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Gas Well Deliquification Workshop Sheraton Hotel, Denver, Colorado February 23 - 26, 2009 Selection and Application of Chemical Foamers for Offshore, North Sea Johannes Visser - Britannia Operator Limited Martin J. Willis* - Nalco Limited

Selection and Application of Chemical Foamers for … · Selection and Application of Chemical Foamers for Offshore, North Sea ... Assessing Well Suitability • ... Selection and

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Gas Well Deliquification WorkshopSheraton Hotel, Denver, Colorado

February 23 - 26, 2009

Selection and Application of Chemical Foamers for Offshore, North Sea

Johannes Visser - Britannia Operator Limited

Martin J. Willis* - Nalco Limited

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

2

Summary• Chemical foamer, Sci-Foam EC7007A, has been

successfully applied offshore North Sea in a condensate loaded well

• Performance has demonstrated clear benefits to well production;– Gas rates, liquids production and flowing time

• Product selection was a result of the robust Nalco 5 step lift process;– Extensive laboratory testing– Well specific modeling– Liaising with the operators to fully understand the issues and

concerns

• Utilising surfactant technology developed specifically for addressing liquid loading

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

3

Contents

• Background

• Assessing Well Suitability

• Product Selection & Recommendation

• Field Trials

• The Future

• Summary

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Background• Britannia Gas Condensate Wells

– Located in UK sector of the North Sea• Block UK 16/26

– Packed completions fitted with SSVs

– Depth circa. 14,000ft

– Numerous wells showing signs of loading • >10 wells were submitted • Some already on intermittent production

– Previous attempts to use artificial lift deemed unsuccessful

– Approach to Nalco for a “Best In Class” foamer

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Rate / Mscf/d A B C D E F GWell

Tubing regim

e Water critical rate 3,208 2,208 2,276 1,866 3,186 3,175 3,383Water + Condensate critical rate 2,636 1,826 1,889 1,287 2,635 2,617 2,781Water + Foam critical rate 2,218 1,512 1,565 1,072 2,189 2,184 2,347Production rate* 11,400 6,000 5,100 5,200 6,000 5,000 9,600% above Critical 255 172 124 179 88 57 184Tubing re

gime

Casing re

gime Water critical rate 5,375 5,234 5,557 4,555 5,183 10,130 10,652

Water + Condensate critical rate 4,416 4,328 4,611 3,770 4,286 8,352 8,758Water + Foam critical rate 3,716 3,585 3,821 2,618 3,561 6,968 7,389Production rate* 11,400 6,000 5,100 5,200 6,000 5,000 9,600% above Critical 112 15 -8 14 16 -51 -10Cas

ing regim

e

* Production rates are recorded from low pressure system, not standard conditions

Assessing Well Suitability

• Nalco’s managed foamer program

• Gathered well data to run the model

• Output inferred loading in the casing region

.

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Product Selection (1 of 2)• Products available

• Key parameter was foamer testing

Water / g 5BOL Condensate / g 95N2 Flowrate / LPM 2Temperature / °C 24

Unloading conditions

Commercial Product Name

Lo Temp Stability

Hi Temp Stability

Flash Point

CEFAS Registered

EC7005A -10°C 140°C >65°C Green Gold

EC7007A -10°C 140°C >65°C Green Gold

EC7008A -15°C 130°C >65°C Red, Sub-list Gold

To be tested if green products unsuccessful

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Product Selection (2 of 2)

• Also completed additional testing;

– Viscosity profiles• Across wide temperature

range viscosity remained low

– Defoamer compatibility• Product identified to work at

levels <10% of foamer treat rate

– Chemical compatibility• Static tests showed

compatibility with majority of other system chemicals

• Only incompatibility was with an oil based product

– Material compatibility• Compatible with a range of

metals, elastomers and packing materials

– Emulsification tendency• No significant tendency

– Partitioning study• Demonstrated the foamer

will favour the water phase

– Core flood study• Various tests were

conducted reporting no impact on gas flow

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Product Recommendation

Selecting the right product is key to prevent topside upsets

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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– Excellent foaming performance evident– Meets other product requirements– Sub-free and gold HQ banding to meet “green” North Sea target

Product Recommendation – Sci-Foam EC7007A

0

10

20

30

40

50

60

70

80

0.00 5.00 10.00 15.00 20.00 25.00 30.00 35.00

Time (min)

Upl

oad

Wei

ght (

g)

Blank

EC7007A5000ppm

EC7007A10000ppm

EC7007A15000ppm

EC7005A5000ppm

EC7005A10000ppm

EC7005A15000ppm

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Trial Proposal

• Topside squirt trial– Ensure no impact on separation performance or oil in

water levels• OiW regulated at 30 mg/l for overboard discharge in the

North Sea

• Downhole batch treatment

• Continuous application

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Topside Squirt Test• Applied volume of

foamer and anti-foam across the test separator in live well fluids

– Foamer volumes where between 5-50 l/hour

– Defoamer at 0.1 l/hour

• Results show no negative impact on OiW and maintained standard overboard discharge

0

10

20

30

40

50

60

70

80

90

100

23/0

8/20

08, 1

3:20

, bas

elin

e

23/0

8/20

08, 1

7:00

, bas

elin

e

24/0

8/20

08, 0

6:00

, bas

elin

e

24/0

8/20

08, 0

9:00

, bas

elin

e

24/0

8/20

08, 1

2:25

, 0.1

/ 5

L pe

r hr

24/0

8/20

08, 1

4:00

, 0.1

/ 10

L pe

r hr

24/0

8/20

08, 1

5:40

, 0.1

/ 15

L pe

r hr

24/0

8/20

08, 1

7:15

, 0 /

15L

per h

r

24/0

8/20

08, 1

8:00

, 0.1

/ 20

L pe

r hr

24/0

8/20

08, 2

0:00

, 0.1

/ 20

L pe

r hr

24/0

8/20

08, 2

0:45

, 0.1

/ 20

L pe

r hr

25/0

8/20

08, 0

6:00

, bas

elin

e

25/0

8/20

08, 0

8:30

, 0.1

/ 25

L pe

r hr

25/0

8/20

08, 0

8:55

, 0.1

/ 25

L pe

r hr

25/0

8/20

08, 1

0:20

, 0.1

/ 30

L pe

r hr

25/0

8/20

08, 1

2:10

, 0 /

30L

per h

r

25/0

8/20

08, 1

3:05

, 0 /

30L

per h

r

25/0

8/20

08, 1

4:30

, 0.1

/ 35

L pe

r hr

25/0

8/20

08, 1

4:55

, 0.1

/ 35

L pe

r hr

25/0

8/20

08, 1

6:30

, 0.1

/ 40

L pe

r hr

25/0

8/20

08, 1

8:40

, 0.1

/ 50

L pe

r hr

Oil

in w

ater

con

tent

(mg/

l)

Oil in water content at Degasser and MP Separator Outlets

DegasserMP

Separator

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Downhole Batch Treatment (1 of 2)• 320 litres / 84 gals (~30,000ppm of calculated liquid volume) of

foamer was pumped down the production tubing of well G

• Well shut-in for 20 hours and allowed to build up to a wellhead pressure of 56 bar / 812 psi

• Well flowed back into HP separator– Only initial surge observed, well did not kick

• Shut-in again for 1.5 hour until the wellhead pressure reached 56 bar / 812 psi

• Well flowed into MP separator– significant kick observed

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Downhole Batch Treatment (2 of 2)C

umul

ativ

e co

nden

sate

/ B

PD

Gas

rate

/ m

msc

f/d

Oct 08 Chemical clean up

Jul 08 Clean up

Oct 08 Gas rate

Jul 08 Gas rate

Variable Previous flow back

Trial results % Gain

Condensate within 30mins / bbls 5 40 700Gas rate after 30mins / mmscfd 5 6.5 30

Condensate after 12 hours / bbls 50 81 62Well uptime / days 6-8 63 >685

North Sea Field Trial - DH Batch

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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The Future

• Britannia is considering additional batch treatments – Condensate dominant wells– Water loaded wells

• Britannia is currently reviewing potential for continuous foamer application– Capillary string material and performance compatibility

completed• Passed all the material compatibilities• Showed product stability at 200°C, 7000psi for ~4 hours

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Summary• Chemical foamer, Sci-Foam EC7007A, has been

successfully applied offshore North Sea in a condensate loaded well

• Performance has demonstrated clear benefits to well production;– Gas rates, liquids production and flowing time

• Product selection was a result of the robust Nalco 5 step lift process;– Extensive laboratory testing– Well specific modeling– Liaising with the operators to fully understand the issues and

concerns

• Utilising surfactant technology developed specifically for addressing liquid loading

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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Acknowledgements

• The authors wish to thank;– Britannia Operator Limited and their Co-Venturers– Nalco Company

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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CopyrightRights to this presentation are owned by the company(ies) and/or author(s) listed on the title page. By submitting this presentation to the Gas Well Deliquification Workshop, they grant to the Workshop, the Artificial Lift Research and Development Council (ALRDC), and the Southwestern Petroleum Short Course (SWPSC), rights to:

– Display the presentation at the Workshop.– Place it on the www.alrdc.com web site, with access to the site to be

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Workshop Steering Committee.Other uses of this presentation are prohibited without the expressed written permission of the company(ies) and/or author(s) who own it and the Workshop Steering Committee.

Feb. 23 - 26, 2009 2009 Gas Well Deliquification Workshop Denver, Colorado

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