foam injection via capillary string in vicksburg dry …...gas well deliquification workshop...
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Gas Well Deliquification Workshop
Sheraton Hotel, Denver, Colorado
February 17 – 20, 2013
Foam Injection Via Capillary String in Vicksburg Dry Gas Wells in South Texas
Adam Pittman, Brent Jackson, Andrea Jimenez,
Dave Senneway
Shell South Texas Production Operations
Outline
• Background
• South Texas History
• South Texas Foam Capillary String Process
• Example Wells
• Key Learnings and Conclusions
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 2
Feb. 17 – 20, 2013
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Foamer Background
What Does
Foam Do For
Us?
• Decrease
Surface
Tension
• Lowers Fluid
Density
• Lowers
critical gas
flow rate - lift
liquids at
lower flow
rate
Time
Prod
uctio
n
Intermittent production
Onset of liquid loading
South Texas Vicksburg Background
SOUTH TEXAS Gulf
of Mexico
Houston
Corpus Christi
Houston
Corpus Christi
Vicksburg Frio
South Texas Asset
• First wells drilled
in 1950’s
• Asset divested in
2011
• 550 Producing
wells
• 150 with Foam
Injection
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 4
Subsurface Background
• Vicksburg and Frio were primary reservoirs
– Tight sandstones (0.1-50 mD perm)
– Dry – Wet gas (0-30 bbl/mmcf condensate)
• Reservoirs also contained water (up to 250
bbl/mmcf depending on the well)
– Typically 30-50 bbl/mmcf
– Salinity ranged from 8000 ppm chlorides to 90,000 ppm
or greater
• Very little H2S or CO2
• No requirement for SCSSV’s
2013 Gas Well Deliquification Workshop
Denver, Colorado
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Typical Tubingless Well Design – With Capillary String Installed
• 2-7/8” or 3-
1/2” casing
with no tubing
• Stacked pay
w/ multiple
fractured
sands
• Capstrings
installed mid-
perf after well
began to
liquid load.
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Capillary String Selection Process
CANDIDATE Condensate
<5 bbl/mmcf
WLR > 0.4 ?
Critical Rate
Check
N
Batch treat well
-Compare to SI of similar length at most 6mo
earlier, if none available then SI well without
batching (same SI time) for comparison
No cap string.
AFE/PM
Capillary
String
Batch Treat
Response
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 7
-Examine WB issues
(fill / fish / damage)
N
Poor
Y Y
Y
P
F
N
Production with Foam Injection
• Foam injection could be widely deployed in
different flow conditions and different points in
well life.
– Delaying move into compression
– Regain production after falling off trend
– Return slugging wells to constant flow
– Eliminate intermittent cycles
– Restore liquid loaded wells
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 8
Foam Example #1
Fell Off Production Trend
• Down to 200 mcfd prior to Foam
• Over 1000 mcfd w/ Foam
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 9
Foam Example #2
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Denver, Colorado
Feb. 17 – 20, 2013 10
Intermittent
• 665 mcfd, 3 bcpd
• Increased to 1012 mcfd, 12 bcpd
Foam Example #3
Liquid Loaded
• 150 mcfd, 1
bcpd, 0 bwpd
average
• Increased to 350
mcfd, 10 bcpd,
10 bwpd
average after CS
installation
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 11
Liquid Loaded
• 125 mcfd, 1
bcpd
• Increased to 350
mcfd, 10 bcpd
Cap String Success Through Time
2007-2010 Program
• 2007 – New
selection process
introduced
• 2008 – AFE process
streamlined
• 2010 – Candidate list
exhausted
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Denver, Colorado
Feb. 17 – 20, 2013 12
South Texas Vicksburg Foam Injection Learnings
• Analytical Tools and Trials combined for best prediction of
success
– Turner/Coleman Critical Rate used as a key indicator
– Batch Treatments also used a key indicator
• Foam injection via capstring widely deployed
– Success with Water to Gas ratio as high as 350 bbl/mm
– Wells with Water to Condensate ratio as low as 50% can still
be successfully foamed.
• Mid Perf placement of capstring better than above top perf
placement
– Depends on fluid level in well
– Well integrity / casing collapse could prevent optimal
capstring placement
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Denver, Colorado
Feb. 17 – 20, 2013 13
Analysis – Critical Rate
14
Turner – Critical
Rate equation
with adjustment
multiplier (red
line)
• Applied
additional
correction
factor to predict
psuedo critical
rate with foam
(blue line)
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013
Analysis – Critical Rate
15
Critical Rate is the Best Indicator for Success
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013
Batch Treatment Screening
Uniform Process
• Compare batch treatment
with production following
a similar shut-in time.
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Batch Treatments in 2009 and Capstring Success
Batch Treatments good indicator for success but even a well
with a poor response can respond to continuous foam 2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 17
Response
> 100 mcfd Response
~ 50- 100 mcfd
Response
< 50 mcfd
Analysis – Capstring More Effective Mid-Perforation
2008-09 Experiment
• Mid perf placement shows better
response than other placements
2013 Gas Well Deliquification Workshop
Denver, Colorado
Feb. 17 – 20, 2013 18
Conclusions
• Well design and environment allowed for continuous
foam injection via capstrings at low upfront cost.
• Foam program in South Texas was very profitable but
increased chemical spending significantly as more wells
were lifted with foam.
• Foam injection via capstring could be deployed by “trial
and error” but some analysis and batch treatment tests
could be used to more accurately predict continuous
foam injection success.
• Some liquid loaded wells flowing at optimal production
rates and responding positively to a batch treatment
could still have poor production response to permanent
capillary string installation.
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Denver, Colorado
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• Reserves: Our use of the term “reserves” in this presentation means SEC proved oil and gas reserves.
• Resources: Our use of the term “resources” in this presentation includes quantities of oil and gas not yet classified as SEC proved oil and gas reserves. Resources
are consistent with the Society of Petroleum Engineers 2P and 2C definitions.
• Organic: Our use of the term Organic includes SEC proved oil and gas reserves excluding changes resulting from acquisitions, divestments and year-average pricing
impact.
•
• The companies in which Royal Dutch Shell plc directly and indirectly owns investments are separate entities. In this announcement "Shell", "Shell Group" and "Royal
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projects and delays in the reimbursement for shared costs; and (m) changes in trading conditions. All forward looking statements contained in this announcement are
expressly qualified in their entirety by the cautionary statements contained or referred to in this section. Readers should not place undue reliance on forward looking
statements. Additional factors that may affect future results are contained in Shell's 20-F for the year ended 31 December 2011 (available at www.shell.com/investor
and www.sec.gov ). These factors also should be considered by the reader. Each forward looking statement speaks only as of the date of this announcement, 5
February 2013. Neither Shell nor any of its subsidiaries nor the Shell Group undertake any obligation to publicly update or revise any forward looking statement as a
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DEFINITIONS AND CAUTIONARY NOTE
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