Foam Injection Via Capillary String in Vicksburg Dry Gas Wells in South Texas

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Transcription:

Gas Well Deliquification Workshop Sheraton Hotel, 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

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 2 Outline Background South Texas History South Texas Foam Capillary String Process Example Wells Key Learnings and Conclusions

Production 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 Onset of liquid loading Intermittent production Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop Time 3

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 4 South Texas Vicksburg Background South Texas Asset First wells drilled in 1950 s Asset divested in 2011 550 Producing wells 150 with Foam Injection Corpus Christi Vicksburg Frio Houston SOUTH TEXAS Gulf of Mexico

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 5 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

Typical Tubingless Well Design With Capillary String Installed Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 6 2-7/8 or 3-1/2 casing with no tubing Stacked pay w/ multiple fractured sands Capstrings installed midperf after well began to liquid load.

Capillary String Selection Process 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 Poor No cap string. N WLR > 0.4? F Batch Treat Response N -Examine WB issues (fill / fish / damage) N Y P Y CANDIDATE Condensate <5 bbl/mmcf Y Critical Rate Check AFE/PM Capillary String Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 7

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 8 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

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 9 Foam Example #1 Fell Off Production Trend Down to 200 mcfd prior to Foam Over 1000 mcfd w/ Foam

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 10 Foam Example #2 Intermittent 665 mcfd, 3 bcpd Increased to 1012 mcfd, 12 bcpd

Foam Example #3 Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 11 Liquid Loaded 125 mcfd, 1 bcpd Increased to 350 mcfd, 10 bcpd Liquid Loaded 150 mcfd, 1 bcpd, 0 bwpd average Increased to 350 mcfd, 10 bcpd, 10 bwpd average after CS installation

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 12 Cap String Success Through Time 2007-2010 Program 2007 New selection process introduced 2008 AFE process streamlined 2010 Candidate list exhausted

South Texas Vicksburg Foam Injection Learnings Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 13 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

Analysis Critical Rate Turner Critical Rate equation with adjustment multiplier (red line) Applied additional correction factor to predict psuedo critical rate with foam (blue line) Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 14

Analysis Critical Rate Critical Rate is the Best Indicator for Success Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 15

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 16 Batch Treatment Screening Uniform Process Compare batch treatment with production following a similar shut-in time.

Batch Treatments in 2009 and Capstring Success Response > 100 mcfd Response ~ 50-100 mcfd Response < 50 mcfd Batch Treatments good indicator for success but even a well with a poor response can respond to continuous foam Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 17

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 18 Analysis Capstring More Effective Mid-Perforation 2008-09 Experiment Mid perf placement shows better response than other placements

Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 19 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.

DEFINITIONS AND CAUTIONARY NOTE 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 Dutch Shell" are sometimes used for convenience where references are made to Royal Dutch Shell plc and its subsidiaries in general. Likewise, the words "we", "us" and "our" are also used to refer to subsidiaries in general or to those who work for them. These expressions are also used where no useful purpose is served by identifying the particular company or companies. "Subsidiaries", "Shell subsidiaries" and "Shell companies" as used in this announcement refer to companies in which Shell either directly or indirectly has control, by having either a majority of the voting rights or the right to exercise a controlling influence. The companies in which Shell has significant influence but not control are referred to as "associated companies" or "associates" and companies in which Shell has joint control are referred to as "jointly controlled entities". In this announcement, associates and jointly controlled entities are also referred to as "equity-accounted investments". The term "Shell interest" is used for convenience to indicate the direct and/or indirect (for example, through our 23 per cent shareholding in Woodside Petroleum Ltd.) ownership interest held by Shell in a venture, partnership or company, after exclusion of all third-party interest. This announcement contains forward looking statements concerning the financial condition, results of operations and businesses of Shell and the Shell Group. All statements other than statements of historical fact are, or may be deemed to be, forward-looking statements. Forward-looking statements are statements of future expectations that are based on management's current expectations and assumptions and involve known and unknown risks and uncertainties that could cause actual results, performance or events to differ materially from those expressed or implied in these statements. Forward-looking statements include, among other things, statements concerning the potential exposure of Shell and the Shell Group to market risks and statements expressing management s expectations, beliefs, estimates, forecasts, projections and assumptions. These forward looking statements are identified by their use of terms and phrases such as "anticipate", "believe", "could", "estimate", "expect", "goals", "intend", "may", "objectives", "outlook", "plan", "probably", "project", "risks", "seek", "should", "target", "will" and similar terms and phrases. There are a number of factors that could affect the future operations of Shell and the Shell Group and could cause those results to differ materially from those expressed in the forward looking statements included in this announcement, including (without limitation): (a) price fluctuations in crude oil and natural gas; (b) changes in demand for Shell's products; (c) currency fluctuations; (d) drilling and production results; (e) reserves estimates; (f) loss of market share and industry competition; (g) environmental and physical risks; (h) risks associated with the identification of suitable potential acquisition properties and targets, and successful negotiation and completion of such transactions; (i) the risk of doing business in developing countries and countries subject to international sanctions; (j) legislative, fiscal and regulatory developments including regulatory measures addressing climate change; (k) economic and financial market conditions in various countries and regions; (l) political risks, including the risks of expropriation and renegotiation of the terms of contracts with governmental entities, delays or advancements in the approval of 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 result of new information, future events or other information. In light of these risks, results could differ materially from those stated, implied or inferred from the forward looking statements contained in this announcement. Shell may have used certain terms, such as resources, in this announcement that the SEC strictly prohibits Shell from including in its filings with the SEC. U.S. investors are urged to consider closely the disclosure in Shell's Form 20-F, File No 1-32575, available on the SEC website www.sec.gov. You can also obtain these forms from the SEC by calling 1-800-SEC-0330.

Copyright Rights 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 as directed by the Workshop Steering Committee. Place it on a CD for distribution and/or sale as directed by the Workshop Steering Committee. Other use of this presentation is prohibited without the expressed written permission of the author(s). The owner company(ies) and/or author(s) may publish this material in other journals or magazines if they refer to the Gas Well Deliquification Workshop where it was first presented. Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 21

Disclaimer The following disclaimer shall be included as the last page of a Technical Presentation or Continuing Education Course. A similar disclaimer is included on the front page of the Gas Well Deliquification Web Site. The Artificial Lift Research and Development Council and its officers and trustees, and the Gas Well Deliquification Workshop Steering Committee members, and their supporting organizations and companies (here-in-after referred to as the Sponsoring Organizations), and the author(s) of this Technical Presentation or Continuing Education Training Course and their company(ies), provide this presentation and/or training material at the Gas Well Deliquification Workshop "as is" without any warranty of any kind, express or implied, as to the accuracy of the information or the products or services referred to by any presenter (in so far as such warranties may be excluded under any relevant law) and these members and their companies will not be liable for unlawful actions and any losses or damage that may result from use of any presentation as a consequence of any inaccuracies in, or any omission from, the information which therein may be contained. The views, opinions, and conclusions expressed in these presentations and/or training materials are those of the author and not necessarily those of the Sponsoring Organizations. The author is solely responsible for the content of the materials. The Sponsoring Organizations cannot and do not warrant the accuracy of these documents beyond the source documents, although we do make every attempt to work from authoritative sources. The Sponsoring Organizations provide these presentations and/or training materials as a service. The Sponsoring Organizations make no representations or warranties, express or implied, with respect to the presentations and/or training materials, or any part thereof, including any warrantees of title, non-infringement of copyright or patent rights of others, merchantability, or fitness or suitability for any purpose. Feb. 17 20, 2013 2013 Gas Well Deliquification Workshop 22