Plunger Lift Lubricators and API 6A Wellhead Compliance

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Gas Well Deliquification Workshop Sheraton Hotel, February 19 22, 2012 Plunger Lift Lubricators and API 6A Wellhead Compliance Séan Emery Regional Product Line Manager Deliquification Weatherford International

Define Plunger Lift Standards 1. How many different styles, specifications and types of Plunger Lift Lubricators are there on the market today? 2. Why do we need Standards to be set by API, NACE, ISO, ASME, EnForm or other governing bodies to build minimum specification requirements? 3. What is our responsibility? 2

API Organization American Petroleum Institute First Standards of API set in 1924 API now maintains 500 standards covering all segments of the oil and gas industry. API standards program has gone global, through active involvement with the International Organization for Standardization (ISO) and other international bodies. API references NACE 3

NACE Organization National Association of Corrosion Engineers Established in 1943 by eleven corrosion engineers in the pipeline industry NACE International s mission statement is to protect people, assets and the environment from corrosion. API references NACE 4

ISO International Organization for Standards (ISO is derived from the Greek meaning equal Established in 1947 ISO has published more than 18,500 International Standards ranging from standards for activities such as agriculture and construction, through mechanical engineering, to medical devices, to the newest information technology developments ISO is the world s largest standards developing organization. 5

Gas Wellhead API 6A Governance Standards Governed by API API has not set regulations to govern Plunger Lift Lubricators 6

What Industry Standards should a Lubricator meet? A Plunger Lift Lubricator is a wellhead component like a flow tee, gate valve, tubing head spool etc.. So at a bare minimum it should meet industry Wellhead specifications (API 6A:ISO 10423 & use NACE MR0175:ISO 15156 Compliant materials) Plungers are the only foreign bodies, besides hydrate releases and rare solid releases, impacting surface equipment So additional consideration of potential impact forces from high velocity arrivals and Lubricator resilience to said impacts must be considered and applied to Lubricator design (EnForm IRP 5 CDN) 7

What Lubricator should be on the Wellhead? 8

What Standard Specifications are Required for our Lubricator? 16 flow port spacing? API 16A? 3K? 5K? Stress-oriented hydrogen-induced cracking? 2.5 Bowen? 4130/4140 steel? 2500 ft/s? -60C/-75F Charpy tested? X750 spring? Manual catch? Flow tee NACE MR0175 standard? replacement? Dual Flanged? 1500 ft/s? How much carbon? Flanged top cap? Injection port location? EUE threads? Alloys? 1 or 2 injection ports? Galvanically-induced hydrogen stress cracking? 14 flow port spacing? 3/4 npt injection port? ASME? Autocatch? 17.4PH spring? ISO? 18 flow port Chlorides? 10K? spacing? 7.31 spacing? ½ npt injection port? What is max impact velocity? 3 Bowen? 2.5 flowport? Retainer ring? Soft zone cracking? Stress corrosion cracking? API 6A? Stepwise H2S partial pressure? EUE Thread torque rating? cracking? -46C/-50F Charpy tested? MP35N spring? 2 npt threadolet? 9 High Nitrale elastomer? API stamped/certified? CO2 partial pressure?

What is the Velocity Consideration? Rise Velocities Safe Operating Window <1000 ft/min(300m/min) Running Hard 1000 ft/min to 2500 ft/min Emergency Shut down(esd) Velocity >2500 ft/min (762m/min) 10

How does Velocity affect Lubricator Specification? Summary Example Calculation 2500 ft/min 3.5 20lbs plunger Impact Force Newtons (N) Lbs Functional Spring (0.03 sec deceleration) Compromised Spring (0.005 sec deceleration) 3900 890 23800 5300 11

Burst lubricator cap 12

EUE threaded lubricator and by pass line 13

Master valve nipple adapter shredded 14

Velocity Pressure Plot (surface vs. downhole) 15

What is Critical for us to Standardize from an Operational Perspective to Reduce Impact Velocities? Safe Operating Procedures for Optimization Bringing plunger to tank, blowing down, Hydrates etc. Extended Shut in caused by Compressor Servicing, Line pressure changes or Turnarounds Standing Valve Integral to Bottom Hole Bumper Spring - To ensure fluid above plunger/hydraulic break 16

What is Critical for us to Standardize from an Operational Perspective to Reduce Impact Velocities? Controller Alarm Flags Remote Well Monitoring For quick arrivals above 1000ft/min Automatic Emergency Shut Down(ESD) on single arrival above 2500ft/min followed by a spring tension check and probable spring replacement Quarterly Service Routes including surface spring tension checks 17

What Thread Type Should we use? Thread Pull Test Bowen vs. EUE Connection 2 3/8 Bowen Top 4.75 c/w 4 Acme 2G Thread Connection pull fail rating of 257,500 lbs. 2 3/8 EUE 8rd Thread Connection pull rating 160,000 lbs. 18

Which API 6A Wellhead requirements do we need to apply? API 6A Recommended PSL Levels 19 2012 Gas Well Deliqufication Workshop PER API / ANSI 6A / ISO 10423:2009 REV 20, October 2010 19

Which API 6A Wellhead requirements do we need to apply? API 6A Wellhead Weld Procedures PER API/ANSI 6A/ISO 10423:2009 REVISION October 2010 20

Which API 6A Wellhead requirements do we need to apply? API 6A Material Class Design Minimum Material Requirements Material Class body, bonnet, end and Pressure controlling parts, outlet connections stems and mandrel hangers AA - General Service carbon or low-alloy steel carbon or low-alloy steel BB - General Service carbon or low-alloy steel stainless steel CC - General Service stainless steel stainless steel DD - Sour Serviceª carbon or low-alloy steel ¹ carbon or low-alloy steel ¹ EE - Sour Serviceª carbon or low-alloy steel ¹ stainless steel ¹ FF - Sour Serviceª stainless steel ¹ stainless steel ¹ HH - Sour Serviceª CRAs ¹²³ CRAs ¹²³ ª As defined by NACE MR0175/ISO 15156. In compliance with NACE MR 0175/ISO 15156. ¹ In compliance with NACE MR0175/ISO 15156. ² CRA required on retained fluid wetted surfaces only; CRA cladding of low alloy or stainless steel is permitted ³ CRA as defined in clause 3 of this International Standard; NACE MR 0175/ISO 15156 definition of CRA does not apply PER API/ANSI 6A/ISO 10423:2009 REVISION 20 OCT 2010 21

Which API 6A Wellhead requirements do we need to apply? API 6A Ring Gaskets API 6A Designations for Metallic Ring Gaskets are correlated to the appropriate seat PER API/ANSI 6A/ISO 10423:2009 REVISION 20 OCT 2010 Ring Gaskets must be replaced if seal is broken, they can not be reused 23

Which API 6A Wellhead requirements do we need to apply? API 6A Temperature Class Design Operating Range Temperature Celsius Fahrenheit Classification min max min max K -60 82-75 180 L -46 82-50 180 N -46 60-50 140 P -29 82-20 180 R Room Temperature Room Temperature S -18 60 0 140 T -18 82 0 180 U -18 121 0 250 V 2 121 35 250 X* -18 180 0 350 Y* -18 345 0 650 Note: Temp Classes may be combined for a broader range * rated working pressure of equipment may be derated for temperature ratings X and Y. PER API/ANSI 6A/ISO 10423:2009 REVISION October 2010

Which API 6A Wellhead requirements do we need to apply? NACE Documentation & Classification NACE SSC regions of environmental severity 26

API 6A Certification Identification 27

What is our Responsibility Today? Safety, Environment & Optimized Production Build internal Safe Operating Procedures(SOP) to mitigate risk exposure, reduce the environmental impact and eliminate economic losses due to failures Maintain the equipment through regular Service /Maintenance Schedules Where possible apply recognized industry standards to define metallurgical requirements, corrosion resistance, processes etc 28

What is the Industry s Responsibility? 1. Minimum Specifications and Guidelines must be set not only for the equipment but also for the safe operation of that equipment 2. Plunger Lift Lubricator Standards must be governed like any other form of artificial lift or wellhead component 29

Contact Details EnForm Phone: 403.516.8000 Toll Free: 800.667.5557rvicenform.ca www.enform.ca API 1220 L Street, NW Washington, DC 20005-4070 USA 202-682-8000 ISO 1, ch. de la Voie-Creuse CP 56 CH-1211 Geneva 20 Switzerland +41 22 749 01 11soorg NACE 1440 South Creek Drive, Houston, Texas 77084-4906 1-800-797-NACE(6223)e @nace.org www.nace.org Presenter Séan Emery Weatherford International 1200, 333 5 th Avenue S.W. Calgary, Alberta Canada 403-693-7599 Sean.emery@ca.weatherford.co m 30

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. 31

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. 32