This application is a U.S. National Phase application under 35 U.S.C. § 371 of International Application No. PCT/NO2019/050107, filed on May 13, 2019 and which claims benefit to Norwegian Patent Application No. 20180680, filed on May 14, 2018. The International Application was published in English on Nov. 21, 2019 as WO 2019/221608 A1 under PCT Article 21(2).
The present invention relates to a process system and to a method of operating a process system, such as a process system for handling fluids in petroleum production plants.
Subsea and topside offshore production and processing systems are continually being developed, in part due to the petroleum industry moving to exploit more remote fields where locating equipment subsea or on a minimum-manned platform is the most cost-efficient or otherwise desirable option. This provides a number of challenges since such equipment may not be readily accessible for maintenance or repairs, or because no permanent operators are on site to perform such maintenance or repairs. There are consequently demanding requirements on such equipment for high reliability and long service life, and operational procedures seek to ensure that the equipment is operated in the most optimal manner to avoid unexpected disturbances or, for example, a need to retrieve equipment for maintenance or repairs.
Drainage of equipment (such as compressors) and piping in process systems (such as a compression station) is often required prior to start-up or after shut-down. This is usually performed either by gravity or by pumps, whereby liquids in the equipment units drains by gravity to a lower location or is pumped out of the equipment.
Publications which may be useful to understand the background of the present invention include WO 2013/026776, WO 2010/102905, WO 2013/062419, EP 2 799 716, WO 2011/008103, NO 341495, and WO 2016/028158.
An aspect of the present invention is to provide further improved systems and methods in this area, or at least alternatives to known technology.
In an embodiment, the present invention provides a process system which includes a process module, an upstream pipe, a downstream pipe, an inlet pipe comprising an inlet isolation valve, an outlet pipe comprising a discharge isolation valve, a bypass comprising a bypass isolation valve, and a drainage line comprising a valve. The process module comprises an inlet, an outlet, and a drainage outlet. The inlet pipe fluidically connects the inlet of the process module to the upstream pipe. The outlet pipe fluidically connects the outlet of the process module to the downstream pipe. The bypass fluidly connects the upstream pipe and the downstream pipe via the bypass isolation valve. The drainage line fluidly connects the drainage outlet of the process module to the downstream pipe via the valve.
The present invention is described in greater detail below on the basis of embodiments and of the drawings in which:
The present invention provides a process system comprising a process module, wherein an inlet of the process module is fluidly connected to an upstream pipe via an inlet pipe having an inlet isolation valve, and wherein an outlet of the process module is fluidly connected to a downstream pipe via an outlet pipe having a discharge isolation valve. The process system comprises a bypass fluidly connecting the upstream pipe and the downstream pipe via a bypass isolation valve, and a drainage line fluidly connecting a drainage outlet of the process module to the downstream pipe via a valve.
These and other characteristics of the present invention will become clear from the following description of illustrative embodiments, which are provided as non-restrictive examples, under reference to the attached drawings.
The process system 100 may be a subsea process system or a topside process system. A topside process system according to embodiments of the present invention may, for example, be suitable for so-called minimum-manned or unmanned platforms. The process system 100 may be remotely operated.
The process module 101 may, for example, be a gas compressor, fluid processing assemblies, vessels, distribution manifolds, or another process system component which may require draining.
The process system 100 is connected to a production pipeline 102,103 which may, for example, carry a flow of multiphase fluids. An upstream part 102 of the production pipeline is connected to an inlet 105 of the process module 101 via an inlet pipe 104. An inlet isolation valve is operable to selectively close the inlet pipe 104 between the upstream part 102 and the inlet 105.
An outlet pipe 107 is arranged between an outlet 106 of the process module 101 and a downstream part 103 of the production pipeline. A discharge isolation valve V-3 is arranged in the outlet pipe 107 and is operable to selectively close the outlet pipe 107 between the outlet 106 and the downstream part 103. In operation, process fluids flowing through the upstream part 102 may be led to the inlet 105, flow through the process module 101 for processing (e.g., pressure boosting), and flow via the outlet 106 to the downstream part 103 and to, for example, a storage or another plant for further processing of the fluids.
A bypass 108 connects the upstream part 102 and the downstream part 103. The bypass 108 comprises a bypass isolation valve V-1, arranged downstream of the inlet pipe 104 and upstream of the outlet pipe 107. When the bypass isolation valve V-1 is open, fluids may flow directly from the upstream part 102 to the downstream part 103 without entering the process module 101. This is the situation illustrated in
The process module 101 has a drainage outlet 110. The drainage outlet 110 is arranged to drain accumulated liquids from the process module 101, and may be connected to, for example, a drainage sump within the process module 101. A drainage line 111 leads from the drainage outlet 110 and is fluidly connected to the upstream part 102 via a drain-to-inlet valve V-5. In this embodiment, the drainage line 111 is connected to the inlet pipe 104 upstream of the inlet isolation valve V-2, however, the drainage line 111 may also be connected directly to the upstream part 102 or to the bypass upstream via the bypass isolation valve V-1.
The drainage line 111 is also fluidly connected to the downstream part 103 via a drain-to-discharge valve V-6. In this embodiment, the drainage line 111 is connected to the outlet pipe 107 downstream of the discharge isolation valve V-3, however, the drainage line 111 may also be connected directly to the downstream part 103 or to the bypass downstream of the bypass isolation valve V-1.
In this embodiment, the drainage line 111 is T-shaped, as can be seen in
Certain embodiments, including that shown in
In
It may, for example, be that the process module 101 has recently been shut down or is about to be started up, and that a draining of liquids from the process module 101 is required.
Inlet isolation valve V-2 is open so as to pressurize the process module 101 with fluid from the upstream part 102 via the inlet 105. This fluid may be predominantly gas. The system drain valve V-4 and the drain-to-discharge valve V-6 are open. Due to the pressure differential, liquids in the process module 101 drain via the drainage line 111 to the downstream part 103 downstream of the flow restriction element DP-1, and drained liquid is removed. The arrangement according to this embodiment consequently achieves a flow pressure drop assisted draining of the process module 101.
In this scenario, the process system is shut down as in
According to embodiments described herein, draining of process modules can be carried out without the aid from a pump or gravitational requirements, or to assist a pump or gravitational drainage system so as to obtain, for example, increased reliability or reduced design requirements for such pump or gravitational systems. Significant savings in weight and cost of the overall process system 100 can, for example, be provided by relaxing elevation requirements or drainage pump requirements.
All operational methods may comprise first establishing that a pressure in one part of the system is higher than in another part of the system before carrying out the steps for draining the process module 101. For example, in the embodiment described in relation to
In any of the embodiments, the fluid provided to the inlet 105 may be a substantially pure gas, a wet gas, or a multiphase fluid comprising liquids and gas. The fluid drained through drainage outlet 110 will normally be predominantly a liquid, but can be a liquid with gas fractions and/or a multiphase fluid. The fluid provided to the inlet 105 for driving the drainage process may be obtained from the production pipeline 102,103 in various ways, depending on the circumstances and operational conditions. If the production pipeline 102,103 handles mainly gas, a gas or gas-rich fluid for this purpose can be retrieved directly from the production pipeline 102,103. If the production pipeline 102,103 handles multiphase fluids, a gas or a gas-rich fluid may be obtained, e.g., by elevated placement of the take-off point in the production pipeline 102,103. If necessary, a separator unit may be arranged in relation to this fluid to provide a high gas fraction of the fluid used for draining.
If the process system 100 and/or the process module 101 is being prepared for a period of non-use (for example, for maintenance or where the module 101 or system 100 is periodically not required to operate), the fluid provided may alternatively be an inert gas, such as nitrogen. The inert gas may be provided via the upstream part 102 or the downstream part 103. Purging or flushing of the process module 101 may thereby be carried out with an inert gas suppled from a downstream side of the production pipeline 102,103 (compare
The different operational configurations and the elements described in relation to
Number | Date | Country | Kind |
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20180680 | May 2018 | NO | national |
Filing Document | Filing Date | Country | Kind |
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PCT/NO2019/050107 | 5/13/2019 | WO |
Publishing Document | Publishing Date | Country | Kind |
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WO2019/221608 | 11/21/2019 | WO | A |
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Number | Date | Country | |
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20210116075 A1 | Apr 2021 | US |