Subsea gas separation system and method for offshore drilling

Information

  • Patent Grant
  • 6276455
  • Patent Number
    6,276,455
  • Date Filed
    Thursday, September 24, 1998
    26 years ago
  • Date Issued
    Tuesday, August 21, 2001
    23 years ago
Abstract
A subsea gas separation system use in drilling an offshore well includes a subsea blowout preventor connected to the well and a gas separator connected to the blowout preventor near the seafloor. Gas released into the well bore during a well control event is removed at the separator and not returned with the drilling mud recirculated to the surface. A method offshore drilling includes a mud circulation circuit established leading down the drill string, through the drill bit, up the borehole, through a subsea pump, and to the surface through a return riser. The subsea pump is protected during critical well control events by removing gas released into the mud at a gas separator located upstream of the subsea pump and in communication with the blowout preventor.
Description




BACKGROUND OF THE INVENTION




The present invention relates to drilling systems and operations. More particularly, the present invention is a method and system for handling formation fluids entering the wellbore in the form of a hydrocarbon gas during well events.




Drilling fluids, also known as muds, cool the drill bit, flush the cuttings away from the bit's formation interface and then out of the system, and stabilize the borehole with a “filter cake” until newly drilled sections are cased. The drilling fluid also performs a crucial well control function and is monitored and adjusted to maintain a pressure with a hydrostatic head in uncased sections of the borehole that prevents the undesired flow of pressured well fluids into the borehole from the formation during drilling operations, i.e., well control events.




Conventional offshore drilling circulates drilling fluids down the drill string and returns the drilling fluids with entrained cuttings through an annulus between the drill string and the casing below the mudline. A riser surrounds the drill string starting from the wellhead at the ocean floor to drilling facilities at the surface and the return circuit for drilling mud continues from the mudline to the surface through the riser/drill string annulus.




In this conventional system, the relative weight of the drilling fluid over that of seawater and the length of the riser in deepwater applications combine to exert an excess hydrostatic pressure in the riser/drill string annulus.




Systems have been conceived to bring the drilling fluid and entrained cuttings out of the annulus at the base of the riser and to deploy a subsea pump to facilitate the return flow through a separate line. One such system is disclosed in U.S. Pat. No. 4,813,495 issued Mar. 21, 1989 to Leach. That system requires complex provisions to ensure the closely synchronous operation of the supply and return pumps critical to the approach disclosed. However, the durability and dependability of such a mud circulation system is suspect in the offshore environment and particularly so in light of the incompatibility of the fluid with pumping operations following a well control event.




Thus, there remains a need for technology facilitating subsea pump operation for the return of drilling fluid to the surface.




A SUMMARY OF THE INVENTION




One aspect of the present invention is a subsea gas separation system for use in drilling an offshore well in which a subsea blowout preventor is connected to the well and a gas separator is connected to the blowout preventor near the seafloor. Gas released into the well bore during a well control event is removed at the separator and not returned with the drilling mud recirculated to the surface.




Another aspect of the present invention is a method for offshore drilling in which a mud circulation circuit is established leading down the drill string, through the drill bit, up the borehole, through a subsea pump, and to the surface through a return riser. The subsea pump is protected during critical well control events by removing gas released into the mud at a gas separator located upstream of the subsea pump and in communication with the blowout preventor.











A BRIEF DESCRIPTION OF THE DRAWINGS




The brief description above, as well as further objects and advantages of the present invention, will be more fully appreciated by reference to the following detailed description of the preferred embodiments which should be read in conjunction with the accompanying drawings in which:





FIG. 1

is a schematic illustration of one embodiment of a subsea pumping system for deepwater drilling;





FIG. 2

is a side elevational view of a one embodiment of a subsea pumping system for deepwater drilling;





FIG. 3

is a side elevational view of the dedicated riser section in the embodiment of

FIG. 2

;





FIG. 4

is a top elevational view of the dedicated riser section of

FIG. 3

;





FIG. 5

is a longitudinally taken cross sectional view of the drill string shut-off valve of

FIG. 2

in a closed position;





FIG. 6

is a longitudinally taken cross sectional view of the drill string shut-off valve of

FIG. 2

in an open position;





FIGS. 7A-7C

are longitudinally taken cross sections of another embodiment of a drill string shut-off.











A DETAILED DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS





FIG. 1

illustrates schematically one embodiment of a drilling fluid circulation system


10


in accordance with the present invention. Drilling fluid is injected into the drill string at the drilling rig facilities


12


above ocean surface


14


. The drilling fluid is transported down a drill string (see FIG.


2


), through the ocean and down borehole


16


below mudline


18


. Near the lower end of the drill string the drilling fluid passes through a drill string shut-off valve (“DSSOV”)


20


and is expelled from the drill string through the drill bit (refer again to FIG.


2


). The drilling fluid scours the bottom of borehole


16


, entraining cuttings, and returns to mud line


18


in annulus


19


. Here, near the ocean floor, the drilling mud is carried to a subsea primary processing facility


22


where waste products, see line


24


, are separated from the drilling fluid. These waste products include at least the coarse cuttings entrained in the drilling fluid. With these waste products


24


separated at facilities


22


, the processed drilling fluid proceeds to subsea return pump


26


where it is pumped to drilling facilities above surface


14


. A secondary processing facility


28


may be employed to separate additional gas at lower pressure and to remove fines from the drilling fluid. The reconditioned drilling fluid is supplied to surface pump system


30


and is ready for recirculation into the drill string at drilling rig


12


. This system removes the mud's hydrostatic head between the surface and the seafloor from the formation and enhances pump life and reliability for subsea return pump system


26


.




The embodiment of

FIG. 1

can be employed in both drilling operations with or without a drilling riser. In either case, the hydrostatic pressure of the mud return through the water column is isolated from the hydrostatic head below the blow-out preventor, near the seafloor. Indeed, with sufficient isolation the return path for the mud could proceed up the drilling riser/drill string annulus. However, it may prove convenient to have a separate riser for mud return whether or not a drilling riser is otherwise employed. Further, even if not used as the mud return line through the water column, it may be convenient to have a drilling riser to run the blowout preventor and separation equipment discussed below. See FIG.


2


.




Returning to

FIG. 1

, another advantage of this embodiment is that gas resulting from a well control event is removed at gas separator


52


and is expelled near seafloor


18


. Pump operation in such well events is critical. In a well control event in which large volumes of gas enter the well, the overall system must handle gas volumes while creating an acceptable back pressure on the wellbore


16


by pumping down heavier weight mud at sufficient volume, rate and pressure. Dropping below this pressure in a well control event will result in additional gas influx, while raising pressure to excess may fracture the borehole. The ability to cycle through muds at weights suited to the immediate need is the primary control on this critical pressure. However, multiphase flow is a challenge to conventional pumps otherwise suited to subsea return pump system


26


. Thus, only substantially gas free mud is pumped to the surface through subsea return pump system


26


, facilitating pump operation during critical well control events. Additional gas may be removed at the surface atmospheric pressure with an additional gas separation system, not shown.





FIG. 2

illustrates the subsea components of one embodiment of drilling fluid circulation system


10


, here with a drilling riser that is not used for returning the mud through the water column. The drilling fluid or mud


32


is injected into drill string


34


which runs within marine drilling riser


36


, through a subsea blow-out preventor (“BOP stack”)


38


near the mudline


18


, through casing


40


, down the uncased borehole


16


to a bottom hole assembly


42


at the lower end of the drill string. The bottom hole assembly includes DSSOV


20


and drill bit


44


.




The flow of drilling mud


32


through drill string


34


and out drill bit


44


serves to cool the drill bit, flush the cuttings away from the bit's formation interface and to stabilizes the uncased borehole with a “filter cake” until additional casing strings


40


are set in newly drilled sections. Drilling mud


32


also performs a crucial well control function in maintaining a pressure with a hydrostatic head in uncased sections of the borehole


16


that prevents the uncontrolled flow of pressured well fluids into the borehole from the formation.




However, in this embodiment, the drilling mud is not returned to the surface through the marine riser/drill string annulus


46


, but rather is withdrawn from the annulus near mudline


18


, e.g., immediately above BOP stack


38


through mud return line


19


. In this illustration, with a drilling riser, the remainder of annulus


46


, to the ocean surface, is filled with seawater


48


which is much less dense than the drilling mud. Deepwater drilling applications may exert a thousand meters or more of hydrostatic head at the base of marine drilling riser


36


. However, when this hydrostatic head is from seawater rather than drilling mud in annulus


32


, the inside of the marine drilling riser remains substantially at ambient pressure in relation to the conditions outside the riser at that depth. The same is true for mud leaving the well bore in riserless embodiments. This allows the drilling mud specification to focus more clearly on well control substantially from the mudline down.




Drilling mud


32


is returned to the surface in drilling fluid circulation system


10


through subsea primary processing


22


, subsea return pump


26


and a second riser


50


serving as the drilling mud return line. In this embodiment, subsea primary processing


22


is illustrated with a two component first stage


22


A carried on the lowermost section of drilling riser


36


and a subsequent stage


22


B on the ocean floor.




In normal operation, solids removal system


54


first draws the return of drilling mud


32


. Here solids removal system


54


is a gumbo box arrangement


68


which operates in a gas filled ambient pressure dry chamber


72


. The hydrostatic head of mud


32


within the annulus


46


drives the mud through the intake line and over weir


74


to spill out over cuttings removal equipment such screens or gumbo slide


78


. Cuttings


76


too coarse to pass between bars or through a mesh screen proceed down the gumbo slide, fall off its far edge beyond mud tank


80


, and exit directly into the ocean through the open bottom of dry chamber


72


. The mud, less the cuttings separated, passes through the gumbo slide and is received in mud tank


80


and exits near the tank base.




Remote maintenance within gumbo box arrangement


68


may be facilitated with a wash spray system to wash the gumbo slide with seawater and a closed circuit television monitor or other electronic data system in the dry chamber.




Cuttings


76


can be prevented from accumulation at the well by placing a cuttings discharge ditch


84


beneath dry chamber


72


to receive cuttings exiting the dry chamber (and perhaps the dump valve). A jet pump


86


injects seawater past a venturi with a sufficient pressure drop to cause seawater and any entrained cuttings to be drawn into cuttings discharge line


88


from cuttings discharge ditch


84


. The cuttings discharge line then transports the cuttings to a location sufficiently removed such that piles of accumulated cuttings will not interfere with well operations.





FIGS. 3 and 4

illustrate in detail an alternate embodiment in which components of first and second stage processing


22


A and


22


B as well as gas separator


52


are mounted on a dedicated riser section


36


A. The dedicated riser needs to be sized to be run through the moonpool of the surface drilling facilities, preferably having a horizontal cross section no greater that the BOP stack outline


104


, illustrated in

FIG. 4

in dotted outline


100


.




Components, here a pair of gumbo boxes


68


and a pair of horizontal gas/mud separators


58


, are mounted on frame


102


secured to dedicated riser joint


36


A. Cuttings discharge ditches


84


, jet pumps


86


, and cuttings discharge lines


88


are also mounted to this riser section. This allows connections between these initial components and the annulus within marine drilling riser


36


and BOP stack


38


to be fully modularly assembled on the surface before the drilling riser is made up to the subsea well.




Returning to

FIG. 2

, the illustrated embodiment also provides subsequent stage processing


22


B, here a further solids removal system


54


A, in the form of a second gumbo box arrangement


68


A in gas filled ambient pressure dry chamber


72


A. The hydrostatic head of mud


32


within tank


80


drives the mud and over weir


74


A to spill out mud and entrained cuttings over more closely spaced bars or a finer mesh screen gumbo slide


78


A. Mud separated in mud/gas separator


52


may join that from tank


80


in this second stage processing. A finer grade of cuttings is removed and carried away with cuttings discharge ditch


84


A and jet pump


86


B, as before, with the processed mud passing to mud tank


80


A.




It may also be desirable to provide the position of normal tank exit and a tank volume that allows settling of additional cuttings able to pass through the gumbo slide. A surface activated dump valve


82


at the very bottom of the mud tank may be used to periodically remove the settled cuttings.




The suction line


94


of subsea return pump


26


is attached to the base of mud tank


80


A. A liquid level control


90


in the mud tank or subsequent subsea mud reservoir activates return pump. The removal of the cuttings from the mud greatly enhances pump operation in this high pressure pumping operation to return the cuttings from the seafloor to the facilities above the ocean surface through a return riser


50


. The return riser may be conveniently secured at its base to a foundation such as an anchor pile


98


and supported at its upper end by surface facilities (not shown), perhaps aided by buoyancy modules (not shown) arranged at intervals along its length. A return pump is provided to propel the mud up the return riser to the surface. A suitable pump may be deployed into the subsea environment or, as in this embodiment, the return pump is housed in an ambient pressure dry chamber


92


which improves the working environment and simplifies pump design and selection.




In well control events, BOP stack


38


is closed and the gas separator


52


intakes from subsea choke lines


33


associated with BOP stack


38


. The intake leads to a vertically oriented tank or vessel


58


having an exit at the top which leads to a gas vent


60


through an inverted u-tube arrangement


62


and a mud takeout


64


near its base which is connected into return line


66


downstream from solids removal system


54


. In such a well control event, gas separator


52


permits removal of gas from mud


32


so that subsea pump system


26


may operate with only a single phase component, i.e., liquid mud. The gas separator


52


may be conveniently mounted with a bracket


57


to the lowermost riser section


36


or, as illustrated in

FIGS. 3 and 4

, a dedicated riser section


36


A.





FIG. 5

details a DSSOV


20


deployed at the base of drill string


34


as part of bottom hole assembly


42


in FIG.


2


. The DSSOV is an automatic valve which uses ported piston pressures/spring balance to throw a valve


112


for containing the hydrostatic head of drilling fluid


32


within the drill string when the bottom hole assembly is in place and the normal circulation of the drilling fluid is interrupted, e.g., to make up another section of drill pipe into the drill string. In such instances the DSSOV closes to prevent the drilling fluid from running down and out of the drill string and up the annulus


46


, displacing the much lighter seawater until equilibrium is reached. See FIG.


2


.





FIGS. 5 and 6

illustrate DSSOV


20


in the closed and open positions, respectively. The DSSOV has a main body


120


and may be conveniently provided with connectors such as a threaded box


122


and pin


124


on either end to make up into the drill string in the region of the bottom hole assembly. The body


120


presents a cylinder


128


which receives a piston


116


having a first pressure face


114


and a second pressure face


130


. First pressure face


114


is presented on the face of the piston and is ported to the upstream side of DSSOV


20


through channel


132


passing through the piston. Channel


132


may be conveniently fitted with a trash cap


134


.




Second pressure face


130


is on the back side of piston


116


and is ported to the downstream side of DSSOV


20


. Further, the first and second pressure faces of piston


116


are isolated by o-rings


136


slidingly sealing between the piston and the cylinder.




Body


120


also has a main flow path


140


interrupted by valve


112


, but interconnected by drilling mud flow channels


126


and a plurality of o-rings


142


between valve


112


and body


120


isolate flow from drilling mud flow channels


126


except through ports


118


.




The DSSOV is used to maintain a positive surface drill pipe pressure at all times. When the surface mud pump system


30


(see

FIG. 1

) is shut off, e.g., to add a section of drill pipe


34


as drilling progresses, valve shut-off spring


110


shuttles valve


112


to a closed position in which valve ports


118


are taken out of alignment with drilling mud flow channels


126


in body


120


. See FIG.


5


. The spring


110


, the surface area of first pressure face


114


, and the surface area of the second pressure face


130


of piston


116


are balanced in design to close valve


112


to maintain the pressure margin created by the differences in density between seawater


48


and mud


32


over the distance between surface


14


and ocean floor


18


. See FIG.


1


. This holds the excess positive pressure in drill pipe


34


, keeping it from dissipating by driving drilling mud down the drill pipe and up annulus


46


, while isolating the excess pressure from borehole


16


. See FIG.


2


.




After a the new drill pipe section has been made up or drilling is otherwise ready to resume, surface pump system


30


(

FIG. 1

) is used to build pressure on valve


112


until the pressure on face


114


of piston


116


overcome the bias of spring


110


, opening valve


112


and resuming circulation. See FIG.


6


.




DSSOV


20


also facilitates a method of determining the necessary mud weight in a well control event. With the DSSOV closed, pump pressure is slowly increased while monitoring carefully for signs of leak-off which is observed as an interruption of pressure building despite continued pump operation. This signals that flow has been established and the pressure is recorded as the pressure to open the DSSOV. Surface pump system


30


is then brought up to kill speed and the circulating pressures are recorded. Kill speed is a reduced pump rate employed to cycle out well fluids while carefully monitoring pressures to prevent additional influx from the formation. The opening pressure, kill speed and circulating pressure are each recorded periodically or when a significant mud weight adjustment has been made.




With such current information, the bottom hole pressure can be determined should a well control event occur. Shutting of surface pump system


30


after a flow is detected will close off DSSOV


20


. The excess pressure causing the event, that is the underbalanced pressure of the formation, will add to the pressure needed to open valve


112


. Pump pressure is then reapplied and increased slowly, monitoring for a leak-off signaling the resumption of flow. The pressure difference between the pre-recorded opening pressure and the pressure after flow is the underbalanced pressure that must be compensated for with adjustments in the density of mud


32


. The kill mud weight is then calculated and drilling and adjustments are made accordingly in the mud formulation.





FIGS. 7A-7C

illustrate another DSSOV embodiment, DSSOV


20


A, in full open, intermediate, and closed positions, respectively. The DSSCOV cylinder has three regions,


128


A,


128


B and


128


C. An additional profile in piston


116


provides paired large and small pressure faces as first pressure faces,


114


A and


114


B paired with corresponding second pressure faces


130


A and


130


B. Pressure faces


130


A and


114


A engage region


128


A of the cylinder during normal mud circulation. Pressure faces


130


A and


114


A have a greater area than pressure faces


130


B and


114


B. This means that a lower pressure differential will keep valve


112


open. However, when the balance shifts such that the DSSOV starts to close, pressure faces


130


A and


114


B disengage from a sealing relationship with the cylinder walls in region


128


A as the piston moves and these faces align with large diameter region


128


B. The smaller area pressure faces


130


B and


114


B are then aligned in a sealing relationship with a reduced region


128


C of the cylinder.




In the illustrated embodiment, some of the components of the subsea primary processing system


22


are provided on the marine drilling riser


36


and others are set directly on ocean floor


18


. As to components which are set on the ocean floor, it may be useful to deploy a minimal template or at least interlocking guideposts and receiving funnels to key components placed as subsea packages into secure, prearranged relative positions. This facilitates making connections between components placed as separate subsea packages with remotely operated vehicles (“ROV”). Such connections include electric lines, gas supply lines, mud transport lines, and cuttings transport lines. A system of gas supply lines (not shown) supply each of the dry chambers


72


,


72


A, and


92


to compensate for the volumetric compression of gas in the open-bottomed dry chambers when air trapped at atmospheric pressure at the surface is submerged to great depths. Other combinations of subsea primary processing components and their placement are possible. Further, some components may be deployed on the return riser


50


analogous to the deployment on marine drilling riser


36


.




Other modifications, changes, and substitutions are also intended in the foregoing disclosure. Further, in some instances, some features of the present invention will be employed without a corresponding use of other features described in these illustrative embodiments. Accordingly, it is appropriate that the appended claims to be construed broadly and in a manner consistent with the spirit and scope of the invention herein.



Claims
  • 1. A subsea gas separation system for use in drilling an offshore well, comprising:a subsea blowout preventor connected to the well; a gas separator connected to the blowout preventor near the seafloor; whereby gas released into the well bore during a well control event is removed at the gas separator so that the gas is not returned with the drilling mud recirculated to the surface.
  • 2. A subsea gas separation system in accordance with claim 1 further comprising a marine drilling riser connected to the blowout preventor and wherein the gas separator is mounted on the marine riser.
  • 3. The gas separation system of claim 1, wherein said gas separator is comprised of:a vertically oriented tank having an exit at its top and a mud takeout near its base; intakes connecting chocke lines connected to the subsea blowout preventor to the vertically oriented tank; a gas vent connected to the exit and leading to the subsea ambient environment through an inverted u-tube section of the gas vent; and a return line connected to the mud takeout.
  • 4. A method for offshore drilling, comprising:establishing a mud circulation circuit of down a drill string, through a drill bit, up a borehole, through a subsea pump, and to the surface through a return riser; and protecting the subsea pump during critical well control events by removing gas released into the mud at a gas separator located upstream of the subsea pump and in communication with a blowout preventor.
  • 5. A subsea gas separation system for use in drilling an offshore well to remove gas introduced into the drilling mud from a well control event, the subsea gas separation system comprising:a subsea blowout preventor connected to the well; subsea choke lines connected to the well through the subsea blowout preventor; and a gas separator near the seafloor connected to the subsea choke lines and operating at ambient pressure whereby pressure fluctuations upstream of the subsea choke lines are controlled and whereby said gas is not returned with the drilling mud to the surface.
  • 6. A subsea gas separation system for use in drilling an offshore well with a drilling system including a subsea pump for returning drilling mud to the surface, the subsea gas separation system comprising:a subsea blowout preventor connected to the well; a gas separator connected to the blowout preventor near the seafloor; whereby gas released into the well bore during a well control event is removed at the gas separator so that the gas is not returned with the drilling mud recirculated to the surface.
  • 7. A method for offshore drilling, comprising:establishing a circulation circuit for the drilling mud of down a drill string, through a drill bit, up a borehole, through a subsea pump and to the surface through a return riser; and protecting the subsea pump during critical well control events by removing gas released into the mud at a gas separator located upstream of the subsea pump and in communication with a blowout preventor, said gas separator operating at subsea ambient pressure whereby the mud passing to the subsea pump is substantially in a single phase liquid state.
  • 8. A subsea gas separation system for use in drilling an offshore well to address gas influx in drilling mud resulting from a well control event, the system comprising:a subsea blowout preventor, having subsea choke lines, connected to the well; a gas separator near the sea floor and connected to the subsea choke lines and operating at subsea ambient pressure whereby well bore pressure from the gas influx is controlled and the gas is separated from the drilling mud prior to the mud being returned to the surface.
Parent Case Info

This application claims priority to provisional application No. 60/060,031 filed Sep. 25, 1997.

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Provisional Applications (1)
Number Date Country
60/060031 Sep 1997 US