Apparatus and method for managed pressure drilling

Information

  • Patent Grant
  • 8631874
  • Patent Number
    8,631,874
  • Date Filed
    Thursday, January 6, 2011
    14 years ago
  • Date Issued
    Tuesday, January 21, 2014
    11 years ago
Abstract
A drilling system employing a main tubular having a plurality of fluid inlet and outlet conduits positioned thereon and a concentric inner tubular having a plurality seals for sealing the annular space between the concentric inner and main tubulars. The fluid inlet and outlet conduits work in cooperation with the annular seals to selectively open and close for effective management of pressure within the tubulars.
Description
TECHNICAL FIELD

This invention relates to a novel method and apparatus for offshore drilling operations. In particular, this invention relates to a method and apparatus for employing a concentric, high-pressure marine riser in deep water offshore drilling. In addition, this invention relates to fluid handling in a riser in the event of an unexpected influx of hydrocarbon, fresh water, natural gas, or other pressurized fluid encountered during drilling operations.


BACKGROUND OF THE INVENTION

Presently a number of hydrocarbon drilling techniques have been proposed to better manage pressures within or exerted upon a wellbore during drilling activities. Broadly, these techniques encompass two categories of wellbore pressure control. In the first, a “closed loop” circulating system is employed. This is usually accomplished by installing a rotating control device (“RCD”) similar to that described in, Williams et al U.S. Pat. No. 5,662,181. The RCD is positioned on top of a conventional blow-out preventor. In this system, the RCD directs the flow of drilling mud from inside and atop the wellbore so that drilling mud may be monitored and so the pumping rate can be regulated. In the second, various methods of using multiple columns of drilling fluids with different densities to manipulate the drilling fluid pressure gradient within the wellbore or adding a pumping system to boost wellbore fluids from the well. Fluid density levels effect the fluid pressure gradient within the wellbore and help boost fluids from the well.


Due to limitations in the physical characteristics of existing marine risers present pressure management techniques cannot be implemented without substantial additional cost and/or time. For example, the method and apparatus disclosed in U.S. Pat. No. 6,273,193 (Hermann et al) employs a concentric inner riser and related elements (support, sealing mechanisms, etc.). However, the Hermann et al method and apparatus require the marine riser system to be substantially disassembled before the concentric riser can be deployed. Disassembling the marine riser system adds significant time and cost to the drilling operation. Additionally, the system of Hermann et al leaves the upper end of the marine riser system unpinned to the underside of the rig. This results in the potential for differential movement of the riser away from the well centerline that could cause eccentric side loading of wellbore annular sealing element. Further, the Hermann et al method employs the upper annular blow-out preventor of the existing BOP to effectively seal and isolate the annulus between the lower end of the concentric riser and the lower end of the marine riser rendering it unavailable for its primary well control function.


Hannegan et al. U.S. Pat. No. 6,263,982 describe a method and apparatus where a RCD is installed on top of a marine riser in a manner similar to Hermann et al method and apparatus. The Hannegan method and apparatus has similar limitations with respect to the time and cost of installing and operating the system. Additionally, without an concentric riser, the burst pressure capacity of the conventional marine riser limits the maximum annular pressure that may be imposed.


The present invention overcomes these limitations by enabling a conventional marine riser that is easily configured and reconfigured to conduct dual gradient and annular drilling capabilities.


BRIEF SUMMARY OF THE INVENTION

The present invention is directed to a drilling system and method that manages pressure within a riser during drilling operations. Specifically, the drilling system employs a main marine riser having a plurality of fluid inlet and outlet conduits, concentric inner riser supported within the main marine riser, a riser rotating control device, and a plurality of annular seals disposed within the annular space between the main marine riser and concentric inner riser. These elements work in cooperation to manage the fluid density in the riser and to control influxes of abnormally pressurized fluids into the risers. The present invention provides an efficient method of preventing blowouts and other potentially disastrous consequences of drilling though formations with water, natural gas, pockets of frozen methane gas, or other underground fluid reservoirs.


A preferred embodiment of the inventive pressure management system is a concentric riser support body that includes a tubular body, a riser annular seal within the tubular body that is configured to sealingly engage a concentric tubular member when the seal is actuated, a concentric riser annular seal within the tubular body below the riser annular seal that is configured to sealingly engage a concentric riser member when actuated, and a concentric riser support within the tubular body below the concentric riser annular seal that is configured to supportingly engage a concentric riser member. The pressure management system may further include a tubular body with a concentric riser fluid inlet above the concentric riser annular seal and a concentric riser annular fluid inlet below the concentric riser annular seal.


The tubular body of the support body may include a concentric riser fluid outlet above the concentric riser annular fluid inlet. The fluid inlets and outlet may be opened, closed, or partially opened. Further, the inlets and outlets may include at least one flow meter.


The concentric riser support body of the preferred embodiment may also include a bottom that is configured to mate with a marine riser pipe and a top that is configured to mate with a telescopic joint, or combinations thereof. The support body may also include a plurality of concentric riser fluid conduits below the riser annular seal, which conduits may include valves that may me independently controlled or controlled as a single value, or combinations thereof. The fluid conduits may also be configured as fluid inlets and fluid outlets.


A preferred embodiment of the pressure management system includes a riser, a riser support connected to the riser, a telescopic joint connected to the riser, a concentric riser support body between the riser telescopic joint and the riser support, and a concentric riser inside the riser and the concentric riser support body. The concentric riser may be sized to create an annular space between the concentric riser and the riser. The concentric riser annular seal may be configured to sealingly engage the concentric riser when the seal is actuated. The concentric riser annular seal is designed to prevent fluid in the annular space between the riser and the concentric riser from flowing past the concentric riser annular seal when the seal is actuated.


The concentric riser system may also include a riser rotating control device positioned within the riser and above the concentric riser. The riser rotating control device may include a riser rotating control device pipe section (sized to create an annular space between the riser rotating control device pipe section and the riser) and a riser rotating control device seal operably positioned within and/or exterior to the riser rotating control device pipe section.


The preferred concentric riser system may also include a concentric riser support body that includes a riser annular seal that is designed to sealingly engage the riser rotating control device pipe section when the seal is actuated. The concentric riser support body may also include a plurality of concentric riser fluid channels and a concentric riser annular channel spaced below the plurality of concentric riser fluid channels.


The concentric riser system may also include flow sensing equipment connected to at least one of the plurality of concentric riser fluid channels. The flow sensing equipment may be configured to measure flow volume and pressure inside the at least one of the plurality of concentric riser fluid channels. The concentric riser system may also include a lower concentric riser annular seal positioned inside the riser and adapted to sealingly engage the concentric riser when actuated. The lower concentric riser annular seal is positioned in close proximity to the bottom of the concentric riser.


In addition to structural embodiments, the invention includes a preferred method of managing pressure and/or riser fluid density. The preferred method includes injecting a fluid of a first density through a drill pipe, injecting a fluid of a second density through an annular space between a riser and a concentric riser, mixing the two fluids below the concentric riser, and returning the mixed density fluid toward the top of the riser in the annular space between the drill pipe and concentric riser.


The method may further include the step of retrieving the mixed density fluid through a port in fluid communication with the top of the concentric riser. The method may also include the step of measuring relevant fluid flow parameters of the mixed density fluid as it is retrieved from the port in fluid communication with the top of the concentric riser. The method may also include the steps of measuring relevant fluid flow parameters of the fluid of the first density, measuring relevant fluid flow parameters of the fluid of the second density, and comparing the parameters of the fluids of the first and second density with the mixed density fluid. Additionally, the comparison may result in controlling a blow out preventor in response to the step of comparing the fluids. Control may include changing the second density responsive to well parameters. The preferred method may also include sealing the annular space between a riser and riser rotating device before the step of injecting the fluid of the second density.


Another preferred embodiment is a drilling system that includes a drilling platform, a main drilling riser connected to the drilling platform, where the main drilling riser includes a plurality of lengths of riser tubulars coupled at generally opposed ends, a blow-out preventor connected to the main drilling riser, a concentric riser within the main drilling riser, where the concentric inner riser comprises a plurality of lengths of riser tubulars coupled at generally opposed ends, and one or more annular seals connected to the main drilling riser, wherein the annular seals are configured to isolate pressure in the annular space between the main and concentric riser and below the annual seal.


The drilling system may also include one or more riser fluid inlet conduits connected to the main riser, wherein the riser fluid inlet conduit is configured to receive fluid. The drilling system may also include one or more riser fluid outlet conduits connected to the main riser, wherein the riser fluid outlet conduit is configured to discharge fluid.


The concentric riser of the drilling system may be configured to receive fluid from a drill pipe and discharge the fluid to a drilling fluid processor. At least one of the annular seals of the drilling system may measure the pressure in the annular space between the main riser and the concentric riser and below the annular seal. The annular seals may be configured to open and close in the event of fluid influx into the main riser or the concentric riser so that pressure within the risers is controlled. The riser fluid inlet conduit may be configured to introduce fluid into the annular space between the main riser and the concentric riser, and wherein the concentric riser is configured to receive fluid from the annular space between the main riser and the concentric riser and discharge fluid to the fluid processing equipment.


The drilling system may also include a riser fluid inlet conduit that is configured to introduce fluid into the annular space between the main and concentric riser, and wherein the concentric riser is configured to receive fluid from the annular space between the main riser and the concentric inner riser, and wherein a riser rotating seal is configured to close so that fluid is discharged through the one or more fluid outlet conduits.


The foregoing has outlined rather broadly the features and technical advantages of the present invention in order that the detailed description of the invention that follows may be better understood. Additional features and advantages of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and specific embodiment disclosed may be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims. The novel features which are believed to be characteristic of the invention, both as to its organization and method of operation, together with further objects and advantages will be better understood from the following description when considered in connection with the accompanying figures. It is to be expressly understood, however, that each of the figures is provided for the purpose of illustration and description only and is not intended as a definition of the limits of the present invention.





BRIEF DESCRIPTION OF THE DRAWINGS


FIG. 1 shows a conventional riser drilling system;



FIG. 2 shows a concentric riser support body installed on a marine riser;



FIG. 3 shows a concentric riser and a riser rotating control device;



FIG. 4 shows a concentric riser support body supporting a concentric riser and a riser rotating device;



FIG. 5 shows a concentric riser drilling system operating in a conventional open loop annular pressure management mode;



FIG. 6 shows a concentric riser drilling system operating in an open loop dual gradient mode;



FIG. 7 shows a concentric riser drilling system operating in a closed loop annular pressure management mode;



FIG. 8 shows a concentric riser drilling system operating in closed loop annular pressure management mode;



FIG. 9 shows a concentric riser drilling system operating in closed loop dual gradient annular pressure mode;





DETAILED DESCRIPTION OF THE INVENTION


FIG. 1 shows a conventional riser drilling system. A conventional riser system includes marine riser (100), riser tensioning system (110), blowout preventor (120), telescopic joint (130), auxiliary buoyancy (140) and auxiliary lines (150).



FIG. 2 shows a preferred embodiment of the invention. Specifically, FIG. 2 shows a marine riser (100) and a riser telescopic joint (130). A riser tensioning system (110) supports and maintains a constant tension on marine riser (100). The bottom of marine riser (100) is connected to a sub-sea blowout preventor (120). Sub-sea blowout preventor (120) is connected to a wellhead (not shown). Positioned above riser tensioning system (110) is the concentric riser support body (200). Concentric riser support body (200) mates with marine riser (100) and telescopic joint (130). Although FIG. 2 does not show any marine riser joints above concentric riser support body (200), one skilled in the art readily understands that such an arrangement is possible. Of importance, however, is the relationship between concentric riser support body (200) and riser tensioning system (110). In the preferred embodiment, concentric riser support body (200) is positioned above riser tensioning system (110). Although a preferred embodiment includes concentric riser support body (200), components of the invention may be incorporated directly into one or more riser tubular members. In this configuration, the system may retain the functionality disclosed herein without a concentric riser support body (200).


Concentric riser support body (200) also includes a concentric riser support (210). Concentric riser support (210) positions and supports concentric riser (300) (FIG. 3) within marine riser (100).


Concentric riser support body (200) also includes riser annular seal (220). Riser annular seal (220) is located above the top of concentric riser (300) (See FIGS. 3 and 4). In a preferred embodiment, riser annular seal (220) is located above the top of concentric riser (300) and concentric riser fluid outlet (230) and adjacent to a portion of the riser rotating control device (310) (See FIGS. 3 and 4). The riser annular seal (220) may be opened, closed, or partially opened.


Concentric riser support body (200) also includes concentric riser annular seal (240). Concentric riser annular seal (240) is located below the top of concentric riser (300). In a preferred embodiment, concentric riser annular seal (240) is located below concentric riser fluid inlet (250), outlet (230), and the bottom of riser rotating control device (310). Concentric riser annular seal (240) may be opened, closed, or partially opened.


A concentric riser drilling system may also include a lower concentric riser seal (260). In a preferred embodiment, lower concentric riser seal (260) is positioned adjacent to bottom of concentric riser (300) (FIG. 4). Lower concentric riser seal (260) may be opened, closed, or partially opened. In operation, concentric riser annular seal (240) and lower concentric riser seal (260) can be closed to isolate marine riser (100) from high pressure fluid in drill string (270) (FIG. 7).


The seals and concentric riser support (210) are shown outside of the marine riser for clarity. One skilled in the art knows the seals and support are inside the marine riser. Additionally, the seals and the support are described as single components, however, one skilled in the art understands these components may actually be one or more. For example, there may be two or more riser annular seals (220). Further, some of the components may not be separate components as described, but may be combined into single units. For example, concentric riser annular seal (240) and concentric riser support (210) may be combined into one unit that performs both functions.


Concentric riser support body (200) may also include a fluid service assembly (not shown) that supplies fluids such as lubrication, cooling and control fluids to riser rotating control device (310). The fluid service assembly is preferably positioned adjacent to riser rotating control device (310).


Concentric riser support body (200) also includes a concentric riser fluid inlet (250) and a concentric riser fluid outlet (230). As will be explained with reference to FIG. 4, concentric riser fluid inlet (250) and outlet (230) are configured to be in a cooperative relationship with riser rotating control device (310) (FIG. 3). Additionally, concentric riser support body (200) includes an annular fluid inlet (280). Although single inlets and outlets are shown, one skilled in the art readily understands the number of inlets and outlets can be varied. For example, in some systems it might be advantageous to have two or more concentric riser fluid inlets (250). Inlets and outlets accessing the same annular space are generally interchangeable. For example, fluid could flow into the system through the concentric riser fluid outlet (230).


The inlets and outlets include valves that can be opened, closed, or partially opened. In most applications, the valves are either open or closed. Additionally, inlets are shown with gauges (290). Although gauges are only shown in conjunction with inlets, one skilled in the art readily understands gauges can be used with both inlets and outlets.



FIG. 3 shows concentric riser (300) and riser rotating control device (310). Concentric riser (300) is preferably a string of high-pressure tubular members configured to be run concentrically inside of marine riser (100) (FIG. 4). In a preferred embodiment, concentric riser (300) is connected at a lower end with an internal tieback hanger (not shown) and lower concentric riser annular seal (260). When actuated, lower concentric riser seal (260) prevents fluid from circulating above lower concentric riser annular seal (260) in the annular space between marine riser (100) and concentric riser (300). In a preferred embodiment, concentric riser (300) is sized to be deployed within a twenty-one inch marine riser (100).



FIG. 3 also shows the riser rotating control device (310). In a preferred embodiment riser rotating control device (310) is positioned within the marine riser (100) and telescoping joint (130), above the concentric riser (300).


Riser rotating control device (310) includes RCD seal (320) and RCD pipe section (330). RCD pipe section (330) is optionally sized to be sealingly engaged by riser annular seal (220). In one embodiment, RCD pipe section (330) is the same size as concentric riser (300). When closed, RCD seal (320) prevents fluid from flowing between RCD pipe section (330) and drill pipe (270). When rotating control device (310) is closed, return fluids can be drawn out of marine riser (100) through concentric riser fluid outlet (230) (FIG. 7). Concentric riser fluid outlet (230) is configured to draw gas out of marine riser (100) and into the atmosphere or the rig's choke manifold where the fluid can be processed by burner booms, ventilation lines or other drilling processing equipment (not shown). It should be noted that rotating control device (310) can installed and actuated within a very short period of time. The concentric riser fluid outlets (230) may also be opened and closed within a short period of time. Rapidly actuating rotating control device (310) and opening and closing the concentric riser fluid outlets (230) enables an operator to quickly control and manage bottom hole pressures.



FIG. 4 shows a preferred embodiment with the relative placement of the concentric riser support body (200) relative to concentric riser (300) and riser rotating control device (310). Although not shown, a fluid service assembly is preferably coupled to rotating control device (310) and riser annular seal (220). In this arrangement, fluids can be supplied through the fluid service assembly (not shown) to the rotating control device (310) as needed for operation of the rotating control device (310).


In operation, the concentric riser support body (200) is preferably installed while installing marine riser (100). Once marine riser (100) is in place (including concentric riser support body (200)), it can be operated as a conventional riser system. For operations in which the operator wishes to use the pressure management system disclosed herein, concentric riser (300) is assembled and lowered into marine riser (100). The length of concentric riser used depends on the length of riser. Concentric riser (300) should extend above concentric riser annular seal (240) and below lower concentric riser seal (260). The bottom of concentric riser should terminate above BOP (120).


Riser rotating control device (310) is installed within the upper body of concentric riser support body (200). Riser rotating control device (310) should be installed such that RCD seal (320) is positioned above riser annular seal (220) and the RCD pipe section (330) extends far enough into marine riser (100) to be engaged by riser annular seal (220). In a typical installation, the bottom of RCD pipe section (330) extends below riser annular seal (220).


It should be noted the riser tensioning system (110) is not shown in FIGS. 4 through 9 for clarity purposes. However, a preferred embodiment includes the riser tensioning system (110) as described above and in FIG. 2.



FIG. 5 shows the concentric riser drilling system in open loop operating mode with components above the concentric riser support body (200) removed for clarity. Concentric riser support body (200) is shown with unactuated (open) seals (220, 240, and 260), closed concentric riser fluid inlet (250), closed concentric riser fluid outlet (230), and unused concentric riser support (210). In this configuration, drilling fluid is pumped through drill pipe (270) with fluid pumping equipment (not shown). The fluid travels down drill pipe (270), through drill bit (not shown), and up the annulus between drill pipe (270) and marine riser (100). Drilling fluid processing equipment (not shown) receives return fluid from the top of the marine riser (100).



FIG. 6 shows the concentric riser system in open loop dual gradient drilling mode. In this embodiment, concentric riser (300) is installed within marine riser (100). Concentric riser annular seal (240) is actuated so that drilling fluid cannot flow to the surface in the annulus between the marine riser (100) and concentric riser (300). Concentric riser support body (200) is shown with unactuated riser annular seal (220) and without the riser rotating control device (310). Although riser rotating control device (310) is not shown in FIG. 6, it may be installed—or if installed does not have to be removed—to operate in open loop dual gradient drilling mode. If installed, riser annular seal (220) and RCD seal (320) are not actuated. Fluid can flow past unactuated riser annular seal (220) and/or unactuated RCD seal (320) and out the top of marine riser (100).


This open loop dual gradient arrangement, enables drilling fluid to be injected though the concentric riser annular fluid inlet (280) into the annulus between marine riser (100) and concentric riser (300). In a dual gradient mode, the fluid injected though the concentric riser annular fluid inlet (280) is a different density (weight) than the fluid circulated down through drill sting (270). As drilling fluid from the concentric riser annular fluid inlet (280) reaches the bottom of concentric riser (300), it mixes with the fluid circulated through drill pipe (270). The mixed fluids are then circulated up the annulus between drill string (270) and concentric riser (300). The direction of fluid flow is shown with arrows.


This configuration has a number of advantages over previously proposed equipment configurations that employ fluid dilution based dual gradient drilling. For example, injecting the diluting fluid into the annular space between concentric riser (300) and marine riser (100) mitigate injection pressure and enable smaller less powerful mud pumps than would otherwise be required to overcome friction losses if the diluting fluid was injected into the bottom of the riser via an auxiliary riser boost line (not shown). Furthermore, this configuration has the additional benefit of reducing the total system volume of diluting fluid required to achieve the desired dual gradient riser mud weight which further reduces the need for large storage tanks and other surface equipment.


The embodiment shown in FIG. 6 is particularly effective in larger wellbore sections where typically high mud flow rates are required to maintain sufficient annular velocity to clean cuttings from the wellbore. While circulating rates for conventional open loop dual gradient systems are approximately 1200 gallons per minute (“gpm”), those of the embodiment shown in FIG. 5 are much greater. For example, using a 2 to 1 dilution rate to achieve a given dual gradient mud weight and a typical twenty-one inch diameter marine riser, the combined dilution and wellbore fluid return rates may be as high as 3600 gpm. Thus, this embodiment provides significantly improved return rates over presently known dual gradient techniques.



FIG. 7 shows the concentric riser drilling system configured for annular pressure management mode. In annular pressure management mode, riser rotating control device (310) and riser annular seal (220) are closed. Fluid is pumped down through drill pipe (270) and out of the concentric riser fluid outlet (230). In the embodiment shown, annular seals (240) and (260) are closed. This isolates the annular space between the marine riser (100) and concentric risers (300). Alternatively, if fluid pressure on marine riser (100) is not an issue, seals (240) and (260) may remain open.


Fluid forced out concentric riser fluid outlet (230) is evaluated for information relevant to the drilling operation. For example, comparing the fluid pumped into the well bore with the fluid pumped out concentric riser fluid outlet (230) will tell an operator whether fluid from the formation is seeping into the wellbore or whether drilling fluid is penetrating into the well bore. Of particular interest is fluid pressure information. Pressure increases can alert an operator to potentially dangerous pressure kicks.



FIG. 8 shows the concentric riser drilling system operating in annular pressure connection mode. This mode is preferably employed to maintain a controlled bottom hole pressure while conventional circulation through drill string (270) has stopped.


In this mode, the marine riser (100) receives fluid though the concentric riser fluid inlet (250) and discharges the fluid out of concentric riser fluid outlet (230). Accordingly, the fluid inlet (250) and outlet (230) are open, and annular seals (220), (240), and (260) are closed. This configuration isolates the annular space between the marine riser (100) and concentric riser (300) between seals (240) and (260). Fluid discharged through concentric riser fluid outlet (230) may be analyzed as described with respect to FIG. 7.


Although not shown in FIG. 8, the annular pressure connection mode may also be employed without the concentric riser (300). This configuration isolates the annular space between the marine riser (100) and drill pipe (270) between seals (240) and (260). The marine riser (100) is configured to receive fluid though the concentric riser fluid inlet (250) and discharge the fluid out of concentric riser fluid outlet (230). Accordingly, the fluid inlet (250) and outlet (230) are open, and annular seals (220), (240), and (260) are closed. The return fluid from the main riser (100) is then optionally directed to a flow metering device, or choke manifold (not shown).



FIG. 9 shows the concentric riser drilling system operating in dual gradient and annular pressure management mode. Fluid is received into both the annulus between the marine riser (100) and concentric riser (300) and drill pipe (270) as described with respect to FIG. 6. The annulus between concentric riser (300) and drill pipe (220) receives the mixed fluids and circulates it upward to concentric riser fluid outlet (230). Fluid discharged through concentric riser fluid outlet (230) is analyzed as described with respect to FIG. 7.


This combination of dual gradient and annular methods presents a number of advantages. First, it provides a closed loop circulating system. Thus, return flow may be precisely measured and controlled. Second, drilling operators may establish and vary a dual gradient to better match the naturally occurring wellbore pressure profile.


Gas permeability (N2, produced gas) of the blowout preventor and riser elastomer elements is important. Accordingly, a preferred embodiment includes elastomer/rubber components not susceptible to failure caused by aerated drilling fluid or gases produced by a sudden pressure drop. Such elastomer/rubber components include, for example, blowout preventor ram sealing elements, blowout preventor bonnet seals, and flex joint elastomer elements.


Although the present invention and its advantages have been described in detail, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention as defined by the appended claims. Moreover, the scope of the present application is not intended to be limited to the particular embodiments of the process, machine, manufacture, composition of matter, means, methods and steps described in the specification. As one of ordinary skill in the art will readily appreciate from the disclosure of the present invention, processes, machines, manufacture, compositions of matter, means, methods, or steps, presently existing or later to be developed that perform substantially the same function or achieve substantially the same result as the corresponding embodiments described herein may be utilized according to the present invention. Accordingly, the appended claims are intended to include within their scope such processes, machines, manufacture, compositions of matter, means, methods, or steps.

Claims
  • 1. A method for controlling pressure and/or riser fluid density in a marine riser by changing the density of a drilling fluid comprising the steps of: injecting a fluid of a first density through a drill pipe in the marine riser;injecting a fluid of a second density through a concentric riser support body into an annular space between the marine riser and a concentric riser, wherein the concentric riser support body includes a plurality of concentric riser fluid channels and a concentric riser annular channel below said plurality of concentric riser fluid channels, wherein the concentric riser support body is connected to the marine riser with a riser support at a position above the riser support body,mixing the two fluids below the concentric riser; andreturning the mixed density fluid toward the top of the riser in an annular space between the drill pipe and concentric riser, wherein the pressure and/or the fluid density in the marine riser is controlled.
  • 2. The method of claim 1 further comprising, retrieving the mixed density fluid through a port in fluid communication with the top of the concentric riser.
  • 3. The method of claim 2 further comprising, measuring relevant fluid flow parameters of the mixed density fluid as it is retrieved from the port in fluid communication with the top of the concentric riser.
  • 4. The method of claim 3, further comprising, measuring relevant fluid flow parameters of the fluid of the first density;measuring relevant fluid flow parameters of the fluid of the second density; andcomparing the parameters of the fluids of the first and second density with the mixed density fluid.
  • 5. The method of claim 4, further comprising controlling a blow out preventer in response to said step of comparing the fluids.
  • 6. The method of claim 1, further comprising changing the density of the fluid of the second density responsive to well parameters.
  • 7. The method of claim 6, further comprising sealing an annular space between the marine riser and riser rotating device before said step of injecting the fluid of the second density.
  • 8. A drilling method comprising the steps of: positioning a tubular body, said tubular body including a concentric riser annular fluid inlet;inserting a concentric tubular member and a concentric riser into said tubular body; actuating a riser annular seal within said tubular body to sealingly engage said concentric tubular member;supporting the concentric riser with a concentric riser support positioned within said tubular member and below said riser annular seal;actuating a concentric riser annular seal within said tubular body to sealingly engage said concentric riser, said concentric riser annular seal positioned below said riser annular seal and above said concentric riser annular fluid inlet.
  • 9. The drilling method of claim 8, further comprising the step of, prior to inserting the concentric tubular member and the concentric riser, connecting said tubular body to a main drilling riser that is connected to a blow out preventer.
  • 10. The drilling method of claim 9, further comprising the step of isolating an annular space between the main drilling riser and the concentric riser from a space in the well below the blow out preventer.
  • 11. The drilling method of claim 10 wherein the step of isolating an annular space between the main drilling riser and the concentric riser includes actuating a concentric riser seal near the blowout preventer.
  • 12. The drilling method of claim 9 further comprising the steps of: injecting a fluid of a first density into the annular space between the concentric riser and the main drilling riser through a concentric riser fluid inlet;injecting a fluid of a second density into a drill string, wherein said second density is different from the fluid of the first density; andmixing the fluid of the first density with the fluid of the second density at a position above the blowout preventer.
  • 13. The drilling method of claim 12 further comprising the step of returning the mixed density fluid through the annular space between the drill string and the concentric riser.
  • 14. The drilling method of claim 8 further comprising the steps of: injecting a fluid of a first density into a space in a marine riser above the concentric riser annular seal;removing fluid from the space in the marine riser above the concentric riser annular seal; andevaluating the fluid removed from the space in the marine riser above the concentric riser annular seal to determine if said fluid includes material other than the fluid of the first density.
  • 15. A method for managing density and pressure during drilling comprising: forming a first fluid flow path within a drill string into a well below a blow out preventer for carrying a drilling fluid of a first density;forming a second fluid flow path above the blowout preventer for carrying a drilling fluid of a second density in a marine riser through a space adjacent to a concentric riser and connecting a concentric riser support body to the marine riser between a telescopic joint and a riser tensioning ring; andmixing the drilling fluid of the first density with the drilling fluid of the second density at a position above the blow out preventer adjacent to the concentric riser.
  • 16. The method of claim 15, wherein the second fluid flow path includes an annular space between the marine riser and the concentric riser below a concentric riser annular seal.
  • 17. The method of claim 16, wherein the space in the marine riser is above the concentric riser and the concentric riser annular seal and below a riser annular seal.
  • 18. The method of claim 15 further comprising the step of passing a drilling fluid in the first fluid flow path in a direction different than the drilling fluid passing in the second fluid flow path.
  • 19. The method of claim 16, wherein the second fluid flow path includes an annular space between the drill string and concentric riser above the blow out preventer.
  • 20. The method of claim 16, wherein the space in the marine riser is below a riser annular seal in the marine riser.
  • 21. The method of claim 15 further comprising the step of forming a third fluid flow path for carrying a drilling fluid through a space in the marine riser.
  • 22. The method of claim 21 further comprising the step of passing drilling fluid through at least one of the first, second or third fluid flow paths in a direction different than the other of the first, second or third flow paths.
  • 23. The method of claim 21 wherein, the second fluid flow path includes an annular space between the marine riser and the concentric riser below a concentric riser annular seal and above the blow out preventer; and the third fluid flow path includes the annular space between the concentric riser and the drill string.
  • 24. The method of claim 23 wherein the third fluid flow path is within the marine riser entirely below a riser annular seal formed in the marine riser.
  • 25. The method of claim 15 further comprising the step of inserting the concentric riser inside the marine riser and the concentric riser support body.
  • 26. The method of claim 25 further comprising actuating one or more annular seals in the concentric riser support body to form the second fluid flow path and a third fluid flow path for carrying drilling fluid within the marine riser.
CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of patent application Ser. No. 11/584,186 filed Oct. 20, 2006, claiming priority to Provisional Patent Application No. 60/728,542, filed Oct. 20, 2005.

US Referenced Citations (120)
Number Name Date Kind
1610372 Hansen Dec 1926 A
3032125 Hiser et al. May 1962 A
3191388 Ludwig Jun 1965 A
3313345 Fischer Apr 1967 A
3380520 Pease Apr 1968 A
3434550 Townsend Mar 1969 A
3497020 Kammerer, Jr. Feb 1970 A
3603409 Watkins Sep 1971 A
3791442 Watkins Feb 1974 A
3981369 Bokenkamp Sep 1976 A
4060130 Hart Nov 1977 A
4170266 Fayren Oct 1979 A
4176722 Wetmore et al. Dec 1979 A
4188156 Fisher et al. Feb 1980 A
4210208 Shanks Jul 1980 A
4216834 Wardlaw Aug 1980 A
4428433 Watkins Jan 1984 A
4524832 Roche et al. Jun 1985 A
4556340 Morton Dec 1985 A
4597447 Roche et al. Jul 1986 A
4615542 Ideno et al. Oct 1986 A
4626135 Roche Dec 1986 A
4653597 Johnson Mar 1987 A
4668126 Burton May 1987 A
4813495 Leach Mar 1989 A
4867254 Gavignet Sep 1989 A
5070949 Gavignet et al. Dec 1991 A
5314022 Cowan et al. May 1994 A
5513706 Jennings, Jr. et al. May 1996 A
5524710 Shinn Jun 1996 A
5533574 Gonzalez Jul 1996 A
5586609 Schuh Dec 1996 A
5662181 Williams et al. Sep 1997 A
5720356 Gardes Feb 1998 A
5873420 Gearhart Feb 1999 A
6045296 Otten et al. Apr 2000 A
6102673 Mott et al. Aug 2000 A
6138772 Miescher et al. Oct 2000 A
6138774 Bourgoyne, Jr. et al. Oct 2000 A
6173781 Milne et al. Jan 2001 B1
6216799 Gonzalez Apr 2001 B1
6230824 Peterman et al. May 2001 B1
6263981 Gonzalez Jul 2001 B1
6263982 Hannegan et al. Jul 2001 B1
6273193 Hermann et al. Aug 2001 B1
6276455 Gonzalez Aug 2001 B1
6308787 Alft Oct 2001 B1
6315061 Boatman et al. Nov 2001 B1
6325159 Peterman et al. Dec 2001 B1
6394195 Schubert et al. May 2002 B1
6401823 Gonzalez et al. Jun 2002 B1
6415877 Fincher et al. Jul 2002 B1
6450262 Regan Sep 2002 B1
6457529 Calder et al. Oct 2002 B2
6470975 Bourgoyne et al. Oct 2002 B1
6474422 Schubert et al. Nov 2002 B2
6499540 Schubert et al. Dec 2002 B2
6505691 Judge et al. Jan 2003 B2
6530437 Maurer et al. Mar 2003 B2
6536540 de Boer Mar 2003 B2
6579832 Jimenez et al. Jun 2003 B2
6607042 Hoyer et al. Aug 2003 B2
6732804 Hosie et al. May 2004 B2
6739397 Ayling et al. May 2004 B2
6739408 Rowden May 2004 B2
6745851 Edvardsen Jun 2004 B1
6745857 Gjedebo Jun 2004 B2
6802379 Dawson et al. Oct 2004 B2
6843331 de Boer Jan 2005 B2
6854532 Fincher et al. Feb 2005 B2
6904981 van Riet et al. Jun 2005 B2
6904982 Judge et al. Jun 2005 B2
6913092 Bourgoyne et al. Jul 2005 B2
6923273 Terry et al. Aug 2005 B2
6926101 deBoer Aug 2005 B2
6966392 deBoer Nov 2005 B2
7027968 Choe et al. Apr 2006 B2
7032691 Humphreys Apr 2006 B2
7044237 Leuchtenberg et al. May 2006 B2
7044343 Anue May 2006 B2
7080685 Bailey et al. Jul 2006 B2
7090036 deBoer Aug 2006 B2
7093662 deBoer Aug 2006 B2
7108066 Jamison Sep 2006 B2
7219739 Robichaux May 2007 B2
7237613 Radi et al. Jul 2007 B2
7264058 Fossli Sep 2007 B2
7270185 Fontana et al. Sep 2007 B2
7303013 Alsobrook et al. Dec 2007 B2
7306042 Bansal et al. Dec 2007 B2
7314087 Robichaux Jan 2008 B2
7334967 Blakseth et al. Feb 2008 B2
7350597 Reitsma et al. Apr 2008 B2
7377323 Walker et al. May 2008 B2
7380609 Page et al. Jun 2008 B2
7395878 Reitsma et al. Jul 2008 B2
7407019 Kinder et al. Aug 2008 B2
7482309 Ravi et al. Jan 2009 B2
7497266 Fossli Mar 2009 B2
7534743 Kirsner et al. May 2009 B2
7658228 Moksvold Feb 2010 B2
7699109 May et al. Apr 2010 B2
20010050185 Calder et al. Dec 2001 A1
20020066597 Schubert et al. Jun 2002 A1
20030070840 Boer Apr 2003 A1
20030111799 Gilmore Jun 2003 A1
20040065440 Farabee et al. Apr 2004 A1
20050061546 Hannegan Mar 2005 A1
20050284641 Watkins et al. Dec 2005 A1
20060021755 Radi et al. Feb 2006 A1
20060065402 Fontana et al. Mar 2006 A9
20060070772 deBoer Apr 2006 A1
20060102387 Bourgoyne et al. May 2006 A1
20070095540 Kozicz et al. May 2007 A1
20070151762 Reitsma Jul 2007 A1
20070284113 Haheim Dec 2007 A1
20080060846 Belcher et al. Mar 2008 A1
20080105434 Orbell et al. May 2008 A1
20090090558 Polizzotti et al. Apr 2009 A1
20090090559 Polizzotti et al. Apr 2009 A1
Foreign Referenced Citations (2)
Number Date Country
10261834 Jul 2004 DE
317295 Oct 2004 NO
Non-Patent Literature Citations (11)
Entry
Kozicz, J., “Reconfigurable Riser—Enabling Drilling Solutions for the Future”, prepared for presentation at the AADE 2005 National Technical Conference and Exhibition, held at the Wyndam Greenspoint in Houston, Texas, Apr. 5-7, 2005; p. 1-11; on-line <http://www.aade.org/TechPapers/2005Papers/Web/Emerging—Technologies/AADE-05-NTCE-23—Kozicz.pdf>.
International Preliminary Report on Patentability issued Apr. 23, 2008, during the prosecution of International Application No. PCT/US2006/040799. Published Apr. 23, 2008.
International Search Report issued Jul. 16, 2007, during the prosecution of International Application No. PCT/US2006/040799. Published Sep. 20, 2007.
Written Opinion issued Jul. 16, 2007, during the prosecution of International Application No. PCT/US2006/040799. Published Apr. 20, 2008.
Herrmann et al., “Concentric Drilling Risers for Ultra Deepwater,” Paper prepared for presentation at the 1998 IADC/SPE Online Conference held in Dallas, TX Mar. 3-6, 1998. Copyright 1996, IAD/SPE Drilling Conference. 11 Pages.
Rike et al., “Recent Innovations in Offshore Completion and Workover Systems,” Copyright 1696. Paper prepared for presentation at the First Annual Offshore technology Conference held in Houston, TX, May 18-21, 1969. Paper No. OTC 1020. 14 Pages.
Roger Stave, Technology Development Manager AGR Subea AS, RMR Riserless Mud Return System Dual Gradient System, powerpoint presentation.
Trade secrets and know-how necessary to implement dual gradient drilling as described in the foregoing patents.
Proprietary DGS Mud Composition / using the ChevronPhillips IO 16-18 as its base fluid.
Modified SS Wellhead connector and internal adapter for subsurface annulus injection through concentric casing (see patent U.S. patent No. 6,926,101).
Dharma, Nyoman and Tregilgas, John, et al. “Managed Pressure Drilling and Downhole Isolation Technologies Deliver High Rate Gas Wells”, presented at 2008 SPE/IADC Managed Pressure Drilling and Underbalanced Conference & Exhibition.
Related Publications (1)
Number Date Country
20110108282 A1 May 2011 US
Provisional Applications (1)
Number Date Country
60728542 Oct 2005 US
Continuations (1)
Number Date Country
Parent 11584186 Oct 2006 US
Child 12985867 US