Not Applicable
1. Field of the Invention
The present invention generally relates to floating offshore platforms. More particularly, it relates to semi-submersible production platforms.
2. Description of the Related Art Including Information Disclosed Under 37 CFR 1.97 and 1.98
This invention relates to semi-submersible vessels used for hydrocarbon production (“production semi”). On semi-submersibles used for drilling operations, fluid storage within the hull is commonplace. However, the fluid quantities needed for drilling operations are typically much less than what would be required for hydrocarbon product storage on a production semi.
Most natural gas extracted from the Earth contains, to varying degrees, low molecular weight hydrocarbon compounds; examples include methane (CH4), ethane (C2H6), propane (C3H8) and butane (C4H10). The natural gas extracted from coal reservoirs and mines (coalbed methane) is the primary exception, being essentially a mix of mostly methane and about 10 percent carbon dioxide (CO2).
Natural-gas condensate is a low-density mixture of hydrocarbon liquids that are present as gaseous components in the raw natural gas produced from many natural gas fields. It condenses out of the raw gas if the temperature is reduced to below the hydrocarbon dew point temperature of the raw gas.
The natural gas condensate is also referred to as simply condensate, or gas condensate, or sometimes natural gasoline because it contains hydrocarbons within the gasoline boiling range. Raw natural gas may come from any one of three types of gas wells.
Raw natural gas that comes from crude oil wells is called “associated gas.” This gas can exist separate from the crude oil in the underground formation, or dissolved in the crude oil. Condensate produced from oil wells is often referred to as “lease condensate.”
“Dry gas wells” typically produce only raw natural gas that does not contain any hydrocarbon liquids. Such gas is called non-associated gas. Condensate from dry gas is extracted at gas processing plants and, hence, is often referred to as plant condensate.
“Condensate wells” produce raw natural gas along with natural gas liquids. Such gas is also called associated gas and often referred to as wet gas.
Raw natural gas typically consists primarily of methane (CH4), the shortest and lightest hydrocarbon molecule. It also contains varying amounts of:
Heavier gaseous hydrocarbons: ethane (C2H6), propane (C3H8), normal butane (n-C4H10), isobutane (i-C4H10), pentanes and even higher molecular weight hydrocarbons. When processed and purified into finished by-products, all of these are collectively referred to as Natural Gas Liquids or NGL.
Most large, modern gas processing plants recover natural gas liquids (NGL) using a cryogenic low temperature distillation process involving expansion of the gas through a turbo-expander followed by distillation in a demethanizing fractionating column. Some gas processing plants use a lean oil absorption process rather than the cryogenic turbo-expander process.
U.S. Pat. No. 7,980,190 entitled “Deep draft semi-submersible LNG floating production, storage and offloading vessel” describes a method, apparatus, and system of a deep-draft semi-submersible hydrocarbon, such as for liquefied natural gas (LNG), floating production and storage vessel that can include a pontoon containing hydrocarbon tanks, fixed ballast at the bottom in a double-bottom portion, and segregated ballasted tanks with variable ballast located generally above the fixed ballast portion that can assist in keeping the pontoon submerged during various storage levels. Multiple vertical columnar supports can penetrate the pontoon from top to bottom and extend above the water surface to support a deck, including various topside structures. An intermediate double-deck on the top of the pontoon can provide access to the tanks, for example, through the vertical columnar supports. The double bottom structure, deck, and vertical columnar supports are said to provide overall structural integrity.
U.S. Pub. No. 2009/0293506 A1 entitled “Semi-Submersible Offshore Structure Having Storage Tanks for Liquefied Gas” describes a semi-submersible offshore structure having storage tanks for liquefied gas, which is constructed so as to improve workability in marine offloading of the liquefied gas stored in the storage tanks while reducing an influence of sloshing. The offshore structure is anchored at sea and has liquefied gas. The offshore structure includes a storage tank storing liquefied gas, a plurality of columns partially submerged under the sea level and each having the storage tank therein, and an upper deck located on the plurality of columns to connect the columns to each other.
The present invention relates to the storage of hydrocarbon liquids inside the hull of a production semi-submersible or tension leg platform (TLP), in particular the storage of liquid hydrocarbons. The hydrocarbon liquids are stored inside the column. There are typically four columns on a semi-submersible. Hydrocarbon liquids may be stored in only two of the four columns, thereby providing a safe-zone where the living quarters are located (see
A semi-submersible vessel according to the invention can be operated at a near-constant draft with minimal CG shift—both horizontally and vertically—and with simple and clear ballast activities. Such a semi-submersible vessel may remain at all times in a storm-ready/hurricane-ready condition.
The present invention may best be understood by reference to the exemplary embodiments shown in the drawing figures. The following reference numbers are used in the drawing figures to denote the listed elements of the invention:
Referring first to
Columns 2 within hydrocarbon storage zone 7 may contain both hydrocarbon storage vessels (hereinafter “cargo tanks” or “cargo bottles”) and variable water ballast tanks. In the embodiment illustrated in
Ballast tank 21 may contain a variable quantity of water ballast 20 which may be added via fill line 9′.
In the embodiment illustrated in
It should be appreciated that, in the embodiment illustrated in
A second exemplary embodiment of the invention is illustrated in
A third exemplary embodiment of the invention is illustrated in
A fourth exemplary embodiment of the invention is illustrated in
A fifth exemplary embodiment of the invention is illustrated in
A sixth exemplary embodiment of the invention is illustrated in
A seventh exemplary embodiment of the invention is illustrated in
In certain embodiments, the minimum clearance between the cargo tank(s) and the semi-submersible exterior hull may be 5 feet. This may provide a similar configuration as found in a “double hull tanker” layout.
The cargo tank and variable ballast tank may be operated in such a manner that the weight of their combined fluids remains within acceptable bounds, or ideally near constant. The cargo tank(s) and the ballast tank(s) may be sized such that their total volume(s) are such that they may hold substantially the same mass of hydrocarbon product and ballast water.
The hydrocarbon storage on a semi-submersible can be an enabling technology. It enables production by semi-submersible from offshore fields that predominantly contain gas but also contain a commercially reasonable amount of hydrocarbon liquids (condensate). Storage of such liquids aboard the vessel obviates the need for an extra pipeline or sending the condensate through the gas export pipeline.
An aspect of the invention is the layout of the cargo and variable ballast tanks which minimizes the shift of the vertical center of gravity and horizontal center of gravity as hydrocarbon product is loaded and unloaded. This reduces the complexity of ballast operations while storing the produced hydrocarbons. This is in contrast to configurations wherein the cargo tank is located above the variable ballast tank which results in a greater range of the vertical center of gravity of the combined cargo and ballast.
In a semi-submersible vessel according to the invention, both the cargo tank(s) and the variable ballast tank(s) may be accessible from top-of-column. One of the advantages of such a configuration is that there is no need to have cargo lines run through other hull compartments. This enhances the safety of the design. A second advantage is that ballast or cargo pumps may be lowered directly into the tanks; all pumps can be serviced from top-of-column; and, there is no need for personnel to enter a hull compartment that contains hydrocarbons.
Locating the cargo tank inside the variable ballast tank results in additional safety in the event the cargo tank is damaged—the cargo will be contained in the variable ballast tank and will not enter into any of the other hull compartments.
The cargo bottle configuration illustrated in
A “double hull” configuration requirement can be met when the cargo tanks are at least 5 feet from the outside hull shell.
The foregoing presents particular embodiments of a system embodying the principles of the invention. Those skilled in the art will be able to devise alternatives and variations which, even if not explicitly disclosed herein, embody those principles and are thus within the scope of the invention. Although particular embodiments of the present invention have been shown and described, they are not intended to limit what this patent covers. One skilled in the art will understand that various changes and modifications may be made without departing from the scope of the present invention as literally and equivalently covered by the following claims.
This application claims the benefit of U.S. Provisional Application No. 62/103,738, filed on Jan. 15, 2015, the contents of which are hereby incorporated by reference in their entirety.
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Number | Date | Country | |
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Number | Date | Country | |
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62103738 | Jan 2015 | US |