Thursday, March 29, 2012

MPD makes the difference in offshore Indonesia offshore gas development program

By Linda Hsieh, managing editor, and Katherine Scott, editorial coordinator


An offshore well in Indonesia’s Ujung Pangkah field went from a potential failure to an invaluable success once managed

Clifford Lang (right), Hess, was among a panel session looking that examinedat the state of play of MPD and UBO technologies from the operator’s perspective at the 2012 MPD and UBO Conference and Exhibition on 21 March in Milan, Italy. The session was moderated by Dag Ove Molde (from left), Statoil, and included Claudio Molaschi, Eni, and Dave Elliott, Shell.


pressure drilling (MPD) was deployed, said Clifford Lang, drilling and completions manager of Europe, Eurasia and North Africa for Hess. “We surveyed the rig for MPD prior to getting on location … as a precaution,” he said during a presentation at the 2012 IADC/SPE MPD and UBO Conference and Exhibition on 21 March in Milan, Italy.


The first well in the gas-drilling program was completed without losses. However, on the second well, during the drilling of a sidetrack through carbonates in the reservoir section, “we hit the cave,” Mr Lang said. Losses totaling 96,000 bbl were experienced before the company began bullheading seawater with high-viscosity pills to push the gas back into place. The goal was to pull the pipe at least partly out of the hole. “We had to get out of the hole to get MPD in place,” he said.


A second gunk pill that was pumped down at 4,652-ft MD gave the team a chance to get out of the hole. Reduced hydrostatic pressure on top of the gunk pill allowed it to support the fluid above and allowed surface pressure to be bled off to zero.  A 9 5/8-in. drillable subsurface plug was set at 4,325-ft MD, and a cement plug was set on top to secure the well. “That took us 10 days of pain and losses,” Mr Lang said.


Once the team rigged up the MPD equipment and went back in with the drill string, the well reached TD and became Hess’ most productive on the field at 55 million standard cu ft/day. Mr Lang believes that surveying the rig for MPD in advance and having a contract in place with a service company was key to turning the well around when “we were staring at failure in the face.”


MPD has reduced the operational NPT associated with losses in the reservoir section to virtually zero, he added. Hess now makes sure that it has MPD equipment hooked up prior to seeing potential issues drilling through carbonates. Specifically on the Ujung Pangkah field, the company ended up deploying MPD twice out of the first six wells. “(MPD) enables us to do things we wouldn’t have been able to do. It will be used on all future wells and exploration wells in that area. Wherever we have carbonates we will be using this,” Mr Lang said.


Instead of fighting Mother Nature with LCM during loss situations, working with her natural pressure profile through the use of MPD techniques could save significant costs and time. “It will save you a fortune,” Mr Lang stated. “It’s safe, practical and it allows us to do so much more than we expected to do with these wells.”


Platinum sponsors for the 2012 SPE/IADC MPD & UBO Conference & Exhibition were Eni and Schlumberger; gold sponsor was Halliburton.


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Successful dual-gradient system follows nature’s pressure profiles

By Katie Mazerov, contributing editor

A dilution-based dual-gradient system dilutes the riser and creates a different pressure profile at the seabed.


A dilution-based dual-gradient system has been shown to deliver significant cost reductions and enhanced well control in deepwater wells. “This is an alternative way of creating a dual-gradient profile in the wellbore, not by means of pumping heavy mud from the seafloor up to the surface but by diluting the riser and creating a different pressure profile at the seabed,” said Luc de Boer, president of Dual Gradient Systems, which collaborated with Transocean in the development of the system. Mr de Boer discussed the testing process in a presentation at the IADC Dual Gradient Drilling Seminar on 19 March in Milan, Italy.


The premise of Transocean’s continuous annular pressure management (CAPM) system is based on using two stable mud densities in the wellbore, a specially designed centrifuge and a rotating control device (RCD) near the top of the riser below the slip joint rated to 1,500 psi.


The $5 million research and development project was conducted over a five-year period. The system is designed to follow the earth’s profiles – the ocean being low pressure and the earth being high pressure – rather than fight them, Mr de Boer noted.


“Initially, the system was designed conventionally, where heavy mud was pumped down the drill string through the bit and up the annulus,” he explained. When Transocean joined the project, the company suggested the use of an RCD to pump the mud. “At the bottom of the riser, the same mud without barite is injected into the return mud stream, creating a lower-density mud in the riser,” he said. An RCD at the top of the riser holds back pressure and directs flow to a choke manifold. Flow meters accurately track barrels in and out of the well. “The control device is at the surface, which also services as a very good safety feature,” he added.


Continuous separation


Testing began in 2002 with the concept to separate the oil-based mud into a high-density mud and a nearly un-weighted mud on a continuous basis. A second phase was launched in 2004 testing an oil-based mud and a water-based mud. In a third test in 2006, a special centrifuge unit with better capacity than a single centrifuge unit was deployed. The final test in 2007 achieved the desired separation process with a specially designed centrifuge that increased the flow from the normal pump rate of 50 gal/min to 600 gal/min, Mr de Boer explained.


In a comparative test in a deepwater Gulf of Mexico well, the conventional single-gradient well design included nine casing and liner seats to total depth (TD). The dilution-based, dual-gradient well design had six casing and liner seats, with a high-density mud weight of 12.8 lb/gal to 16.3 lb/gal, a riser mud weight of 9.9 lb/gal to 11.3 lb/gal and a dilution ratio of 2.4 to 3.1. “The reduction in casing strings, at $10 million per string, is significant,” Mr de Boer pointed out.


A third scenario featured a dual-gradient drilling (DGD) design with dilution below the mud line. The system resulted in four casing and liner seats, with a high-density mud weight of 17.3 lb/gal, riser mud weight of 10.9 lb/gal and a dilution ratio of 2.9. “We call this the prize,” Mr de Boer said. “This design takes more work to get the dilution below the seabed, but it gives us extended reach.” The dilution-below-mudline system also can be used for low-cost open-hole sidetracks and for low-cost exploration drilling.


With the DGD dilution system, all equipment is on the surface and can be repaired with little downtime; the CAPM riser system and flow controls enhance well control. The system also can be switched from dual-gradient to single gradient in an hour if necessary, Mr de Boer said.


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The essentials of dual-gradient drilling: Several variations under development

By Linda Hsieh, managing editor, and Katherine Scott, editorial coordinator


Although dual-gradient drilling has been around for years, many in the industry appear to remain unclear as to how the technology works or what it does. In a presentation at the 2012 IADC Dual Gradient Drilling Seminar on 19 March in Milan, Italy, AGR Subsea senior technology advisor Roger Sverre Stave reiterated IADC’s definition of dual-gradient drilling as a variation of managed pressure drilling that uses “two or more pressure gradients within selected sections to manage the well pressure profile.”

Roger Sverre Stave, AGR Subsea, noted that a significant industry focus on dual-gradient technologies has led the IADC Dual Gradient Subcommittee to take on many new initiatives, including organizing the 2012 IADC Dual Gradient Drilling Seminar on 19 March in Milan, Italy.


Whereas in conventional drilling, bottomhole pressure (BHP) is a function of single-gradient mud, dual-gradient methods make up BHP “based on multiple columns of fluid such that bottomhole pressure is a sum of two or more columns of fluid,” Mr Stave said.


“As long as the pore and frac pressures are increasing with depth, you will create a pressure gradient this is more compatible than pore pressure and frac pressure by introducing dual-gradient technologies,” he said. Effectively, dual-gradient drilling opens the “drilling window” by increasing margins. The technology also provides opportunities for faster recognition of instability, including loss and influx, as well as faster response to reestablish pressure balance.


Several variations of dual-gradient technology are under development within the industry, such as controlled annular mud level technologies and mudline pumping riserless technologies. Dual-gradient mudlift is another example, which is expected to be deployed by Chevron later this year in the deepwater Gulf of Mexico (GOM). Statoil too plans to deploy “light” versions of two variations of dual-gradient drilling in a pilot project in 2013, according to a separate presentation at the same seminar by John-Morten Godhavn, principal researcher for Statoil.


“And we have other technologies that create the dual-gradient effect by diluting and lightening the gradient in annulars of the drilling riser either by gas or fluid,” Mr Stave added.


Dual gradient goes back to as early as 1975 with the Howell patent and has been studied under various joint industry projects through the years, such as the MudLift JIP with ChevronTexaco, Conoco, BP and Hydril, and DeepVision with BP, ChevronTexaco, Transocean and Baker Hughes. “Shell SubSea Pumping system was also one major effort at the time with a seawater-filled riser but also having a separator system on the seafloor to pump out the solids and leave the cuttings behind on the seafloor,” Mr Stave said.


While only the MudLift JIP made it through to a successful field trial in 2001, Mr Stave notes that the need for dual gradient technologies has certainly not disappeared, particularly with the growing importance of the ultra-deepwater market in the GOM. “What I have seen is more industry focus along with various initiatives post-Macondo, but more related to safety now than previously when it was more focused on drilling efficiency,” he said.


Further, Mr Stave believes that ultra-deepwater leases and advanced drilling rigs may require dual-gradient drilling as an enabling technology going forward, meaning that it is impossible or very hard to drill those prospects without the dual-gradient drilling technique to manage the equivalent circulating density or dynamic friction loses. The technology allows the pressure gradient to fall more naturally within the pore and frac pressures of the well, he said.


Mr Stave acknowledged that dual-gradient technologies have been difficult to commercialize due to the investments required, as well as equipment integration issues. However, the concept remains on the agenda for many companies who are seeking to develop ultra-deepwater resources. “We are moving forward and we are making progress, but it takes a long time to implement these kinds of technologies.”


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Candidate selection could be key to successful underbalanced drilling project

AppId is over the quota
AppId is over the quota
A successful UBD operation begins with the right candidate selection and good communication among the stakeholders.

By Katie Mazerov, contributing editor

Upfront planning and appropriate candidate selection are critical to achieving success in underbalanced drilling operations, especially as the industry begins to look to deepwater as the next frontier for the application, Patrick Brand, executive VP for Blade Energy Partners, said in a presentation at the 2012 SPE/IADC Managed Pressure Drilling & Underbalanced Operations Conference & Exhibition, 20-21 March in Milan, Italy. “Underbalanced drilling (UBD) has been around for more than 100 years in one form or another, but there are still issues that we as an industry see every time we get into underbalanced projects,” Mr Brand said.

The key for success in UBD lies in the preliminary work, starting with candidate selection, or the process of choosing the right reservoir for the application of underbalanced drilling, he said. “UBD cannot create value where it does not exist. … If you don’t get the candidate right, you are bound to have a failed project. Companies that try and short-cut this phase of the work ultimately run into accidents, nonproductive time (NPT) and failures.

“Doing the work up front and getting it right leads to proper equipment, procedures and training, which is what makes the project successful,” he continued. At the center of that process is good communication among all stakeholders involved in the project.

Mr Brand maintains there are still several concepts about UBD that the industry has not fully grasped. For one, UBD is a reservoir exploitation tool first and foremost, not a drilling technique, he said. “We’re trying to enhance the reservoir by increasing productivity and ultimate recovery or determine the reservoir’s characteristics.” He identified reservoir characterization as a process where many companies are missing out on an opportunity to use clean data to determine the true permeability of the reservoir, which can aid in the final completion design. “For example, knowing where the fractures are can really help us get the most out of the reservoir.”

Do your homework

Another issue concerns the over-estimation of equipment required for multi-phase hole cleaning. “We all work under the same general rules, but we’re learning that often these rules are very conservative and that we can easily drill wells at lower parameters,” Mr Brand said. “We have actually killed projects for problems that don’t exist.”

There is also confusion in the industry as to when to use UBD versus managed pressure drilling (MPD). “MPD has really taken over in a lot of areas, but knowing when to use the right technique is very important,” he said. It’s also critical to understand the chemical interaction between produced and pumped fluids and equipment. “In cases where oxygen or produced fluids are pumped with gas, if you don’t do your homework correctly, you can have problems with elastomers or chemical reactions.”

In deepwater, Mr Brand believes the biggest challenge for deployment of UBD involves the loads on the riser. “If we’re looking at taking the returns of multi-phase fluid up in that riser, we need to make sure we can control the well safely, especially when we encounter the possibility of leaks or anything else in the rotating control device, and the unloading of that riser,” he said.

In addition to deepwater applications, challenges for UBD include tripping and running completions efficiently, wellbore stability, barrier policies, equipment certification and specifications, and low-rate metering/multi-phase metering. “It’s easy to drill underbalanced,” Mr Brand said. “The challenges come in getting out of the hole and getting the completion in the hole. We need to do a lot of work in that area and get better tools for doing it effectively.”


View the original article here

Wednesday, March 28, 2012

Hot spot for geothermal research - Connexus

 

The Christensen Diamond Products manufacturing plant opened in Celle, Germany, in 1957. The facility built diamond core heads and drill bits and later expanded to make downhole tools. In 1977, the Celle engineering and manufacturing team introduced the Navi-Drill™ line of downhole drilling motors.


After a series of mergers and acquisitions that began in the late 1970s, the facility became part of Baker Hughes in 1990 with the acquisition of Eastman Christensen. Other innovations developed in Celle include the industry’s first steerable motor system and the AutoTrak™ rotary steerable closed-loop system.


The Celle Technology Center (CTC), as it’s called today, was expanded in 2009 to support joint technology developments, including geothermal, with operators and local universities. Since its grand reopening, the CTC is also home to the Baker Hughes Center of Excellence for geothermal and high-temperature research and development.


In 2009, Baker Hughes and the Niedersachsen (Lower Saxony) state government jointly launched a multimillion euro, five-year cooperative university research project aimed at improving the technology for generating geothermal energy from very deep (4000 m to 6000 m) [13,123 ft to 19,685 ft] geological formations. With guidance from Baker Hughes scientists in Celle, Lower Saxony’s technical universities will combine their acknowledged strengths in geosciences, material sciences, drilling technology and technical systems in order to generate leading-edge research results for Baker Hughes to integrate into the development of sustainable and marketable products and services.


The Lower Saxony state government is also providing financial support for Baker Hughes’ research and development of high-temperature electronics for use in drilling and evaluation, as well as completion and production applications. In addition, Germany’s federal government has awarded Baker Hughes a cofunded project to develop cost-efficient drilling technologies for geothermal wells.


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US Steel Tubular Products to open Innovation & Technology Center for industry customers

By Joanne Liou, editorial coordinator


U.S. Steel Tubular Products (USS) will open the Innovation & Technology Center at its Houston offices on 28 March. The 10,000-sq-ft facility will serve as a training and education facility for customers, stakeholders and the community; it will be open to host events, such as lunch-and-learn sessions, industry association meetings and employee training. The center features six areas of interest devoted to research and development innovations; services and connections; manufacturing; inspection and testing; raw materials; and an overview area showcasing the company’s history.


The six areas reflect the company’s integrated supply chain and vision. “We started this vision of customer-driven tubular focus within our tubular segment,” Douglas R. Matthews, senior vice president – tubular operations of USS, said at a media event last week. “We need to be a stronger supporter – supporting technology developments that help our customers do their job easier, faster, better, cheaper.” The display of artificial iron ore, coke and limestone show the process of selecting and mining the materials. In the manufacturing exhibit, visitors can learn about the process and how materials are refined.


USS’ technologies and services are featured in the products, services and connections area of the center. Some of the company’s latest advances, such as the USS Buttress Thread, are showcased in the R&D innovations area. The interactive inspection and testing exhibit allows guests to test the performance capacity of various products through a touch-screen virtual testing system. Throughout the center, videos, posters and simulations give visitors an in-depth look and understanding of different technologies and process involved within the steel and tube-making process.


“We’re excited about this step in the evolutionary process of being tubular focus and customer driven,” Mr Matthews said. “We’re making sure our customers are at the forefront and identifying what their needs are and being responsive and proactive to supporting those needs, and we feel that this grand opening of our innovation and technology center is a step in that direction.”


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Geothermal Energy Production - Connexus

Today, there is more interest than ever in geothermal power. A 2010 report by the Geothermal Energy Association called “Geothermal Energy: International Market Update” states that both the number of countries producing geothermal power and the total worldwide geothermal power capacity under development appear to be increasing significantly.


The report found that between 2005 and 2010, Germany was the fastest growing geothermal power producer in the world with a whopping 2,774 percent increase in installed megawatt capacity.


Increased awareness of “clean” energy to reduce CO2 emissions, concern over continued world oil production and rising costs of energy exports are all helping to expand Germany’s renewable energy market. But perhaps the biggest driver powering the growth is the country’s Renewable Energy Sources Act—a very ambitious plan to replace 30 percent of the total electricity consumption in Germany with renewable energy by 2030. By 2050, the goal is 60 percent.


Germany announced its new energy goals at the end of the last millennium and today is one of the leading industrial nations in the renewable energy sources sector, according to the country’s Federal Ministry for the Environment, Nature Conservation and Nuclear Safety.


Helping fuel this trend toward climate-friendly energy are government incentives in the form of grants to industries and universities to research and develop enhanced geothermal technologies, and 20-year fixed feed-in tariffs to power plant operators that give priority to electricity that comes from renewable energy sources, such as geothermal—making higher risk and higher cost projects more feasible.


This increase in geothermal drilling and production has made geothermal the fastest growing business for Baker Hughes in continental Europe. Plus, with the Baker Hughes Center of Excellence for geothermal and high-temperature research and development in Celle, Germany, the company is well positioned to support the growing demand for products and services, as well as the government’s ambitious target.


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Special webcast: Defining challenges and potential solutions for MPD in deepwater drilling

Posted on 27 March 2012

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IADC group VP/publisher Mike Killalea sat down with David Pavel, global director of business development for Weatherford International, and Gavin Humphreys, manager – technology and new business for Stena Drilling, at the 2012 SPE/IADC Managed Pressure and Underbalanced Operations Conference & Exhibition in Milan, Italy on 20 March to discuss the challenges and possible solutions to MPD applications in deepwater. Key barriers to implementation include issues related to planning, procurement and operations. “Right now the challenge for drilling deepwater MPD is getting the fleet that exist in the world today … to a point where we can deploy this type of equipment and procedure on these rigs,” Mr Pavel said.

Read more about MPD-ready rigs in here.


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Continuous circulation systems build healthier wells, reduce risk in difficult environments

 

By Linda Hsieh, managing editor, and Katherine Scott, editorial coordinator


Just as humans can be injured even by a short interruption of the blood supply through our arteries and veins, wellbores also need continuous flow through the pipe and annulus to prevent potential harm. That was the analogy used by Angelo Ligrone, vice president logistics for Eni, at the 2012 SPE/IADC Managed Pressure Drilling and Underbalanced Operations Conference and Exhibition on 20 March in Milan, Italy. He presented Eni’s work on two proprietary technologies – a circulation device called the e-CD and a near-balance drilling technology called e-NBD. The company has used both to significantly reduce risks during the drilling process, particularly in difficult deepwater drilling environments.

Angelo Ligrone presented work related to Eni’s e-CD and e-NBD are proprietary technologies, which that enable the company to maintain constant bottomhole pressure with continuous circulation, at the 2012 SPE/IADC Managed Pressure Drilling and Underbalanced Operations Conference and Exhibition on 20 March in Milan, Italy.


“If we can get performance but without safety, this is not performance. Safety and performance have to come hand in hand,” said Mr Ligrone, who until recently served as vice president of drilling technology for Eni.


The e-CD, introduced in 2005, is a system that allows for continuous mud circulation to maintain constant bottomhole pressure while making up or breaking out drill pipe connections during drilling operations. “We have controlled the ECD (equivalent circulating density) throughout the drilling process, thus eliminating mud pressure fluctuations,” Mr Ligrone explained. This in turn prevents problems such as wellbore instability, as well as reduces nonproductive time.


In 2010, Eni introduced e-NBD, a technology born out of the company’s success with the e-CD. “By adding a rotating BOP and bringing it down on top of the conventional BOP stack and the active choke system, the e-CD becomes the e-NBD system,” he said. The technology allows for the maintenance of constant bottomhole annular pressure at all times while circulating and to manage the annular dynamic hydraulic pressure profile. “The benefits indeed are well control and safety first of all … and improving hole conditions.”


He added that e-NBD is an enabling technology helping Eni get to targets where conventional technologies cannot, particularly for operations within narrow pore/fracture pressure gradients, as well as for HPHT and underbalanced operations. In March 2008, for example, Eni completed its first e-NBD HPHT well in Egpyt at 5,450 meters TD; this “nightmare” scenario involved 2.25 sg mud, 2.23 pore gradient and 2.26 equivalent mud weight fracture gradient.


In another example offshore Libya, the e-NBD system was deployed from a floating rig to reenter a temporarily abandoned exploration well where drilling activities had been stopped due to conventional drilling limits. The bottomhole target was reached without problems using e-NBD, Mr Ligrone said.


Onshore as well, the technology has been used in difficult drilling environments. A vertical land well in Pakistan used e-NBD to drill the 10 5/8-in. and 8 ½-in. sections to reach the gas targets. “The decision to drill the section with the e-NBD system was taken based on the fact that such phases were explorative, and the only data available from one reference well in the area was showing a high formation pressure with an incremental trend of the pore pressure gradient,” he said. The reference weight had been suspended due to continuous formation pressure increase and strong gas showed a high percentage of gas present and well construction limitations, he continued.


“I will stress again that safety and performance have to go hand in hand. We cannot have performance without safety or safety without performance,” Mr Ligrone emphasized. “They are essential in ensuring a sustainable drilling business. Continuous circulation is recognized as a key factor for safer and faster drilling.”


e-CD and e-NBD are trademarks of Eni.


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Tuesday, March 27, 2012

Baker Hughes to Present at Howard Weil Energy Conference

HOUSTON, March 26, 2012 /PRNewswire/ -- Baker Hughes (NYSE: BHI) announced today that its President and CEO Martin Craighead will be presenting on March 27, 2012, at the Howard Weil Energy Conference in New Orleans, Louisiana. The presentation materials are available on the "Events & Presentations" page at:  www.bakerhughes.com/investor.  


Baker Hughes is a leading supplier of oilfield services, products, technology and systems to the worldwide oil and natural gas industry. The company's 57,000-plus employees today work in more than 80 countries helping customers find, evaluate, drill, produce, transport and process hydrocarbon resources. For more information on Baker Hughes' century-long history, visit www.bakerhughes.com.


Forward Looking Statements:


This news release (and oral statements made regarding the subjects of this release) contain forward-looking statements within the meaning of Section 27A of the Securities Act of 1933, as amended, and Section 21E of the Securities Exchange Act of 1934, as amended, (each a "forward—looking statement"). The words "anticipate," "believe," "ensure," "expect," "if," "intend," "estimate," "project," "forecasts," "predict," "outlook," "aim," "will," "could," "should," "potential," "would," "may," "probable," "likely," and similar expressions, and the negative thereof, are intended to identify forward—looking statements. There are many risks and uncertainties that could cause actual results to differ materially from our forward-looking statements. These forward-looking statements are also affected by the risk factors described in the company's Annual Report on Form 10-K for the year ended December 31, 2011 and those set forth from time to time in other filings with the Securities and Exchange Commission ("SEC"). The documents are available through the company's website at http://www.bakerhughes.com/investor or through the SEC's Electronic Data Gathering and Analysis Retrieval System (EDGAR) at http://www.sec.gov. We undertake no obligation to publicly update or revise any forward—looking statement.


CONTACTS:


Media Relations:         Teresa Wong, +1.713.439.8110, teresa.wong@bakerhughes.com
Investor Relations:      Adam Anderson, +1.713.439.8039, adam.anderson@bakerhughes.com


SOURCE Baker Hughes


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Texas agency approves mobile system to recycle produced, flowback water

Posted on 26 March 2012


Texas-based Water Rescue Services has received approval from the Railroad Commission of Texas to operate a mobile recycling system to recycle produced and flowback water created through the hydraulic fracturing process.


“Only a handful of companies meet the stringent requirements to recycle flowback and produced water, which allows for substantial gains in efficiency while performing on location,” said Wes Williams, president of Water Rescue Services. “We believe our customers with active Texas drilling operations will enjoy a significant market advantage when utilizing Water Rescue’s mobile treatment technology to recycle water on site, thus lowering costs and saving time through this recycling process.”


Water Rescue Services recently signed a strategic alliance with Select Energy Services that gives Select access to a mobile water treatment and recycling technology through Water Rescue’s electro-coagulation units.


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Houston college, university programs give students an edge into industry

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In the mecca of the oil and gas industry, Houston-area college and university programs are giving students a leg up into the industry, from field services to petroleum engineering. As the industry continues to expand, these institutions recognize the demand and opportunity to provide an educational background that leads to a career in the realm of oil and gas.


Companies have actively recruited graduates of Lone Star College’s drilling program, which began in January 2011. In one semester (16 weeks), students, who include veterans and professionals of other industries, can graduate with a marketable skills award certificate, which makes them a top candidate to local service companies. For more information on Lone Star College’s program, click here.


One of only a few programs in the US, the undergraduate petroleum engineering program at the University of Houston has received support from industry and has worked with companies to provide students with internships through their college career. The program, which began in fall 2009, was developed in response to the industry’s need for more engineers. For more information on the University of Houston’s program, click here.


In these videos, DC editorial coordinators Joanne Liou and Katherine Scott provide an overview of these programs being offered at Lone Star College and the University of Houston.


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From the President: IADC stands ready for the future

By Lee Hunt, IADC president, 1990-2012

Dr Lee Hunt, IADC president, 1990-2011


It’s been a distinct pleasure to have served as president of IADC for the past 22 years and to have served with the association before that for six additional years. The time comes for a changing of the guard at the top, and I’m pleased to announce that my successor is Stephen Colville, who most recently was vice president of communications for Shell’s projects and technology business. Stephen has more than 30 years’ experience in government policy and relations, corporate public affairs and lobbying with organizations such as Chevron and the UK Department of Trade and Industry.


While it may seem an unusual step for an association representing drilling contractors to appoint someone with operator/producer experience, lessons learned from Macondo have taught us that we are all stakeholders in this industry. We are in this together. It takes mutual understanding of how we each operate in order to achieve collaborative success.


Over the past nearly three decades, the association has emerged as a global authority for the drilling industry. Our membership has expanded to drilling contractors, operating companies and service companies headquartered around the world, truly achieving a global membership base.


Guiding us through this expansion has been the principle of “Do what is right for the rig.” The rig is the great equalizer in service to our membership, no matter how many rigs or how few in the fleet, no matter the size of the company, and no matter whether they are geographically localized or globally positioned. IADC believes that by pursuing the best interests of the rigs, we are acting in the best interest of our member companies.


In the process, keeping our focus on the rigs means we’re also keeping our feet planted firmly. Our efforts are directly beneficial to the work force of our members, from roustabout to CEO.


Over the years, we also have achieved an increasing level of professionalization in the IADC staff. Many have advanced, professional degrees. All have years of industry experience. Most are recognized as leading experts in the areas they staff, and this makes them very valuable partners with our members.


Our staff has worked and will continue to work to be proactively relevant to the daily business of our members. Companies in today’s drilling business want options and speed, and IADC has a responsive staff to provide what they need.


I am excited and encouraged to deliver into the hands of my successor a highly successful, capable, competent, professional and outstanding IADC. I look forward to watching us rise to the industry’s future challenges and doing what it will take to move IADC to the next level. I know we can. I know we will.


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Monday, March 26, 2012

New software modules enhance drilling riser monitoring system

By Katherine Scott, editorial coordinator

 Pulse Structural Monitoring, an Acteon company, unveiled three new software modules developed to complement its DrillASSURE drilling riser monitoring system software during a launch event at the 2012 IADC/SPE Drilling Conference and Exhibition in San Diego, Calif., on 7 March. Developed in conjunction with 2H Offshore, the new modules are DrillJOINT, DrillWINDOW and DrillADVISE and add to the current modules DrillFATIGUE, DrillTRANSIT and DrillVIV. The new interfaces are designed to help operators and contractors optimize use of their drill joint inventory, identify optimum operating windows and conduct safe campaigns by constantly analyzing conditions in real time.

“Improvement in safety, productivity and efficiency are increased and lower operating costs are the major benefits we see for integrating the software into (a company’s) operations,” said Jeff Diestler, business development manager for Pulse.

The DrillJOINT module is a complete inventory detailing the location, availability, technical specification, previous use and maintenance history of the owner’s drill joint. It enables  operators and contractors to source riser joints and assemble a robust drilling stack on screen prior to drilling, saving time and enhancing safety and efficiency.

DrillWINDOW offers pre-drilling analysis of static and dynamic operating windows and hang-off envelopes. The user inputs known environmental data, such as wave height, current velocity and mud density, then the software evaluates these data points against approved safety margins to calculate the fatigue life of the drill stack.

Lastly, the DrillADVISE module calculates parameters such as vessel position, flex joint angles and environmental conditions, then presents easily interpretable data in real time to guide the user on proceeding safely and efficiently. Feedback is presented in colors: Green shows all parameters are within thresholds, amber indicated caution or corrective action are required, and red is an instruction to disconnect immediately.

The combination of hardware and software modules creates the DrillASSURE system, which provides information to support day-to-day drilling operation and longer-term integrity management. The system uses real-time software in conjunction with inputs from sensors on the topside vessel, lower marine riser package and along the length of the riser.

“With our DrillASSURE systems (we can) monitor fatigue accumulation on critical components,” Mr Diestler said.


View the original article here

Reservoir drives choice of RSS vs mud motors

Rotary steerables suit narrow formations; mud motors may be more cost-effective in broader boundaries


By Eric Malcore, Weatherford International Ltd


The ratio of directionally drilled wells to vertically placed wells is increasing. Access to progressively harder to reach reserves is driving more complex well geometries, which predicate the use of rotary steerable systems (RSS) to enhance rate of penetration (ROP), improve borehole quality and reduce torque and drag and stick slip. The various RSS technologies available today have revolutionized the drilling process in horizontal and deviated wells by facilitating greater intermediate reaches and longer laterals, allowing casing to be run more easily and allow proper weight transfer.


The service industry estimates that RSS technologies account for approximately $3.5 billion of the estimated $15 billion directional drilling market. The dynamics are shifting in favor of RSS.


Although not a new technology, high-performance mud motors also have become an accepted and reliable method in directional drilling operations, in many cases providing a cost-effective alternative to more costly rotary steerable tools.


Knowing when to choose a rotary steerable system and when to use a high-performance mud motor is critically important to optimize the drilling project from both an engineering performance and a cost perspective.


Many horizontal or deviated wells are extremely difficult or impossible to drill without an RSS. A key benefit of RSS technology is that it directs well trajectory without sliding, a condition that impacts the stability and orientation of the drill string to rotate in one direction. Without proper rotation, the entire drill string can stick to the borehole wall, making it difficult to achieve the desired weight transfer to the bit to achieve planned penetration rates. RSS tools provide continuous rotation of the drill pipe, minimizing the risk of the pipe becoming stuck or buckling.


Sliding also creates more waste because the lack of rotation keeps the fluid in a static state, making it more difficult to remove cuttings. The cuttings then pack off around the bottomhole assembly, causing the drill string to stick. With the continuous rotation enabled by rotary steerable tools, however, the friction holds the cuttings in suspension, allowing the fluid to create a vortex around the drill string to provide consistent hole-cleaning.


RSS technology also reduces drag, allowing extension in well reach, especially important in horizontal applications. Rotary steerables typically deliver a smooth in-gauge wellbore and control the toolface at the bit, which provides more accurate directional control and less tortuosity. They also enable the use of logging-while-drilling (LWD) azimuthal sensors to obtain full borehole images.


Applying Precise Directional Control


An important factor in rotary steerable systems is that they provide precise directional control and are therefore suited to narrow zones as tight as 1 ½ ft. In that regard, the tools also can provide geosteering in these narrow reservoirs, where corrections can be made in real time without sliding.


An RSS was used to successfully drill and complete a section of a horizontal water-injection well with an 8 ½-in. hole in Abu Dhabi.


Using Weatherford’s Revolution rotary steerable system, the operator was able to drill 2,200 ft (671 meters) at a depth of 8,725 to 12,918 ft (2,659 to 3,937 meters) in less than 90 hrs in one run, saving 41 hrs of drilling time and achieving a significant cost savings without nonproductive time.


The same system was used in another Abu Dhabi water-injection well to facilitate drilling and completion of an ultra-narrow, 6-ft zone with a 6-in. hole size and a run length of 4,193 ft (1,278 meters).


The operator was able to drill almost 20 ft (6 meters) deeper than anticipated, reaching a target that otherwise would have been missed.


In an onshore Saudi Arabian field prone to lost circulation, differential sticking and hydrogen-sulfide challenges, the same technology drilled a 3°/100-ft (30-meter) dogleg section with a 6 1/8-in. hole in an extended-reach horizontal water-injection well to a target depth of 16,856 ft (5,138 meters). Average ROP was 35 ft/hr (11 meters/hr). Prior to deployment of the system, optimal ROP had been difficult to achieve with a steerable motor assembly.


The system drilled a total of 7,316 ft (2,230 meters) in one run, achieving a field run-length record and meeting the operator’s goal to minimize excess tripping time. The operation saved 24 hours in drilling time and associated costs and allowed the operator to avoid stuck-pipe and lost-in-hole risks that occur in similar extended-reach wells.


In the Bay of Bengal in Eastern India, the same RSS technology performed a record-breaking shoe-to-shoe run in a claystone formation, with interbedded sandstone, marl and calcareous clay. The deep exploratory well had an inclination of 34°. The system drilled a 12 ¼-in. in-gauge hole and then drilled to a measured depth of 4,918 ft (1,499 meters) to improve the average ROP and reduce the number of wiper trips and backreaming. Drilling time was 192 hrs, with an average ROP of 25.6 ft/hr (7.8 meters/hr).


RSS technology has been enhanced in recent years by the development of motorized rotary steerable systems, where a power section placed on the RSS tool provides additional rpm and torque while still achieving the benefits of control and eliminated sliding. This hybrid-type application is increasingly being used in regions such as the Middle East, where the rock and carbonates are especially hard.

High-performance mud motors can save 50% or more a day over rotary steerable systems. Mud motors also can be used with smaller rigs that can’t rotate fast enough to enable the rotary steerable mechanism to perform. However, rotary steerables provide greater precision in directional control, an advantage in tight formations.


High-performance Alternative


Despite its many benefits, rotary steerable technologies can present some disadvantages, including cost, if used in situations where precise directional control is not the primary objective. For example, to justify the expense of using a rotary steerable system, the savings in rig time and other costs must be greater than the rotary steerable cost.


Rotary steerable drilling performance is delivered from the use of surface rotation, making them rig-dependent. They offer limited selection of bit sizes and speeds, and they involve greater complexities, both mechanically and electronically compared with motors. The high rotation speeds can cause premature wear to the casing and drill string, which can be slightly decoupled by using an integrated power section with the RSS, albeit adding significantly to the cost.


The replacement cost of a rotary steerable system, if it is lost in the hole, can exceed $1 million, depending on the system and size. That does not include the replacement cost of the accessory tools.


In cases where deploying an RSS is either cost-prohibitive or impractical, a high-performance mud motor can also achieve desired results, provided it is used in the proper application. However, high-performance mud motors are best suited to broad target areas and zones that require less precision, or in doglegs that are too aggressive for an RSS.


Used since the early 1990s for a multitude of oilfield applications, high-performance mud motors achieve greater torque and ROP than conventional mud motors. The mud motor leverages the reduced rubber profile in the power section to gain additional torque, which creates less deformation as the rotor spins. The reduced rubber deformation translates into more torque for the bit, which in turn allows for higher ROP and more aggressive bit designs.


For operators, the key advantage is that a high-performance mud motor can result in daily cost savings of 50% or more over an RSS. Lost-in-hole costs also are significantly lower; a 6 ¾-in. high-performance mud motor has a typical lost-in-hole cost of $168,000.


High-performance mud motors can often out-perform standard, non-motorized RSS, which depend on the rig rotary table to spin the bit. The motor power component of the high-performance mud motor, on the other hand, provides bit rotation and power directly to the bit. High-performance mud motors also can be used in situations that involve smaller rigs that can’t rotate fast enough to enable the rotary steerable mechanism to perform.


Another benefit is that all bit types and sizes can be used with a high-performance mud motor, making it useful for a variety of applications, including situations where a particular bit that is not compatible with an RSS must be run.


High-performance mud motors do, however, require sliding for directional control, which typically reduces ROP. They offer poor and inconsistent hole-cleaning and poor hole gauge. Also, LWD sensors often get pushed back farther from the bit. Motor bend with high-performance mud motors can limit the drill string rotary speed or not allow any rotation at all. These factors must be considered in selecting this method of drilling.

It’s believed that rotary steerable technologies account for approximately $3.5 billion of the estimated $15 billion directional drilling market.


UAE Test Cases


High-performance mud motors have been used successfully in many deviated drilling operations and have achieved better-than-average ROP rates in three offshore test cases – the Thamama, Hith and Arab formations in the United Arab Emirates.


Seven wells in the Thamama Formation featured multiple target zones and were characterized by hard, Cretaceous limestone, but they presented no sliding issues. The operator used high-performance mud motors to drill the wells, which were not horizontal but had deviations ranging from 0° to 30° and had 8 ½-in. hole sizes.


The high-performance mud motors performed with an average ROP of 28 ft/hr (8.5 meters/hr). The best performance for the motors was 44 ft/hr (143.4 meters/hr), and the worst performance was 17 ft /hr (5.2 meters/hr). The Hith Formation also featured hard drilling conditions, with Jurassic anhydrite and dolomite rock but no sliding issues. The operator again drilled seven hole sections, all deviated but not horizontal, with 8 ½-in. hole sizes and a build section of 25° to 90°. In this case, the high-performance mud motors delivered an average ROP of 18 ft/hr (5.5 meters/hr). The highest ROP was 41 ft/hr (12.5 meters/hr), and the lowest was 9.88 ft/hr (3 meters/hr).


In the Arab Formation, featuring Jurassic carbonate/anhydrite rock, both sliding and directional control challenges were present. The lateral section was +/- 90°. Again, the operator drilled seven 8 ½-in. hole sections with high-performance mud motors.


The operation achieved an average ROP of 18 ft/hr (5.5 meters/hr). The best performance was 31 ft/hr (9.4 meters/hr), while the worst performance was 10 ft/hr (3 meters/hr).


The emergence of multiple technologies to optimize the drilling process can make selection of the proper technology confusing. Understanding reservoir properties along with diligent analysis of the well program, including formation, bit selection, directional program and other factors, must be considered when determining whether an RSS or a high-performance mud motor will achieve the best results in terms of cost and efficiency.


In tight or narrow formations where precise, directional control is needed, RSS are often the optimal choice for achieving drilling optimization and increased ROP. In zones with broader boundaries, a high-performance mud motor can provide results at a lower cost, provided issues such as sliding are carefully examined.


Revolution rotary steerable system is a trademark of Weatherford.


View the original article here

Case study: Algerian underground blowout

Incident demonstrates need for well-trained crews, adequate mud equipment


By Pedro Martinez Aguilar, Repsol Exploration; Michael Arnold, John Lee, Boots & Coots, a Halliburton Service

Partial mud-loss in the Tournasian formation occurred because the formation permeability and porosity were sufficiently high to allow loss of whole mud. An open-hole formation integrity test (FIT) should be performed after repairing the loss zone and regaining circulation to ensure the wellbore pressure integrity is still equivalent to the FIT recorded at the last shoe depth.


The outcome of a well control and blowout incident reflects how well a crew is trained and prepared. This article will discuss the sequence of a well control operation that occurred in Algeria in December 2008, which includes the influx, steps to identify the situation, operations to control the underground blowout and the response of the well.


An operator drilled a 12 1/4-in. exploratory well at 11,516 ft in the Emsian formation and set a string of 13 3/8-in. casing at 5,250 ft. A pit gain was observed, and the well was shut in. The maximum annulus pressure recorded after shut-in was 570 psi. A sudden drop in annulus pressure to 325 psi suggested lost circulation and was assumed to be in the Tournasian formation (5,305 ft to 6,180 ft), where severe lost returns had been recorded while drilling (5,580 ft to 5,740 ft).


The pressure drop made it difficult to assess the kick, thus hindering conventional well-control techniques.


Initial Well-Control Actions


Pore-pressure equivalent mud weight (EMW) at the Emsian formation was estimated to be 11.7 to 12.7 lbm/gal. The formation-strength EMW at the Tournasian formation was estimated to be 10.0 to 11.7 lbm/gal. Believing the well was experiencing losses to the Tournasian, 189 bbl of 11.6-lbm/gal mud was pumped into the casing annulus. The annulus pressure remained constant, indicating the possibility of an underground blowout.


As the annulus pressure continued to increase to 1,000 psi, 340 bbl of 11.6-lbm/gal mud was pumped down the casing annulus to reduce the pressure. A volume of 340 bbl of 9.9-lbm/gal mud was pumped down the drill string while maintaining a maximum choke-back pressure of 1,600 psi. After pumping the mud, the stabilized pressure was used to determine the bottomhole pressure. While adjusting the choke, an influx entered the wellbore.


To prevent the annulus pressure from increasing beyond 1,000 psi, batches of 13.3-lbm/gal mud were pumped periodically into the annulus. The initial volumes of mud contained lost-circulation material (LCM) to help cure the losses.


The drill pipe was filled periodically to avoid gas migration up the drill string. Shut-in drill pressure remained at 0 psi. Losses in the annulus were reduced when the LCM reached the loss zone, and the shut-in drill pipe pressure gauge began indicating pressure.


Sandwich-Kill Attempt


The hole was displaced through both the drill pipe and the annulus, “sandwiching” the influx into the lost zone.


The Emsian formation pressure was predicted to be between 12.1 and 12.7 lbm/gal EMW, meaning a 15.9-lbm/gal kill mud would overbalance the Emsian formation by +/- 3.2 lbm/gal. A cement unit was used to pump 818 bbl of 11.6-lbm/gal mud down the casing annulus, and rig pumps were used to pump 1,006 bbl of 15.9-lbm/gal mud down the drill pipe.


The operation was partially successful because the annulus pressure was still 600 psi at the end of the procedure. However, it confirmed that the bottomhole pressure and the pressure at the loss zone were higher than predicted.


Casing pressure began to increase, and drill pipe pressure remained at 0 psi. Once the casing pressure reached 2,050 psi, the drill pipe pressure increased proportionally to the casing pressure.


Communication between the annulus and the drill string was demonstrated by bleeding off 300 psi on the casing, causing a 25-psi drill pipe-pressure decrease. To keep the casing pressure as low as possible, gas was bled from the casing annulus until fluid was observed at the surface. Thereafter, the casing pressure could not be further reduced.


Circulation-Kill Attempt


Heavy mud was pumped down the drill string to control bottomhole pressure and to circulate gas out of the well. Without an accurate value for the bottomhole pressure, the proposed kill-mud weight was 13.3 lbm/gal, based on the mud hydrostatic pressure and the shut-in casing pressure but neglecting the height of the gas in the annulus.


After pumping began, drill pipe pressure dropped to 0 psi. Consequently, the choke had to be adjusted without a reference value for drill pipe pressure. The choke position was kept constant, adjusted only when annulus pressure increased. Mud losses were difficult to quantify, and the well was shut in when the rig ran out of mud.


During the mud buildup, temperature and pressure logs were run to the depth of the downhole motor in the bottomhole assembly. These logs indicated the fluid level was around 4,216 ft and the pressure at 11,411 ft total depth was 4,630 psi.


The temperature log detected disturbance around 5,600 ft, which corresponded to the depth of the Tournasian formation. The log response was interpreted as fluid movement. The repeat section of the log corroborated the crossflow at the Tournasian formation at the same depth where losses were experienced in drilling.


Annulus-Pressure-Control Attempt


Because drill pipe pressure was 0 psi, there was no reference for operating the choke. It was decided to maintain constant annulus pressure or allow it to decrease. Four LCM pills were pumped. As the first pill reached the thief zone, the losses decreased to zero. Subsequently, the pit levels increased, indicating slight gains. The volume pumped and the time when the LCM reached the surface indicated the hole was in gauge.


Once the losses were reduced to a minimum, the pump rate was increased and the choke was opened slightly to counteract the vacuum effect on the drill pipe. However, the mud level in the drill pipe dropped continuously.


When the choke opened to 1/16 in., casing pressure dropped more than expected. This jeopardized the control of the influx from the Emsian formation. The pumps were stopped, and after a few minutes, the drill pipe pressure began to increase. An influx of gas appeared to migrate inside the string, prompting the pipe to be displaced with 13.3-lbm/gal mud.


The well response indicated gas remained in the annulus, and the integrity of the Tournasian formation was still low. The kill operation resumed, and 239 bbl of 12.1-lbm/gal mud were pumped ahead of the 13.3-lbm/gal mud. The 12.1-lbm/gal mud did not reach the Tournasian formation. Consequently, the pressure in front of the weak zone at the Tournasian formation was minimized. At that point, more LCM pills were pumped.


While making repairs to the mud-gas separator, additional influxes entered the wellbore. When pumping restarted, pressure peaks suggested partial plugging of the ports in the circulation sub. As a precaution, no further LCM was pumped.

The drilling log reflects the sequence of events of an underground blowout and the well control operations that occurred in Algeria in December 2008.


Low-Choke Attempt


Changes in the annulus pressure after shutting in the well indicated that there was still a small amount of gas in the annulus or at least above the Tournasian formation. The “low-choke” method was used, attempting to control the influx from the kick zone at the bottom of the well while allowing the loss zone to deplete to a lower pressure. The basis was to hold the choke pressure equal to or slightly greater than the last recorded shut-in value while circulating as fast as safely possible. The mud density was designed to sufficiently overbalance the kick zone.


An 11.6-lbm/gal mud provided 50-psi hydrostatic pressure, in addition to annulus friction-pressure overbalance to the kick zone. The choke pressure was calculated using the casing pressure observed at the beginning of the operation, with an additional 200-psi safety factor added. The circulating rate used was as fast as the surface equipment would allow. Sixty-three bbl of 12.2-lbm/gal mud were pumped into the annulus.


An increase in drill pipe pressure suggested the presence of gas inside the pipe. The operation was stopped when bottoms-up volumes from the Tournasian and the Emsian formations were observed at the surface, and the crew prepared to reduce the annulus pressure. Operations resumed after the drill pipe was filled.


The well was monitored, and the casing pressure was bled off 100 psi to test communication between the annulus and the drill pipe. An unexpected 200-psi increase in drill pipe pressure occurred, indicating there were now two different pressure systems partially isolated by one or more packoffs in the annulus.


Once the bottoms-up volume from the Emsian formation reached surface, the choke was opened at separate intervals to bleed off 200 psi. Four intervals were needed to reduce the casing pressure to 500 psi. Because it was difficult to keep the casing pressure stable, it was decided to fully open the choke, allowing the casing pressure to rapidly bleed off to 0 psi. No returns were recorded at surface.


The pump rate was increased without result, except for a brief increase in pipe pressure, which suggested a restriction or packoff was present in the annulus. A total of 110 bbl of mud, along with 60 bbl of water, was pumped down the annulus to compensate for the fluid-level drop. The calculated fluid level was 1,371 ft.


Once pumping into the annulus stopped and the casing pressure dropped to 0 psi, the blowout preventer was opened to monitor the well. Because of the possibility of pipe plugging and annulus packoff, the pipe was worked. Five feet of pipe movement was gained, but rotation was impossible. The well was shut in with the annular preventer when mud overflowed at the bell nipple.


An attempt was made to establish circulation. Initially, the casing pressure rose very quickly to more than 3,000 psi. On the second attempt, the drill pipe pressure increased from 1,800 psi to 3,500 psi after pumping only 31 bbl of mud. With an entire drill pipe capacity of 187 bbl, this indicated the pipe was plugged. Further, the casing pressure did not reflect the pressure changes. It was concluded that one or more packoffs were present in the annulus.


An unsuccessful attempt was made to break the packoffs by pumping down the annulus. Subsequent efforts focused on bleeding off the annulus pressure and attempting to work the pipe to free the drill string, and a “lubricate and bleed” method was attempted. Large amounts of gas were recorded at surface, resulting in the annulus pressure dropping to 0 psi, and losses were also recorded. After filling up the hole with 13.3-lbm/gal mud and water, the well again began to flow. A 50-bbl mud cap using a 13.3-lbm/gal high-viscosity pill was pumped down the annulus but was unsuccessful in preventing gas from percolating to the surface.


When the annulus was bled off and the mud level was confirmed to be at surface, the pipe was worked. The drill string was torqued-up and continued to be worked. The string did not become free, moving 8 ft upward without releasing any torque.


The pipe was completely stuck, and circulation was impossible. The operator abandoned the drilled section of the well. The inside of the drill string was killed by isolating the inside diameter with cement or mechanical plugs. The drill string was perforated as deeply as possible to isolate the annulus using cement. A coiled-tubing unit was then used to cut the drill string, and the Tournasian formation was allowed to unload.


Lessons Learned


• The Tournasian partial mud-loss event occurred because the formation permeability and porosity were high to allow loss of whole mud (natural losses). This was evident by treating the losses with LCM. It is recommended that an open-hole formation integrity test (FIT) be performed after repairing the loss zone and regaining circulation. This helps ensure the wellbore pressure integrity is equivalent to the FIT recorded at the last shoe depth.


• If leak-off occurs before the equivalent shoe FIT is reached, wellbore maximum allowable surface pressure and kick tolerance should be recalculated at the loss-zone depth to accommodate the downgraded FIT.


• If creditable formation-pressure data is not available, the heaviest kill-mud weight possible should be used.


• Training in kick detection and BOP shut-in on all rigs is recommended.


The main lesson learned from this incident was the necessity for well-trained and experienced drilling crews and the importance of adequately sized mud-mixing and handling equipment.


The authors thank the management of Repsol Exploration and Boots & Coots for permission to present this paper.


This article is based on a presentation at the 2011 IADC Critical Issues Asia Pacific Conference & Exhibition, 23-24 November, Kuala Lumpur, Malaysia.


View the original article here

News Cuttings


Justin Hodges awarded for committee leadership


 Joe Hurt (right), IADC regional vice president North America and lead staff land/HSE, presents Justin Hodges (left), director of safety, claims &  risk at Hodges Trucking, with the IADC Committee Chairman’s plaque for leading the Rig Moving Committee from 2010 through 2011. Mr Hodges’ successor is Anthony Zacniewski, director of HSE at Bandera Drilling.


Geer named IADC regional director – ME & Africa


Dave Geer has joined IADC as regional director for the Middle East & Africa, responsible for coordinating and promoting the IADC’s activities in those regions.


Mr Geer has more than 34 years of experience in the drilling industry, including 15-plus years working offshore in several positions and 19 years in management positions in sales, project management and marine operations.


He has expertise in MODU operations, risk management, safety and loss control, regulations and contracts.


View the original article here

OOC awards recognize IADC SEMS work

Two IADC staff members were among 10 people who received recognition awards from the Offshore Operators Committee (OOC) on 7 December 2011 in recognition of their efforts and contributions in the development and rollout of the SEMS Toolkit last year. Thr

The Offshore Operators Committee recognized major contributors to the SEMS Toolkit on 7 December. Front row from left are Brenda Kelly and Julia Swindle, IADC; Milton Bell, ExxonMobil; and Bill Walker, Cobalt International Energy. Back row from left are Troy Nugent, Baker Hughes; Greg Duncan, ConocoPhillips; and Jeff Ostmeyer, Anadarko.


ough an OOC task force and in cooperation with the Center for Offshore Safety (COS), the toolkit was developed to address consistency and compliance with new requirements by the US Bureau of Ocean Energy Management (BOEM), as well as their effective networking with other industry representatives.


IADC’s Dr Brenda Kelly, senior director of accreditation and certification, and Julia Swindle, industry compliance specialist, attended the ceremony to receive the awards from OOC chairperson Susan Hathcock, Anadarko Petroleum.


Dr Kelly’s contributions were her leadership of the Competence Subcommittee, development of the Knowledge and Skills Documentation Tool, contributions to the SEMS Compliance Readiness Worksheet and other tools, and speaking at a series of rollout conferences held in August and September last year. Ms Swindle contributed to review of all tools and provided administrative support of the entire SEMS Toolkit development effort. IADC has seconded Ms Swindle to work with the COS for one year to help with the initial establishment of the COS.


Besides Dr Kelly and Ms Swindle, other recipients of the award included Milton Bell, ExxonMobil; Greg Duncan, ConocoPhillips; Roger Molaison, BHP Billiton; Troy Nugent, Baker Hughes; Jeff Ostmeyer, Anadarko; Kim Parker, Hercules Offshore; Ruth Rodriguez, Delmar; and Bill Walker, Cobalt International Energy. Each recipient contributed significantly to the development of the tools in the toolkit, working with subcommittees and/or providing administrative support. A significant number of IADC member companies also contributed to the effort.


“The participants on the task force have my sincerest gratitude and respect for their leadership and contributions to the SEMS toolkit, which is of immeasurable value to our industry,” said Mr Ostmeyer, who led the toolkit development effort.


Currently, the OOC SEMS Subcommittee and its task groups have concluded their work with the public release of 8 SEMS Toolkit products. Tools developed were:


• Audit checklist;


• Contractor readiness tool;


• Matrix of regulatory required training for drilling, production and marine positions;


• SEMS orientation curriculum;


• Knowledge and skills documentation tool;


• Operator-contractor agree letter templates; and


• Definitions.


These tools are available on the IADC website.


The COS will adopt all tools and maintain them going forward, although a small team from the OOC SEMS Subcommittee continues to work with the COS in the development of the Auditor Certification Program.


View the original article here

Hendricks to lead Patterson-UTI upon Wall’s retirement


William Andrew Hendricks Jr will join Patterson-UTI Energy as chief operating officer on 2 April, the company announced today. Mr Hendricks comes from Schlumberger, where he has served since 2010 as president of the Drilling and Measurements division. In addition, Patterson-UTI announced that Doug Wall, president and chief executive officer, will retire later this year. It is expected that Mr Hendricks will assume the position of president and chief executive officer upon Mr Wall’s retirement.


“Andy’s vast experience successfully managing diverse businesses – businesses with technology and geographic challenges – demonstrate his ability to lead and manage. We believe this experience and leadership ability make him the right person to help us execute our current strategic plan of continuing to grow our two core businesses – land drilling and pressure pumping in North America,” Mark Siegel, Patterson-UTI chairman, said.


He said of Mr Wall’s retirement: “We greatly appreciate the excellent leadership that he has provided; during his tenure, our company has made enormous strides. Our APEX rig programs, which numbered six rigs when he arrived, now stand at 94 new APEX rigs. Within our overall fleet of approximately 330 marketable rigs, we now have approximately 150 that are highly capable of drilling shale and other unconventional plays. Moreover, during his tenure, we have more than quadrupled our pressure pumping fleet and significantly expanded the geographic footprint of our pressure pumping business.


Mr Wall will continue as CEO until his retirement later in the year and will remain as a consultant for two years to ensure a smooth transition


Mr Hendricks received a bachelor of science degree in petroleum engineering from Texas A&M University in 1987. He also completed executive finance training at IMD in Switzerland in 2008. Mr Hendricks started his career working for Ocean Drilling and Exploration Company as a roustabout and roughneck on the Ocean Spur jackup in the Gulf of Mexico.


Click here to watch IADC group VP/publisher Mike Killalea talk with Andy Hendricks at the 2012 IADC/SPE Drilling Conference in San Diego to discuss recently launched technologies.


View the original article here

Sunday, March 25, 2012

Tubular fracturing: Pinpointing the cause

Improper heat treatment can trigger temper embrittlement in oilfield tubulars  


By Srinivasa Koneti, Samit Gokhale, Thomas Wadsworth, T.H. Hill Associates

Figure 1 (left): Intergranular cracking, characterized by triple points, rock-candy or a faceted appearance, occurs at and along the grain boundaries of metal. Figure 2 (right): Transgranular cracking occurs through or across the crystals or metal grains and is characterized by cleavage steps, river patterns, feather markings and tongues. This shows an example of a transgranular fracture on the fracture surface of low-carbon steels.


Brittle fracture of oilfield tubular components can occur due to the material having low fracture toughness – such material often presents low Charpy V-notch (CVN) impact energy values – or from exposure of the material under load to certain corrosive operating environments. A brittle fracture can show characteristics of transgranular or intergranular cracking when analyzed through a scanning electron microscope (SEM).


Intergranular cracking is the cracking or fracture that occurs at and along the grain boundaries of a metal. It is characterized by triple points, rock-candy or a faceted appearance when the fracture is analyzed through SEM. Figure 1 shows a typical example of an intergranular fracture on the fracture surface of low carbon steels.


Transgranular cracking is the cracking or fracture that occurs through or across the crystals or metal grains. It is characterized by cleavage steps, river patterns, feather markings and tongues when the fracture is analyzed through a SEM. Figure 2 shows a typical example of a transgranular fracture on the fracture surface of low-carbon steels.


Intergranular cracking is often the mode of fracture that occurs when tubular components are exposed to environmental conditions that contain aqueous H2S. Such failures promulgate the notion that detection of intergranular cracking morphology on fracture surfaces is confirmation of failure through sulfide stress cracking (SSC) or hydrogen embrittlement, even when no evidence exists for exposure to H2S or a source of nascent hydrogen.


Study of intergranular cracking related failures has shown that such failures can occur not only when the component is exposed to nascent hydrogen but can also be caused by temper embrittlement of the material resulting from improper heat treatment.


Temper embrittlement typically occurs when carbon or low-alloy steels are held at or slowly cooled through the temperature range of 375°C (705°F) to 575°C (1,065°F) during the tempering process. If the steels are tempered or slowly cooled at these temperatures, the material shows brittle characteristics (loss of impact toughness).


Steels that have experienced temper embrittlement can be restored to their original or expected toughness by heating (tempering) to 600°C (1,100°F) or above, followed by rapid cooling to below approximately 300°C (570°F).The fracture surface of a material with low CVN impact energy values (brittle material) would normally show transgranular signatures when analyzed under a SEM, whereas a ductile material affected by environmental attack, such as hydrogen embrittlement, shows intergranular separation at grain boundaries.


However, brittle fracture of a material that undergoes temper embrittlement also shows signs of intergranular cracking. Examination of the fracture surface of a component that has undergone temper embrittlement can present intergranular or mixed mode of intergranular and transgranular fracture morphology.

n Case 1 from South Texas, the pin connection of a new saver sub failed. The drilling engineer recognized the failure as a brittle failure.


Case studies of Temper Embrittlement Failure


Case 1 – South Texas, onshore US


In March 2009, while making up the pin connection (6 5/8-in. reg) of a saver sub, the pin connection on the sub failed. The operator reported that the saver sub was procured new and was in service for three days before the failure occurred.


Based on the appearance of the fracture surface, the proximate cause of the failure was readily recognized by the drilling engineer as a brittle failure. To confirm the failure mechanism, the failed sub was sent for failure investigation.

In Case 2 from Oklahoma, the pin connection twisted off while making up the pin connection of a saver sub.


Case 2 – East Oklahoma, onshore US


In May 2010, while making up the pin connection (6 5/8-in. reg) of a saver


sub, the pin connection twisted off. Based on the fracture surface morphology, the failure mechanism was identified as a brittle fracture with rapid crack propagation. To confirm the cause of the failure, the failed sub was sent for further investigation.


Case 3 – Northeast Trinidad, offshore


In April 2010, the operator was in the final stage of drilling a horizontal well that entailed the pullback of the 36-in. production pipeline. While pulling back drill pipe joint No. 90, a 7 5/8-in. reg pin connection on a sub that fastened the 42-in. hole-opener to the 500-ton swivel failed downhole.

In Case 3 from Northeast Trinidad (lower left), a pin connection on a sub that fastened the hole-opener to the swivel failed downhole.


The attached fractured sub was pulled out, and the mating portion of the sub was not recovered by fishing and subsequently resulted in losing the well. Based on the appearance of the fracture surface, the proximate cause of the failure was identified as fatigue, followed by a brittle fracture. To confirm the failure mechanism, the failed sub was sent for investigation.


Metallurgical Analysis of Failed Subs


Metallurgical analysis of the fractured pin connections on the subs was performed to identify the cause of the failure and the factors that contributed to the failure. To differentiate the fractured pin connections of the subs, the subs will be referred to as:


C1: Sub from Case 1


C2: Sub from Case 2


C3: Sub from Case 3


The fractures of all the pin connections were located in the last engaged threads of the pin connections. The last engaged threads of a connection experiences higher stresses and stress concentrations compared with the rest of the connection, making these threads susceptible to cracking. The as-received condition of the failed subs is presented in Figure 3. The C3 sub was received after initial metallurgical testing was performed by another lab. A portion of the sample that was used for previous testing was missing.

Figure 4: The fracture on the Case 1 sub showed a grainy texture and “chevron marks” that point toward the initiation site, which is typical morphology for brittle cracking.


The overall appearance of the fracture surfaces on the subs was flat and oriented perpendicular to the sub axis. The fracture on C1 and C2 exhibited a grainy texture and “chevron marks” that point toward the initiation site. This is typical morphology for brittle cracking (Figure 4).


The fracture on C3 exhibited a small fatigue region (approximately 5%) that was followed by brittle fracture. The fracture surface also had the grainy appearance (Figure 5). All three fracture surfaces present a minuscule shear lip, which is also typical of a brittle fracture. Note that the missing material was used for testing during previous investigation.


A thread profile analysis of the failed pin connections of C1 and C2 was performed to check for stretched threads, but no signs of such were observed. This gave further evidence that the pin connections on C1 and C2 failed in a brittle manner and not through ductile torsional/tensile overload.

Figure 5: The fracture on C3 exhibited a small fatigue region that was followed by brittle fracture. The fracture surface had a grainy appearance and presented a minuscule shear lip, which is also typical of a brittle fracture.


Material Testing


Material testing of the failed subs was performed to verify compliance with API Specification 7-1 and Standard DS-1 and to determine if improper material properties contributed to the failures. Tensile tests, chemical analysis and CVN tests were performed on the failed pin connection material of the subs.


Tensile strength and yield strength met the minimum requirements specified in API Specification 7-1 and Standard DS-1 for sub material. However, the CVN impact energy values did not meet the minimum requirements specified.


Typically, for the type of chemistry used, CVN values correlate well with fracture toughness. Low fracture toughness makes the material notch sensitive and typically results in predominately brittle fracture.


This indicates that the heat treatment processes were not performed properly to achieve the correct mechanical properties on the subs.


With temper embrittlement, generally, there is no detectable drop in expected yield strength, tensile strength and percent elongation of the material. A drop in the CVN values is often experienced.


In cases of extreme embrittlement, there may be a drop in the percent reduction of area. The material test results obtained on the failed subs are similar to test results commonly observed on components that have experienced temper embrittlement.


Because there is no major change in the tensile properties of the material, hardness testing cannot be used to detect temper embrittlement. Performing CVN tests followed by examination of the fracture surface of the CVN samples under a SEM are necessary to ascertain failure through temper embrittlement.

Figure 6: No signs of stretched threads were observed after a thread profile analysis of the failed pin connections of C1 and C2 was performed.


Scanning Electron Microscopy Analysis


The fracture surfaces of the failed pin connections on C1, C2 and C3 were electrolytically cleaned to remove oxides, which mask the fracture signatures. The cleaned fracture surfaces were then observed through a SEM. The fracture examination on C1 and C2 revealed features typical of transgranular fracture. The examination also revealed signatures of intergranular cracking (Figure 7).


The presence of both intergranular and transgranular features indicates a mixed mode fracture morphology. As discussed, the presence of intergranular cracking is often considered proof of failure induced through environmentally assisted cracking, such as SSC or hydrogen embrittlement. However, a saver sub is unlikely to come into contact with downhole corrosive environment.


Moreover, review of the operating conditions and environment provided no evidence of a source of nascent hydrogen. In this instance, presence of a mixed mode of intergranular and transgranular morphology on the fracture surface, combined with the low CVN values, indicates that the failure is more likely associated with temper embrittlement of the material resulting from improper heat treatment of the component.

Figure 7: The fracture examination using a SEM on C1 and C2 revealed features typical of transgranular fracture (left and middle) and signatures of intergranular cracking (left and right). The presence of both intergranular and transgranular features indicates a mixed-mode fracture morphology.


SEM analysis of C3 was also performed. However, no signatures were observed as the fracture surface was too corroded for examination.


To confirm if the subs underwent temper embrittlement, the fracture surface of the CVN impact test samples were analyzed under a SEM. Typically, examination of the fracture surface of CVN samples from a ductile material can present portions of ductile dimples and transgranular “cleavage” cracking.


This morphology is also expected on CVN samples that are machined from an inherently brittle material or a ductile material that has fractured through SSC or hydrogen embrittlement. The fracture examination of the CVN samples from the failed subs revealed mixed mode of intergranular, transgranular and some ductile dimple features (Figure 8).


This mixed mode of intergranular and transgranular cracking indicates that the subs likely underwent temper embrittlement resulting from improper heat treatment. Hence, presence of intergranular cracking does not confirm environmental cracking. Instead, CVN testing should be performed to check the fracture toughness of the material.


Additionally, the fracture surface of the CVN samples should be analyzed under a SEM to verify the fracture mode. Temper embrittlement of material is a strong possibility if the material presents low CVN values along with presence of intergranular or mixed mode of intergranular and transgranular cracking signatures on the fracture surface of the CVN sample.

Figure 8: The fracture examination of the CVN samples from the failed subs C1 (left), C2 (middle) and C3 (right) revealed mixed mode of intergranular, transgranular and some ductile dimple features. This indicates the subs likely underwent temper embrittlement resulting from improper heat treatment.


Guidelines on Alloying Elements


Temper embrittlement is often associated with the concentration of certain trace alloying elements, such as arsenic, antimony, tin and especially phosphorus. These minor impurities segregate along the austenitic grain boundaries during the tempering process and cause cracking along the grain boundaries.


Molybdenum, tungsten and zirconium greatly reduce embrittlement, and nickel, titanium and vanadium slightly reduce the temper embrittlement effects.


API Specification 7-1 and Standard DS-1 do not have any requirements for chemistry on subs. However, API Specification 5DP and Standard DS-1 have chemistry requirements for drill pipe tube and tool joints for phosphorus (0.020% max) and sulfur (0.015% max).


The sulfur content obtained on all the three failures was above the maximum allowed for drill pipe tube. The phosphorus obtained on C3 was above the maximum requirement, while the content for C1 and C2 was near the maximum allowed. This provides basis for strict control on these elements to minimize the possibility of temper embrittlement problems.


If not already required in the governing standard, supplementary requirements on content of phosphorus (0.02% max) and sulfur (0.015% max) should be specified when tubular components are ordered.


To check if the failure mechanism of the failed sub C1 was temper embrittlement, the sub material was re-heat treated. The re-heat treatment was also performed to confirm whether the sub was improperly heat-treated at the mill.


Sections of the failed pin connection were re-heat treated with the following conditions:


Condition 1: Temper at 657°C (1,215°F) for 45 min, and cool.


Condition 2: Austenitize at 872°C  (1,602°F) for 55 min; water quench; temper at 1,215°F (657°C) for 45 min; and cool.


The heat treatment procedures listed in the material test report (MTR) were used for re-heat treatment of the sub material. These conditions were chosen because the tempering temperature listed in the MTR does not fall in the temper embrittlement range.


If the sub was heat-treated at the mill with the conditions indicated in the MTR, temper embrittlement likely would not have occurred. After re-heat treating the sections from the failed pin connection with the conditions listed above, CVN impact tests were performed.


Significant improvement in the CVN values was observed from the re-heat treated material under both conditions. The reason for higher CVN values obtained through Condition 1 compared with Condition 2 is that the Condition 1 material underwent a double tempering process at the mill, and again during the re-heat treatment process.


The minimum and average impact energy of the re-heat treated sections was greater than the minimum required value specified in API Specification 7-1 and Standard DS-1. This confirmed that the failed sub was not heat-treated to the parameters listed in the MTRs.

Figure 9: To check if temper embrittlement still existed after re-heat treatment, the fracture surfaces of the CVN samples were analyzed under a SEM. Microvoid coalescence, seen as ductile dimples, was observed, which is indicative of ductile overload of the material.


To check if temper embrittlement still existed, the fracture surfaces of the re-heat treated CVN samples were analyzed under a SEM. Figure 9 present the fracture surfaces of the re-heat treated CVN samples as seen under SEM.


Microvoid coalescence (seen as ductile dimples) was observed on the fracture surface of the CVN sample, which is indicative of ductile overload of the material. No features of intergranular or mixed mode of intergranular and transgranular cracking were observed.


Hence, temper embrittlement was eliminated by performing the re-heat treatment on the failed sub material. Temper embrittlement was eliminated with only tempering the sub material (Condition 1). This confirms that temper embrittlement can be reversed with a tempering process performed at the appropriate temperature.


1. Detection of intergranular cracking morphology on fracture surfaces of a failed component is often considered to be confirmation of failure through SSC or hydrogen embrittlement, even when no evidence exists for exposure to H2S or a source of nascent hydrogen.


Study of intergranular cracking related failures has shown that intergranular fractures can occur not only when the component is exposed to corrosive environment, such as aqueous H2S, but can also be caused by temper embrittlement of the material resulting from improper heat treatment.


2. Temper embrittlement typically occurs when carbon or low-alloy steels are held at or slowly cooled through the temperature range of 375°C (705°F) to 575°C (1,065°F) during the tempering process.


3. Temper embrittlement is often associated with the concentration of certain trace alloying elements, such as arsenic, antimony, tin and especially phosphorus. These minor impurities segregate along the austenitic grain boundaries during the tempering process and cause cracking along the grain boundaries. If not already required in the governing standard, supplementary requirements on content of phosphorus (0.02% max) and sulfur (0.015% max) should be specified when tubular components are ordered.


4. The fracture surface of a failed component that has experienced temper embrittlement can present intergranular or mixed mode of intergranular and transgranular fracture morphology when analyzed under a SEM.


5. Generally, temper embrittlement of a material, does not lead to a detectable drop in expected yield strength, tensile strength and percent elongation of the material. However, a drop in the CVN impact energy values is often experienced, and in cases of extreme embrittlement, there may be a drop in the percent reduction of area.


6. Since there is no major change in the tensile properties of the material, hardness testing cannot be used to detect temper embrittlement of a material. Performing CVN tests followed by examination of the fracture surface of the CVN sample under a SEM are necessary to ascertain failure through temper embrittlement.


7. If the fracture surface on the failed components presents signatures of intergranular fracture, then it should not be presumed that the failure is associated with environmental cracking like SSC. Instead, CVN testing should be performed to check if the material has low impact energy values.


Once tested, SEM analysis of the fracture surface of the CVN sample must be performed to check for intergranular or mixed mode of intergranular and transgranular cracking. Presence of intergranular or a mixed mode of intergranular and transgranular morphology on the fracture surface of the CVN samples, combined with low CVN values, indicates a failure more likely associated with temper embrittlement of the material.


8. If the component being tested, such as tubing, does not have sufficient thickness to machine minimum required size CVN samples according to the governing API specification (minimum size accepted by API is 10 mm x 5 mm), then CVN samples should be machined to 10 mm x 2.5 mm (¼-in.) size to perform CVN testing.


Although the values obtained through testing cannot be compared against API specification requirements, the fracture surface of the CVN samples can still be analyzed under a SEM to check for intergranular or mixed mode of intergranular and transgranular cracking.


9. Temper embrittlement is a reversible process. Carbon and low-alloy steels that have experienced temper embrittlement can be restored to their original (or expected) toughness by heating (tempering) to 600°C (1,100°F) or above, followed by rapid cooling to below approximately 300°C (570°F). Material susceptibility to temper embrittlement can also be reduced by strict control and reduction of embrittling impurities, such as phosphorus.


This article is based on SPE/IADC 139762, “Intergranular Cracking of Oil Field Tubular Components Resulting from the Tempering Process,” SPE/IADC Drilling Conference & Exhibition, Amsterdam, The Netherlands, 1-3 March 2011.


References
1. API Specification 7-1, Specification for Rotary drill Stem Elements, first edition, American Petroleum Institute (March 2006),
Section 7.5, Page 26.
2. API Specification 5DP, Specification for Drillpipe, first edition, American Petroleum Institute (August 2009), Table C.4, Page 86.
3. Hill, T.H.: Drill String Design and Failure Prevention, T H Hill Associates, Inc. (September 2002).
4. Metals handbook, Volume 4, Heat treating, ninth edition, American society for metals (November 1981), Page 84.
5. Metals handbook, Volume 11, Heat treating, ninth edition, American society for metals (November 1981), Page 6, 11, 99.
6. Metals handbook, Volume 12, Heat treating, ninth edition, American society for metals (November 1981), Page 13, 174.
7. Standard DS-1® Volume 1: Drilling Tubular Product Specification, third edition, fourth printing, T H Hill Associates, Inc. (January
2004), Table 3.2.1, Page 20 and Table 3.1, Page 13.
8. William T. Becker. ASM International Course 0335, Principles of Failure Analysis, Lesson 3: Ductile and Brittle Fracture, Page
61, 62, 63.


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