diverter overshot packer brands

Cameron diverters are fully customizable for your floater and jackup rig operations, respectively. Designed for reliable, efficient use, each system consists of a housing, outlet valves, running tools, controls system, diverter assembly, overshot packers, and storage skids.

The CF-A diverter supports up to 75.5-in rotary tables and has a hang-off capacity of up to 2,500,000 lbm. It uses a single annular packing element with a pressure rating up to 500 psi. The CF-A diverter features four hydraulic locking dogs that reduce hosing and simplify operation. It eliminates the need to secure hoses to the diverter assembly while providing hydraulic fluid for the operations.

The CF-B diverter supports up to 47-in rotary tables and is qualified up to 2,000 psi. Packers can be split and hinged to allow them to be changed out with pipe in the hole. J-slot type running tools are entirely mechanical and require no hydraulics.

A permanent diverter housing attached under the rotary table eliminates mechanical connections of the flowline and accessory lines, and expedites rig operations

Diverters are used with casing advancement systems when drilling through overburden. The diverters slip over the top of the casing to direct cutting, and fluids away from the hole. A hose can be connected to the diverter outlet to further direct the flow away from the hole. Please contact your Hole Products representative for additional product details.

The diverter assembly is the uppermost component of the riser system.It is not used to shur or seal the well completely, but to either direct the teturing drill fluit or control the blowout and surface layer gas, when encountering the gas, the diverter can close off around drillpipe or casing,and open the special direction vent line on board at the same time

By utilizing our time-tested SEALFAST® inflatable and mechanical seals and packers, we are able to offer many flexible and configurable drilling stack solutions. Our products allow users to adjust for the height, angular alignment, and eccentricities in the drilling stack with unparalleled speed and efficiency. Our, fixed, telescoping, and spherical adjustment riser and mud flow line systems can be designed to accommodate down hole pressures from 5-2000 psig pressure ratings, with process mud temperatures of up to 300° F. Our active sealing technology continues to provide optimal sealing on mandrels and reducing faces, even if they corrode and wear over time, leading to lower maintenance costs

Mechanical Research & Design, Inc. designs and manufactures an assortment of fully certified Diverter and BOP support, restraint, lift, and storage equipment. Most units come certified for offshore portable equipment lifting and can include rated tie-down to deck structural steel for divert and upthrust events. Units can be adapted for integral nozzle load restraint for mud flow lines and safety rated work platforms. These frames are also used as make-up and load-rated hang-off platforms for surface drilling stacks.

• Design pressure ratings vary from 10 PSIG for some bell nipple overshot seal housings, to 2000 PSIG for higher pressure-rated diverter overshot packers.

These housings can be mounted under the drill floor or to under-deck structural beams, can integrate a full mud pan, as well as other process and flow lines necessary for managing mud elevations and quality during returns. These units are also ideal for use as weld or bolt-on adjustable low-pressure riser seal housings and diverter overshot seal housings.  They allow rapid height adjustment during diverter change-out

• Bell Nipple Overshot Seal Housings: General drilling mud collection and containment housings with integral mud pan; bleed, fill, trip, flow, and swarf lines/nozzles available upon request.

• Diverter Overshot Packer Seal Housings: quick and easy installation and actuation for high-pressure applications – can have integral flow lines to act as a t-spool for diverter stacks.

• Telescoping LP Riser Seal Housings: Best for use with telescoping low-pressure riser systems that require flexible height adjustment and large angular make-up requirements. Often referred to as telescoping riser seal housings or packer seal housings.

These dynamic seal housings are often found on floating production oil rigs, barges, and on drillships. They are commonly paired up with our inflatable spherical packers on KFDS diverter systems or as conductor unions, allowing for the drilling stack to accommodate vertical displacement from standard wave and tidal action, as well as ocean swells. These units come with low-friction mandrels and specially formulated “wear rings” for maximum life.

Often used as an alternative to reducing mandrel spools in bell nipple systems, our SEALFAST® Inflatable and Mechanical drop-in reducers give clients another way to manage various riser and conductor sizes needed for the multiple diverters and BOP stacks needed in some drilling programs. These units are a flexible solution to quickly reduce conductor, and riser sizes while maintaining full drill-through capability. These units can be designed for full hang-off and nozzle loads for the drill stack and can be paired with a mud box or housing that interfaces to the rig floor or underfloor structure.

Available in a wide array of sizes and pressures, our housings can be used laterally, vertically, or on inclines. These units come with and without integral mechanical restraint for full nozzle load requirements. Our new, cutting edge, inflatable and spherical seal housing packers allow for the ultimate flexibility for your mud transport, drill through, or flow line requirements.

Cameron diverters are fully customizable for your floater and jackup rig operations, respectively. Designed for reliable, efficient use, each system consists of a housing, outlet valves, running tools, controls system, diverter assembly, overshot packers, and storage skids.

The CF-A diverter supports up to 75.5-in rotary tables and has a hang-off capacity of up to 2,500,000 lbm. It uses a single annular packing element with a pressure rating up to 500 psi. The CF-A diverter features four hydraulic locking dogs that reduce hosing and simplify operation. It eliminates the need to secure hoses to the diverter assembly while providing hydraulic fluid for the operations.

The CF-B diverter supports up to 47-in rotary tables and is qualified up to 2,000 psi. Packers can be split and hinged to allow them to be changed out with pipe in the hole. J-slot type running tools are entirely mechanical and require no hydraulics.

At a time when the Offshore Equipment market is in turmoil, a new Manufacturer of Fixed Diverter Systems has emerged, providing New Technology, Patented in the United States, European Union and Singapore. AVERT-TEK LLC has focus on our customers (Drilling Contractors & Oil Companies) who require repairs, maintenance, and spare parts for their in-service equipment and also new equipment technology for the Diverter Well Control Systems.

Avert-Tek has compiled years of Diverter knowledge and capabilities, providing the current model KFDJ technology, and is introducing new technology in its Model DSP Diverter system. “DSP” stands for Diverter System Platforms and is focused on support of Jackup & Platform Shallow Water drilling.

OVERSHOTS - FOR WORK IN CASING 5" OD 4" CATCH SIZE WITH 2-7/8" SPIRAL GRAPPLE,A TYPE PACKER, SPIRAL GRAPPLE CONTROL AND 2-3/8" BASKET GRAPPLE,MILL CONTROLPACKER, TYPEF.S. UPPER CONN. NC26 BOX

OD 5-7/8" CATCH SIZE WITH 5" SPIRAL GRAPPLE,A TYPE PACKER, SPIRAL GRAPPLE CONTROL AND 4-1/2" BASKET GRAPPLE,MILL CONTROLPACKER, TYPE S.H. UPPER CONN. NC50 BOX

Petroleum and natural gas industries — Drilling and productionequipment — Shallow gas diverter equipmentIndustries du pétrole et du gaz naturel — Équipements de forage et de production — Équipement déflecteurpour gaz de surfaceOGP Draft 113354

Foreword..............................................................................................................................................................v Introduction ........................................................................................................................................................vi 1  Scope ......................................................................................................................................................1 2  Normative references ............................................................................................................................1 3  Terms and definitions ...........................................................................................................................1 4  Diverter system equipment...................................................................................................................7 4.1  General purpose ....................................................................................................................................7 4.2  Findings of blowout reports .................................................................................................................7 4.3  Applications of diverter systems .........................................................................................................8 4.4  Design considerations — Land rigs and bottom-supported marine structures .............................8 4.4.1  General....................................................................................................................................................8 4.4.2  Types of annular sealing devices in use .............................................................................................8 4.4.3  Vent outlets ..........................................................................................................................................12 4.4.4  Diverter valves .....................................................................................................................................14 4.4.5  Diverter piping .....................................................................................................................................15 4.4.6  The control system ..............................................................................................................................18 4.4.7  Kill-line facility .....................................................................................................................................18 4.4.8  Additional functions for the diverter system ....................................................................................18 4.5  Design considerations — Floating rigs .............................................................................................18 4.5.1  General..................................................................................................................................................18 4.5.2  Annular sealing devices in use ..........................................................................................................19 4.5.3  Auxiliary diverter system equipment for riser drilling .....................................................................21 4.5.4  Diverter outlets and valves .................................................................................................................23 4.5.5  Diverter piping .....................................................................................................................................23 4.5.6  Control system .....................................................................................................................................24 5  Floating rigs — Specific aspects .......................................................................................................24 5.1  Use of the marine riser ........................................................................................................................24 5.2  Additional functions of the diverter system .....................................................................................27 5.3  Comparison of types of floating support ..........................................................................................27 5.3.1  Moored drill ships ................................................................................................................................27 5.3.2  DP drill-ships ........................................................................................................................................28 5.3.3  Semi-submersibles ..............................................................................................................................28 5.3.4  Conclusion ...........................................................................................................................................28 6  Preparation for shallow gas operations ............................................................................................30 6.1  Call for tender ......................................................................................................................................30 6.2  Important issues ..................................................................................................................................30 6.3  Pre-spud checks ..................................................................................................................................31 6.3.1  Diesel engines and electrical equipment ..........................................................................................31 6.3.2  Kick and loss detection.......................................................................................................................31 6.3.3  Offshore rescue ...................................................................................................................................31 6.3.4  Offshore cooling recommendations ..................................................................................................31 6.3.5  Offshore emergency-release requirements ......................................................................................31 6.3.6  Rig safety equipment ..........................................................................................................................32 6.3.7  Safety precautions ...............................................................................................................................32 6.3.8  Diverter system ....................................................................................................................................32 6.4  Pre-spud meetings ..............................................................................................................................33 6.5  Pre-spud drills ......................................................................................................................................34 6.6  Preparing the response to a shallow-gas flow .................................................................................34 6.6.1  General..................................................................................................................................................34 6.6.2  Reminders ............................................................................................................................................35

6.6.3  Basic well-control aspects ................................................................................................................. 357  Diverter system maintenance ............................................................................................................ 38 7.1  General ................................................................................................................................................. 38 7.2  Certification and recertification ......................................................................................................... 38 7.3  Diverter system piping ........................................................................................................................ 38 7.4  Manufacturer documentation ............................................................................................................. 39 Bibliography ...................................................................................................................................................... 40

 Many past shallow-gas kicks turned into uncontrolled blowouts due to the failure of former diverter systems installed several decades ago. Failure is seen as a result of the system"s complexity, its lack of functional reliability and its inability to cope with the severe dynamic loads,

1 ScopeThis International Standard specifies requirements for the selection of the diverter equipment for rigs used todrill shallow-gas-bearing formations. It covers both onshore and offshore drilling operations, and considersalso the auxiliary equipment associated with floating rigs.

3.11control functioncontrol system circuit (hydraulic, pneumatic, electrical, mechanical, or a combination thereof) used to operatethe position selection of a diverter unit, BOP, valve or regulator

3.13diverterdevice attached to the wellhead or marine riser to close the vertical access and to direct any flow into a set ofvent lines and away from the drilling unit

3.18diverter systemassemblage, comprising an annular sealing device, flow control means, vent system components and controlsystem, which facilitates closure of the upward flow path of the well fluid and opening of the vent to theatmosphere

3.54subsea diverterseabed diverterset-up of equipment attached to the bottom of the marine riser and connected to the 762 mm (30 in) subseawellhead housing, designed to close the well in case of shallow-gas influx and to direct it through two subsealateral vent outlets

3.58telescopic joint packertorus-shaped, hydraulically, pneumatically or mechanically actuated, resilient element between the inner andouter barrels of the telescopic joint which serves to retain drilling fluid inside the marine riser

The diverter system is designed to permit the drilling crew to blow down shallow-gas accumulations downwindof the rig. Until a sufficient casing length has been set to allow a well to be shut-in during a kick, the divertersystem is the only line of defence, and is only expected to contain the hazard temporarily, although as long aspossible.

The diverter system is not intended to be a well-control device. It simply allows the flow to be diverted in asafe manner in order to allow enough time to attempt regaining primary control of the well and, should thelatter fail, enough time for proper evacuation of the drilling crew or for proper move-off of the drilling unit fromthe location (floating rigs), until the flow stops due to gas accumulation blow-down, hole bridging, holecollapse, etc.

Blowout inquiries have concluded that the original designs underestimated the fact that shallow-gas blowoutsproduce huge amounts of gas, together with abrasive solids, flowing at very high speed, producing severedynamic loads, and eroding and destroying many parts of the existing diverter systems.

Statistics obtained in the 1990s in Norway have shown that 54 % of shallow-gas blowouts caused severedamage or total loss of the drilling structure and support, due to the failure of the diverter system.Unfortunately, many lives were lost during those dramatic events.

It is therefore of paramount importance to select suitable equipment able to function in a reliable and safemanner, i.e. able to operate whenever required under the worst possible conditions. Diverter equipment shallalso be able to cope with the prevailing dynamic loads and associated effects.

In the insert-type diverter assembly, the insert packing is latched in place into a diverter assembly, which inturn is locked inside the support housing. This housing provides two outlets, one for the mud returns to flowtowards the shakers, one for the diverted fluids to flow out through the vent line(s). The insert is removed priorto pulling or running the bottom-hole assembly (see Figure 1).

This set-up requires a conventional bag-type preventer and a drilling spool (or diverter spool) which aredirectly located on top of the first casing (conductor pipe, drive pipe). This set-up is therefore below the rotarytable and below the flow-line, unlike the insert-type diverter assembly (see Figure 2).

Key1 Bell nipple 6 Vent line2 Flow line 7 Diverter spool3 Fill-up line 8 Hydraulically operated full opening valve4 Annular packing element 9 Drive / Conductor pipe5 Standard bag-type preventer

 insert-type packer usually closes fast (a few seconds), while the operation of the vent and flow- line valves takes much longer (> 40 s), hence imposing a sequencing system to prevent closure of the packer prior to proper operation of the valves;

The standard hook-up option eliminates the need for a flow-line valve, as the flow-line is located at the level ofthe bell nipple, well above the diverter set-up.

The use of an overshot packer, required for length adjustment below the diverter system, is also eliminated,hence removing a potential leak point at pack-off level. Conversely, this adjustment joint and its packer can beused without risk above the bag preventer, as it will not experience any gas flow pressure.

Another safe alternative is to use an integral diverter assembly, which integrates the diverter spool and theannular packing into a single piece of equipment.

In this system the motion of the annular piston is used, in one stroke, to first open the vent lines and then stopthe upward flow. The flow-line is located at the level of the bell-nipple, well above the integral diverterassembly, hence eliminating the need for a specific flow-line valve (see Figures 3 and 4).

Several types of valve are commonly associated with diverter systems: gate valves, ball valves, switchablethree-way target valves, knife valves, valves integral to the diverter unit and sometimes burst disks.

For insert-type diverter systems requiring actuation of valves on both shaker and vent lines, an interlocksystem shall prevent the diverter from closing before the valves are in the correct position (i.e. shaker valveclosed, vent-line valve open). This is of paramount importance with these systems, where the response timeof the insert packer is much lower than that of the shaker and vent-line valves [usually less than 10 s to closeon a 127 mm (5 in) drill pipe].

Actuators fitted to a diverter valve shall be sized to open the valve at least with the rated working pressure(WP) of the diverter system applied across the valve.

The safest and most reliable option is the integral diverter system (see Figures 3 and 4) in which the physicalneed for valves is eliminated. In such a system, the shaker and fill-up lines are located far above the divertersystem within the rig sub-structures, and do not require any shut-off valves.

Diverter piping shall consequently be sized and its layout designed such that the anticipated back-pressure,calculated with realistic gas flow rates, do not exceed the rated working pressure of the diverter system, donot exceed the design pressure of other equipment, and do not place undue pressure on the wellbore.

At the rig site location, the diverter vent-lines shall extend a sufficient distance in the most appropriatedirection from the rig to permit safe venting of diverted well fluids.

Consequently, the minimum required nominal internal diameter (ID) of diverter outlets and vent-lines shall be355,6 mm (14 in). The piping wall thickness shall not be less than 19,05 mm (0,75 in).

The diverter control system shall be designed and sized in accordance with API 16D:2005, Section 5.5. It shallcontain the minimum of functions. Preferably, a one-button or lever-activated function shall operate the entirediverter system.

A 38,1 mm (1½ in) hydraulic operating line should be used for diverter systems with a 1½ in NPT closingchamber port size. The hydraulic line for the opening chamber port may be 25,4 mm (1 in).

Many shallow-gas blowout reports have mentioned failures of the pneumatic control system used to operatediverter valves (e.g. failure to work as required when valves stems are blocked with solids). A pneumaticcontrol system shall therefore be avoided on rigs, if possible.

Each diverter system should incorporate a kill-line facility (including a check valve) to allow pressure-testing ofthe annular packing element closed on open hole, with no pipe in hole. This facility can also be used toperiodically flush the system clean.

Another advantage of a kill-line facility is to pump water through the diverter system during a gas-flow divertingoperation, in order to wet the gas and accordingly reduce the fire risk.

The use of a diverter system (alone or combined with a BOP set-up) should be considered on multi-wellplatforms, due to potential hazards such as collision with adjacent wells or surface-gas accumulations due topoorly cemented casings.

Though many parts of the diverter system are identical to those used on land rigs and bottom-supportedmarine structures, others are specific to floating units and are reviewed hereafter.

When drilling shallow-gas-bearing formations with a riser, two types of sealing device are used: the surfaceinsert-type diverter assembly and the subsea diverter.

By design, this system is basically similar to the system used on land rigs and bottom-supported marinestructures. The diverter support housing is permanently fixed to the drill-floor substructure below the rotarytable at the upper end of the marine riser system, and provides outlets for the shakers and for ventingpurposes. The diverter assembly is locked down inside the housing, and the insert packer is locked inside thelatter.

For floating supports, the possibilities to improve the surface vent-lines network and routing being substantiallyreduced, the subsea diverter system is a safer alternative. The basic set-up includes, from top to bottom: aflex joint, an annular BOP (or a shear ram unit), a diverter spool and a riser hydraulic connector (seeFigure 6).

If the subsea diverter option is selected, it is recommended to hook up a riser booster line above the upperclosing unit (bag or shear ram), to eliminate any gas which has entered the riser before complete well shut-off.An additional diverter system (e.g. the basic insert-type assembly) is required at surface to deal with this gasinflux (see also 4.5.2.3 and 5.2).

Prior to choosing this option, it is important to look carefully at the water depth and the type of support vesselwhich has been selected. Even after its transit through the water column, gas still represents a potentialexplosion and fire hazard, mainly as it concentrates in the moon-pool area. With gas being vented at seabedlevel and percolating up to surface, the subsea diverter is probably not the best choice with a drill-ship inshallow water depths.

Key Key1 539,7 mm (21 1/4’’) Flex Joint 1 539,7 mm (21 1/4’’) Flex Joint2 539,7 mm (21 1/4’’) Annular BOP 2 539,7 mm (21 1/4’’) Annular BOP3 539,7 mm (21 1/4’’) Diverter spool w/ integral valving 3 539,7 mm (21 1/4’’) Shear ram and 304,8 mm (12’’) outlets 4 539,7 mm (21 1/4’’) Diverter spool4 Guide structure 5 Outlet nozzle5 762mm (30’’) Hydraulic connector 6 762 mm (30’’) Hydraulic connector

NOTE The diverter is shown here in the drilling mode. When the diverter closes in case of gas influx, the piston movesupward, opening the flow path to the vent line while closing the flow path to the flow line.

Should surface diverting be considered as too hazardous (in particular if the integral diverter system is notavailable), the requirement for safe operation is to use the subsea diverter. Its use depends however on thewater depth at the drilling location, the virulence of reported local shallow-gas events, the type of supportvessel contemplated and the competence of the chartered drilling contractor.

The insert-type diverter system should only be used in conjunction with a subsea diverter or with a BOP stack,to circulate and vent out any gas trapped in the riser (see 5.2).

The same comments for land rigs and bottom-supported marine structures given in 4.4.3 and 4.4.4 apply tovent outlets and diverter valves for floating rigs.

On floating rigs (as for land rigs and bottom-supported marine structures), since the size and number of vent-lines have a great influence on surface and downhole hazards, two properly sized vent-lines shall be used.The minimum nominal ID of diverter outlets and vent-lines shall be 355,6 mm (14 in).

Key1 Flow selector always open2 Diverter with integral valve functions3 To Shale shaker4 To Vent lines5 To Starboard vent line6 To Port vent line

The diverter control system shall be designed and sized according to API 16D:2005, Section 5.5. Pneumaticcontrol systems shall be avoided on rigs working in shallow-gas-prone areas.

Each operating company has its own drilling policy with respect to using (or not) the marine riser while drillingshallow-gas-prone formations. The general mistrust of existing diverter systems on most floating rigs has ledsome operators to adopt a riserless approach. The following comments can be made.

Whatever the pros and cons of riser use, a preliminary careful and thorough review of the reliability andcapacity of the rig diverter system (see 4.5.2) and of the reliability and capacity of the emergency-releasesystem of the floating-support mooring lines can provide decisive criteria to assist in selecting the beststrategy.

 Gas can inadvertently enter the riser when the BOP is shut-in on a kick. Gas can also enter the riser if the rams leak after the BOP is closed. Using the diverter system, the gas in the riser can be safely removed and diverted overboard,

 After a kick circulation is completed, some compressed trapped gas can remain between the closed BOP and the choke-line connection. This gas will tend to migrate into the riser when the BOP is re-opened. Using the diverter system, this gas can also be safely removed and diverted overboard.

 a competent drilling crew, having past experience in shallow-gas drilling, purposely trained and familiar with the diverter equipment and its proper testing, maintenance, and operation;

Prior to drilling a shallow-gas formation, all the diverter system components shall be inspected and tested toascertain proper installation and function. As a minimum, the following tasks shall be carried out.

 Ensure that any fill-up line which can be exposed to the gas flow is protected with a check valve; this line and check valve shall have a WP equivalent to that of the diverter system.

d) Simulate loss of rig air supply to the diverter control system and determine effects, if any, on the diverter system, valves, and back-up systems.

On a routine basis, when in primary diverter service (no BOP installed), function tests should be performeddaily using the driller’s panel to verify that functions are operable. Fluid should be regularly pumped througheach diverter line during drilling operations to ensure that they are clear of obstructions at all times.

 review all preliminary checks related to, among others, the diverter system, kick detection equipment, kill mud volumes, emergency power supply, safety, rescue and emergency equipment, emergency communication systems, mooring equipment if applicable, etc.;

All concerned personnel should therefore be familiar with the diverter system components and installation,and should be capable of reacting quickly and efficiently to potential situations requiring use of the diverter.

Any defect or problem with equipment or personnel identified during any of these pre-spud drills should beimmediately reported and dealt with before drilling is permitted to start. Thereafter, drills should be conductedat appropriate intervals to ensure personnel are capable of quickly and competently reacting to situationsrequiring use of the diverter.

If practically feasible, a tentative well kill should be attempted immediately with heavy kill mud and themaximum pumping rate available, after the diverter system has been activated, to try to stop the gas flowdownhole, prior to complete well unloading.

A schedule for routine inspection and maintenance of diverter systems equipment should be prepared andmaintained by the rig operating personnel. Specific guidelines for each diverter component or sub-systemshould be based on installation, operation and maintenance manuals provided by the equipmentmanufacturer.

 During diverter function tests, observe all components of the diverter system including the diverter, valves, valve actuators, piping, and control panel to verify that there are no leaks in the system. If a leak is discovered, it should be repaired immediately.

 All diverter equipment shall be maintained with original equipment manufacturer’s (OEM) genuine or approved spares and shall be operated and tested in accordance with that manufacturer"s recommended procedures. Major repairs, overhaul on and recertification of diverter equipment shall be performed either by the OEM or an alternative provider, but then only when approved by the OEM.

 A visual inspection, a body-pressure test and a full-function test shall be carried out once a year on a diverter test stump at surface, in accordance with the manufacturer"s specification for such a test and witnessed by a certified third party. Results of the inspections and tests, including follow-up, shall be documented, providing full traceability and be part of the formal service history.

 At least every five years, the diverter system components shall be inspected for repair or remanufacturing by the OEM or OEM-approved service provider. Upon completion of the inspection, the OEM shall provide a Certificate of Conformance (COC).

The wall thickness on all undesirable turns and bends (if any) in the diverter system piping should be checkedat least annually and after each use of the system to divert a well kick. Erosion of metal from the turns andbends can be severe if sustained flows of gas-associated solids are diverted through the system.

Installation, operation and maintenance manuals furnished by the manufacturers of the various components ofthe diverter system should be readily available for training, reference, and use by maintenance personnel.