COMPACT DUAL HEADER MANIFOLD LAYOUT

20240026757 ยท 2024-01-25

    Inventors

    Cpc classification

    International classification

    Abstract

    A dual header oil and gas industry hydrocarbon production manifold. A plurality of three-way directional valves separate fluid flow between a well side of manifold and a pipeline side of the manifold. Two headers include header bodies and header flow paths and a pipeline side couplings. Each of two elbow pipes, provide a flow path between one of the headers, and a port on one of the plurality of three-way valves. At least one T-pipe, provides a flow path between one of the headers, and a port on two of the plurality of three-way valves. A manifold body or any of its main parts may be hipped. A layout with such a manifold is also disclosed.

    Claims

    1. A dual header oil and gas industry hydrocarbon production manifold comprising: a plurality of three-way directional valves with three fluid ports adapted to separate fluid flow between a well side of manifold and a pipeline side of the manifold; a first header with a first header body and a first header flow path and a first pipeline side coupling; a second header with a second header body and a second header flow path and a second pipeline side coupling; at least two elbow pipes, each providing a flow path between one of the first header and the second header, and a port on one of the plurality of three-way valves; at least one T-pipe, providing a flow path between one of the first header and the second header, and a port on two of the plurality of three-way valves; and a well side coupling on each of the plurality of three-way valves.

    2. The dual header oil and gas industry hydrocarbon production manifold of claim 1, wherein the first header body and the second header body are Hot Isostatically Pressed (hipped) elements.

    3. The dual header oil and gas industry hydrocarbon production manifold of claim 2, wherein the least two elbow pipes are integrated in at least one of the first header body and the second header body as Hot Isostatically Pressed (hipped) elements.

    4. The dual header oil and gas industry hydrocarbon production manifold of claim 2, wherein the at least one T-pipe, is integrated in at least one of the first header body and the second header body as Hot Isostatically Pressed (hipped) elements.

    5. The dual header oil and gas industry hydrocarbon production manifold of claim 2, wherein the at least one T-pipe, the least two elbow pipes and valve bodies of the plurality of three-way directional valves are integrated in the first header body and the second header body as one Hot Isostatically Pressed (hipped) manifold body.

    6. The dual header oil and gas industry hydrocarbon production manifold of claim 1, wherein the first and the second header includes a sealed end.

    7. The dual header oil and gas industry hydrocarbon production manifold of claim 1, wherein the first and the second header includes a second pipeline side coupling.

    8. The dual header oil and gas industry hydrocarbon production manifold of claim 1, wherein the hydrocarbon production manifold is made of a Super-duplex material.

    9. A hydrocarbon conveying pipeline layout allowing round trip pigging including a first and a second dual header oil and gas industry hydrocarbon manifold of claim 1; wherein a first branch pipe connected to the first dual header manifold is branched off from a dual ILT, connecting the first dual header manifold to a first pipeline; wherein a second branch pipe connected to the first dual header manifold is branched off from the dual ILT, connecting the first dual header manifold to the second pipeline; wherein a first branch pipe connected to the second dual header manifold is branched off from a first ILT, connecting the second dual header manifold to the first pipeline; and wherein a second branch pipe of the second dual header manifold is branched off from a second ILT, connecting the second dual header manifold to the second pipeline.

    10. A use of hot isostatic pressing to manufacture an oil and gas industry hydrocarbon production manifold of claim 1.

    Description

    BRIEF DESCRIPTION OF DRAWINGS

    [0028] FIG. 1 is a perspective view of a compact manifold of the invention;

    [0029] FIG. 2 is a top view of the manifold of FIG. 1;

    [0030] FIG. 3 is a side view of the manifold of FIG. 1; and

    [0031] FIG. 4 is a schematic representation of the hipped, hydrocarbon production manifold of the invention installed in an oil and gas industry pipeline configuration.

    DETAILED DESCRIPTION

    [0032] Similar reference numerals refer to similar parts throughout this detailed description.

    [0033] The manifold can be used both in an injection manifold and a production manifold. In a production manifold, will the branch port be an inlet port, and the produced fluid will exit through a header port. In an injection manifold, will however, the branch port be an exit port. The manifold is formed with a HIP'ed (hot isostatic pressing) valve body, pipes and fittings, and two-way directional valves.

    [0034] The flow described in connection with the manifolds 1, 2 and 3 assumes that wells are producing fluid and that the flow direction is from wells and out of the pipelines.

    [0035] FIG. 1, shows a compact, hipped hydrocarbon production manifold 1 with two headers with header bodies 22, 23 and header flow paths 25, 26 forming a first header 9, and a second header 10, thus forming a dual header compact production manifold. The first header 9 has a first connecting portion 6 with a male hub for attachment of a metal seal to allow full pressure and structural integrity once connected to a subsea branch pipe to a pipeline or directly to a pipeline. The hub connecting portions may include threads or flanges, typically API flanges. The hubs may include a means for attachment to a clamp connector. All parts of the manifold are formed by HIP'ed material, where any sensor or injection points integrated into the HIP'ed parts.

    [0036] Couplings 6, 7, 8 may include flanges or hubs typically connected with a clamp connector. Each jumper coupling is typically connected to a x-mas tree through a jumper. Alternatively, could the valves include independent or common, permanently installed powered actuators.

    [0037] Four three-way valves 2, 4 are in line with each other in a row (a three-way valve is a valve with three ports). Each valve incudes a valve body 24 and a third port forming a jumper port 11 with a well side coupling 8 such as a jumper coupling in the form of a hub or a flange, and a tool bucket 3, to control the flow between a jumper (the well side of the manifold) and the two headers 9, 10 (on the pipeline side of the manifold). The valves form the border between the well side of the manifold and the pipeline side of the manifold. A first port is connected to a flow path to the first header 9 and a second port connected to a flow path to the second header 10. The three ports are located in a T-configuration where two ports have a common central axis. In-line in this context indicate that this common central axis is common for all the valves. The four in-line three-way valves 2, 4 are connected with three T-pipes 13, whereof two T-pipes are connected to the first header 9, and one T-pipe is connected to the second header 10. Two elbow pipes 12 connect the valves 4 at the ends of the row with the second header 10. The above configuration with the T-pipes enables each valve 2, 4 to selectively allow flow between a jumper and either of the two headers 9, 10 or to stop the flow completely. The configuration also allow flow through a first valve, through a second valve and then into a header. The headers 9, 10 are parallel to each other, have branch pipe couplings 6, 7 such as hubs or flanges facing in opposite directions and are sealed at one end. The manifold includes a complete manifold body 27.

    [0038] FIG. 2 shows the manifold 1 of FIG. 1 from above with the four valves 2 including the four valve bodies 24 to clearly show the compact design with the parallel headers 9, 10 in close proximity to each other and the alternating directions of the well side couplings 8. Each inclined T-pipe 13 form a flow path between two valves 2 and a header 9, 10. Each of the two inclined elbow pipes 12 form a flow path between one valve 2 and a header 9, 10.

    [0039] FIG. 3 shows the manifold 1 of FIG. 1 from the side to clearly show the compact design with the parallel headers in close proximity to each other and an upside-down V-configuration of the T-pipes 13 and the elbow pipes 12. The upside-down V-configuration allows the valves 2 to be located above the headers to thus form a narrow design with the valves on top for easy access from an ROV and easy access to the well side couplings 8.

    [0040] The tool connector/torque tool bucket 3 on each valve includes a connection for a tool on an ROV to actuate each valve through a valve mechanism 5 independently. The valves are typically gate valves.

    [0041] The alternate positioning of the well side coupling 8 facing in opposite directions and away from each other provide improved room for the couplings.

    [0042] The valves 2, 4 are included to enable isolation of each hydrocarbon well connected to the manifold individually.

    [0043] The headers typically have an internal diameter in the range from 8-16 (203.2 mm-406.4 mm) and the transversal duct/branch holes have an internal diameter in the range from 5-8 (127.0 mm-203.2 mm). The header main duct typically has a diameter corresponding to the inner diameter of a flowline to be connected to the manifold to allow pigging.

    [0044] Clearly, the manifold may include two, three, five or more valves.

    [0045] FIG. 4 is a schematic representation of a pipeline configuration with a manifold of the present invention. A pipeline in this context is primarily an export pipeline, but such a pipeline may also be used for well injection purposes. The term pipeline is however intended to exclude elements such as jumpers between a well and the manifold on a well side of the manifold valves. A first pipeline 18 from a remote location (typically a facility receiving hydrocarbon fluids) is interrupted by a first In-line Tee (ILT) 16a and terminates in a connecting arrangement with a cut off valve in a dual In-line Tee (ILT) 17. A second pipeline 19 from the remote location is interrupted by a second In-line Tee (ILT) 16b and terminates in the dual In-line Tee (ILT) 17. The dual ILT 17 includes two ports for connection to branch pipes 21a, 21b from a first dual header manifold 1a. The first and second pipeline are permanently welded to the Dual ILT 17.

    [0046] Each of two manifolds 1a, 1b of the invention are connected to four wells 14 with jumpers 15. The well side couplings 8 for the jumpers 15 and the branch pipe couplings 6, 7 for the branch pipes 21a, 21b, 21c, 21d typically include hubs and clamp connectors. Clearly, the number of wells connected to each manifold 1 can depart from four. The pipeline configuration can be used with only one or more than two manifolds 1a, 1b.

    [0047] The jumpers 15 connect each well 14 with a manifold 1a, 1b through wellheads. Flow paths are provided by branch pipes 21a, 21b, 21c, 21d between ILT's 16a, 16b, 17 and the manifolds 1a, 1b.

    [0048] The dual ILT 17 is a full bore ILT allowing a pig to pass from the first pipeline 18 to the second pipeline 19 when the cut-off valve 20 in the dual ILT 17 is open. The first ILT 16 and the second ILT 16 are also full bore ILTs allowing a pig to pass. The ports to the branch pipes and the branch pipes do however not need to be full fore as the pig is not circulated through the branch pipes or the manifolds.

    [0049] Accordingly, a pig can be circulated through the pipeline 18, past the first ILT 16a further through the first pipeline 18, through the dual ILT 17 into the second pipeline 19, through the second ILT 16b and further through the second pipeline 19. The first and the second ILTs 16a, 16b also include cut-off valves to cut the flow of fluids between the pipelines 18, 19 and the branch pipes 21c, 21d while maintaining the flow through the pipelines 18, 19.

    [0050] The pig will not be circulated through any of the manifolds 1a, 1b, and each manifold will only handle fluids from the wells that specific manifold is connected to.

    [0051] During normal operation (not pigging), the valve connecting the first pipeline 18 and the second pipeline 19 in the dual ILT 17 is closed, isolating first pipeline 18 from the second pipeline 19.