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1 Hearing How Preformed Particle Gels Can Control Water Production in Mature Oilfields Missouri University of Science and Technology (Formerly University of MissouriRolla) August 26, 2015 Presentation at the Mature Fields North America 2015 Summit

Day 2: Baojun Bai, Professor, University of Missouri-Rolla · Hearing How Preformed Particle Gels Can Control Water Production in Mature Oilfields ... • Gel treatments are often

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1

Hearing How Preformed Particle Gels Can Control Water Production

in Mature Oilfields

Missouri University of Science and Technology

(Formerly University of Missouri—Rolla)

August 26, 2015

Presentation at the Mature Fields

North America 2015 Summit

Outline

• What is Preformed Particle Gel (PPG)

• Importance of Gel Treatment for Water Production Control

• A Few Questions Often Being Asked for PPG Treatment

• Case Studies of Field Applications

• Lessons Learned from More Than 5,000 PPG Treatments

• Summary

• Acknowledgement

2

(a) Before swelling (b) After swelling

• Cross-linked polyacrylamide powder, Super Absorbent Polymer

• Size ranging from nano-meter to millimeter

What is Preformed Particle Gel (PPG)

3

Importance of Gel Treatment for Water

Production Control in Mature Oilfields

• Excess water production is the most serious problem to

reduce oil production as oilfields are maturing.

• The total cost to separate, treat, and dispose of water is

approximately $50 billion per year.

• Gel treatments are often one best choice to mitigate

channeling through fractures and super-K streaks.

• Gel treatment is one of cost-effective methods to improve

sweep efficiency.

4

Gel Treatments to Block/Reduce Water Flow through High Permeability Zone/Streak

• Near Wellbore Problems

– High-permeability matrix-rock strata without crossflow

• Far-wellbore Reservoir Problems

5

(c) Fracture

channeling

(a) Vertical heterogeneity

with crossflow (b) High permeability

streaks

(d) Solution

channels

Gels Used for Conformance Control

• In-situ gel systems: Gelant is

injected into formation and gel is

formed under reservoir conditions

after placement. Gelation occurs in

the reservoir.

6

• Preformed gel systems: Gel is formed in surface facilities

before injection, and then gel is injected into reservoirs. No

gelation occurs in reservoir.

Current Preformed Particle Gel Systems

Name Developer Particle Size Applications

Bright

Water®

Chevron, BP and

Nalco (Tirco)

Sub-Micro

(< 1 µm)

60+

injectors

Microgel IFP Micro

(1-10 µm)

10+

producers

PPG PetroChina

MS&T

Halliburton

Millimeter

(10 µm to

millimeters)

5,000+

Injectors in

China

pH Sensitive

polymer

UT Micro Not reported

7

A Few Questions Often Being Asked for PPG Treatment

Q1. Why using particle gels for conformance control?

Q2. Why developing millimeter-sized particles at very

beginning?

Q3, Can mm-sized particles propagating through md-level

formation?

Q4. Can particle gels fully block open fractures, voids, and

conduits?

8

Q1. Why Particle Gels For Conformance Control

9

• Inherent disadvantages of In-Situ Gel

Crosslinking reactions and gel quality are strongly affected by

– Shear of pump, wellbore and porous media

– Adsorption and chromatography of chemical

compositions

– Dilution of formation water

• Particle gel is deformable and easier to transport

through porous media than Hard particle.

• Single component and easy operation in oilfields

Q2: Why using mm-sized (>10µm) particle gels?

• Fractures or high-permeability streaks/channels exist extensively in mature water-flooded reservoirs.

• Millimeter-sized PPGs can preferentially enter into fractures or fracture-like channels/conduits while minimizing gel penetration into low-permeability zones/matrixes.

10

KL

Kh

Water Flooding

KL

Kh

• More polymer

enters low-K

zones comparing

to W.F.

• More polymer

needs to be used

Polymer Flooding

In-situ gel treatment

Nano-particles

Mm-size particles

gel treatment

Q3: Can mm-sized propagate mD porous media?

• Millimeter sized particles cannot penetrate into the porous media with a permeability less than 1000 md.

• If particle size and strength are appropriate, no non-permeable cakes can be formed on the surface of rocks.

Core surface after PPG injection

(a)No damage

(b)Cake but can be flushed out.

Large particles cannot

damage conventional

permeable rocks

11

• If the particles are weak, mm-sized PPGs would form

a cake rather than penetrating into the cores.

(1) Crossflow reduce the negative effect

(2) Acid soak near wellbore to remove cake (SPE172352)

Q3. Can mm-sized propagate mD porous media?

12

A Reservoir with Fracture(s) or Super-K Channels

13

A Reservoir without fractures or Super-K Channels

14

Trial and Error Technique

Q4: Can particle gels fully block

open fractures, voids, and conduits?

• Particle moved piston-like in open fractures and formed

permeable Gelpack.

• The permeability of Gelpack can be a few hundreds to a

few thousands of md, depending on gel strength, particle

size and flow rates.

15

Particles moved piston-like and formed GelPack

Gel movement during PPG injection

(t = 0.2 PV)

(t = 1.5 PV)

(t = 3.2 PV)

(t = 2.5 PV)

Gel Particles is a fracturing-filling material. Particles will form a

particle pack in open fracture/fracture-like features. 16

Brine Created Channels and Flowed in GelPack

(t = 0 PV)

(t = 2.5 PV)

Brine movement during brine injection into Permeable GelPack

in the fracture

(t = 0.8 PV)

(t = 1.5 PV)

PPG cannot fully block open fractures but forms permeable GelPack of

which permeability can be controlled by particle strength and sizes

17

Field Applications

More than 5,000 applications in China and other

countries.

PPG treatment has been successfully applied in:

• Water flooding mature reservoirs without natural

fractures or intentionally hydraulic fractures

• Fracture reservoirs

• High temperature (up to 130°C) high salinity (30%)

reservoirs

• CO2 Flooding Reservoirs

• Polymer Flooding wells

• ASP Flooding wells

PPG weight: 6,600 ~88,000 lbs/well, commonly 17,600-

33,000 lbs per well18

Case 1: First Pilot in Daqing, PetroChina

• Well No and Location: X7-2-F24

• Formation brine salinity: 4,500 mg/L

• Temperature: 40 ºC

• Reservoir type: Sandstone without

natural fractures or intended

hydraulic fractures

• Permeability: Recorded maximum

permeability is 1, 200 md.

19

Case 1: First Pilot in Daqing, PetroChina

• Reservoir Heterogeneity

– Vertical Heterogeneity (Injection profile): only 1/5 perforated zone absorbed water

20

Case 1: First Pilot in Daqing, PetroChina

• Treatment Design

– PPG amounts: 34,100 lbs

– PPG suspension: 3,000 m3 PPG suspension using produced water

– PPG Properties:

• Size: 1.5 mm, 3 mm, and 5 mm

• Swelling ratio: 60~80 times

• Stability: no dehydration within 2 years

– Injection method: PPG Suspension alternated with produced water

21

Case 1: First Pilot in Daqing, PetroChina

Electric source

Pump Mixers

Produced

Jet Pump Water

X7-2-24 Mixing Tank

Injection scheme (facilities)

22

Injection performance– multiple stages

Conc

(%)

Size

( mm)

Vol

(m3)

1st 1.0 5 100

2nd 0.5 1.5 600

3rd 0.5 3 1700

4th 0.5 5 6000

2

4

6

8

10

12

14

0 500 1000 1500 2000 2500 3000 3500

Inje

ctio

n P

res

su

re(

MP

a)

PG suspension Volume(m3)

2nd. 3rd 4th

1st

Case 1: First Pilot in Daqing, PetroChina

23Water alternated PPG injection

Case 1: Results from First Pilot in Daqing

• Water injection pressure: increased from 5.0 to 8.2 MPa.

• Oil production: 17,500 bbl of increased Oil within 7 months.

• Injection profile: Water absorption zone thickness from 11.5 m

to 21.5 m.

Before Treatment After Treatment

24

Case 2: PPG Application in High Salinity High

Temperature Water Flooding Reservoirs

Reservoir Conditions:

Sandstone without natural fractures or intended

hydraulic fractures

Formation temperature: 125 ℃ (257℉)

Formation salinity: 23×104 ppm

Permeability: 0.23 D

Tracer test: 60 d breakthrough

Reason for treatment: High-permeability channels exist

25

Case 2: PPG Application in HSHT Reservoirs

Treatment:

• Treated wells: 4 injection wells

• PPG amounts: 375,782 lbs (93,946 lbs/well)

• PPG suspension: 69,260 m3 (17,315 m3/well)

PPG properties:

• Size: 28 μm~1 mm

• Swelling ratio: 15~25 times

• Stability: no dehydration within one year

• High temperature (284 ℉) and salinity resistance (23%)

Slide 26

26

Case 2: PPG Application in HSHT Reservoirs

Slide 27

Injection Pressure Monitoring Results

PPG injection Curve for Well 4

0

435870

1305

17402175

261030453480

Inje

cti

on

Pre

ss

ure

(p

si)

2nd slug

microgel≤28μm24.345t

0

314.5

629

943.5

1258

1572.5

1887

Inje

cti

on

Ra

te

(b

bl/

d)

0

1000

2000

3000

2012.12.2 12/17 2013.1.1 1/16 1/31 2/15 3/2 3/17 4/1 4/16 5/1 5/16

Co

nc

en

tra

tio

n

(p

pm)

4th slug

PPG0.1-0.25mm13.912t

3rd slug

PPG≤0.1mm10.432t

5th slug

PPG0.25-0.5mm12.519t

1st slug

microgel≤28μm2.782t

6th slug

PPG+Gel0.25-0.5mm8.346t

27

Case 2: PPG Application in HSHT Reservoirs

Slide 28

Drawdown Test for Injection Well 4

Pressure drawdown test for Well 4

0

500

1000

1500

2000

2500

3000

3500

0 15 30 45 60 75 90

Pre

ss

ure

(p

si)

Time (90 min)

2nd slug

3rd slug

4th slug

5th slug

after treatment

before treatment

28

Case 2: PPG Application in HSHT Reservoirs

Slide 29

Increased Oil 204,188 bbl

Oil incr. per

PPG 170.5 t/t

Decline Curve for 9 Production Wells

Before Treatment After Treatment

0

20

40

60

80

100

120

140

160

180

0 12 24 36

Pro

du

cti

on

Ra

te (

t/d

)

Time(month)

27,971 t

29

Case 3: PPG Application in Polymer Flooding

Reservoir Conditions:

Sandstone with natural fracture

Temperature: 33oC (91.4℉)

Salinity: 5600~5700 ppm

Permeability: 0.16 D

Reason for treatment:

Polymer early breakthrough

Slide 30

30

PPG Application in Polymer Flooding

Slide 31

0

100

200

300

400

500

600

700

800

20101026 20110114 20110517 20110720 20111010 20111222 20120409 20120629 20120918 20130109

Po

lym

er

Co

ncen

trati

on

(p

pm)

Time(d)

After treatmentBefore treatment

Polymer concentration for 18 production wells

Treatment

31

Lessons Learned

from Field Application Results

• Fracture or fracture-like channels widely exists in

mature oilfields but it has not been recognized by

those engineers without field experience.

• No injectivity problem was found for most treatments

even though these reservoirs have no natural fractures

or intentionally hydraulic fractures.

• “Trial and Error” technique can be used for better gel

treatment results

• Negative effect was rarely found.

• PPG treatment is a simple and cost-effective method to

control water production.32

Summary

• PPGs have been successfully synthesized in commercial scale

and applied in mature oilfields to control water production

• PPG strength and size are controllable. It can overcome some

distinct drawbacks inherent to in-situ gelation systems.

• Swollen PPG forms a gel-pack after placement in a fracture,

and the gel-pack permeability can be controlled by particle size

and strength.

• Millimeter-sized (10 µm-mm) PPGs have been successfully

applied in more than 5000 wells without injectivity problems

• Trial and Error method can be used for mm-sized PPG

treatments.

• PPG treatment is a simple and cost-effective method to control

conformance for water and polymer flooding. 33

Acknowledgements

34

Selected Journal Publications for Particle Gels

1. Imqam, A.**; Elue,H.; Bai,B*., Hydrochloric Acid Applications to Improve Preformed Particle Gel Conformance Control Treatment, SPE Production. (in revision)

2. Imqam, A.; Bai,B., (2015), Optimize the Strength and Size of Preformed Particle Gels for Better Conformance Control Treatment, Fuel 148, 178-185, 2015.

3. Goudarzi, A.; Zhang, H.**; Varavei, A.; Taksaudom, P.; Hu Y.**; Delshad, M.; Bai, B.; Sepehrnoori, K.; “A Laboratory and Simulation Study of Preformed Particle Gels for Water Conformance Control,” Fuel, 140, 502-513.

4. Imqam, A.**; Bai, B*.; Preformed Particle Gel Extrusion through Open Conduits during Conformance Control Treatments, SPE Journal, 2014

5. Muhammed, F.A.**; Bai, B.*; Tang, T.**, (2012) Experimental Study of the Interaction between Surfactants and Super Absorbent Polymer Gel, Journal of Petroleum Sciences and Engineering 90: 159-164.

6. Elsharafi, M**, Bai, B*. (2012) Effect of Weak Preformed Particle Gel on Unswept Oil Zones/Areas during Conformance Control Treatments, Ind. Eng. Chem. Res.51 (35), 11547–11554.

7. Zhang, H.**; Bai, B*. (2011) “Preformed Particle Gel Transport through Open Fractures and its Effect on Water Flow,” SPE Journal 16(2), 388-400.

8. Wu, Y.**, Tang, T**., Bai, B.* (2011) “An experimental study of interaction between surfactant and particle hydrogels”, Polymer 52, 452-460.

9. **Zhang, H., Challa, R., and Bai, B*. (2010), “Using Screening Test Results to Predict the Effective Viscosity of Swollen Superabsorbent Polymer Particles Extrusion through an Open Fracture” Industrial & Engineering Chemistry 49, 12284-12293.

10. Bai, B.*, Li, L., Liu, Y., Li, Y., (2007) “Conformance Control by Preformed Particle Gel: Factors Affecting its Properties and Applications,” SPE Reservoir Evaluation and Engineering 10 (4), 415-421. DOI: 10.2118/89389-PA

11. Bai, B.*, Liu, Y., Coste, J-P., (2007) “Preformed Particle Gel for Conformance Control: Transport Mechanism through Porous Media,” SPE Reservoir Evaluation and Engineering, 10 (2), 176-184. DOI: 10.2118/89468-PA

35

PPG

Dispersion

preparation

Screw pumpWater-injection station

Facilities to Pump PPG

• Large amount of

PPG injection for

multiple wells

• The second largest chemical EOR technology after polymer flooding in China

• Field-wide application rather than single well treatment 37

Facilities to Pump PPG

Picture of PPG Injection Site

38

Facilities to Pump PPG

Picture of PPG Injection Site

39

0.05% Brine 0.25% Brine 1% Brine 10 % Brine

Fully Swollen Partially Swollen

Dry particle (stiff particle)

The more swelling, the more deformable

Q4: Do we need control swelling rate if we

only consider injectivity?

40

Experiment Descriptions

PPG size (dry): ~ 0.6 mm

Tubes ID : 10.922, 3.048,1.752, and 0.774 mm

Brine Concentrations: 0.05, 0.25, 1, and 10%

0

50

100

150

200

0.05 0.25 1 10Brine concentrations, %

Swelling Ratio

0

200

400

600

800

1000

1200

1400

0.05 0.25 1 10

Brine concentrations, %

Gel strength, pa

41

Conduit Experiment: Methodology and Experiment

1

10

100

1000

0 500 1000 1500 2000 2500

Ge

l in

jec

tio

n p

res

su

re (

ps

i)

Gel injection velocity (ft/day)

0.05% 0.25% 1% 10%

Conduit opening size 3.048 mm

PPG Injection Pressure

Conduit opening size 1.752 mm

Fully Swelling Particles have better Injectivity than Partially

Swelling Particles

Particle strength is more dominant particle movement than

particle size

1

10

100

1000

0 1000 2000 3000

Ge

l In

jec

tio

n P

res

su

re, p

si

Gel Injection Velocity, ft/day

0 1000 2000 3000

Gel Injection Velocity, ft/day

10% 1%0.25% 0.05%

0 1000 2000 3000

Gel Injection Velocity, ft/day

Conduit opening size 10.922 mmConduit opening size 3.048 mm

PPG Injection Pressure

1

10

100

1000

10000

100000

1000000

1 100 10000

Resid

ual

Resis

tan

ce F

acto

r

Brine Injection Velocity, ft/day

1 100 10000

Brine Injection Velocity, ft/day

0.05% 10%

1 100 10000

Brine Injection Velocity, ft/day

Conduit opening size 1.75 mm Conduit opening size 3.048 mm Conduit opening size 10.92 mm

PPG Resistance to Water Flow

45

A Swollen Particle Transport through a Throat

a. PPG moving to throat b. Losing water from PPG front

c. Elongated particle filling throat d. Particle through throat

particle

glass

A Process of a Particle through Throat(s)

a. PG was moving to throat. b. PG was broken into two particles c. Bigger part tried to pass

through throat

d. PG become more arched e. Two ends of PG enter two

throats

f. PG was broken again and

passed through throat

glass

Throat

PPG