Patent Grant
9919911
This is a U.S. national stage of application No. PCT/EP2011/070977, filed on Nov. 24, 2011. Priority is claimed on the following application: French Application No. 1059911 filed on Nov. 30, 2010, the content of which is incorporated here by reference.
The present invention relates to a device and a method for transferring fluid, preferably a liquid or gaseous petroleum fluid, from a support located in open sea, in grounded or floating manner, i.e. either resting on or anchored to the sea bottom, and preferably it relates to a device and a method for transferring fluid between a said support and a ship, preferably of the methane tanker type, arranged alongside or in tandem relative to said support. Said transfer device comprises a plurality of n flexible pipes that are stored or suitable for being stored on a said support with the help of a device for storing flexible pipes, with a first end of each of said flexible pipe being fastened to that device, and with said flexible pipes preferably extending or being suitable for extending between said support and a said ship. 1 Translation of the title as established ex officio.
The present invention also relates to a said transfer device also including a said support, where appropriate a said ship that is preferably of the methane tanker type arranged alongside or in tandem relative to said floating support, a said storage device, preferably a said storage and guide device, and at least two flexible pipes, preferably at least three flexible pipes, extending from a said support on which said flexible pipes are stored with the help of a said storage device. The transfer device of the invention includes a connection and valve device that is useful in particular for purging flexible pipes.
A storage device for flexible pipes arranged on board a support of the invention serves to handle said flexible pipes in order to store them in the wound state between two transfers of fluid within said flexible pipes between the floating support and an offloading ship, and for unwinding said pipes in order to perform a said fluid transfer between a said floating support and a said ship, preferably of the methane tanker type.
A more particular technical field of use of a support of the invention is the field of offloading petroleum fluids at sea, including equally well liquid crude oil or gasoil or liquefied gas, in particular liquefied natural gas (LNG), or indeed gas in the gaseous state, from a said support, e.g. at an oil field, to an offloading ship that may be arranged alongside or in tandem, as explained below.
The technical sector of the invention is still more particularly the field of transferring liquefied natural gas (LNG) at −165 ° C. while at sea, between a floating support having at least one LNG storage tank and a ship, preferably of the methane tanker type, arranged in tandem, i.e. at a certain distance from the floating support in the same longitudinal direction as said floating support.
On oil fields in open sea, situated a long way off-shore, petroleum fluids such as crude oil or gas are generally recovered, processed, and stored on board a said floating support often referred to as an FPSO (floating-production-storage-offloading). Petroleum fluids such as crude oil and/or gas are then exported by offloading ships that call regularly, e.g. every week, to recover the production from the oil fields. Three techniques are commonly used for this purpose.
A first technique consists in installing a buoy a long way from the FPSO, i.e. at about 1000 meters (m) to 1500 m, which buoy is referred to as a loading buoy and is connected to the FPSO by an undersea pipe, with oil or gas being transferred to said loading buoy via said undersea pipe. An offloading tanker then moors on said loading buoy and the load is recovered via flexible connection pipes connected to said buoy floating on the surface of the sea, the oil or gas then being driven by a pump on board the FPSO in order to load the offloading tanker.
A second technique consists in causing the offloading tanker to draw up alongside the FPSO, i.e. side against side. Under such circumstances, transfer is performed either by hinge-type loading arms, as is common practice for transfers in port, or else by flexible pipes of short length.
A third technique consists in placing the offloading ship in tandem with the FPSO, i.e. the offloading ship takes up a position on the axis of the FPSO at a safe distance of at least 50 m to 150 m, and then moors thereto, after which it recovers the ends of floating pipes that extend from the floating support where they are connected to a tank at their ends opposite from their ends floating on the sea, the recovered ends being connected on board said offloading ship, and oil or gas then being driven by a pump from the FPSO in order to load the offloading tanker.
On oil fields, it is generally preferred to use a loading buoy, while nevertheless associating it in general with a redundancy device that may be either an alongside device, i.e. a device in which the offloading ship is arranged alongside the FPSO, or else a tandem device, i.e. a device in which an offloading ship is arranged in tandem with the FPSO, and sometimes even both such devices.
In all configurations, with crude oil, the connection pipes either to a loading buoy or to an offloading ship are kept full, either with crude oil or else with an oil product, generally gasoil, that takes the place of crude oil when there is a risk of the crude oil solidifying (paraffinic crudes).
In contrast, when transferring liquefied gas of the LNG type at −165° C., transfer devices include at least one go connection pipe for the liquefied gas and a return connection pipe, in general of smaller diameter, for removing gas from the tanks of the offloading ship progressively as they are filled with LNG, and in particular for removing methane gas so that it can be reliquefied on board the FPSO. Furthermore, the connecting flexible pipes need to be emptied practically completely after offloading so as to avoid ice forming and accumulating on said pipes and more particularly on the mechanical connections of said pipes. Furthermore, the pipes need to include extremely good insulation so as to limit the amount of liquid methane (LNG) that is regassified during transfer. That is why, for this purpose, it is preferred to use offloading techniques with alongside and tandem devices in which firstly the connecting pipes are not undersea pipes but rather pipes that float on the surface, and secondly said pipes are of relatively short length.
Nevertheless, offloading alongside is very difficult since it is possible to envisage bringing an offloading ship into a position parallel with the FPSO and at a distance of less than 5 m therefrom only under sea conditions that are very clement. With rough sea, transfer becomes impossible, and if the FPSO is full that can make it necessary to stop production, which constitutes a serious handicap for the profitability of installations exploiting the oil fields in question. The transfer means are then constituted either by conventional loading arms, or by devices having flexible pipes installed on board said FPSO. Patent EP-2 239 190 describes such an alongside offloading device.
Tandem offloading presents much greater safety, but offloading pipes are longer and therefore more complicated to handle and store on board the FPSO. For this purpose, numerous devices have been developed for storing and guiding flexible pipes on board an FPSO. Some of them use of a considerable carrier structure of the hinge type supporting a plurality of rigid pipes including rotary joints as hinges, as described in detail in U.S. Pat. No. 4,393,906.
Other solutions include using rigid pipes hinged with rotary joints, or flexible pipes arranged in festoons between the FPSO and the offloading ship, as explained in patent WO 01/04041.
Another technical field is one in which LNG is stored at sea close to a utilization site, e.g. in order to deliver gas to land after it has been regassified, or indeed to transform it on site into electricity for delivering said electricity to the local network. Under such circumstances, the ship comes to unload its cargo of LNG and the floating support is referred to as an FSRU (floating storage regasification unit).
An object of the present invention is to provide an improved transfer device for performing transfers between a support and a methane tanker type ship arranged alongside or in tandem, in particular for offloading from said support to an offloading ship.
More particularly, the object of the present invention is to provide an improved transfer device using flexible pipes that extend from a support at sea that is fitted with a device for supporting and guiding flexible pipes, the device facilitating the handling of said pipes in order to perform fluid transfer between said support and an offloading ship, and also to store said flexible pipes on board the support between two transfers.
A problem to be solved is facilitating the coupling of the ends of the flexible pipes on board an offloading ship when said pipes are pipes for transferring petroleum fluid extending from a support installed at sea to a said offloading ship, and also to facilitate the emptying of the flexible transfer pipes after offloading said oil fluid and before restoring them with the help of a storage device on board said support.
To do this, the present invention relates to a transfer device for acting between a support installed at sea, the support being fitted with a device for storing flexible pipes having the first ends of a plurality of flexible pipes connected thereto, the pipes preferably extending between said support and a ship that is preferably of the methane tanker type, said pipes being connected to one another at their second ends by a first connection and valve device having n first pipe portions suitable for being connected to a second connection and valve device that is preferably installed on board a said ship that is preferably of the methane tanker type.
More precisely, the present invention provides a device for transferring fluid from a support installed at sea, in grounded or floating manner, preferably between a said support and a ship, preferably of the methane tanker type, arranged alongside or in tandem adjacent to said support, said fluid transfer device comprising a plurality, n, of flexible pipes that are stored or suitable for being stored on a said support by means of a flexible pipe storage device to which a first end of each of said flexible pipes is fastened, said flexible pipes preferably being suitable for extending between said support and a ship, preferably of the methane tanker type, arranged alongside or in tandem adjacent to said support, the device being characterized in that it comprises a first connection and valve device, said flexible pipes being connected together at their second ends by said first connection and valve device, said first connection and valve device having n preferably rigid first pipe portions held in preferably parallel fixed positions relative to one another, n being an integer not less than 3, each said first pipe portion comprising:
It can be understood that each first connection valve situated between said first coupling element and said branch connection is suitable for allowing or preventing fluid from flowing in said first pipe portion towards or from said first coupling element when the valve is respectively open or closed.
A connection and valve device of the invention is particularly useful for purging a set of flexible pipes after they have been used for offloading a liquid petroleum fluid between a said support installed at sea and a said offloading ship as described below, prior to storing the pipes with the help of a said storage device, in order firstly to avoid any damage to said flexible pipes and in order secondly to facilitate restoring them with the help of said storage device.
Preferably, the transfer device of the invention further comprises a second connection and valve device arranged or suitable for being arranged on board a said ship, preferably of the methane tanker type, arranged alongside or in tandem adjacent to said support, in particular facing a side of said support, said first connection and valve device being connected or suitable for being connected to said second connection and valve device, said second connection and valve device comprising:
More particularly, said flexible pipes comprise at least one flexible pipe, a “first” flexible pipe, preferably at least two flexible pipes, “first” and “second” flexible pipes, suitable for transferring liquefied gas therein between said floating support and at least one second tank of said ship, preferably of the methane tanker type, and of a second flexible pipe, preferably of diameter smaller than the diameter of said first and second pipes, within which gas corresponding to the gas ceiling of the second tank is suitable for being transferred from a said second tank to a first tank within said floating support or to a liquefaction unit on a said support prior to being transferred to a said first tank, in particular during filling of said second tank.
In particular, when said methane tanker is an offloading ship and said liquefied gas is being offloaded from said floating support to said offloading ship, gas return from said offloading ship to said floating support takes place progressively as said second tank within said offloading ship is filled.
Even more particularly, a fluid transfer device, in particular a liquid or gaseous petroleum product, comprises a said support, a said storage device, preferably a storage and guide device, and at least two said flexible pipes, preferably via at least three flexible pipes, extending between a said support and a said ship, preferably of the methane tanker type, arranged alongside or in tandem adjacent to said floating support, at least some of said flexible pipes being stored with the help of a said storage and guide device, said flexible pipes being fitted with a said first connection and valve device, connected to a said second connection and valve device arranged or suitable for being arranged on board a said ship.
In a first implementation, said transfer consists in offloading liquefied gas from said support to a said ship referred to as an offloading ship.
In a second implementation, said transfer consists in loading liquefied gas onto said support from a said ship, referred to as a supply ship. In general this involves loading liquefied gas that is regassified within said support in order to be transferred to land in gaseous form or in order to be used to produce electricity. Under such circumstances, said floating support may also contain a unit for producing electricity from said gas and a transformer station for delivering electricity to land. Under such circumstances, said support is advantageously a support grounded on the sea bottom.
More particularly, in a transfer method of the invention, said flexible pipes are floating pipes, floating on the surface over at least a fraction of the distance between said support and said ship, preferably of the methane tanker type.
The present invention also provides a method of transferring a fluid, preferably a liquid or gaseous petroleum fluid, from a support installed at sea, in grounded or floating manner, preferably between a said support and a ship, preferably of the methane tanker type, arranged alongside or in tandem adjacent to said support by means of a device of the invention, wherein said liquid petroleum fluid, preferably liquid natural gas LNG, is transferred to two said first and second flexible pipes, and then said first and second flexible pipes used for transferring the liquid product, preferably liquid natural gas LNG, between said support and a said ship, preferably of the methane tanker type, are purged by performing the following successive steps:
a. closing said first and second connection valves, and disconnecting said first and second connection and valve devices from each other;
b. injecting gas into the first end of a first flexible pipe from said support and opening at least one said first communication valve between said first flexible pipe and a second flexible pipe assembled to the same said first connection and valve device, the other said first communication valves being closed; and then
c. closing said first communication valve between said first and second pipes when said first pipe has been emptied sufficiently, and preferably substantially completely emptied.
Emptying is said to be “sufficient” when the inside volume of said pipe filled with residual fluid represents no more than 10% of the total inside volume of said pipe, preferably no more than 5%, i.e. an inside volume that is at least 90% empty, preferably at least 95% empty, and more preferably at least 98% of its total internal volume is empty.
The method thus makes it possible to empty the content of said first flexible pipe via said second flexible pipe, thereby making it possible after step c) to empty said first flexible pipe substantially or indeed completely. In contrast, there may still remain in general at least 10% and possibly up to 15% of the inside volume of said second pipe that has not been emptied, even when the inside volume of said first pipe has been emptied completely.
In particular it is more difficult to empty the second flexible pipe completely after step c), since the end portion of the second flexible pipe corresponding to the substantially vertical portion between sea level and the level of its access to said storage device on the deck of said support with which it co-operates, generally remains at least partially filled with fluid after step c) because the two-phase fluid is moving upwards while gravity naturally tends to bring it back down to sea level.
Preferably, after step c), said second pipe is purged completely by performing the following successive steps:
d. injecting gas from the support into said first end of said second pipe and opening said first communication valve between said second pipe and a third flexible pipe of smaller diameter than said second pipe so that the flow rate of purge gas is such that the speed of said gas is greater than 1.5 meters per second (m/s), preferably greater than 3 m/s, more preferably greater than 5 m/s, said other first communication valves being closed; and
e. closing said first communication valve between said second and third pipes when said second pipe has been emptied sufficiently, and preferably emptied substantially completely.
It can be understood that in this implementation, the inside volume of the liquid fluid contained in the second pipe is removed completely via said third pipe. The fact that said third pipe is of smaller diameter facilitates complete emptying of said third pipe, in particular in its substantially vertical portion between sea level and its entry onto the corresponding turntable after step e), once said second pipe has been substantially completely emptied. It is particularly advantageous to perform the combination of steps a) to e) in order to empty all three of said first, second, and third pipes.
Another problem to be solved by the present invention is providing a device for storing and guiding said flexible pipes that makes it possible in controlled manner to adjust the tension and the length between said floating support and said offloading ship, in particular so as to avoid interference between a plurality of connection pipes extending between said floating support and said offloading ship from the storage and guide device.
To do this, in the present invention said transfer device comprises a said support installed at sea and fitted, preferably on its surface, in particular on deck, with a device for storing and guiding flexible pipes, the device essentially comprising:
More precisely, said support is fitted on its surface with a storage and guide device for storing and guiding flexible pipes and suitable for storing and guiding a plurality of said flexible pipes, and preferably at least three of them, said storage and guide device comprising:
It can be understood that the pipe portion leaving the turntable corresponds to the unwound pipe portion in continuity with the last turn of the wound pipe, in particular during winding or unwinding.
This storage and guide device of the invention is particularly advantageous for positioning the various pipes leaving the turntables relative to one another and for independently adjusting their lengths and/or tensions between said turntables and the second ends of the flexible pipes leading in particular to a second ship, in particular an offloading ship, in such a manner as to avoid the pipes from interfering with one another or indeed striking one another, in particular while unwinding or winding a pipe respectively before or after deployment of said pipe between said floating support and said offloading ship.
This independent adjustment of the rotation of the various turntables is particularly useful and advantageous when the various flexible pipes wound on the various turntables are of different diameters and therefore require different winding or unwinding speeds in order to maintain substantially constant length or tension on leaving said turntables while the pipes are being wound and unwound.
This applies in particular when transferring liquefied gas of the LNG type from a floating support of the invention to an offloading ship 2 while another flexible pipe, generally of smaller diameter, is being used to transfer gas in the gaseous state corresponding to the gas ceilings in the tanks, from said offloading ship back to said floating ship, as explained below.
Of a vessel (ship or floating support), the term “side” is used herein to mean any external wall of the hull of the vessel, i.e. not only the longitudinally extending lateral walls of the hull but also transverse walls at the longitudinal ends thereof, i.e. the bow and stern walls of said vessel.
The term “flexible pipe” is used herein for pipes also known as “hoses” that are well known to the person skilled in the art and that are described in standards documents published by the American Petroleum Institute (API), more particularly under the references API 17J and API RP 17B. Such hoses are manufactured and sold in particular by the supplier Coflexip in France. Such flexible pipes generally comprise inner sealing layers of thermoplastic materials associated with layers that withstand pressure inside the pipe, generally made of steel or of composite materials and in the form of strips wound in touching spiral turns inside the thermoplastic pipe in order to withstand the internal bursting pressure, and associated with external reinforcement over the tubular thermoplastic layer and likewise in the form of strips that are spiral-wound with touching turns, but at a longer pitch, i.e. with a smaller angle of inclination for the helix, in particular lying in the range 15° to 55°.
More particularly, at least one said flexible pipe is wound, at least in part, against and around a said central cylinder in concentric juxtaposed spiral turns of increasing diameters resting on said turntable, said central cylinder presenting a radius greater than the minimum radius of curvature of said flexible pipe, there being preferably at least three flexible pipes wound, at least in part, respectively on at least three said turntables, including at least one flexible pipe of diameter smaller than the others.
Still more particularly, in a transfer device of the invention, each guide means is arranged at a different height facing a respective one of each of said turntables so as to be suitable for supporting an intermediate curved pipe portion between a downstream portion of said pipe in a substantially vertical position beside said side and a said upstream pipe portion leaving the turntable in continuity with the wound pipe portion resting on a said turntable, said upstream pipe portion leaving the turntable extending on a virtual plane P that is substantially tangential to the surface of the top face of said turntable on which said wound pipe portion is wound, the various downstream pipe portions in substantially vertical positions beside said side being arranged in positions that are offset relative to one another in a said direction Y2Y2′ parallel to said side on leaving said sheaves.
Still more particularly, each said guide means comprises a sheave mounted to revolve about a horizontal first axis of rotation Y1Y1′, said sheave also being suitable for swiveling, preferably freely, about a vertical second axis of rotation Z1Z1′ extending along a diameter of the sheave, said first axis of rotation about which each said sheave revolves preferably being controlled by a second motor, preferably synchronously with said first motor of each said turntable.
Thus, because said sheave is free to swivel about its vertical second axis of rotation Z1Z1′ and because said synchronous motor-driven rotation of said sheave about its horizontal first axis of rotation Y1Y1′, a said curved intermediate pipe portion supported by said sheave can remain permanently in the same substantially vertical plane P1, P2, P3 as a said upstream pipe portion leaving the turntable, with the various planes P1, P2, P3 being oriented at different angles α1, α2, α3 relative to said direction Y1Y′1 in order to reach said turntables in continuity and in tangential alignment with the ends of the last turns of the pipes wound thereon, thus enabling the pipes to be properly spooled progressively as they are wound or unwound about said central cylinders.
It can be understood that such a vertical axial plane P1, P2, P3 is the common substantially vertical plane in which the upstream and intermediate portions of a pipe are situated, whereas in contrast the axial plane of the downstream pipe portion in a substantially vertical position is not necessarily situated in the same vertical plane.
In a variant embodiment of a floating support of the invention, said guide means are constituted merely by chutes.
Still more particularly, the various sheaves are arranged offset side by side relative to one another in said horizontal direction Y1Y′1 parallel to said side at different heights, the top of each sheave preferably being positioned substantially level with a plane P tangential to the top face of a said turntable.
It can be understood that the various downstream pipe portions in substantially vertical positions beside said side are thus arranged side by side in a said direction Y1Y1′ that is parallel to said side at the outlet from said sheaves, with each sheave preferably being adjustable in height relative to said portion of its said second carrier structure fastened to said side.
Still more particularly, each sheave is supported by a second carrier structure arranged outside said floating support and fastened to a common side at a different position in a said horizontal direction Y1Y1′ parallel to said side, each sheave being mounted to swivel about said vertical second axis of rotation Z1Z1′ relative to a portion of its said second carrier structure fastened to said side.
Still more particularly, each said turntable includes or co-operates on its under face with wheels suitable for co-operating with or respectively supported by elements of said carrier structure, and each said turntable including a bearing at said central orifice, the bearing being secured to said carrier structure and being suitable for enabling said turntable to rotate relative to said first carrier structure.
In variant embodiments, said turntables may be such that:
The term “concave” or “convex” is used herein of a frustoconical shape to indicate that the virtual apex of said cone lies below or respectively above said surface of frustoconical shape. It can be understood that the cone angle α relative to the horizontal lies in the range 1° to 10°.
A turntable of convex or concave frustoconical shape is particularly useful for purging the residual load from a flexible pipe filled with liquid, and in particular liquefied gas, when the pipe is stored and wound on its said turntable, as explained below.
According to other characteristics of the transfer method of the invention, said storage device comprises a plurality of turntables arranged one above another on which, when all of said flexible pipes have been purged sufficiently, said flexible pipes are rewound until the second ends of all of said flexible pipes are above water, preferably with said first connection and valve device coming just under the lowest of the turntables co-operating with one of said flexible pipes.
It can be understood that said first valve and connection device remains permanently fastened to said second ends of all of said first flexible pipes with which it co-operates when it is desired to rewind said flexible pipes, and that said first connection and valve device remains above water, preferably at the level of the lowest turntable.
Still more particularly, in a transfer method of the invention:
It can be understood that any residual liquid in said second and third pipes can thus flow towards the tank via said lower first ends of said pipes under residual natural gravity while the pipe is being wound.
Other characteristics and advantages of the present invention appear better in the light of the following detailed description made by way of non-limiting illustration and with reference to the drawings, in which:
Said FPSO possesses equipment 1b for processing and liquefying gas together with first tanks 11 for storing LNG incorporated within its hull.
A methane tanker type offloading ship 2 is positioned in tandem substantially on the axis of said FPSO and is connected thereto by a set of three flexible pipes 3A, 3B, and 3C that are handled by means of a storage and guide device 4 of the invention for storing and guiding flexible pipes 3, which device is described in greater detail below.
Said flexible pipes 3 are floating flexible pipes of the type manufactured and sold by the supplier Trelleborg (France), being constituted essentially by metal or composite reinforcement together with thermoplastics or vulcanized elastomers.
Such pipes for offload transfer of liquefied gas conventionally presents inside diameters lying in the range 250 millimeters (mm) to 600 mm, and outside diameters in the range 400 mm to 1000 mm. They are generally manufactured in lengths of 12 m and they are assembled together via their ends that are fitted with flanges so as to obtain lengths lying in the range 120 m to 250 m. In the same manner, the pipes for return transfer of gas in the gaseous state between the offloading ship 2 and the floating support 1 in a manner that is explained below, present the same total lengths but are advantageously of smaller diameter, having an inside diameter lying in the range 150 mm to 400 mm.
Under certain circumstances, it is preferable for gas return to have pipes that are identical to the LNG transfer pipes, thereby presenting an advantage in terms of storing spare parts, since all of the elements are then identical.
The three turntables 4-1 are supported by a first carrier structure 5 resting on the deck 1c of the floating support 1 close to a side 1d and at one of its longitudinal ends.
As shown in
At its center, each of said turntables presents an orifice 4-2 together with a bearing 4-4, e.g. a roller bearing, said bearing being secured in part to a said horizontal carrier structure 5a and enabling said rotation of the turntable about its central axis of rotation ZZ′ with the help of a first motor 6 and of wheels 4-5 that are described below.
Each turntable 4-1 is supported at its periphery and via its bottom face by a series of wheels 4-5, that are preferably uniformly distributed around its periphery, the supports 4-5a of said wheels 4-5 being secured to a said horizontal carrier structure 5a.
Each turntable 4-1 is set into rotation about its vertical axis ZZ′ by means of a first motor 6, preferably a hydraulic motor, that imparts rotary drive to an outlet shaft carrying a gear that co-operates with a toothed wheel 6-1 secured to said turntable 4-1, thereby driving said turntable in rotation when said outlet shaft is itself driven in rotation.
A central cylinder 4-3 is arranged on top of said orifice 4-2 in each of said turntables. The outside radius of said central cylinder 4-3 is greater than the minimum radius of curvature of said flexible pipe that is to be wound with concentric touching spiral turns resting side by side on said turntable. Said central cylinder 4-3 is secured to said turntable 4-1.
As shown in
It is constituted by a rotary joint proper 7-1 having a top portion fitted with a top bend 7-2 with its end coming against the wall of said central cylinder 4-3. The end of the top bend 7-2 is connected in leaktight manner at 7a to a first end 3-1 of a flexible pipe 3 that is to be spiral-wound against and around said central cylinder 4-3 when said turntable 4-1 is driven in rotation. The bottom portion of the rotary joint 7-1 comprises a bottom 7-3 that remains stationary while said top bend 7-2 is driven in rotating by rotation of said turntable 4-1. The bottom bend 7-3 is itself connected in leaktight manner to an end 8-1 of a transfer pipe 8 having its other end connected either to a first tank 11 of the FPSO 1, thereby enabling LNG coming from said first tank 11 to be taken to the FPSO 1, or else to a reliquefaction unit on board the FPSO, thereby enabling gas coming from said offloading ship 2 to be returned to said reliquefaction unit.
All of the various transfer pipes 8 pass through respective central orifices 4-2 of the various turntables 4-1.
Each flexible pipe 3, 3a-3b-3c is guided by guide means 10, only one of which is shown in
The sheave 10-1 presents a radius that is greater than the minimum radius of curvature of said flexible pipe 3 that is to be wound around said sheave.
Said sheaves 10-1, 10-1a, 10-1b, 10-1c are arranged close to and facing respective ones of said turntables 4-1 in such a manner that the groove in each of said sheaves has its highest point substantially level with a virtual plane P that is tangential to the top face 4-1a, which virtual plane P has resting thereon the pipe portion 3-2 that leaves said turntable.
In other words, the generator line for the surface of revolution constituting the top face 4-1a of said circular turntable 4-1 is tangential to the groove of said sheave at its highest point.
In this way, the flexible pipe portion 3-2 leaving said turntable 4-1, i.e. that is in continuity with the last turn wound on said turntable 4-1, is guided more accurately during operations of winding and unwinding said pipe during rotation of said turntable 4-1 and during rotation of said sheave 10-1 about its horizontal axis X1X′1.
Each sheave 10-1 is secured to a second carrier structure 10-1 comprising a vertical support 10-3 terminated at its top end by a fork supporting the horizontal hub arranged on the first axis of rotation Y1Y′1 about which the sheave 10-1a of
Furthermore, the vertical support 10-3 supporting the sheave 10-1 is suitable for being moved vertically in order to adjust the position of the top of the sheave relative to the plane tangential to the top face of the turntable 4-1 in front of which it is arranged.
As shown in
Also in
Said axial planes P1, P2, and P3 of the three sheaves also correspond to the substantially vertical axial planes of the three upstream pipe portions extending between each of said turntables and each of said sheaves, respectively.
Each sheave 10-1 is preferably motor driven by a second motor 10-6, preferably a hydraulic motor, co-operating with a toothed ring (not shown) secured to said sheave and enabling each of said sheaves 10-1 to be driven to revolve about its own horizontal said first axis of revolution Y1Y′1.
The fact that the various sheaves 10-1 are arranged at different heights corresponding to the heights of said turntable 4-1 that it serves, and the fact that said sheaves 10-1 are arranged one beside another in a manner that is offset in the direction Y1Y′1, in spite of the swivel angles α1, α2, and α3 of each of the three sheaves 10-1a, 10-1b, 10-1c, there is no risk of said sheaves interfering with one another.
As shown in
As shown in
In
By way of illustration, a turntable 4-1 presents a diameter of about 20 m. The height of the storage device 4, i.e. the height of the various posts 5b is about 15 m to 20 m for three turntables 4-1 that are spaced apart from one another vertically by 4 m to 5 m. A central cylinder 4-3 typically presents a diameter lying in the range 5 m to 8 m.
Such a device 4 is particularly suitable for receiving flexible pipes having a diameter lying in the range 120 mm to 600 mm and presenting a length lying in the range 120 m to 250 m.
Each of said turntables 4-1 can be set into rotation about its axis ZZ′ independently of any of the others. The same applies to the motor drive for said rotary movement of said sheaves 10-1 about their first axis of rotation. It is thus possible to adjust the tension and the length of each of said flexible pipes 3a, 3b, and 3c independently of any of the others so that said flexible pipes extend between the vertical portions 3-4 at the outlet from the sheaves 10-1 and a common valve device 13, also known as a connection and purge device, that is located on board the offloading ship 2 and to which the various second ends of the various flexible pipes 3a, 3b, and 3c are connected, with the tensions and lengths of said pipes being adjusted to be substantially equal throughout all winding and unwinding operations of said flexible pipe. Generally speaking, since the respective diameters of each said flexible pipes may be different, it is necessary to have different numbers of revolutions of the turntables for each of said flexible pipes 3a, 3b, and 3c in order to store the same length for each flexible pipe.
Once the pipes are rewound onto their respective turntables 4-1, it is advantageous to use a turntable having a top face 4-1a that is of frustoconical shape that is concave 4-1b or convex 4-1c, as shown in
The flexible pipes 3b, 3c conveying LNG stored in a first tank 11 of the support 1 to the ship 2 are of very large diameter in order to optimize the rate at which LNG is transferred, whereas the returning gas can be conveyed using a single pipe, generally a pipe of smaller diameter, since head losses are much smaller for gas than for LNG.
It should be recalled that LNG is essentially constituted by liquid methane at −165° C., and that the offloading ships are constituted by methane tankers, i.e. by ships that transport LNG in tanks that, when empty, are in fact full of gaseous methane, possibly together with some nitrogen, coming from the regasification of LNG. The use of gas return pipes is intended firstly to remove the gas ceilings from the second tanks progressively as they are being filled with LNG coming from the first tanks, and secondly to remove LNG that has become regassified while it is being transported as a result of relative heating. Once the gas has been returned to the support 1, it is reliquefied to become LNG.
There follows a description of the connection and valve device 13 together with the method of purging flexible pipes before they are rewound on their turntables. This purging is necessary firstly to lighten the flexible pipes and make them easier to rewind, and also to avoid damaging said flexible pipes while they are being rewound on said turntables, where such damage could arise as a result of the pipes being excessively heavy when full of liquid, and because of the presence of sea water ice on the surface of the pipes or on the connection elements.
The connection and valve device 13 shown in
a) a first valve and connection device 13-1 arranged at the ends of said flexible pipes 3a, 3b, and 3c, and comprising:
b) a second connection and valve device 13-2 arranged on board said offloading ship 2 and comprising:
Advantageously, the various valves are ball valves or butterfly valves.
Because said first coupling elements are held together securely at constant distances from one another by said first support 24 to which they are secured at 24a, 24b, and 24c, and because said first complementary coupling elements are likewise held firstly at constant distances from one another that are identical to the distances between said first coupling elements, said first and second devices 13-1 and 13-2 can be connected together automatically by remotely controlled actuators (not shown), with it being possible for this to be done in a single sequence.
In
For clarity of explanations with reference to
The first valve device 13-1 is provided with a third series of communication valves between said first pipe portions 21a-21b-21c that are arranged as follows:
During operations of transferring LNG from the offloading ship 2, said three vales 30ab, 30ac, and 30bc are in the closed position, as shown in
In order not to leave the flexible pipes 3a, 3b, 3c floating on the sea between two transfers of LNG, which might represent a duration of several weeks, the flexible pipes are rewound on the turntables 4-1, preferably after they have been purged as follows:
More particularly, and as a general rule, the pipe 3b is empty while liquid remains in the pipe 3c occupying 10% to 20% of the inside volume of the pipe 3c, in particular in its substantially vertical portion 3-4, as shown in
The purge process described above with reference to
In order to optimize emptying of the rising vertical pipe portion, it is appropriate to create a purge gas speed greater than 1.5 m/s, preferably greater than 3 m/s, and more preferably greater than 5 m/s. Thus, giving consideration to a pipe of small diameter, the gas flow rate needed to obtain such a speed decreases with the square of the ratio of the diameters, thus illustrating the advantageous nature of having a gas return pipe that is of smaller diameter.
To further improve this stage of purging the pipes 3b and 3c, it is advantageous to proceed sequentially as shown in
For the pipe portion 3-4 having a height lying in the range 30 m to 35 m, corresponding to a pressure difference of 1.5 bars to 2 bars, the bubbles in the bottom portion will have a diameter lying in the range 5 mm to 10 mm, while the bubbles in the top portion will have a much larger diameter as a result of the pressure difference, lying in the range several centimeters to several decimeters, thereby having the effect of reducing the density of the two-phase mixture in the fluid column and thus encouraging its entrainment and offload at the level of the turntable: with this phenomenon being referred to as “gas-lift”.
In the purging technique described with reference to
When the gas return pipe presents an inside diameter that is smaller than the inside diameter of the LNG pipes, the preferred purging method comprises the following two purging steps:
After the three pipes 3a, 3b, and 3c have been purged, they are rewound onto their respective turntables until said first connection device 13-1 comes above the level of the water, and more particularly substantially just below the lowest turntable of the flexible pipes held together by the device 13-1, as shown in
By way of example, a transfer device of the invention comprises:
The procedure of purging the pipes is performed at a gas speed of 4 m/s under such conditions and occupies a total duration of 30 minutes (min) to 45 min so as to obtain an overall residue of LNG that is less than 1% of the overall volume of a pipe, which represents about 425 liters (L) of residual LNG that then produce 250 cubic meters (m3) of gaseous methane that will thus ultimately be reliquefied on board the FPSO.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 59911 | Nov 2010 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2011/070977 | 11/24/2011 | WO | 00 | 5/22/2013 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2012/072499 | 6/7/2012 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 3541622 | Harlow | Nov 1970 | A |
| 4261398 | Haley | Apr 1981 | A |
| 4376452 | Tax | Mar 1983 | A |
| 4388948 | Carminati | Jun 1983 | A |
| 4406636 | Van Heijst | Sep 1983 | A |
| 6637479 | Eide | Oct 2003 | B1 |
| 7438617 | Poldervaart | Oct 2008 | B2 |
| 7793605 | Poldervaart | Sep 2010 | B2 |
| 8590472 | Biaggi | Nov 2013 | B2 |
| 9308972 | Hallot | Apr 2016 | B2 |
| 20100326667 | Coppens | Dec 2010 | A1 |
| Number | Date | Country |
|---|---|---|
| 1705111 | Sep 2006 | EP |
| 2239190 | Oct 2010 | EP |
| 2420319 | May 2006 | GB |
| 60-88298 | May 1985 | JP |
| WO 9935031 | Jul 1999 | WO |
| WO 0104041 | Jan 2001 | WO |
| WO 2010059052 | May 2010 | WO |
| Entry |
|---|
| English Abstract of Shigeru JP 60-88298. |
| International Search Report dated Dec. 29, 2011. |
| Number | Date | Country | |
|---|---|---|---|
| 20130240085 A1 | Sep 2013 | US |
