Hydrocarbons occupy a vital role in our life and continue to play an important role for many more years to come. We need to follow all technological innovations to continue our productivity standards to achieve our production targets. Let us extend our vision to achieve this mission.

Tuesday, May 20, 2014

Oil and Gas: Dynamic Treatment Challenges Abound in Vast, Booming Industry

By Jeff Gunderson

Oil and gas production is a colossal, fast-evolving, and wide-ranging industry that is shaped by significant market drivers, is vital to the global economy, and represents the world's largest industry in terms of capital value. Like the industry itself, water and wastewater treatment in oil and gas is broad and complex, with numerous issues, and spanning several areas -- from the upstream and downstream segments to conventional oil and gas to the unconventional plays including shale gas and liquids, coalbed methane, tight gas, and heavy oil, among others.

Oil and gas is not just one market, it's many markets, and some have water and wastewater treatment challenges that are highly specific and require unique and increasingly innovative solutions, observed Jonathan Rhone, president and CEO of Vancouver, B.C.-based Axine Water Technologies.

A mud pit in North Dakota's Bakken Formation. Photo by Joshua Doubek.

Many of the treatment issues in oil and gas are also based on the regional geology, much like the mining industry, said Rosemary Niechcial, director of infrastructure – mining, oil & gas with Black & Veatch. "For example, there are treatment challenges specific to the Alberta oil sands or the Bakken Shale Formation that aren't found anywhere else in the world," she said.

In recent years, the industry as a whole has begun to experience a significant change as increasingly more attention moves towards unconventional sources. In An Overview of Unconventional Oil and Natural Gas: Resources and Federal Actions, a report prepared by the Congressional Research Service, advances in hydraulic fracturing, directional well drilling, and reservoir stimulation has enabled oil and gas production from tight, impermeable unconventional formations that were previously uneconomical to produce, changing the U.S. energy posture and global energy markets.

Fracking operations in progress in the Bakken Formation. Photo by Joshua Doubek.

This global shift to unconventional sources represents a huge driver for the treatment industry and an enormous opportunity for new technologies, according to Rhone. "Many of the extraction techniques associated with these newer plays -- such as steam-assisted gravity drainage and water flood -- are very water- intensive and generate high volumes of wastewater, which can be very complicated," he said. "Plus, as many of the old oil fields reach the end of their productive lives, these methods are now also being used on conventional sources to drive out the last remaining hydrocarbons."

Water Recycling

As in other industries, water recycling is taking on increasing significance in the oil and gas industry, especially as water resources become scarcer.

"Raw water costs are also rising significantly, generating higher interest in adopting advanced technologies so that wastewater can be treated and recycled back in operations, reducing freshwater intake requirements," Rhone said.

Manish Backliwal, international business development manager with Aquatech, said due to stringent environmental regulations, oil companies are looking at economical and innovative ways to recycle more produced water as opposed to discharging it.

Backliwal, who specializes in upstream oil and gas, said companies are striving to recycle as much as 95 to 98 percent of produced water coming from enhanced oil recovery operations. "More and more, innovation in water recycling is being focused on addressing that last 2 to 5 percent and how to economically treat those highly-concentrated impurities," Backliwal said.

Water Sources

In addition to driving more water recycling, water scarcity is also pushing more oil and gas producers to find alternative, lower-quality sources of water that can be utilized for meeting process water needs. Doing so, however, can present a new set of treatment challenges.

"Brackish water is increasingly coming into the picture, but this type of water also has greater levels of total dissolved solids," Backliwal said. "The chemistry of the produced water can be very complex, with high concentrations of organics, silica or other elements creating distinct treatment challenges."

As higher quality sources become more difficult to access, oil and gas companies are also turning more to wastewater treatment plant effluent, according to Black & Veatch's Niechcial. "We are seeing more of this across the board, wherever an operation is in close proximity to a municipality, such as in Mexico," she said.

"But in many cases, the newer unconventional plays are not located within easy distance to municipalities," she added. "Then, the trend is to utilize poorer-quality, non-potable water, and this is where the treatment challenges really come in because a lot of these sources are highly saline."

Technologies, Innovations and Solutions

Many long-standing and new drivers in the oil and gas industry, propelled by macro demands, are continuously pushing the market in terms of the development of new treatment technologies and innovations. In addition to solutions that help solve problems such as meeting higher water quality discharge requirements, end users increasingly need solutions that are more adaptive, robust and that are capable of treating more problematic sourced water. At the same time, oil and gas companies are also pressing for technologies that offer greater treatment performance at lower costs.

Becky Tomasek, upstream market sector leader for CH2M HILL's water market, said as the upstream industry moves towards more brackish water use, companies are relying more and more on chemical addition and mechanical filtration for removing iron and other metals that can cause scaling. "For hydraulic fracturing, many operators want to develop a clean brine from either brackish water sources or recycled produced water, and so in some cases they are focusing on removing suspended solids and hardness," Tomasek said. "If the produced water isn't needed, then flash evaporation can be used, leaving only the solids to be discharged."

In terms of treatment innovations, Tomasek sees advancements both in membranes and in distillation. "A lot of the new water sources have total dissolved solids levels that are higher than what a typical membrane can handle. So we are seeing more robust, ceramic-type membranes that can withstand the fouling that may occur," she said. "With distillation, technologies are being introduced that can vaporize and condense salt water in a very efficient fashion"

Devesh Mittal, vice president and general manager of Aquatech's shale gas division, said fluctuating oil and gas prices are prompting drillers to move operations more frequently, which in turn is forcing treatment specialists to be more adaptive. "Oil and gas is a constantly-changing industry. Drillers will change plans quickly and move to another formation if the economics of drilling are more favorable," he said.

Aquatech's SmartMOD is a modular evaporator that is flexible, redeployable and specifically engineered for the harsh environment of the Alberta oil sands.

For example, more drillers right now are shifting to the oil- or liquid-bearing regions because oil prices are collectively higher than the price of gas, Mittal noted. "When these shifts occur, we need to be able to respond quickly, have the right assets in the correct locations, and be prepared to handle new water characteristics and different water balance dynamics," he said.

For meeting challenges associated with changing treatment needs, Aquatech provides solutions that are flexible, adaptive and that offer service in multiple formats, according to Mittal. "We are also focusing on making systems simpler and developing combined solutions that are capable of serving the broader oil and gas market," he said.

Indeed, in many instances, solutions to problems may not necessarily require new technologies but rather an integration of existing technologies, said Samir Davé, downstream market sector leader for CH2M HILL's water market. "What matters are the technologies chosen, how they are integrated and in what sequence they are used," Davé said. "The treatment strategies should also vary based on the dynamics of the formation. For example, the water characteristics in the Eagle Ford Formation could be very different compared to the Marcellus Shale, requiring different approaches."

An integrated approach is also critical in addressing challenges on the downstream side of the industry, Davé said. "We are seeing lots of interest from clients who need help meeting very stringent limits related to nitrogen, phosphorus, metals like copper and selenium, and also with regard to effluent temperature," he said. "With regulations requiring selenium to be removed to parts per billion level, an integration of technologies is needed."

Another area of focused innovation and development is in the design of modular treatment systems that are compact, easily-transported and can be installed very quickly.

"These types of units are inspired by the off-shore industry where space is at a premium and can be very effective in places where labor costs are high, such as Alberta and Australia," said Aquatech's Backliwal. "Since modular treatment systems are already essentially built, the onsite installations are mainly limited to assembly, which can be much more cost-effective."

Aquatech has developed a modular evaporator specifically for the oil sands market that is flexible, redeployable and engineered to withstand the extreme climate of northern Alberta. Called the SmartMOD, the technology is capable of significantly reducing field installation labor and costs.

About the Author: Jeff Gunderson is a correspondent for Industrial WaterWorld. He is a professional writer with over 10 years of experience, specializing in areas connected to water, environment and building, including wastewater, stormwater, infrastructure, natural resources, and sustainable design. He holds a master's degree in environmental science and engineering from the Colorado School of Mines and a bachelor's degree in general science from the University of Oregon.

Tuesday, May 6, 2014

Fwd: We're Hiring


 

 

ICM have the following open vacancies on Cyber & Conventional Jackup rigs (Long term) to be filled urgently:

 

·         OIM (Drilling background) x2

·         Barge Master x2

·         Tool Pusher x4

·         Driller x4

·         Assistant Driller x4

·         Derrick man x4

·         Pump man x4

·         Floorman x12

·         Maintenance Supervisor x2

·         Chief Mechanic x2

·         Mechanics x4

·         Chief Electrician x2

·         Electricians x4

·         Electronic technician x2

 

Also looking for:

·         Toolpusher – cyber jackup- Rusia (European only)

·         QHSE Manager (French/ English) residential position (Nebosh & Drilling experience is a requirement) – West Africa

·         Advance Drilling Instructor (residential / rotational) Europe

 

To apply send your CV in Word Format, State Nationality, Date of Birth, Availability & expected dayrate in USD.

 

Please follow us on LinkedIn : http://www.linkedin.com/company/3105337?trk=tyah for exciting more updates

 

Looking forward to your application

 

Best Regards,

HR Manager

International Consulting Management

hr@icmpeople.com

 

 

 

 

 


Saturday, May 3, 2014

Well Control - Preliminary record of information

Well Control - Preliminary record of information

Pre-recording of information.Proper secondary well control follows a planned course of action. Pre-recording relevant information avoids unnecessary delay. The following aspects concerning the pre-recording of information are discussed:

  • Kick control worksheet.
  • Checking pump pressure at reduced pump speeds.
  • Establishing the weighting material mixing capacity of the rig.
  • Relationship between bottom hole pressure, formation strength at shoe and mud gradient.
  • Determining the maximum allowable annular surface pressure (MAASP).

1 Kick control worksheet

A Kick Control Worksheet is available (CLICK LINK).

During drilling operations, the Worksheet must be updated regularly to correct depth-dependent data and additionally, whenever significant changes occur in parameters such as casing and hole sizes, mud gradient, drillstring configuration, nozzle sizes, formation characteristics, etc.

Kick control worksheets should be available at all times that BOPs are installed and in use.

For development they should be updated before entering the potential oil reservoirs. For exploration or appraisal wells, they should be updated at least daily or every 200 m, whichever is the sooner.

2 Checking pump pressures at reduced pump speeds

Well control operations are performed at reduced pump speeds in order to:

·allow weighting up and degassing of the mud;
·reduce loads on surface equipment;
·increase reaction time for correct choke adjustments.

Operation of the pump at a pressure too close to the setting of its relief valve is dangerous. If the relief valve opens, mud will flow back through the drillpipe and standpipe manifold.

Circulation pressures at the reduced pump speeds must be known. Before starting to drill with a new bit and at the beginning of each shift, the driller shall observe pump pressures at selected circulation rates and record the results in the daily drilling report and kick control worksheet.

Circulation pressures may differ considerably when using a different equipment hook-up (e.g. circulating head/chicksans vs kelly or top drive).

Slow circulation rates should be taken with the equipment hook-up which is planned, or most likely to be used during the well killing operation.

Slow circulation rates and pressures can be plotted as a straight line on a graph using log log paper. Appropriate pump pressures for any pump rate can be found using this graph, provided the mud properties and drillstring configuration do not change.

2.1 Friction losses in subsea BOP stack kill-and choke lines

Friction losses in subsea BOP stack kill-and choke lines represent a significant proportion of the back pressure developed in the annulus and, if not taken into account, could lead to a fracture of the formation around the casing shoe.

The friction losses in kill-and choke lines (both separate and combined) should be determined at various rates after landing and testing the BOP stack, but before drilling out the cement in the casing.

The pressure losses can be established by comparing pump pressures obtained whilst circulating:

·Down the drillpipe and up the marine riser.
·Down the drillpipe and up the kill-and choke lines separately and combined.

Alternatively, the value of the friction losses can be measured directly, and perhaps more accurately, by pumping down the lines, separately then combined, with returns up the marine riser.

In deep water operations, suitably low circulation rates should be selected.

Choke and/or kill line pressure losses for a particular subsea BOP stack set-up and waterdepth will only change when different mud properties are used.

3 Establishing the weighting material mixing capacity of the rig

The weighting up capacity depends on the maximum rate at which barytes can be added over prolonged periods. It is recommended that this rate is established for mud gradients in normal use.

An important advantage of the balanced mud method is that a well can be controlled in one circulation. This is done by employing a constant pump speed whilst circulating a mud which has been weighted up.

If mud mixing facilities cannot achieve the required increase in mud gradient, it will not be possible to control the well in one circulation.

Several circulations may be required, the gradient being raised in stages during each circulation, or on a gradual continuous basis while pumping.

One option to obtain the required mud weight quickly is to prepare kill mud prior to drilling ahead in possible overpressured formations. This practice will facilitate speedy well killing operations.

Preparing kill mud in advance is recommended for wells in which increased mud weights are expected to be used. The recommended kill mud gradient depends on the expected formation pressures to be encoutered, but as a general rule may be 10-20% higher than the actual mud weight in use. The correct mud weight can be obtained quickly by diluting the kill mud with the original mud.

4 Relationship between bottom hole pressure, formation strength at the casing shoe, mud density, and influx volume

There is a close relationship between the above parameters and the ability to safely handle a kick without causing formation failure in the open-hole section. Given certain fixed (or assumed) values of these parameters, combined with an acceptable kick tolerance for the rig drilling the well, a minimum required formation strength at the shoe may be specified.

The ability to safely handle a kick without causing formation failure in the open hole section needs to be reviewed as soon as the actual formation strength at the shoe is known and whenever any of the other parameters change.

Section 6.13 contains equations which show how the minimum required formation strength is calculated for specific influx volumes.

4.1 Kick tolerance

Influx volumes of 5-15 m3 (30-90 bbl) may be used as the maximum allowable kick tolerance. This depends on the following:

  • knowledge about geological control, PVT characteristics, etc.;
  • accuracy and reliability of the kick detection system;
  • rig type (floater/bottom supported rigs);
  • crew reaction time to close in the well.

Likely influx volumes for the drilling and reservoir conditions prevailing can be calculated/determined from equations given in the Casing design guide However, results largely depend on realistic values of kick detection threshold volumes for the rig used to drill the well. Experience has indicated that well-trained crews can perform BOP drills in three to four minutes. BOP drills shall be carried out to achieve and maintain this performance standard.

Periodic checks shall be made to establish the magnitude of the influx which can still be safely handled with the mud currently in the hole (kick tolerance), i.e. without causing formation failure. These checks will indicate the extent to which the density can be increased to control formation pressure or whether casing should be set prior to drilling deeper. New calculations shall be made whenever any of the parameters have, or will be changed.

5 Determining the maximum allowable annular surface pressure (MAASP)

In drilling operations the borehole fluid pressure must not exceed the formation strength at any point in the open hole. During well control operations the maximum allowable borehole fluid pressure at the casing shoe is normally considered to be the critical factor, based on the assumption that the weakest formation is at the shoe. For practical purposes, this pressure is referred to at the surface as the Maximum Allowable Annular Surface Pressure (MAASP).

The MAASP equals the "formation strength" at the casing shoe minus the hydrostatic head of the mud and/or influx in the casing. The "formation strength" is generally established by making a leak-off test during the course of the drilling operation.

In principle, MAASP should not be exceeded during well control operations, as long as the top influx has not yet reached the shoe, because of the danger of breaking the formation which may result in a (internal) blowout. However, there are situations which may justify exceeding the leak-off value during well control operations when the detrimental effects of having larger influx volumes entering the borehole are considered worse than the risk of encountering losses. There are exceptional cases where it would be better to take the risk of breaking the formation and to have an internal blowout than to have a flow to surface. Exceeding MAASP before top influx is at the shoe will not always have such detrimental effects, because of hidden safety factors in MAASP which are explained as follows:

  • the formation intake pressure obtained during the leak-off test is usually lower than the formation breakdown pressure;
  • the influx is dispersed in the mud and the actual position of top gas is much higher than the theoretical top of gas when well killing commences. This means that the influx will not reach the shoe as one bubble, but part of the influx is already inside the casing shoe when the theoretical top of influx should be at the shoe. The actual shoe pressure is therefore lower than the calculated shoe pressure using MAASP;
  • leak-off tests are usually done in "virgin" hole. In principle, higher leak-off test results are obtained with time due to the plastering effect of mud.

The decision to exceed MAASP and the extent to which it could be exceeded depends very much on the circumstances under which the kick is experienced.

Drilling staff should be sufficiently conversant with well control principles that they can recognise and handle such situations. Main criteria to be considered are:

  • severity of the kick (inflow performance low/high?);
  • casing shoe depth (deep shoe, less chance of cratering);
  • strength/depth of weakest formation;
  • position of influx in open hole when MAASP is reached and estimation of how much MAASP will be exceeded when the theoretical top influx has reached the shoe.

5.1 Automatic MAASP control

Some control panels of remotely controlled chokes have an automatic MAASP control feature which keeps MAASP constant as soon as it is reached. When this feature is used in situations whereby MAASP should be exceeded, for instance when top influx is already inside the casing shoe, more influx is allowed to enter the hole unnecessarily which may lead to worsening situations. It is recommended not to use this feature, but to adjust the remotely controlled choke(s) manually from the control panel.

5.2 Calculation of the MAASP

To calculate MAASP, three parameters should be known:

  • the hydrostatic head in the annulus above the weakest formation;
  • the true vertical depth of the weakest formation;
  • the strength of the weakest formation.

If any of these three parameters changes, the MAASP has to be re-calculated.

Well Control Barriers

Discussion on Suitability of Barriers (well control)

this article discuss the suitability of barrier for the following:

  1. Fluids
  2. Mechanical Barriers in completed Wells
  3. Sub-surface Safety Valve
  4. Sustension of a perforated well (with xmas tree)
  5. Sub Sea Well Suspensions
  6. Two Way Check Valve (TWCV)

1. Fluids as a Barrier

Only drilling mud can be defined as a truly independent fluid well barrier. It has the fundamental requirements of both overbalance and a method of sustaining the fluid column by means of the mud cake preventing the overbalance pressure injecting the fluid into the formation.

Brine (or other non-particulate fluids),on the other hand ,cannot be said to be an independent  barrier. Brine is designed not to damage the perforation/formation and cannot "Pack off" in the same manner as mud.

When brine is used as the column of fluids which provides hydrostatic overbalance , the brine requires to be isolated from the perforations to prevent it dissipating into the formation ,and thus reducing the hydrostatic head.

For this reason, brine and plug (mechanical or cement) which retains the brine cannot be considered as two independent pressure barriers ,as the brine is completely dependant on the plug not leaking.

The brine can only be said to provide a true barrier it its level can be observed continuously to ensure maintenance of the hydrostatic head. In practice this is not normally possible , especially when an upper mechanical barrier encloses the brine column.

Discussion fluids as a barrier

Consider the case of a lower and upper pressure tested barrier with a column of overbalanced brine held in place between the two barriers by the integrity of the lower barrier ;If the lower barrier should leak then hydrostatic overbalance pressure will cause the brine to dissipate beneath this barrier towards the formation .The head of brine will continue falling until the hydrostatic overbalance disappears .It is not possible to detect /observe this fall in level without disturbing the integrity of the upper barrier.

Once of the overbalance has disappeared, then the leak allows hydrocarbons to percolate past the lower pressure barrier. Trapped below the upper pressure barrier, the only way the hydrocarbons can expand as they travel up through the brine is to displace more brine through the leaking lower barrier, exacerbating   the fall in level of brine .Ultimately pressurised hydrocarbons build up undetected underneath the upper barrier.

The brine is thus completely dependent upon the lower mechanical barrier not leaking. If this lower barrier remains leak tight then it contains the well pressure satisfactorily and there is no need for a supplementary barrier.

Taking the argument to its extreme, the brine in this situation appears not to provide any significant increase in safety benefits above the existing mechanical barriers.

In evaluating the role of brine as a barrier, the main argument in its defence is that the leakage past the lower plug would probably take some considerable time before overbalance was lost. Certainly this timescale could have consequences for the integrity of Sub-sea barriers, where by the very nature of the operation all barriers shall be capable of providing long term integrity.

A certain "level of comfort" appears to be derived by having circulated an annulus and tubing contents to brine. From the above argument brine is clearly not an independent barrier and thus does not provide a "third" barrier as is often suggested.

If only the tubing contents were to be displaced to brine, leaving the annulus remaining with, say inhibited sea water , then this would be a clear case of dual standards in respect of barriers for the tubing annulus.

A justification exists for using overbalanced brine with some wireline plugs to assist the lower mechanical barrier in the tubing, as there may be the need to energise the "Vee" packings in wireline plugs. The latter require a differential pressure to maintain the seal is energised in the opposite direction to the formation, i.e.from above only. Secondly the seal systems on these plugs are not symmetrical and thus sealing from above is not a good indication of pressure integrity from below.


2. Mechanical Barriers (Completed Well)

Only the deepest set mechanical barrier can be truly leak tested in the direction of formation pressure .The upper , mechanical barrier therefore can only be tested  from above, unless tubing/annulus communication exists above the bottom barrier.

In the case of only being able to pressure test the upper barrier from above, the sealing mechanism between the mechanical barrier and the tubing (and the sealing mechanism between any bleed-off device and the mechanical barrier) shall have symmetrical seals so that a pressure test from above is a good indication of pressure integrity from below.

NOTE: A two way check valve should not be used in this case as a test from above does not indicate that it will hold pressure from below, the sealing faces being different for each direction of flow. (See section 6.)

Discussion mechanical barriers

The mechanical pressure barriers in the annulus consist of the lower packer and upper tubing hanger/ wellheads   seal .These mechanical barriers(packers) are set under as near ideal conditions as can be achieved down hole. Tubing hanger seals /wellhead seals are now designed to provide metal to metal sealing as the primary seal. There is a high level of confidence in both barriers ability to contain well pressure and remain leak tight as during the operation of the well they have been tested (monitored) over a considerable length of time.

The "quality" of the mechanical pressure barriers set in the tubing should ideally give the same degree of confidence in their ability to remain leak tight and contain well pressure.

There appears to be no documented evidence on the subject of long term integrity of wireline plugs for use as mechanical pressure barriers in tubing and therefore personal experience, etc has been used in any discussion on the subject to date.Subsequently this topic was reviewed during two QRAS on barriers Requirements , and subjective reliability figures used. The result of these QRAs was to convince the HSE (who had queried our adoption of two barriers as our standard, instead of their stated requirement for three),that indeed two independent barriers, if properly tested, was the optimum.

For general purposes, and longer term suspension programmes in particular ,especially in sub-sea wells, a retrievable packer/bridge plug system is preferred , as with these systems energy is locked into the seal system by virtue of the setting operation .A standard wireline plug system using Vee  packings, relies on the seal being maintained by pressure differential .Wireline plugs using modulec seals are available for TFL completions, but require pressure assistance to install. The seal still relies on differential pressure and may be difficult to retrieve.

Retrievable bridge plugs have been developed and used successfully as both a lower and upper mechanical pressure barrier in the tubing string. These retrievable plugs are considered to be capable of providing a long term barrier.

Communication between anulus and tubing in a completed well

If the integrity of the bottom pressure barrier is confirmed then communication between annulus and tubing above this bottom barrier does not require any extra barrier over and above the second upper barrier.

The concept of "two pressure vessels" is maintained with reservoir pressure contained by :

  1. The lower line of defence comprising the integrity of both the packer in the annulus and the mechanical pressure barrier in the tubing.
  2. The upper line of defence comprising the tubing hanger/ wellhead seals (and side outlet valves) in the annulus and the upper mechanical pressure in the tubing

    In this case the upper mechanical pressure barrier in the tubing can be pressure tested from below via the communication with the annulus.


    3. Sub-surface Safety Valve as a Well Barrier

    A Subsurface Safety Valve (SSSV) may be used as a well barrier provided

    1. the SSSV is leak tested and confirmed leak tight.
    2. the tubing integrity from the packer to the SSSV is satisfactory and confirmed leak tight, and
    3. the SSSV is inhibited from opening by isolation of the hydraulic control and balance lines.

      This implies that Ball Valve type  SSSVs are superior as a barrier (see below)

      The SSSV is designed to retain the maximum differential pressure across the valve that may be generated in a well .This differential is normally seen during routine testing. Prior to being installed in a well ,the SSSV is tested onshore to its working pressure.

      Having proved the SSSV to be leak tight in the well, then should pressure increase below the SSSV this will assist the sealing mechanism of the valve.

      The SSSV is designed to retain pressure across the range of temperatures observed in a well. This is applicable to both the metallic parts and the elastomers.

      In the case of a wireline Retrievable SSSV  of a wireline Retrievable SSSV, the mode of retention of the SSSV in the nipple is fundamentally the same at the mechanical retention of a wireline plug set in a nipple .The ability to remain set in the nipple is tested during the leak test .A Tubing  Retrievable SSSV  is designed and installed as a part of production tubing completion .Thus there is no potential to move up-hole under application of differential pressure.

      The type of SSSV (Ball or Flapper) has a bearing on the reability of the valve to remain sealing:

      Ball Valve

      In the case of a Ball Valve isolating the accumulator from the balance line positively prevent the ball rotating and hence maintains the seal integrity .Any flow of fluid down through the valve ,lifting it off its seat, will be temporary ,and any reversal of flow /pressure will immediately reseat the ball.

      Flapper Valve

      In the case of flapper valve, unlike the ball, there is no certainly that the flapper will remain our reseat once differential pressure is removed – The spring which induces flapper closure can not be relied on the same way. Thus, a flapper valve should not relied on as a barrier where there is the possibility of it being unseated, e.g. by pressure reversal or a dropped object.

      The argument that a flapper valve is of  no use as an emergency device(its prime function in life), does not follow , as the valve will close an a flowing well situation irrespective of spring action ,where fluid dynamics will ensure the flapper moves the closed position once the protective sleeve moves up. This is also the case for a well suspended with the Xmas Tree installed (See section 5) , where a flapper valve is the normal safety device that would be installed during the production phase of the well.

      In considering the case of an SSSV that is used as a barrier, the problem that arises of how one can leak test the surface barrier,e.g .the tree or a retrievable bridge plug, This arises as once can not easily trap pressure between the SSSV and surface with a chance of observing meaningful flow through the barrier, except in a gas environment. In this case its considered acceptable to adopt the following procedures:

      1. If a Xmas Tree Valve is to be used as the surface barrier , then first leak test the Tree Valve , open it close and leak test the SSSV ,and then close the Tree valve. Due to the high reliability of gate valves this procedure is acceptable (See 4 and 5 below)
      2. If a plug is to be used as a surface barrier , it must be of a type that a pressure test from above gives assurance that the plug will hold pressure from below First  close and leak test SSSV, and then set and pressure test the plug.

      In both cases, leave the pressure differential across the SSSV,i.e, do not equalise. This ensures that work is carried out in a situation where there is no pressure below the top barrier.

      If the SSSV is found not to be leak tight when tested, then either a replacement SSSV may be run and tested, or a wireline plug may be set in the nipple profile ,in that its seal bore is know to be in good shape( being in continual use for the SSSV) and that the condition of this upper nipple profile with regards to erosion and sealing is generally found to be significantly better than on deeper nipples.

      Using the SSSV as the top (secondary) Barrier

      When proposing/ accepting an SSSV as a barrier ,one must consider the potential mode of failure in the particular application. Unseating and re- sealing of the valve has been considered above . The other prime failure mode is due to impact  of a dropped object. Primarily a wireline toolstring past the Xmas Tree valves with the BOP/ Lubricator removed) , then the valve is directly exposed to the possible impact if the string were to be dropped . This possibility is real , and it has happened , even recently.

      The consequences  are likely to be different for Ball and Flapper types valves .A flapper valve is likely  to shatter , and toolstring  and debris will fall into the lower plug, not only causing and awkward fishing problem, but possibly compromising the integrity of the lower barrier. For this reason a flapper valve is not generally acceptable in this relative position ( but see  below).

      On the other hand a valve type SSSV is known to be extremely robust, and attempting to shatter the ball in a failed valve to gain access to the lower part of the well has caused great difficulty .The  sealing ability of the ball  after such as impact  is likely to have been impaired , but it will still provide an availability of the tree valves this provides sufficient confidence to consider the arrangement acceptable practice. Use of the technique should still be treated with caution, especially in high pressure situations, and in particular gas wells.

      In order to use a Flapper type SSSV as the top barrier when removing the BOPs / tree , it is therefore necessary to use , e.g.a TWCV , as a debris barrier. This is also good practice for Ball type SSSVs in that  any debris that would otherwise fall into the well during the Tree/Bop removal process may be recovered easily, as well protecting SSSV from impact damage .Note that the TWCV may provide additional isolation security but it can NOT be relied on formally to act as a barrier (See Note 6).


      4. Suspension of a perforated well (with xmas tree)

      a perforated well may be suspended if the completion and Xmas tree has been run, utilising  the Sub-Surface  Safety Valve (SSSV) to provide the primary well barrier in the tubing. This is conditional on the integrity of the packer and the tubing from the packer  to the SSSV having been tested as leak tight.

      The SSSV shall be leak tested to confirm it as being leak tight ( and set in its nipple if wireline retrievable ). Do not equalise pressure across the SSSV prior to closing  the surface (Tree) valve  (see below).

      If the SSSV is not leak tight, then it can either be replaced with a new valve, or a wireline plug set above it and tested.

      If the tubing from packer to SSSV is leaking then a wireline plug shall be set below the packer (in the tailpipe) and leak tested.

      The second barrier is provided by the tested casing , the integrity of tubing hanger seals in the wellhead and the Xmas tree.

      The Xmas Tree is considered to be a single barrier with redundancy. It is good practice to consider the tree outer valves as the working  barrier , with the UMGV and LMGV remaining open and providing redundancy should a problem develop .This will not be possible if the purpose of the suspension is to repair a tree valve , in which case the next lower valve may be used. The benefit of this is that is possible to monitor the status of the lower barrier by measuring the pressure in the tree, either using SCADA ( e.g. CAPO) or by attaching a pressure gauge to the tree cap and cracking the swab valve.

      In this case the integrity of the valve(s) to hold pressure from below shall be ascertained prior to setting the primacy barrier ( closed SSSV or wireline plug) The valve then has to be opened to allow setting /testing of the primacy barrier .The design of the tree valves is such that there is high confidence in their ability to maintain an effective barrier after single open/ close operation .

      However it must also be realised that that with these valves ( both split gate and slab gate styles ) a pressure test from above is not a satisfactory indication of the valves ability to hold pressure from below.

      In the case of long term isolation , it may be considered appropriate to close the UMGV to minimise potential leak paths. However, should the UMGV prove to be leaking (across the valve) and unable to be leak tested satisfactory , then the LMGV may be used to provide the well barrier.

      On Platform wells the integrity of the barriers in the suspended well shall be monitored at advised intervals via the Xmas tree and annulus side outlets.

      Leaking packer

      If the packer is leaking then a cement plug shall be set below the packer to isolate the annulus from well communication.

      This may be achieved by a cement plug set a cross the perforations or by a column of cement set above an expandable , mechanical "through tubing bridge plug"; In both cases the integrity and position of the TTBP/ Cement plug must be properly ascertained before proceeding to use this as the barrier.

      For Subsea Well Suspensions, refer to section 5


      5. Sub Sea Well Suspensions

      Sub sea wells may be suspended following completion and perforation / production testing utilising the principle of two mechanical barriers.

      The primary barrier is provided by the packer , tubing and TRSSSV ,which are leak tested as being leak tight.

      The secondary barrier is provided by the pressure tested casing, the tubing hanger seals in the wellhead and the sub-sea Xmas tree valves(FWV, SWAB, ANSWAB,ASV) previously tested leak tight.

      A further, dependent barrier exists within the Xmas tree ,i.e a previously tested UMGV and AMGV.

      The use of the TRSSSV, completion and Xmas tree valves to provide well barriers in a suspended sub-sea well are considered effective and minimise the need for further intervention ( and exposure to risk) to either install or remove additional mechanical or fluids barriers.

      Suspension after flow test without monitoring facilities

      A Sub-sea well will be suspended as such after production testing via the vertical riser system, and prior to the flowline and monitoring facilities being hooked up/ commissioned at the platform .The condition of the valves (TRSSSV and Xmas Tree Valves) and tubing is therefore expected to be at their best , and the well will not be suspended ( and the rig move of location) before these valves have been satisfactorily leak tested.

      It has to be assumed that the design of the Xmas tree valves, having been previously tested immediately prior to leak testing of the TRSSSV will ensure repeated confidence to hold pressure from below after their further operation to perform the leak test of the TRSSSV.It must be noted that the design of the Xmas tree valves does not allow a pressure test from above to indicate the valve's ability to hold pressure from below.

      The possibility of hydrocarbon leakage past valves must always be assumed to exist , which could result in pressure developing under the tree cap or to the flowline isolation valve.

      Pressure developing under the tree cap would prevent its removal and the gaining of vertical entry until the well could be "killed". Direct vertical entry of a sub-sea well provides the normal route by which such a well would be "killed". If vertical  entry is inhibited by internal Xmas tree valve leakage then a kill facility other than by direct vertical entry shall be provided. This shall be by providing the guide base. A bleed/ monitoring facility shall be provided between the Xmas tree and the FIV if the flowline is left suspended .

      Access to the flowline downstream of the FIV may be via a number of methods .Usually this would be by gaining vertical access to an adjacent well, where the flowlines are already manifold together .The kill path would then be across the top of this well to the adjacent tree. Access to the flowline then allows both the tubing and the annulus, via the annulus cross –over valve , to be squeeze killed . If the flow line is suspended downstream of the Flowline Isolation Valve, then should the well need to be killed it will be necessary to provide a flexible riser connection from the flowline  to the rig .

      If vertical re-entry is required to such a suspended well, then pressure monitoring facilities shall be re-established, before removal of the tree cap. If it not possible to re-establish pressure monitoring facilities, then the well shall be "killed" prior to the vertical re-entry.

      Flowline tie-in

      The preferred option regarding flowlines and suspended wells is to have the flowline installed (to the manifold) and hooked up to the Xmas tree prior to production flow testing , their by avoiding heavy lifting/ pull-in work in the vicinity of a 'live 'Xmas tree.

      Pump out plugs

      The use of pump out plugs with an under balanced fluid column in the tubing for long duration sub-sea suspensions has been considered. Gas migration past the plug would be excepted , which may induce pressures that could exceed the shear rating of the plug .Also , thermal effects may give rise to significant pressures that could exceed the shear rating of the plug. Their use, including the use of Pressure Cycled Plug (which in sub-sea applications gives rise to concerns about the fluid contents in both the flowline and the well , and hence the pressures that are actually being exerted on the plug when trying to cycle it) is not supported for long term isolation.

      Control system hook-up

      There is considerable risk in hooking up and testing of the control system to a suspended sub-sea well. There is a risk that the TRSSSV and Xmas tree valves could end up simultaneously in the open position.

      The preferred option is therefore to suspend wells with the control and monitoring systems hooked up and fully commissioned .If this is not possible , then during hook up of the control system , the manually operated LMGV shall be closed to provide and additional barrier in the tubing. The annulus is protected by the packer and tubing integrity.


      6. Two Way Check Valve (TWCV)

      The use of TWO-WAY Check Valves (TWCV) as a means of providing an upper mechanical barrier in the completion tubing gives rise for concern , primarily in regard to the setting method .Furthermore  TWCV can only  be tested properly, if annulus / tubing communication exists , and even then , dirt ingress could prevent the check  from reseating if there is a pressure reversal across the valve. A test from above a TWCV does not indicate that it will hold pressure from below , as the sealing faces are different for each direction of flow.

      The TWCV should be set properly in a profile within hanger pressure control equipment .i.e. a Back Pressure Lubricator consisting of a 2'' polished solid rod and "Palmer Lee" Wrenches to grip and apply torque through the pressure retaining body /system. The Back Pressure Lubricator is a cumbersome device and has a poor  operability record.

      The main concern in setting a TWCV with this equipment is that the 2" polished rod, passing through all the Xmas tree valves renders the Xmas tree inoperable as a pressure control device and hence as a well barrier .There is a high potential for becoming stuck with an improperly seated TWCV and unable to release the polished rod from the TWCV .

      In many instances the TWCV as the upper mechanical barrier has been secured without the use of pressure control equipment (B.P.L).This has been achieved by the use of a lower mechanical barrier and a column of brine above. This practise is considered inappropriate.

      The development of wireline set tubing hanger plugs   and wireline retrievable bridge plugs have now provided a safer alternative upper tubing barrier.

      The TWCV can still perform a useful role as a debris barrier, and may provide additional security against pressure , but it should not be used as a pressure barrier in its own right.

      Wednesday, April 23, 2014

      7 Must-Read Future Technology Articles for Every Business Leader

      If you're a regular follower of my LinkedIn posts, you'll know that connectivity - and how mobile technology is transforming societies, businesses and governments - is a key theme I like to share my views on and discuss. The impact that the connected world is having on the workforce and the workplace is a real passion of mine, and something that will continue to develop throughout our careers.

      There are many different views on exactly how companies, countries, brands and communities will change over the next century, but pretty much everyone I hear from agrees that these key pillars of our world will look very different at the end of the 21 century compared to how they looked at the start.

      To broaden out the debate, this week, I'd like to share with you seven great articles that explore some of these topics in more depth than I can go into here.

      First a small disclaimer. These articles are from the new Future Thinking interactive microsite recently launched by my company, EE. Future Thinking is all about engaging with business users and entrepreneurs at organisations large and small, private and public sector.

      The content is editorial-driven from a team of respected business technology writers and we have also partnered with The Economist and The Telegraph to provide a wide range of insights into the future of technology for business owners and IT professionals.

      I hope you enjoy these articles – I would love to hear about the key strands of technology that you think will be the disruptors of the modern workforce, workplace and business world at large.

      1. On yer bike - how mobile tech is driving a no-car, no-office revolution
      As work becomes more something people do than a place they go we consider five genres of apps - from Wi-Fi and office space finders to travel for the car-less, office-less mobile worker.

      2. Machine-to-machine (M2M) and the Internet of Things (IoT) - ready for business?
      Far from being pure futuristic sci-fi fantasy ordinary businesses, both small and large, are already using and getting value out of the IoT. By starting to think in terms of connected things, organisations can reduce the risk of finding themselves, quite literally, outsmarted.

      3. Q&A: Jim Ginsburgh - the 'father of BYOD'
      Back in a pre-iPhone and tablet 2005 Jim Ginsburgh led a 'digital consumer' initiative at energy giant BP that gave staff an allowance to buy their own IT kit. In this exclusive interview nine years later Jim reflects on the lessons of that BP project and talks about the impact of consumerisation of technology on business IT today.

      4. BYOD and the post-PC mobile device tipping point for the workplace
      The desktop world gave corporate IT departments certainty. But we're now at an inflection point that sees tablets and smartphones outnumbering desktops and PCs and employees are increasingly bringing their own mobile devices. What does this mean for the future workplace?

      5. Cheat Sheet: How to build your own app store
      So-called enterprise app stores - internal mobile app repositories that enable employees to download apps in a similar style to commercial stores such as Apple's App Store and Google Play - are on the rise. This cheat sheet explains all you need to know to get up to speed.

      6. How mobility, cloud and Big Data will dominate the business IT agenda in 2014
      An in-depth look at the top priorities for chief information officers (CIOs) in 2014. It will be a year in which companies will become either masters or servants of these major disruptive technology forces and the pressure is on IT leaders to steer their organisations on the right course through these choppy waters.

      7. How small businesses (SMEs) can tackle mobile security without breaking the bank
      SMEs have to balance a lack of in-house IT skills and cash for mobile related security with the potential risks. This article explores some of the key threats and how SMEs can tackle them on a budget using cloud-based software and tools such as mobile device management (MDM).

      Thanks for visiting the site and your interest in oil and gas drilling

      free counters