Gas Well Dewatering PetromRomania –Member of …€¦ · requires no batch treating or shut-in...
Transcript of Gas Well Dewatering PetromRomania –Member of …€¦ · requires no batch treating or shut-in...
Gas Well Dewatering Petrom Romania – Member of OMV Group
August 2009Vasile Stanculescu, Nicolae
Gheorghe
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Presentation contents
� Background
� Selection criteria
� Lifting methods
� History
� Application results
� Operational challenges
� Summary of results
� Conclusions
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Background – As Related to Gas Well Dewatering
� Petrom is the Largest Producer of Oil and Gas in South Easter Europe
� In 2004 a 51% Acquisition of shares by OMV occurred
� In February 2007 a Service Company was approached by Petrom to discuss
Dewatering Options for approximately 100 gas wells
� April 2007 Initial Data was captured indicating that there was a solid
opportunity for Gas Well Dewatering
� In June 2007 a Test Contract was signed
� During the 4th Quarter of 2007 Designs were completed and first
installations occurred
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Initial Well Evaluations
► Signs of liquid loading:
►high differential casing-tubing pressure between 9 -20 bars
►decreasing liquid production
►decreasing gas rate
►not constant/rather fluctuating gas and liquid production
► Evaluation
► Initial evaluations were completed to determine optimal lift type and uplift potential
►The optimal lift type was chose based on economical and technical (pressure, rate, tubulars, perforated interval, water cut…) criteria
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Lift Methods Evaluated
Most Common Dewatering Methods► Velocity Strings► Foamer Application
► Batch► Continuous
- Capillary injection- Injection in annulus
► Soap Sticks► Plunger Lift► Compression
Less common however still applied with larger volumes► Gas Lift ► Rod-Pump
Other Forms of Lift also used for Dewatering in specific cases► Hydraulic Lift► Progressive Cavity Pump► Electric Submersible Pump
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Continuous Foam Injection
Annulus Injection► Advantages:
► really cheap method► easy to install ► requires no batch treating or shut-in time
► Disadvantages: ► Not applicable in wells with packer► Results can be influenced by the tubing
Capillary Injection► Advantages:
► Applicable in Packer completions and in deep application► Simple to operate
► Disadvantages: ► Costly compared to Annular injection► Potential Operational Issues
- Limits Wellbore Access- Emergency Shut down options
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Plunger Lift System
Advantages:► Requires no outside energy source; uses well’s energy to lift► Rig not required for installation► Easy maintenance ► Keeps well clean of paraffin deposits► Low-cost artificial lift method► Handles gassy wells► Good in deviated wells
Disadvantages:► Specific GLRs to drive system:
►400 Scf/bbl/1000feet no Packer►1000 Scf/bbl/1000feet with Packer
► Low-volume potential (<200 BPD)► Solids► Requires surveillance to be optimized► Requires ID tubular to be constant
Lubricator
Catcher
Solar Panel
Controller
Dual “T” Pad
Plunger
Bumper
Spring
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History
► In 4th Q of 2007 and 1st Q of 2008, 6 wells in one of the Petromfields, were analyzed and installed with dewatering methods:
► 4 continuous foam injection in the annulus
► 1 capillary injection banded
► 1 plunger lift
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Pilot Test - Results
► In 4th Q of 2007, 3 wells were equipped with foam injection method resulting in a gas rate of 33000 Sm3/day.
► At the 1st Q of 2008 after installing the other 3 wells Petromobtained a total increase of 49000 Sm3/day; an average of 8300 Sm3/day/well equipped Pilot Test Contract
100000
110000
120000
130000
140000
150000
160000
170000
180000
190000
200000
1-Oct-07
21-Oct-07
10-Nov-07
30-Nov-07
20-Dec-07
9-Jan-08
29-Jan-08
18-Feb-08
9-Mar-08
29-Mar-08
Gas R
ate
[Sm
3/d
ay]
Gas Rate Before Installation Gas Rate After Installation
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Q2 –Q3 of 2008
► In 2nd and 3rd Q of 2008 the main focus was:
►maintaining the increase obtained for the wells in the pilot test
►gathering information for the new wells and analyzing them for future installation
►preparing the new Dewatering Contract between Petrom and Service Company
► In the last part of 3rd Quarter the first 5 wells from the Dewatering contract, have been installed (continuous foam injection into annulus)
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End of Q3 2008
Wells installed at end of 3rd Q 2008
60000
65000
70000
75000
80000
85000
90000
1-Apr-08
1-May-08
1-Jun-08
1-Jul-08
1-Aug-08
31-Aug-08
1-Oct-08
31-Oct-08
Gas R
ate
[S
m3/d
ay]
Gas Rate Before Installation Gas Rate After Installation
� The total increase of gas production for these 5 foam injection
methods was 18300 Sm3/day; an average of 3700
Sm3/day/well
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Q3 of 2008 – Detailed Results
W1-Field 3 – Results► Well description:
► This well was a Gas Lift well which was receiving 12000 Sm3/day of injection gas per day to lift. Gas Production from formation was 3000 Sm3/day with 0.2 m3/day of oil and 0.5 m3/day of water
► Objective:► reducing costs with gas injection► reducing gas injection rate► obtaining a constant gas rate as high as possible
► Results:► well was equipped with continuous foam injection in the annulus► by the end of 4th Q of 2008 the gas injection rate was decreased from 12000-15000 Sm3/day to 6000 Sm3/day
► the reservoir gas rate increased from an average of 3000 Sm3/day to a constant gas rate of 4000 Sm3/day
► in April 2009 it was decided to stop gas injection and to produce the well only with foamer injection. The gas rate remained at the same value of 4000 Sm3/day surveillance
► well is under close surveillance
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Well W1-Field 3 –- Gas Lift Well/Converted to flowing Gas
Well
W1 Real Results
0
5000
10000
15000
20000
25000
30000
11-Mar-08 30-Apr-08 19-Jun-08 8-Aug-08 27-Sep-08 16-Nov-08 5-Jan-09 24-Feb-09 15-Apr-09 4-Jun-09
Gas R
ate
[S
m3/d
ay]
0
5
10
15
20
25
Liq
uid
rate
[m
3/d
ay]
Reservoir Gas Rate Injection Gas Rate Liquid Rate
Installation of
continuous
foam injection in
the annulus
Injection rate
was dropped to
6000 Sm3/dayInjection rate
was dropped to
0 Sm3/day
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� In 4th Q of 2008, 26 wells were installed, resulting in an increase of gas production of
105000 Sm3/day, an average of 4300 Sm3/day/well installed
Q4 of 2008
Wells Installed in 4th Q 2008
300000
320000
340000
360000
380000
400000
420000
440000
460000
480000
500000
1-Jul-08
21-Jul-08
10-Aug-08
30-Aug-08
19-Sep
-08
9-Oct-08
29-Oct-08
18-Nov-08
Gas R
ate
[Sm
3/d
ay]
Gas Rate After Installation Gas Rate Before Installation
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Q4 of 2008 - Detailed Results
W2 Field 2 – Results► Well description:
► During the previous year the wells production decreased from 50000 Sm3/day to 18-23000 Sm3/day.
► casing-tubing differential pressure, increased from 10 bars to 23 bars
► liquid production decreased from 30 m3/day to 15 m3/day ► Objective:
►maintaining gas rate to a value of 28000 Sm3/day and avoiding well from stopping production
►unloading the well► Results
►well was equipped with continuous foam injection in the annulus► first month after installation the gas rate increased from 18000 Sm3/day to 46000 Sm3/day
►water rate increased from 18 m3/day to 30 m3/day►well is under close surveillance
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W2 Field 2 – Real Results
W2 Real Results
0
10000
20000
30000
40000
50000
60000
70000
80000
90000
100000
3-Mar-08 22-Apr-08 11-Jun-08 31-Jul-08 19-Sep-08 8-Nov-08 28-Dec-08
Gas R
ate
[S
m3/d
ay]
-4
6
16
26
36
46
56
Tu
bin
g P
ressu
re, C
asin
g P
ressu
re [
bars
]; L
iqu
id R
ate
[m
3/d
ay]
Gas Rate Tubing Pressure Casing Pressure Liquid Rate
The well started to load up
Installing of
continuous
foamer
injection
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Q4 of 2008 - Detailed Results
W3 Field 2 – Result ► Well description:
► Well has an fluctuating production with gas fluctuations between 17000 Sm3/dy and 27000 Sm3/day
► 4-5months before installation soap sticks have been used as treatment but even with this method well continued to have:
- High differential casing-tubing pressure of 15-18 bars- Fluctuating gas rates between 17000-27000 Sm3/day - Fluctuating liquid production
► Objective:►maintaining gas rate to a constant value of 27000 Sm3/day ►unloading the well
► Results:► well was equipped with continuous foam injection in the annulus
► first month after installation the gas production was increasedto 37000 Sm3/day
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W3 Field 2 – Real Result
W3 Real Result
0
10000
20000
30000
40000
29-Feb-08 19-Apr-08 8-Jun-08 28-Jul-08 16-Sep-08 5-Nov-08 25-Dec-08
Ga
s R
ate
[S
m3
/da
y]
0
5
10
15
20
25
30
35
40
45
50
Tu
bin
g P
res
su
re, C
as
ing
Pre
ss
ure
[b
ars
]; W
ate
r R
ate
[m
3/d
ay
]
Gas Rate Tubing Pressure Casing Pressure Liquid Rate
Performed soap
stick treatment
Installing of
continuous
foamer
injection
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Challenges During Operations
► Condensate Production – Production figures provided were not always accurate due to inconsistent measurements. In some cases this made optimization difficult
► Holes in Tubing – Initially major issues were found with un-diagnosed holes in the tubing. Solution was to require Echometer tests as part of evaluation process
► Flow Line Pressure – Significant difference in flow line pressure during Summer and Winter changed the impact of the lift method applied
► Choke Size Limitations – Wellhead chokes sizes if not properly modeled, may only result in higher flowing tubing pressure with minimal increase in production
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Overall View - Dewatering Project in 2008
► At the end of 2008 have been installed 35 wells►1 plunger technology►1 capillary banded technology►4 continuous foam injection through capillary technology►29 continuous foam injection in the annulus technology
► Total increase of production obtained was 125000 Sm3/day, an average of 3500 Sm3/day/well installed
► Other benefits :►Corrosion Problem
- applying chemicals reduced corrosion problems significantly► Paraffin Problems
- applying plunger reduced the paraffin and scale problems
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Overall view regarding Dewatering in 2008
Overall View - 2008
500000
550000
600000
650000
700000
750000
1-Oct-07
15-Dec-07
28-Feb-08
13-May-08
27-Jul-08
10-Oct-08
24-Dec-08
Gas r
ate
[Sm
3/d
ay]
Gas Rate Before Installation Gas Rate After Installation
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Conclusions
� The results of the application of modern dewatering methods, increased the
average gas production of equipped wells by 22%.
� The success is based on a good cooperation between Petrom and Service
Company.
� Petrom will continue and expand the application of gas dewatering methods
in it’s operations.