BOP operating system with quick dump valve

Information

  • Patent Grant
  • 6779543
  • Patent Number
    6,779,543
  • Date Filed
    Wednesday, October 29, 2003
    21 years ago
  • Date Issued
    Tuesday, August 24, 2004
    20 years ago
Abstract
In some prior art Blowout Preventer (BOP) operating systems, high velocity fluid flows and low differential pressures induced vibration in the system. This vibration may result in collapsed and failure of hydraulic hoses in the system. A quick dump valve has been added at or near the open port on the BOP assembly to reduce vibration and other problems. The dump valve has a vent position and an open position. Several alternative embodiments add a ball check valve assembly to the shuttle in the quick dump valve.
Description




BACKGROUND OF INVENTION




Drilling rigs use blowout preventers (BOPs) to shut in a well during emergencies and for other purposes. The BOP operating system needs to be reliable in order to protect lives, the environment, and property. This invention relates to an improved BOP operating system and a quick dump valve. The quick dump valve includes a shuttle that has some structural similarity to shuttle valves used for control functions in prior art BOP operating systems. Specifically, the quick dump valve has some structural similarities to the Low Interflow Hydraulic Shuttle Valve which is the subject of a pending U.S. patent application Ser. No. 09/452,594 filed on Dec. 1, 1999 and a pending U.S. patent application Ser. No. 09/653,415 for a Pressure Biased Shuttle Valve filed on Sep. 1, 2000, both of which are incorporated herein by reference. Gilmore Valve Co. is the owner of these two pending U.S. Patent Applications, the present patent application for BOP Operating System with Quick Dump Valve and other U.S. patents for shuttle valves including U.S. Pat. Nos. 3,533,431 and 4,253,481. However, the present invention is structurally distinct from these prior art shuttle valves and it performs a different function as discussed below.




DESCRIPTION OF THE PRIOR ART




Subsea wellhead systems are often relied upon during deep-water exploration for oil and natural gas. The subsea wellhead system includes a stack of BOPs. Annular BOPs are actuated on a routine basis to snub or otherwise control pressure during normal drilling operations. Other blowout preventers, such as blind rams, pipe rams, and shear rams will also be included in the stack on the subsea wellhead. When these types of rams are actuated, operations in the well cease in order to control pressure or some other anomaly. Blind rams, pipe rams, shear rams and annular preventers are periodically functioned and tested to make sure that they are operational.




BOPs are tested periodically to ensure that they will function in emergencies and in other situations. Prior art subsea BOP operating systems include a control podcontrol pods, the lower marine riser package (LMRP), the BOP stack and interconnecting hoses and pipes. From time to time it may be necessary to perform an emergency disconnect of the LMRP from the BOP stack, for example, if a drill ship drifts off station or if a storm approaches. If it is necessary to make an emergency disconnect of the LMRP from the BOP stack, it will be necessary to close the shear rams. During the closing sequence, hydraulic fluid is forced through pipes or hose, a shuttle valve and additional segments of pipes or hose before it finally reaches the directional control valve vent port on the control pod where it is vented to the ocean. This circuitous hydraulic vent path results in a high differential pressure, which decreases flow of control fluid through the close side of the operating system. The decreased flow consumes valuable seconds, and as such, increases the time required to close the shear rams and disconnect the LMRP from the BOP stack. In prior art BOP operating systems, pilot operated check valves or conventional sub-plate mounted (SPM) poppet valves were used to vent this fluid during the closing sequence. These prior art vent devices rely upon springs or pilot pressure to operate properly.




The present dump valve for use in the improved BOP operating system utilizes a ported shuttle that automatically shifts with the direction of hydraulic pressure to either expose or seal the vent port in the valve. The present dump valve has two positions vent and open. It has several advantages over the prior art due to its location in the BOP operating system and its design. These advantages occur when the valve is in both the vent and the open positions as discussed below. The present dump valve is a much simpler design than the prior art pilot operated check valves and conventional SPM valves.




The present dump valve and improved BOP operating system are designed to reduce hydraulic shock and vibration, to reduce the incidence of hose collapse on both the close side and the open side of the system, to facilitate installation and maintenance, and to shorten the emergency disconnect sequence of the LMRP from the BOP stack. In some prior art systems, hydraulic shock and vibration would sometimes accompany the closing function.




In the improved BOP operating system the dump valve of the present invention is located at or near the open port of the BOP. During the closing sequence in the improved BOP operating system, the present dump valve is shifted to the vent position. In this position fluid is vented from the BOP operating system. When it is time to open the shear rams, fluid flow reverses through the dump valve and it moves to the open position. In the open position, the vent is closed allowing fluid to move through the open port into the BOP to open the rams.




Some BOP hoses may collapse in deep water when subjected to high velocity flows of hydraulic fluid resulting from functioning of the BOPs with large capacity operators. Hose collapse is, of course, undesirable. The present dump valve and the improved BOP operating system are designed to reduce flow velocities in the control system, and thereby reduce the incidence of BOP control hose collapse. In the improved BOP operating system, the dump valve is positioned at or near the open port on the BOP to vent fluid from the system during the closing sequence. Because the dump valve is located at or near the open port on the Ram's BOP, this high velocity fluid is vented and does not pass through the open side hose. The control hoses on the open side of the BOP will, therefore, be less prone to collapse because they are no longer exposed to the hydraulic shock and negative pressure waves caused by high velocity flow of fluid when the BOP rams are being closed.




When the rams are being opened, the dump valve also acts as a dampener to reduce the incidence of hose collapse on the close side of the operating system. In a preferred embodiment, when the rams are functioned open, fluid passing through the dump valve is restricted because the orifice through the dump valve is smaller than the inside diameter of the hose leading to and exiting from the dump valve. This flow restrictor will effectively slow down the velocity of the fluid entering the BOP rams. In turn, the velocity of the exhausting fluid from the close side will be reduced to a rate that reduces hydraulic shock and therefore reduces the incidence of hose collapse. In some prior art BOP operating systems, it may take as much as 20 seconds to close and open the rams. The improved BOP operating system with quick dump valve should allow the rams to close in approximately 5 to 15 seconds; however, it may take more than 30 seconds for the rams to open.




Maintenance on prior art BOP operating systems is sometimes lengthy and expensive. The present dump valve is smaller and lighter than conventional SPM valves or pilot operated check valves, which will facilitate valve installation reliability and maintenance.




The improved BOP operating system with quick dump valve should reduce the amount of time it takes to make an emergency disconnect of the LMRP from the BOP stack. In prior art BOP operating systems when it was necessary to close the rams, fluid was forced through a length of hydraulic hose, a shuttle valve and additional segments of tubing or hose before it finally reached the directional control valve vent port on the control pod. This circuitous hydraulic vent path on the close side of prior art operating systems results in a high differential pressure, which decreases flow of control fluid when the rams are being closed. The decreased flow consumes valuable seconds and, as such, increases the time required to close the rams and disconnect the LMRP from the BOP stack. Positioning the quick dump valve at or near the BOP Ram's open port will substantially shorten the hydraulic vent path and reduce the differential pressure. All of these features will reduce the amount of time required to close the BOP rams during an emergency and thus speed up the disconnect of the LMRP from the BOP stack.




SUMMARY OF INVENTION




The quick dump valve uses a ported shuttle design that shifts to either expose or seal off the vent port in the valve. When the BOP is being closed, the shuttle moves to the vent position allowing fluid to be vented from the improved operating system. This vent function which is located at or near the BOP prevents high velocity fluid from passing through the open side hose thus reducing the incidence of hydraulic shock, vibration and hose collapse.




When the BOP is being opened, the shuttle in the dump valve moves to the open position allowing fluid to pass through the dump valve and into the BOP. A flow restrictor is positioned in the shuttle, which acts as a dampener to reduce hydraulic shock, vibration and the incidence of hose collapse on the close side of the BOP rams. While the BOP is being opened, it is important that the shuttle achieve a good seal to prevent fluid from escaping to vent. The diameter on the supply side of the shuttle is larger than the diameter on the BOP side which results in more force being applied to the seals to prevent unwanted fluid from escaping to vent while the BOP is being opened.




In some situations, it is desirable to prevent fluid from flowing to supply when fluid is escaping to vent while the BOP is being opened. In the first alternative embodiment, a ball check valve, is positioned in the shuttle to block fluid flow from the BOP to supply when the dump valve is in the vent position. In the first alternative embodiment, the diameter on the supply side of the shuttle is larger than the diameter on the BOP side, which results in more force being applied to the seals to prevent unwanted fluid from escaping to vent while the BOP is being opened.




In the second alternative embodiment, a ball check valve is positioned in the shuttle to block fluid flow from the BOP to supply when the dump valve is in the vent position. In the second alternative embodiment, the diameter on the supply side of the shuttle is the same diameter as in the BOP side. The cracking pressure of the check valve results in the differential pressure and force required to energize the metal to metal face seal. Differential area was utilized to accomplish this in the alternative and first alternative embodiment.




In the third alternative embodiment, there is no internal check valve and the diameter on the supply side of the shuttle is the same diameter as on the BOP side. In the third alternative embodiment soft seals are used on both sides of the shuttle to achieve a seal. These seals may be located in either the shuttle or adapters.











BRIEF DESCRIPTION OF DRAWINGS




In order to more fully understand the aforementioned features, advantages and objects of the present invention, a more detailed description of the invention is provided in the appended drawings. It is noted, however, that the appended drawings illustrate only a typical embodiment of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments. Reference the appended drawings, wherein:





FIG. 1

is a hydraulic circuit showing the BOP rams in the closed position and the quick dump valve of the present invention in the vent position.





FIG. 2

is a hydraulic circuit showing the BOP rams in the open position and the dump valve of the present invention in the open position.





FIG. 3

is a perspective view of a preferred embodiment of the quick dump valve of the present invention.





FIG. 4

is a section view of the quick dump valve of

FIG. 3

in the vent position with flow arrows showing the direction of fluid flow from the BOP through the dump valve and out the vent.





FIG. 5

is a section view of the dump valve of

FIG. 3

in the open position with flow arrows showing the flow of fluid from supply through the dump valve through the BOP.





FIG. 6

is an enlargement of the metal to metal seal


6


shown in FIG.


5


.





FIG. 7

is an alternative embodiment of the dump valve of the present invention including a ball check valve. This ball check valve eliminates all return flow through the supply side hydraulics during venting. The supply side of the shuttle has a larger diameter than the BOP side.





FIG. 8

is a second alternative embodiment of the dump valve of the present invention including a ball check valve. Both sides of the shuttle are the same diameter. The spring in the ball check valve creates a differential pressure across the shuttle and the force necessary to energize the metal seal.





FIG. 9

is a third alternative embodiment of the dump valve of the present invention having soft seals. Both sides of the shuttle have approximately the same diameter. Axial force is not required to energize these seals as in the previously described embodiment.











DETAILED DESCRIPTION




The quick dump valve uses a ported shuttle design that shifts to either expose or seal off the vent port in the valve. When the BOP is being closed, the shuttle moves to the vent position, allowing fluid to be vented from the improved operating system. This vent function which is located at or near the BOP prevents high velocity fluid from passing through the open side hose, thus reducing the incidence of hydraulic shock, vibration and hose collapse.




Control pods, attached to the LMRP, direct hydraulic operating fluid to all the functions on the BOP and LMRP. The LMRP is positioned on the BOP stack. BOP control systems have two (2) redundant hydraulic systems commonly referred to in the industry as blue and yellow pods.





FIG. 1

is a hydraulic circuit diagram of a portion of the improved BOP operating system with the quick dump valve


10


positioned at or near the open port on the BOP. In

FIG. 1

, fluid flows from the yellow pod hydraulic supply through valves on the control pod through the shuttle valve generally identified by the numeral


12


through hoses


14


as identified by the flow arrow to the close port


16


in the BOP assembly


18


. This side of the operating system is referred to as the close side of the system because fluid flows into this side when the rams are functioned close. A piston


20


divides the BOP assembly


18


into a close chamber


22


and an open chamber


24


. A rod


26


extends from the piston


20


to the BOP rams.




The open chamber


24


connects to an open port


28


, which connects to a short conduit


30


, which connects to the quick dump valve


10


. Alternatively, the dump valve


10


can be directly connected to the open port


28


. Additional hoses


32


connect the dump valve


10


to one of three ports on the shuttle valve generally identified by the numeral


35


. The other two ports on the shuttle valve


35


connect to the blue pod and the yellow pod hydraulic supply as well known to those skilled in the art. When either the blue pod accumulators or the yellow pod accumulators are energizedWhen hydraulic fluid is directed from either the blue or yellow pods, the shuttle valve


35


seals off the path of the non-energized hydraulic system and routes the fluid to the BOP.




In order to open the rams as shown in

FIG. 1

, high pressure fluid exits from a pod, in this case the yellow pod, and moves through the shuttle valve


12


, the conduit


14


, the close port


16


and enters the close chamber


22


thus moving the piston


20


to the left-hand side of the BOP assembly


18


as shown in FIG.


1


. As high-pressure fluid enters the close chamber


22


, fluid must exit the open chamber


24


. As the piston


20


moves to the closed position, the fluid in the open chamber


24


moves into the dump valve


10


, shifting it to the vent position (

FIG. 4

) thus venting the fluid to sea. During the closing process fluid is being vented through the dump valve


10


. After the BOP is closed, the pressure in the close chamber


24


equalizes and no further fluid is vented. However, the shuttle


36


in the dump valve


10


remains in the vent position until the BOP is opened. During vent flow the majority of the fluid exhausts through the vent port


44


of the dump valve


10


. A small portion of fluid, between 10 to 20%, flows through the flow restrictor passage


82


in the shuttle, and back through the shuttle valves


35


where it exhausts to the ocean (via components not shown in FIG.


1


). Because the flow rate back through the shuttle valves is greatly reduced, energy which can trigger vibration or oscillation is also low. As an alternative configuration a check valve can be employed in the inside of the dump valve


10


to totally eliminate this flow.




The BOP assembly


18


operates with fluids that are flowing as fast as 320 gpm at pressures of 1500 to 3000 psi. These high pressures and high flow rates sometimes create hydraulic shock and vibration in the BOP operating system generally shown in FIG.


1


. Prior art SPM's and pilot operated check valves are sometimes installed in “Tee” connections located near the BOP on both the opening and closing sides. These valves are actuated by external means to vent return flow to the ocean. This is similar to the function performed by the dump valve


10


, however, the dump valve


10


is a much simpler device containing fewer moving parts, and therefore improved reliability. Also due to the greater size of the prior art SPM's and pilot operated check valves, they must be mounted in the BOP frame or other structure which is a greater distance away than the location of the present dump valve


10


, increasing the resistance to vent flow. In the improved operating system of

FIG. 1

, the dump valve


10


is installed at the open port


28


or in close proximity thereto by conduit


30


. When the BOP is closed as shown in

FIG. 1

, the dump valve


10


is in the vent position allowing fluid from the close chamber


24


to vent from the operating system. This reduces hydraulic shock and vibration and the incident of hose collapse on the open side of the operating system. The improved BOP operating system of

FIG. 1

with the quick dump valve


10


allows the BOP rams to be closed more quickly than most prior art systems because the fluid from the open chamber


24


is vented from the system at or near the open port


28


. Some prior art systems took up to 20 seconds to close. The present invention should be able to close in 5-15 seconds.




The dump valve


10


is smaller and lighter than conventional SPM or pilot operated check valves which should facilitate installation and maintenance on the improved BOP operating system. The dump valve


10


is a simpler more reliable design than prior art SPM and pilot operated check valves.





FIG. 2

is a partial hydraulic circuit diagram portion of the improved BOP operating system. In order to open the BOP rams, high pressure fluid flows from the blue pod hydraulic supply through the shuttle valve


35


through the piping and/or hose


32


and enters the dump valve


10


. The velocity of this fluid causes the dump valve to move from the vent position of

FIG. 4

to the open position of FIG.


5


. In the open position, fluid passes through a flow restrictor in the dump valve


10


to the open port


28


and into the open chamber


24


. This causes the piston


20


to move towards the right-hand side of the drawing, which retracts the rod


26


thus opening the BOP. As the piston


20


moves from the full closed position of

FIG. 1

to the full open position, fluid in the closed chamber


22


moves through the close port


16


and the hose


14


on the close side of the BOP operating system. In order to dampen hydraulic shock, the present invention will take more than 30 seconds to open, but this is acceptable because the open function does not occur under emergency conditions.





FIG. 3

is a perspective view of the dump valve


10


, which is supported by brackets


38


and


40


. The dump valve


10


has a supply port


34


, which connects to the hose


32


on the open side of the operating system. A BOP port


42


connects to the hose


30


or directly to the open port


28


. A vent port


44


is connected to conduits, which are vented to sea.





FIG. 4

is a section view of the dump valve


10


in the vent position. In this position, fluid moves from the open chamber


24


, through the valve


10


and is vented to sea. When the shuttle


36


is in the vent position fluid flows through the dump valve


10


as shown by the flow arrows in the drawing. Fluid enters the dump valve


10


through the BOP port


42


and exits through the vent port


44


as shown by the flow arrows. The body


46


has a longitudinal bore that is threaded to receive the supply adapter


48


and the BOP adapter


50


. An O-ring


52


is positioned in channel


51


and between the body


46


and the BOP adapter


50


thus creating a seal between these two components. Another O-ring


54


is positioned between the supply adapter


48


and the body


46


to create a seal between these two components. The body also has a transverse bore which forms the vent port


44


and which connects to the longitudinal bore.




The shuttle


36


has a central radial collar


56


and opposing end portions


58


and


60


. The diameter, identified by the arrow A, of the end portion


58


, is larger than the diameter, identified by the arrow B. of the end portion


60


. This step in diameter produces greater area on the supply end


58


. When the shuttle


36


is in the open position shown in

FIG. 5

, and the BOP piston


20


has reached full travel stopping flow and equalizing the pressure across the shuttle, a difference in force is created by this greater area on the supply end holding the shuttle in the open position and effecting a metal to metal seal as shown in

FIGS. 5 and 6

. The area of the end portion


58


should be larger than the area of the end portion


60


to ensure a good seal. Applicants have determined that a good seal can be achieved if the area of end portion


58


is approximately 1.5 times greater than the area of the end portion


60


; however other area ratios may be suitable, provided that a good seal is achieved when the valve


10


is in the open position as shown in

FIGS. 5 and 6

.




The end portion


58


has an O-ring groove


61


formed therein. An O-ring


62


and a first backup ring


64


and a second backup ring


66


are positioned in the O-ring groove


61


. The O-ring can be formed from conventional materials such as nitrile rubber provided that they will meet operational temperatures in the subsea environment. The backup rings are typically produced from polymers such as Delrin® or Teflon®.




The end portion


60


includes a plurality of apertures


68


,


70


,


72


,


74


and others not shown. These transverse apertures connect with a bore


76


to allow fluids to flow through the dump valve


10


to the vent port


44


as shown by the flow arrows in FIG.


4


. Fluids flow from the open chamber


24


to the open port


28


, through the conduit


30


to the BOP port


42


through the bore


76


, and the plurality of apertures


68


,


70


,


72


and


74


to the vent port


44


and hence to sea.




A bore


80


is formed in the longitudinal axis of the end portion


58


of the shuttle


36


. A flow restrictor


82


allows fluid communication between the bore


80


and the bore


76


better seen in the next figureFIG.


5


.





FIG. 5

is a section view of the dump valve


10


in the open position allowing fluid to flow through the dump valve


10


to the open chamber


24


of the BOP assembly


18


as shown by the flow arrows. Fluid enters the supply port


34


, passes through the bore


80


, the flow restrictor


82


, the bore


76


, the BOP port


42


and thereafter flows into the open chamber


24


in the BOP assembly


18


as better seen in FIG.


1


. For a one inch dump valve, applicants have determined that a flow restrictor with an I.D. of from 0.156 to 0.375 inches is suitable. The 0.156 inch I.D. flow restrictor allows a flow rate of 20 gpm at 1500 psi differential pressure.




The shuttle


36


is typically located in one of two positions. The vent position is shown in FIG.


4


and the open position is shown in FIG.


5


. When the shuttle is in the vent position of

FIG. 4

the shoulder


55


abuts the supply adapter


48


. When the shuttle


36


is in the open position of

FIG. 5

, the end portion


58


of shuttle


36


is in sealing engagement with the supply adapter


48


and the end portion


60


of shuttle


36


is in sealing engagement with the BOP adapter


50


. Various types of seals could be used to accomplish a seal between the end portion


58


and the adapter


48


and the end portion


60


and the adapter


50


, including metal to metal seals or soft seals. It is important that the seals utilized withstand the high pressures and flow velocities encountered in this application. It is important that the shuttle


36


achieve a seal with the adapter


48


and adapter


50


when the shuttle is in the open position as shown in FIG.


5


. Otherwise hydraulic fluid will bleed out the vent and slow down or thwart efforts to open the BOP rams. Likewise a good seal between the shuttle


36


and the adapter


48


and adapter


50


is important when the valve


10


is in the vent position.





FIG. 6

is an enlarged section view of the end portion


60


of the shuttle


36


and a portion of the BOP adapter


50


using metal to metal seals. Again, other types of seals may be suitable for this valve and the selection of metal to metal seals is a manufacturing choice. The shuttle


36


includes a circumferential flange


56


with a shoulder


57


which is a part of end portion


60


. An outwardly tapered metal sealing surface


100


is formed on the shoulder


57


. Applicants believe that a taper of approximately 8° is optimum for this application. However, other tapers in the range of 5-15° may also be effective so long as they create a coining effect on the metal valve seat


102


of the supply adapter


50


. The only requirement for the angle of taper is to achieve coining and therefore sealing between the sealing surface


100


and the metal valve seat


102


.

FIG. 6

shows the sealing surfaces after the dump valve


10


has been manufactured but before any coining has occurred.




The adapter


50


includes a chamfer


104


recessed behind the metal valve seat


102


to thereby create an obtuse metal point


106


that will contact the tapered metal sealing surface


100


on the flange


56


of the shuttle


36


. Coining occurs when the shuttle moves back and forth from the vent to the open positions. As the shuttle moves back and forth, the tapered metal sealing surface


100


impacts the point


106


and metal it displaced from the point


106


to the chamfer


104


. This displacement of metal is referred to as coining.





FIG. 6

shows the metal valve seat


102


and the metal sealing surface


100


on the end portion


60


of shuttle


36


before any coining has occurred. Applicant uses a chamfer with a 15° angle and a 0.015 inch radius. However, the exact size and depth of the chamfer are not particularly critical because this is merely a recess or space into which displaced metal will move due to progressive coining. A step back shoulder or other recess in lieu of the chamfer may also prove effective provided that there is room to receive the displaced metal from the point


106


such that it does not interfere with movement of the shuttle


36


.




After the shuttle


36


has moved back and forth on several occasions, the metal sealing surface


100


of the shuttle


36


impacts the point


106


of the metal valve seat


102


, and a portion of the metal in the point


106


is displaced into the chamfer


104


. A metal to metal seal is therefore achieved between the metal valve seat


102


and the outwardly tapered metal sealing surface


100


of the flange


56


on the shuttle


36


.





FIG. 7

is an alternative embodiment of the dump valve in the vent position. The valve


210


is constructed in a manner similar to the valve of FIG.


4


and includes a body


246


defining a vent port


244


, a BOP adapter


250


defining a BOP port


242


and a supply adapter


248


defining a supply port


234


. The shuttle


236


includes an end portion


258


and opposite end portion


260


. The shuttle


236


includes a bore


280


having a shoulder


294


. A ball check valve assembly


283


includes a ball


284


that is held in place against a valve seat


288


by spring


286


which rests against the shoulder


294


. The valve seat


288


threadably engages the shuttle at shuttle threads


292


and seat threads


290


.




When the valve


210


is in vent position, as is shown by the flow arrows in FIG.


7


, the spring


286


holds the ball


284


against the valve seat


288


to prevent fluid flow to the supply port


234


. The end portion


258


has an O-ring groove


61


formed therein. An O-ring


62


is positioned in the O-ring groove


61


creating a seal between the adapter


248


and the shuttle


236


. Thus, when the valve


210


is in the vent position as shown, in

FIG. 7

no fluid flows to supply because of the seal achieved by the O-ring


62


with adapter


248


and the ball check valve assembly


283


. However, when the valve


210


is in the open position, fluid pressure acting on the ball overcomes the spring force moving the ball away from the seal and allowing fluid to flow from supply to the BOP. The O-ring


62


makes a seal with adapter


248


to prevent fluid from escaping to vent when the valve is in the open position. The metal valve seat


102


and the metal sealing surface


100


on end portion


260


achieve a seal between the shuttle


236


and the adapter


250


, to likewise prevent fluid from escaping to vent when the valve is in the open position.




The diameter of the end portion


258


is larger than the diameter of end portion


260


. This step in diameter produces greater area on the supply end


258


. When the shuttle


236


is in the open position, and the BOP piston


20


has reached full travel stopping flow and equalizing the pressure across the shuttle, a difference in force is created by this greater area on the supply end portion


258


holding the shuttle in the open position. Applicants have determined that a metal to metal seal can be achieved if the area of end portion


258


is approximately 1.5 times greater than the area of the end portion


260


; however, other area ratios maybe suitable, provided that a good seal is achieved when the valve is in the open position.





FIG. 8

illustrates a second alternative embodiment of the dump valve which includes the ball check assembly


283


, and including supply, vent and BOP ports of essentially the equal diameter. The body


346


defines the vent port


344


, and the adapters


350


and


348394


define the BOP port


342


and the supply port


334


respectively. The ball check valve assembly


283


includes a ball


384


, a spring


394386


and a valve seat


388


.




The metal valve seat


102


and the sealing surface


100


on the end portion


360


of shuttle


336


achieve a seal between the shuffle


336


and the adapter


350


, to prevent fluid from escaping to vent when the valve is in the open position.




The shuttle


336


has end portion


358


and opposite end portion


360


of approximately equal diameters. When in the open position, the spring


386


in the ball check valve results in the pressure on the supply side of the shuttle


336


to be greater than the pressure on the BOP side of the shuttle, resulting in a force pushing the shuttle


336


against the BOP adapter


350


, and effecting a seal between the tapered sealing surface


100


and the metal valve seat


102


.





FIG. 9

is a third alternative embodiment of the dump valve. The valve


410


is constructed in the same manner as the valve of

FIGS. 3-5

, with the exception of the shuttle, the relative port diameters and the soft seal assembly. The shuttle


436


has end portion


458


and opposing end portion


460


. End portion


458


engages supply adapter


448


. End portion


460


engages BOP adapter


450


. Adapters


448


and


450


are of equal size and shape. In

FIG. 9

the metal to metal seal illustrated in

FIG. 6

is replaced by a soft seal created by O-ring


96


which is located in channel


98


of the shuttle


436


. Further, the diameters of the supply port


434


, vent port


444


and BOP port


442


are all the same diameter, which may be advantageous for particular applications. The type of seals employed do not require axial force to be energized as in the previous embodiments discussed.




The shuttle


436


has end portion


458


and opposing end portion


460


, both of which are of approximately equal diameter. Thus, the forces exerted by the fluid on the shuttle


436


are balanced when the shuttle


436


is in the vent position of FIG.


9


and the open position, not shown. As previously discussed, the type of seal is a matter of manufacturing convenience. The valve


410


uses two soft seals, i.e., the O-ring


96


and the O-ring


62


. As a matter of manufacturing choice, other types of seals could also be employed. A check valve could also be utilized in this concept if desired.




Having described the invention in detail, those skilled in the art will appreciate that modifications may be made of the invention without departing from its spirit and scope. Therefore, it is not intended that the scope of the invention be limited to the specific embodiments described. Rather, it is intended that the scope of the invention be determined by the appended claims and their equivalents.



Claims
  • 1. An improved quick dump valve comprising:a body having a central longitudinal bore with first and second opposing ends, the first end being configured to receive and secure a supply port adapter, the second end being configured to receive and secure a BOP port adapter, the body further including a transverse bore in fluid communication with the central longitudinal bore, the transverse bore defining a vent port; the supply port adapter defining a supply port and the BOP port adapter defining a BOP port; a shuttle having first and second ends with a longitudinal central bore extending from the first end to the second end, the longitudinal central bore including a reduced diameter flow restrictor; a seal between the first end of the shuttle and the supply port adapter and a seal between the second end of the shuttle and the BOP port adapter; the first end of the shuttle being of a larger diameter than the second end; and the shuttle being adapted to slidably reciprocate in the body central bore from a vent position where the shuttle first end is in sealing contact with the supply port adapter, to an open position where the shuttle first end is in sealing contact with the supply port adapter and the shuttle second end is in sealing contact with the BOP port adapter; a ball check valve positioned in the longitudinal central bore of the shuttle to prevent fluid flow to the supply port through the longitudinal central bore of the shuttle when the valve is in the vent position; and whereby upon increased fluid pressure in the BOP port the shuttle slides towards the supply port adapter into the vent position, thereby allowing a plurality of shuttle apertures to come into fluid communication with the transverse bore, allowing fluid to flow from the BOP port to the vent port, and whereby upon increased fluid pressure in the supply port the shuttle slides towards the BOP port adapter into the open position, thereby removing the shuttle apertures from fluid communication with the transverse bore to allow fluid flow from and through the supply port, through the longitudinal central bore of the shuttle, the reduced diameter flow restrictor and to and through the BOP port.
  • 2. The apparatus of claim 1 wherein the seal between the first end of the shuttle and the supply port adapter is elastomeric and the seal between the second end of the shuttle and the BOP port adapter is metal to metal.
  • 3. An improved quick dump valve comprising:a body having a central longitudinal bore with first and second opposing ends, the first end being configured to receive and secure a supply port adapter, the second end being configured to receive and secure a BOP port adapter, the body further including a transverse bore in fluid communication with the central longitudinal bore, the transverse bore defining a vent port; the supply port adapter defining a supply port and the BOP port adapter defining a BOP port; a shuttle having first and second ends with a longitudinal central bore extending from the shuttle first end to the second end, the longitudinal central bore having a reduced diameter flow restrictor; a seal between the first end of the shuttle and the supply port adapter and a seal between the second end of the shuttle and the BOP port adapter; the first end of the shuttle engaging the supply port adapter and the second end engaging the BOP port adapter, the second end including a plurality of apertures, the shuttle being adapted to slidably reciprocate in the body central bore from a vent position where the shuttle first end is in sealing contact with the supply port adapter, to an open position where the shuttle first end is in sealing contact with the supply port adapter and the second end is in sealing contact with the BOP adapter; a ball check valve located in the longitudinal central bore of the shuttle to prevent fluid leakage through the longitudinal central bore of the shuttle to the supply port when the valve is in the vent position; and whereby upon increased fluid pressure in the BOP port the shuttle slides towards the supply port adapter into the vent position, thereby allowing the shuttle apertures to come into fluid communication with the transverse bore, allowing fluid to flow from the BOP port to the vent port, and whereby upon increased fluid pressure in the supply port the shuttle slides towards the BOP port into the open position, thereby removing the shuttle apertures from fluid communication with the transverse bore to allow fluid flow from and through the supply port, through the longitudinal central bore of the shuttle, the reduced diameter flow restrictor, and to and through the BOP port.
  • 4. The apparatus of claim 3 wherein the seal between the first end of the shuttle and the supply port adapter is elastomeric and the seal between the second end of the shuttle and the BOP port adapter is metal to metal.
  • 5. An improved quick dump valve comprising:a body having a central longitudinal bore with first and second opposing ends, the first end being configured to receive and secure a supply port adapter, the second end being configured to receive and secure a BOP port adapter, the body further including a transverse bore in fluid communication with the central longitudinal bore, the transverse bore defining a vent port, the supply port adapter defining a supply port and the BOP port adapter defining a BOP port; a shuttle having first and second ends with a longitudinal central bore extending from the first end to the second end, the longitudinal central bore including a reduced diameter flow restrictor; a seal between the first end of the shuttle and the supply port adapter and a seal between the second end of the shuttle and the BOP port adapter; the first end of the shuttle being of a larger diameter than the second end; and the shuttle being adapted to reciprocate in the body central bore from a vent position where the shuttle first end is in sealing contact with the supply port adapter, to an open position where the shuttle first end is in sealing contact with the supply port adapter and the shuttle second end is in sealing contact with the BOP port adapter; a ball check valve positioned in the longitudinal central bore of the shuttle to prevent fluid flow to the supply port through the longitudinal central bore of the shuttle when the valve is in the vent position; and whereby upon increased fluid pressure in the BOP port the shuttle slides towards the supply port adapter into the vent position, thereby allowing a plurality of shuttle apertures to come into fluid communication with the transverse bore, allowing fluid to flow from the BOP port to the vent port, and whereby upon increased fluid pressure in the supply port the shuttle slides towards the BOP port adapter into the open position, thereby removing the shuttle apertures from fluid communication with the transverse bore to allow fluid flow from and through the supply port, through the longitudinal central bore of the shuttle, the reduced diameter flow restrictor and to and through the BOP port.
  • 6. An improved BOP operating system having a BOP stack with open ports and close ports and hydraulically controlled rams adapted to move from an open position to a close position, wherein the improvement comprises: a plurality of quick dump valves proximate the open ports of the BOP stack, whereby the quick dump valve reduces the incidence of hydraulic shock, vibration and hose collapse and reduces the time necessary to move the shear rams from the open position to the close position and each dump valve includes:a body having a central longitudinal bore with first and second opposing ends, the first end being configured to receive and secure a supply port adapter, the second end being configured to receive and secure a BOP port adapter, the body further including a transverse bore in fluid communication with the central longitudinal bore, the transverse bore defining a vent port; the supply port adapter defining a supply port and the BOP port adapter defining a BOP port; a shuttle having first and second ends with a longitudinal central bore extending from the shuttle first end to the second end, the longitudinal central bore having a reduced diameter flow restrictor; a seal between the first end of the shuttle and the supply port adapter and a seal between the second end of the shuttle and the BOP port adapter; the first end of the shuttle engaging the supply port adapter and the second end engaging the BOP port adapter, the second end including a plurality of apertures, the shuttle being adapted to slidably reciprocate in the body central bore from a vent position where the shuttle first end is in sealing contact with the supply port adapter, to an open position where the shuttle first end is in sealing contact with the supply port adapter and the second end is in sealing contact with the BOP adapter; a ball check valve located in the longitudinal central bore of the shuttle to prevent fluid flow through the longitudinal central bore of the shuttle to the supply port when the valve is in the vent position; and whereby upon increased fluid pressure in the BOP port the shuttle slides towards the supply port adapter into the vent position, thereby allowing the shuttle apertures to come into fluid communication with the transverse bore, allowing fluid to flow from the BOP port to the vent port, and whereby upon increased fluid pressure in the supply port the shuttle slides towards the BOP port into the open position, thereby removing the shuttle apertures from fluid communication with the transverse bore to allow fluid flow from and through the supply port, through the longitudinal central bore of the shuttle, the reduced diameter flow restrictor, and to through the BOP port.
CROSS REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. patent application Ser. No. 09/910,245 filed on Jul. 20, 2001 now U.S. Pat. No. 6,655,405 which application claims priority of U.S. provisional patent application No. 60/265,444 filed Jan. 31, 2001.

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Provisional Applications (1)
Number Date Country
60/265444 Jan 2001 US