (sl/min) X1 T (

F) X2 Polymer loading (lb/1000gal) X3

Breaker X4

Closure Stress (psi) X5

Proppant conc. (ppa) X6

Fluid rate (gpm) X7

1 1.75 200 20 half loading 4000 1.25 1.12 0.5 150 30 normal loading 2000 0.5 1.53 3 150 30 no breaker 2000 2 0.7

4 0.5 250 10 normal loading 2000 2 0.75 0.5 250 30 no breaker 6000 0.5 0.76 1.75 200 20 half loading 4000 1.25 1.17 3 250 30 normal loading 6000 2 1.58 3 250 10 no breaker 2000 0.5 1.59 0.5 150 10 no breaker 6000 2 1.5

10 3 150 10 normal loading 6000 0.5 0.711 1.75 200 20 half loading 4000 1.25 1.112 3 250 10 no breaker 6000 2 0.713 3 150 30 no breaker 6000 0.5 1.514 0.5 150 10 no breaker 2000 0.5 0.715 0.5 250 10 normal loading 6000 0.5 1.516 0.5 250 30 no breaker 2000 2 1.5

17 3 250 30 normal loading 2000 0.5 0.7

18 0.5 150 30 normal loading 6000 2 0.7

19 3 150 10 normal loading 2000 2 1.5

20 1.75 200 20 half loading 4000 1.25 1.1

RPSEA Unconventional Gas Conference – April 6th, 2010 14

Recent Results

300

350

400

450

500

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600

650

700

0 5 10 15 20 25 30

Time (hours)

Kf-

w (

md

-ft)

Polymer concentration: 10 lb/Mgal Clean-Up Gas Rate: 0.5 slm Cleanup Efficiency: 57.2%

RPSEA Unconventional Gas Conference – April 6th, 2010 15

Dynamic Fracture Conductivity Experiments-Future Work

Continue running experiments based on the experimental schedule

Identify the most critical factors affecting dynamic fracture conductivity

Determine the effect of these critical factors on dynamic fracture conductivity

Develop correlations for predicting dynamic fracture conductivity based on critical variables

RPSEA Unconventional Gas Conference – April 6th, 2010 16

Gel Damage Investigation(Task 5)

RPSEA Unconventional Gas Conference – April 6th, 2010 17

Gel Damage Investigation - Objectives

Yield stress measurement Investigating the relationship between yield

stress, polymer concentration and breaker concentration

Modeling of gel movement in proppant pack

RPSEA Unconventional Gas Conference – April 6th, 2010 18

Static Yield Stress Measurement

DigitalScale

Water Outlet

Water

Fracturing Gel

A range of polymer concentration was tested

Force change is (static yield stress) measured while water is drained

Building relationship between the gel concentration and yield stress

RPSEA Unconventional Gas Conference – April 6th, 2010 19

20 40 60 80 100 120 140 160 180 200 2200

10

20

30

40

50

60

70

Gel Concentration (lb/Mgal)

Yie

ld S

tres

s (P

a)

Static Yield Stress of Polymer Gel

RPSEA Unconventional Gas Conference – April 6th, 2010 20

0 2 4 6 8 10 12 14 160

10

20

30

40

50

60

70

80 lb/Mgal guar

100 lb/Mgal guar

150 lb/Mgal guar

200 lb/Mgal guar

Breaker Concentration (gal/Mgal)

Yie

ld S

tres

s (P

a)

Yield Stress of Polymer Gel with Breaker Concentration

RPSEA Unconventional Gas Conference – April 6th, 2010 21

0 2 4 6 8 10 12 14 160

10

20

30

40

50

60

70

80

80 lb/Mgal guar

100 lb/Mgal guar

150 lb/Mgal guar

200 lb/Mgal guar

Breaker Concentration (gal/Mgal)

FIG

(psi

/ft) Porosity = 0.2

Proppant Pack Permeability = 80 Darcies

Flow Initiation Gradient (FIG) with Breaker Concentration

RPSEA Unconventional Gas Conference – April 6th, 2010

Gas Velocity

Formation

Filter CakeDelta P

Gel Movement Modeling

Flow in cylindrical tubeSolve equations of

motion and momentum with appropriate boundary conditions

Velocity profile must be continuous

Stress profile must be continuous

No slip boundary condition at the walls of the tube

RPSEA Unconventional Gas Conference – April 6th, 2010

Stress Distribution in Tube

For a given pressure gradient, the linear shear stress profile is given by

This equation is independent of the fluid properties and state of fluid motion (i.e., laminar or turbulent)

RPSEA Unconventional Gas Conference – April 6th, 2010

Laminar Flow

Newtonian Flow (Gas)

Yield Pseudo-Plastic Fluid (Gel)

shear rate combined with

RPSEA Unconventional Gas Conference – April 6th, 2010

Case 1 Case 2 Case 3

Flow Patterns Identified Under Imposed Pressure Gradients

RPSEA Unconventional Gas Conference – April 6th, 2010 26

Future Work- Gel Damage

Identify the critical gas flow rate for gel clean up for tube geometry

Derive equations for 2-phase stratified flow in the turbulent flow regime

Extend the results to flow in porous proppant pack

RPSEA Unconventional Gas Conference – April 6th, 2010 27

Tight Gas Sand Advisory System(Task 6)

RPSEA Unconventional Gas Conference – April 6th, 2010 28

Tight Gas Sand Advisory System – Previous Work

Literature review of hydraulic fracturing practices in tight gas reservoirs

Development and testing of Tight Gas Sand Advisory System

Source: SPE 126708

RPSEA Unconventional Gas Conference – April 6th, 2010 29

TGS – Current and Future Work

Communication with Newfield Exploration Company for data to support current studies

A rigorous field study of the Tight Gas Sand Advisory System

Application of the TGS Advisory System in fracture treatment design

RPSEA Unconventional Gas Conference – April 6th, 2010 30

Tentative Field Study Plan

Receive stimulation and production data for the Cromwell formation in the Arkoma Basin from Newfield Exploration Company

Compare the stimulation treatment designs and well performances to the suggestions made by the Advisory System

Review micro-seismic and pressure data from fracture treatments

Optimize the stimulation design for the Cromwell formation using the results of the field study

RPSEA Unconventional Gas Conference – April 6th, 2010 31

TGS – Advanced Treatment Design

Combine information from….

• TGS Advisory System• Dynamic Fracture Conductivity Experiments• Gel Damage Studies

….To develop an optimized fracturing design methodology.

RPSEA Unconventional Gas Conference – April 6th, 2010 32

Thank youPrincipal Investigators: Dr. D. Zhu and Dr. A. D. Hill

Harold Vance Department of Petroleum Engineering Texas A&M University 3116 TAMU, Richardson Building College Station, TX 77843-3116

Advanced Hydraulic Fracturing Technology For Unconventional Tight

Gas Reservoirs