US20100059221A1 - Subsea fluid sampling and analysis - Google Patents
Subsea fluid sampling and analysis Download PDFInfo
- Publication number
- US20100059221A1 US20100059221A1 US12/477,190 US47719009A US2010059221A1 US 20100059221 A1 US20100059221 A1 US 20100059221A1 US 47719009 A US47719009 A US 47719009A US 2010059221 A1 US2010059221 A1 US 2010059221A1
- Authority
- US
- United States
- Prior art keywords
- fluid
- subsea
- flowline
- sample
- sampling
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B49/00—Testing the nature of borehole walls; Formation testing; Methods or apparatus for obtaining samples of soil or well fluids, specially adapted to earth drilling or wells
- E21B49/08—Obtaining fluid samples or testing fluids, in boreholes or wells
- E21B49/081—Obtaining fluid samples or testing fluids, in boreholes or wells with down-hole means for trapping a fluid sample
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B33/00—Sealing or packing boreholes or wells
- E21B33/02—Surface sealing or packing
- E21B33/03—Well heads; Setting-up thereof
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
- E21B41/04—Manipulators for underwater operations, e.g. temporarily connected to well heads
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B49/00—Testing the nature of borehole walls; Formation testing; Methods or apparatus for obtaining samples of soil or well fluids, specially adapted to earth drilling or wells
- E21B49/08—Obtaining fluid samples or testing fluids, in boreholes or wells
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B49/00—Testing the nature of borehole walls; Formation testing; Methods or apparatus for obtaining samples of soil or well fluids, specially adapted to earth drilling or wells
- E21B49/08—Obtaining fluid samples or testing fluids, in boreholes or wells
- E21B49/086—Withdrawing samples at the surface
Definitions
- This invention relates to subsea apparatus for fluid sampling and/or analysis.
- the invention relates to a subsea apparatus for fluid sampling and/or analysis used in the oil and gas industry.
- Fluid sampling and/or analysis may be performed during various phases of the exploration, development and production phases of a reservoir.
- Conventional tools are able to take a fluid sample from the well and bring it to surface where it is processed and analysed. For example, often times the phase behavior of the fluid may be studied using an analysis known in the industry as PVT analysis which measures, inter alia, the bubble point of the fluid as well as its wax, and asphaltene content.
- PVT analysis measures, inter alia, the bubble point of the fluid as well as its wax, and asphaltene content.
- compositional analysis of the fluid sample may be performed as well as analysis of its H 2S , CO 2 , Hg, and heavy metal content.
- well known are tools and methods for measuring the density and viscosity of the fluid its, water content, etc.
- U.S. Pat. No. 6,435,279 discloses a method and apparatus for sampling fluids from an undersea wellbore utilizing a self-propelled underwater vehicle, and a collection and storage device.
- the '279 patent describes a method for sampling a fluid produced from a subsea well, the method comprising a remotely operated vehicle (ROV) having a collecting device for collecting a sample of fluid and a storage facility for the collected sample of fluid wherein said collecting device and storage facility are connected to the ROV.
- the collecting device is used to collect a sample from a subsea location, storing the sample in the ROV and then transferring it to a surface location.
- ROV remotely operated vehicle
- WO 2008/087156 disclose various systems and methods for subsea sampling.
- the WO 2008/087156 patent application describes a subsea sampling and data collection device that is coupled to a flowline at a flowline installation.
- the WO 2008/087156 sampling and data collection device includes a sample collection system having a probe insertable into a flowline to collect a fluid sample.
- the WO 2008/087156 application is assigned to the same assignee as the present invention and it is hereby incorporated by reference for all purposes allowable under the law to the extent that its disclosure does not contradict with the present invention.
- the present invention provides an improved apparatus and associated method that facilitate the sampling and the characterization of the fluids at a subsea environment, and as close as possible to each well head.
- the present invention and method also enable analysis of sampled fluid to occur on a real time basis and thus obtain accurate real time analysis data for well performance and management.
- a first aspect of this invention provides subsea apparatus for sampling and analysing fluid from a subsea fluid flowline proximate a subsea well, comprising:
- the fluid analysis data can be real time data, and this real time data is communicated to at least one electronic device which incorporates at least one software model used to provide information regarding the production of said subsea well.
- the software model may also used to provide predictions regarding the production of the well.
- the fluid analysis data is used to control at least one piece of subsea equipment.
- the fluid processing apparatus separates the sample of fluid into at least a liquid and a gaseous phase, or mixes the sample of fluid with at least one other different fluid, or enriches the sample of fluid.
- the fluid sampling device is in communication with the well fluid.
- the fluid sampling device may also be in communication with a fluid processing apparatus, the fluid processing apparatus being in communication with the well fluid.
- At least one data processing device may be locatable in the housing and may be in communication with the fluid analysing device.
- the data processing device processes data received from the fluid analysis device and communicates the data.
- the conveying means may be an attachment for a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV).
- a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV).
- ROV remotely operated vehicle
- AUV autonomous underwater vehicle
- the subsea apparatus may further comprise a plurality of housings which are connectable to each other in a modular fashion.
- the fluid analysis device of each housing may be in fluid communication with the fluid analysis device of another connected housing.
- the fluid sampling device of each housing may be in fluid communication with the fluid sampling device of another fluid sampling device of a connected housing
- the data processing device of each housing may be in fluid communication with the data processing device of a connected housing.
- a second aspect of this invention provides a method of sampling and analysing fluid from a subsea well, the method comprising:
- the fluid sampling device is in fluid communication with a fluid processing apparatus, the fluid processing apparatus being in fluid communication with the well fluid flowing in the subsea flowline and the sample of fluid is obtained from the well fluid in the subsea flowline via the fluid processing apparatus.
- the fluid sampling device may also be in communication with a fluid processing apparatus that is in communication with the well fluid.
- At least one data processing device may be locatable in the housing and may be in fluid communication with the fluid analysis device, and which further comprises processing fluid analysis data received from the fluid analysis device by means of the data processing device and communicating the processed data to another apparatus or to the surface.
- the method may further include processing fluid data received from the fluid analysis device and communicating the data.
- the method may also comprise deploying one or more housings of the apparatus by means of a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV), the housings being connectable to each other.
- a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV)
- ROV remotely operated vehicle
- AUV autonomous underwater vehicle
- each fluid analysis device of each housing is in fluid communication with each other
- each fluid sampling device of each housing is in fluid communication with each other.
- FIG. 1 shows a schematic side view of a subsea apparatus for sampling and/or analysing fluid from a well according to one embodiment of the invention
- FIGS. 2 shows a schematic side view of a housing of the subsea apparatus for sampling and analysing fluid from a well as shown in FIG. 1 , attached to a remotely operated vehicle (ROV);
- ROV remotely operated vehicle
- FIG. 3 shows a schematic side view of the subsea apparatus for sampling and/or analysing fluid attached to a fluid processing device indicating the flow direction through the components of the fluid processing device;
- FIG. 4 shows a diagrammatic view of a hydraulic sampling device of the subsea apparatus for sampling and/or analysing fluid from a well according to one embodiment of the invention
- FIG. 5 a shows a diagrammatic view of a passive sampling device of the subsea apparatus for sampling and/or analysing fluid from a well according to another embodiment of the invention
- FIG. 5 b shows a diagrammatic view of a passive sampling device of the subsea apparatus for sampling and/or analysing fluid from a well which uses venturi according to another embodiment of the invention
- FIG. 6 shows a diagrammatic view of an active sampling device of the subsea apparatus for sampling and/or analysing fluid flow which uses a pump according to a further embodiment of the invention
- FIGS. 7 a , 7 b and 7 c show a series of diagrammatic views of an adjustable inlet of a sampling device according to an embodiment of the invention
- FIG. 8 shows a schematic layout of a fluid analyser of the subsea apparatus for analysing fluid from a well
- FIG. 9 shows a schematic side view of a section of an in-line fluid analyser of the subsea apparatus for sampling and analysing fluid from a well according to one embodiment of the invention.
- FIG. 10 shows a schematic side view of a section of an in-line fluid analyser of the subsea apparatus for sampling and analysing fluid from a well which includes a phase behaviour fluid analyser according to another embodiment of the invention
- FIGS. 11 , 11 a , 11 b and 11 c show schematic side view of a sampling bottle for low shock sampling with a piston inside the bottle of the subsea apparatus according to one embodiment of the invention
- FIGS. 12 , 12 a , 12 b and 12 c show schematic side view of a sampling bottle for low shock sampling without a piston inside the bottle of the subsea apparatus according to one embodiment of the invention
- FIG. 13 shows schematic view of a self retrievable sampling bottle apparatus of the subsea apparatus according to one embodiment of the invention.
- FIG. 14 shows a schematic overview of a controller configuration used for the control of a number of subsea apparatuses according to one embodiment of the invention.
- FIG. 1 illustrates the basic layout of a subsea apparatus 10 for sampling and/or analysing fluid from a well according to the invention.
- Subsea apparatus 10 is located in close proximity to the wellhead of a well and includes a subsea fluid processing device 12 for processing fluid samples obtained from the well.
- the subsea processing device 12 can be a phase separator, a phase accumulator, a boosting pump, a water treatment unit, chemical injector or an injection pump, depending on the application required.
- the subsea processing device 12 includes a fluid sampling device 14 .
- the fluid sampling device 14 consists of a network of pipes connected to different sampling points in the processing device 12 .
- the fluid sampling device 14 can also include a distributor that can redirect the sampled fluid to different outlet.
- Subsea apparatus 10 further includes a remote operating device (ROV) docking station 16 which allows the docking and attachment of a remote operating device (ROV) 18 to the subsea processing device 12 .
- ROV remote operating device
- FIG. 1 there is a fluid interface 20 in communication with the sampling device 14 which is located below the ROV docking station 16 .
- the fluid interface 20 allows a hydraulic connection between the ROV 18 and the processing device 12 , and thus fluid at well pressure can travel between them. This hydraulic connection can be initiated when the ROV 18 is docked at the docking station and it can be disconnected when the ROV 18 is removed.
- a frame or skid 22 could also be docked to the docking station with the help of an ROV 18 .
- the skid 22 is attached to the ROV 18 with several instrumentation modules connected thereto. This will be further described below.
- Skid 22 can be docked to the docking station 16 as the ROV 18 approaches the installation.
- the skid 22 can then be detached from the ROV 18 through a specific skid/ROV interface 24 and it can then be left permanently on the installation of apparatus 10 .
- the skid/ROV interface 24 may be a fluid interface and skid 22 is in communication with the fluid interface 20 .
- the well fluid can be directed to the instrumentation module 26 which is located on the skid 22 .
- Skid 22 is designed so that other skids 22 of a similar type can be connected to it.
- the design is modular so that the skids 22 can be configured and assembled in different orders, and then used for different purposes.
- Skid 22 can also be deployed using an autonomous under water vehicle AUV.
- the skid interface 24 may include instrumentation for the positioning of the AUV during docking.
- Instrumentation module 26 is located inside skid 22 and is connected to a controller/communication module 28 .
- Instrumentation module 26 contains the fluid analyzer and it is used to perform fluid analysis and/or fluid sampling. It is connected to the fluid interface 20 and it can receive the fluid collected by the fluid sampling device 14 .
- the type of analysis and the sampling sequence is managed by the controller/communication module 28 .
- the controller/communication module 28 performs control either through a pre-defined sequence stored in the controller, from the surface with the use of a communication link, or in a completely automated mode with the use of the fluid analysis data obtained by the fluid analyzer in instrumentation module 26 . It is used to enable decisions to be made on how to process the sample of fluid.
- the fluid analyzer in instrumentation module 26 consists in a network of pipe connected to pumps, fluid properties sensors, sample chambers, fluid conditioners and injectors. This system is managed through the controller/communication module 28 .
- the fluid analysis data obtained by apparatus 10 is used to control various types of subsea or surface equipment.
- This fluid analysis data is based on real time sample measurements obtained from the fluid sample that is obtained and also possibly analyzed at wellhead conditions.
- This real time fluid data may be communicated to an electronic device which incorporates at least one software model and this model may be used to provide information regarding the production of the well and to provide predictions regarding the production of the well. Thus information regarding reservoir assurance, or flow assurance management may be obtained through the processing of this fluid data.
- FIG. 3 illustrates an embodiment of the subsea apparatus for sampling and/or analysing fluid from a well according to the invention, which further includes a phase separator 30 .
- the phase separator 30 which may be used is one of the typical examples of phase separators known in the art.
- a typical phase separator consists of a pressure vessel 32 with an internal pipe drilled with radial holes.
- the pressure vessel 32 includes a fluid inlet 34 and fluid outlet 36 .
- the direction of fluid flow is shown by arrows A in FIG. 3 .
- the phase generator 30 was initially designed in the art as a device for fluid mixing purposes but it can also be used as a fluid separator.
- the fluid segregates depending on its density, with gas separating out on top and the liquid (oil and water) separating out at the bottom.
- the phases are remixed, leading to a mixed fluid flow leaving at the outlet.
- Phase generator 30 allows liquid can be sampled at the bottom of the vessel while gas can be sampled at the top.
- FIG. 3 further shows a retrievable ROV 18 with a skip 22 including a fluid sampling or analysis module 26 to be used for fluid sampling, as well as a skip 22 including a fluid sampling or analysis module 26 to be used for fluid analysis, and then a multi-phase flow meter 38 .
- the hydraulic sampling device of apparatus 10 is illustrated in FIGS. 5 and 6 .
- Fluid sampling can be done either through a passive or an active sampler.
- the fluid sampling or analysis module 26 has internal piping connecting the liquid sampling pipe 44 to the gas sampling pipe 46 . It further includes an inlet pipe 40 to sample the fluid from the separator to the fluid analyzer in module 26 and an outlet pipe 42 to re-inject the fluid to the separator or main fluid flow line after it has been analyzed.
- the direction of fluid flow is shown in FIGS. 5 a , 5 b and 6 by arrows B.
- Passive sampling devices 26 do not require any pump to sample the fluid as these devices are based on passive mechanisms.
- FIGS. 5 a and 5 b Two different possible implementations of passive sampling devices are shown in FIGS. 5 a and 5 b .
- the fluid movement inside the sampling tubes is generated using a venturi device 48 .
- the outlet pipe 42 is connected to venturi device 48 which is located further down the fluid flow line.
- the venturi device 48 generates a pressure difference that drives the fluid through the piping system and the fluid sampling or analysis module 26 or from the inlet to the outlet.
- FIG. 6 describes an active sampler using a pump 52 to generate the fluid flow from the inlet to the outlet.
- inlet pipes 40 . 1 and 40 . 2 with different heights as is illustrated in FIG. 7 a . If required, the flow from these sampling pipes could be directed to a manifold before being routed to the fluid sampling or analysis module 26 .
- FIG. 7 b Another possibility which is described in FIG. 7 b is to have a sampling pipe with an adjustable height that is adjustable with the use of mechanical actuators 56 .
- the height H may then be adjusted according to what is required. With time, the ratio between the different phases of fluid produced by the well changes. With such an adjustable sampling inlet, it is thus possible to adapt the sampling device to the changes in production conditions.
- FIG. 7 c describes an adjustable fluid sampling or analyzing module 26 which uses a series of controllable valves 57 and 58 connected thereto to change the sampling point position.
- the valves 57 and 58 can be selectively closed. In the normal operation, all valves 58 are closed except for the valve 57 which is at the level of the sampling point.
- the fluid flow is illustrated in FIG. 7 by arrows E.
- this skid 22 includes the fluid interface 20 , power/communication module 28 , skid or ROV interface 24 , a local controller module and a fluid sampling or analysis module 26 .
- the local controller module controls the working of the sampling or fluid analysis module 26 .
- Apparatus 10 may be provided in different kinds of modules. Fluid, communication and skid or ROV interfaces are designed to be fully interoperable so that different kinds of modules of apparatus 10 can be interconnected and configured in many different types of configurations.
- modules of apparatus 10 including skids 22 may be installed either on a temporary basis or on a semi-permanent basis.
- skids 22 are fully engaged in an ROV 18 and connected to the various fluid interfaces.
- An individual module of apparatus 10 comprising a skid 22 and its attached equipment can be retrieved as required by an ROV 18 .
- the fluid sampling or analyzing device 26 which is mounted in a skid 22 in apparatus 10 is shown in more detail in FIG. 8 .
- the device 26 is enclosed in a tool housing 59 and it includes fluid flow lines 60 connected together and guiding the fluid from an inlet to an outlet.
- the device 26 further includes pumps 62 which can move the fluid there through.
- Fluid conditioners 64 which are used to process the fluid and change properties such as the ratio between the different fluid phases, or the fluid pressure, volume or temperature are also included in device 26 .
- Fluid processing devices 12 may further include a separator, a mixer, and a PVT (pressure, volume and temperature) device.
- injectors 66 can be used to inject fluids which are different from the fluid which is flowing in a particular flow line 60 .
- the injected fluid can be used to generate an inhibitory chemical reaction with the sampled fluid or it can change the phase behavior of the fluid.
- Sample bottles or chambers 68 in device 26 are used to take and store samples of the fluid inside a flow line 60 .
- Fluid property sensors 70 are also shown located on flow lines 60 in device 26 .
- FIG. 9 illustrates an embodiment of the fluid sampling or analysis device 26 of apparatus 10 to be used for fluid analysis with one possible configuration of sensors 70 .
- device 26 is in-line with the sampling piping.
- sensors 70 are shown in the in-line configuration in a fluid flow line 60 .
- These sensors may be, for example, a lamp 72 and spectrophotometer 74 arrangement, a fluorescence detector 76 , a resistivity sensor 78 , an X-ray or gamma ray density sensor 80 , a pressure and temperature gauge 82 , a density or viscosity sensor 84 , a vibrating wire 86 , an in-line CO2 sensor 88 , or an in-line H2S sensor 90 .
- the fluid sample is shown to flow in either direction through the flow line 60 .
- the fluorescence detector 76 can be used to, for example, detect traces of oil in water. This information can be useful for the assessment of subsea processing, for example, when water is separated from oil before being re-injected into the formation.
- the fluid resistivity sensor 78 can be used to detect water resistivity, which can be very useful information which can in turn be used to detect injection water breakthrough. Injection water used for reservoir stimulation will usually have a resistivity different from that of formation water. Water resistivity changes, therefore, can be correlated with injection water breakthrough.
- the fluid sampling or analysis device 26 can also include fluid conditioners.
- One possible fluid conditioner is a phase separator. This can be used for water or oil sampling. The main phase separator will give a liquid or gas separation. The phase separator within the fluid sampling or analysis device 26 can therefore be used to separate the oil from the water if necessary.
- sample flashing consists of dropping the pressure of sample before injecting it with a specific sensor. This method is well known in the analysis of HP (high pressure) live oil samples by using gas chromatography.
- the embodiment of device 26 which is illustrated in FIG. 9 is suitable for different types of application. These could include, for example, NMR characterization for composition analysis or viscosity measurement, gas chromatography, mass spectroscopy, inductive coupled plasma chemical (ICP) analysis, electro-chemical sensors, or pH or ion concentration measurement in water phase using colorimetric methods.
- NMR characterization for composition analysis or viscosity measurement
- gas chromatography mass spectroscopy
- ICP inductive coupled plasma chemical
- electro-chemical sensors electro-chemical sensors
- pH or ion concentration measurement in water phase using colorimetric methods pH or ion concentration measurement in water phase using colorimetric methods.
- FIG. 10 illustrates a further embodiment of apparatus 10 of the invention which includes a fluid sampling or analysis device 26 to be used for fluid analysis that has a further possible configuration of sensors 70 .
- Device 26 in this embodiment can be used for several types of measurement.
- Device 26 includes two seal valves 92 and 94 that can be opened and closed in order to trap a fluid sample in between them.
- the volume of fluid in the piping system between the two seal valves 92 and 94 forms a fluid circulation loop.
- the fluid in the circulation loop can be circulated with the circulation pump 96 and pump unit 103 .
- Seal valve 98 is used to force the fluid flow through the circulation loop before valves 92 and 94 are closed.
- a piston unit that is used to increase the volume trapped between the seal valves and consequently to reduce sample pressure.
- the piston is preferably retracted when the circulation pump 96 is operating.
- the agitation created by the fluid moving helps to prevent a problem posed by fluid supersaturation. It is well-known in the art that estimation of bubble point requires some agitation as the pressure is changed.
- the circulation loop can include an ultrasonic transducer that will also generate agitation and this helps to prevent supersaturation.
- a scattering detector 100 sensor is used in device 26 in order to detect bubbles or solid particles forming in a fluid flow line 60 .
- the scattering detector 100 used is known in the art and is used to measure the attenuation of light as it passes through a cell. Formation of solid particles and gas bubbles will lead to an increase in the attenuation of light.
- This sensor is used to detect the fluid bubble point which indicates at which pressure gas starts to form in the flow line.
- Such sensors can be used to detect the gas condensate dew point, the fluid bubble point, gas bubble formation or the presence of solid particles.
- a density and viscosity sensor 84 may also be included in device 26 . It is used to measure the evolution of the parameters of density and viscosity against pressure.
- An optical spectrometer (the lamp 72 and spectrometer 74 arrangement) may also be included in device 26 to measure fluid optical absorption at various wavelengths.
- the optical spectrometer for example, can be used to estimate fluid composition by NIR spectroscopy. It is of particular interest for hydrocarbon analysis as the hydrocarbons have characteristic absorption peaks around [1600; 1800] nm. Spectral analysis in the visible range can also be used for monitoring asphaltene content of the fluid.
- Device 26 may also include a camera 102 which is used to monitor the condition of the fluid in the flow lines for the presence of bubbles or solid particles.
- device 26 may also enclose a US transducer sensor 104 .
- Device 26 may be enclosed in a temperature control unit 106 .
- the temperature control unit 106 may enable the temperature of the fluid to be changed. In this way by combining pressure and temperature changes, device 26 can provide a comprehensive phase diagram for the fluid trapped in the fluid flow lines 60 of the device.
- Device 26 may be used in various downhole conditions and can be used in various applications such as, for example, the study of fluid phase diagrams (bubble point detection, wax or asphaltene onset, hydrate locus, etc), the study of fluid density and viscosity versus pressure, and the study of fluid composition.
- fluid phase diagrams bubble point detection, wax or asphaltene onset, hydrate locus, etc
- fluid density and viscosity versus pressure the study of fluid composition.
- FIG. 11 gives a possible configuration for a sampling bottle 108 .
- the sampling bottles 108 of apparatus 10 are configured for low shock sampling.
- Low shock sampling comprises filling a bottle 108 with the sample with a controlled flow rate. The goal is to avoid fast pressure changes of the sample which could lead to phase transition before the bottle 108 is filled.
- the sampling bottle 108 can be implemented as follows:
- a cylindrical bottle 108 with a piston 110 defining two chamber spaces as it moves along the bottle's main axis.
- the sample chamber 112 is located on one side of piston 110 is and the water cushion chamber 114 is located on the other side of piston 110 .
- Bottle 108 is connected to the fluid sampling line as shown in FIG. 11 .
- the volume of sample chamber 112 is minimal while the cushion water chamber 114 side is full.
- the solenoid valve 116 and the choke valve 118 are opened.
- the rate of sampling can be controlled by the choke 120 .
- the choke 120 controls the fluid flow and therefore the fluid flow rate in the sample chamber 112 .
- the sampling is completed once the piston 110 reaches its final position on the other side of the bottle 108 .
- Both the solenoid valve 116 and the choke 120 can be closed. Due to the controlled flow rate, the fluid is sampled with minimum pressure changes.
- low shock sampling can also be done without the piston 110 being in the bottle as shown in FIG. 12 c .
- the sampling bottle 108 must be flashed long enough to remove any of the initial filling water.
- FIG. 11 b illustrates bottle 108 during sampling.
- Low shock sampling is a well known technique for downhole fluid sampling. Other possible variations of fluid sampling have also been described in the prior art.
- the fluid sampling can be controlled either from surface or it can be controlled through a predetermined sequence of actions to be taken on a periodic base.
- the combination of the fact that the fluid sampling or analysis device 26 can be installed on a semi-permanent basis, the configuration of the sampling skid 22 and the possibility that sample can be obtained on a periodic basis, means that it is possible to sample the fluid without mobilizing an ROV 18 with its support vessel.
- Device 26 can therefore perform time-lapsed sampling during the time it is installed on a subsea apparatus 10 .
- the sampling can be performed though period of time from a few months to a few years.
- Sample bottles 108 can be retrieved at the surface by using an ROV 18 to pick up the skid 22 on which the sample bottles 108 are located.
- a sampling bottle 108 may also include a temperature control unit 122 .
- Temperature control allows the sample temperature to be kept the same as when it was in the fluid flow of the well. It would avoid phase transition due to temperature changes. In practice, the sample will tend to cool when it is sent to the bottle 108 .
- the temperature control system can consist of a simple electrical heating system wrapped around the bottle.
- the bottle 108 may include means for energy storage, a positioning system and a propulsion mechanism.
- An embodiment of the apparatus 10 according to the invention which illustrates such a configuration of a sample bottle 108 is shown in FIG. 13 .
- the bottle 108 in this embodiment is filled with compressed gas.
- An inflatable structure such as a balloon 124 is connected to the bottle 108 that is filled with compressed gas.
- the balloon 124 is connected to the compressed gas through a solenoid valve 116 .
- the bottle 108 end fittings use male/female hot stabs 107 that can be released through a command sent from the skid controller.
- the bottle 108 is fixed to the skid chassis through a mechanical interface that can also be released by a command sent by the skid controller.
- the bottle 108 also includes a localization system that can communicate with the surface. When the bottle 108 needs to be released a command is sent from the surface and this triggers the inflation of the balloon 124 , as well as the release of the end fitting and mechanical interface. In addition this also activates a localization beacon 126 .
- the bottle 108 is then buoyed to the surface. Once back at surface, the bottle 108 can be located and retrieved by a surface support vessel 128 .
- FIG. 4 of the drawings the fluid sampling section and the skids are shown to be in a modular configuration.
- the fluid sampling device 26 is configured according to the configuration described in FIG. 5 a .
- the device 26 includes two sampling lines located at different heights as is described in FIG. 7 a .
- the longer sampling line will sample liquid while the other shorter one will sample gas.
- An extraction pipe 130 is common to the gas 44 and liquid 46 sampling pipes. They form two primary loops through which production fluid circulates.
- the mechanical and hydraulic fluid interfaces are based on standardized stab plates 134 including electrical and hydraulic connections, as well as hydraulic valves 136 and 138 .
- the valves 138 are closed when a skid 22 is engaged on top of it. In all other circumstances the valves 136 and 138 are open.
- the mechanical interfaces of the stab plates 134 and valves 136 and 138 are the same on top of the phase separator as they are on the skids 22 . In this way the skids 22 can be stacked in any configuration on top of the separator 30 .
- the valves 136 and 138 are configured to connect the fluid sampling lines 46 with the extraction line 130 . As the skids 22 are connected one on top of another, the valves 138 from the lower skids are closed while the upper valves 136 are opened. The valves 138 of the lower skid 22 are closed when the upper skid connects to it. This takes place after hydraulic connection is completed. The configuration of the valves 136 and 138 allows the liquid to circulate from the separator 30 to the upper skid 22 .
- Fluid sampling and analysis devices 26 are located between the sampling pipes 44 and the extraction pipes 130 . There may be a pump 132 associated with these devices 26 in order to circulate the fluid from the sampling line 44 to the extraction line 130 .
- This configuration as shown in FIG. 4 allows for a fully modular configuration.
- Another important feature of the invention is the use of subsea fluid analysis measurement by apparatus 10 to be used to control subsea equipment.
- the information from the apparatus 10 can be used, for example to control subsea equipment in a fully automated mode, or to control subsea equipment from the surface using the information obtained from apparatus 10 .
- Different controllers/communication modules 28 are connected in a network configuration with, for example, an Ethernet architecture, which allows communication and control between the different skids 22 .
- the information can either be sent to the surface or processed at seabed level for the direct management of the control of other subsea modules.
- the information obtained from the sensors is directly processed at the seabed and a decision is made at subsea apparatus 10 .
- the information can be used to optimize choke opening for example. Another possible example is the optimization of chemical or water injection and the optimization of phase separator operating conditions.
- the information can also be sent to the surface for human based interpretation and decision making.
- FIG. 14 shows one embodiment of the subsea apparatus 10 and method according to the invention in which a template of fluid platforms are located on the seabed.
- FIG. 14 illustrates the flow of fluids from different wellheads which are mixed through sets of manifolds before being sent to the surface. Fluid platforms are shown placed between a wellhead and a manifold. This configuration enables the production fluid flow of each individual well to be characterized.
- Another important feature of the subsea apparatus 10 and method according to the invention is the ability to combine the measurements obtained from the fluid sensors of devices 26 in apparatus 10 with the measurements obtained from other sensors on the seabed.
- One possibility is to combine fluid analysis results with multiphase flow meter measurement for flow assurance prediction.
- the measurement results can be fed to simulation software such as OLGA® to predict possible flow assurance problems along the subsea installation.
- simulation software such as OLGA® to predict possible flow assurance problems along the subsea installation.
- Critical inputs for this type of software are phase diagrams as well as the respective flow of each phase (water, oil and gas) of the fluid.
- a phase diagram of each phase can be obtained from a PVT sensor as illustrated in FIG. 10 .
- composition measurement Another possibility is the use of composition measurement.
- a gas chromatograph could be installed on the fluid sampling or analysis device 26 to be used for analysis so as to provide the detailed composition. Combined with equation of state this could provide a phase diagram for each phase.
- the apparatus 10 and method according to this invention in combination with multiphase flow meter data may be used to obtain real-time flow assurance prediction by feeding fluid properties directly into the software models that are used for this purpose. This would allow the control of subsea equipment to optimize production condition.
- Another possible application of the apparatus and method according to the invention is its use for the optimization of chemical injection.
- Many chemicals are injected at different points in a subsea installation to manage a flow assurance problem.
- By sampling the fluid at the injector output after the inhibitor is mixed with the production fluid it is possible to assess the efficiency of the chemical treatment and optimize the quantity of chemical to be injected.
- the measurements of a phase behavior analyzer can be used to assess the efficiency of the treatment.
- the measurement from the fluid sampling or analysis device 26 can also be used for a more accurate estimation of the flow rate from each of the different phases from a multiphase flowmeter.
- An important input parameter of a multiphase flow meter used in the oil and gas industry is the density of each phase.
- the fluid analysis device of FIG. 9 could provide an estimation of the density of each phase that could be feedback in real-time to the multiphase flow meter for a more accurate estimation of individual flow rate.
- the fluid flow from the different wellheads is mixed through the manifolds before being brought back to the surface.
- allocation The problem of identifying the contribution of each well is known in the art as allocation.
- the fluids before mixing can come from different formations and from different pay zones. In addition, operators may sometimes share export lines.
- allocation is extremely important.
- fluid properties as well as flow rate must be considered.
- the important parameters are H2S content, CO2 content as well as hydrocarbon phase composition. Therefore fluid analysis data obtained from the apparatus 10 could be used for real time correction of allocation calculation.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Sampling And Sample Adjustment (AREA)
Abstract
Subsea apparatus and a method for sampling and analysing fluid from a subsea fluid flowline proximate a subsea well is provided, wherein the apparatus comprises at least one housing located in close proximity to said subsea fluid flowline; at least one fluid sampling device located in the housing in fluid communication with a said subsea fluid flowline for obtaining a sample of fluid from the subsea fluid flowline; at least one fluid processing apparatus located in the housing in fluid communication with said subsea fluid flowline for receiving and processing a portion of the fluid flowing through said fluid flowline or in fluid communication with the fluid sampling device, for processing the sample of fluid obtained from the subsea fluid flowline for analysis, while keeping the sample of fluid at subsea conditions; a fluid analysis device located in the housing, the fluid analysis device being in fluid communication with the fluid processing device and/or with the fluid sampling device, the fluid analysis device being used for analysing said sample of fluid or the processed sample of fluid to generate data relating to a plurality of properties of said sample of fluid and communicating said data to a surface data processor or to at least one other subsea apparatus; and conveying means included in the housing for conveying the housing means from one subsea fluid flowline to another subsea fluid flowline or for conveying the housing to the surface.
Description
- This invention relates to subsea apparatus for fluid sampling and/or analysis. In particular, the invention relates to a subsea apparatus for fluid sampling and/or analysis used in the oil and gas industry.
- Understanding the properties of fluids in wells in the oil and gas industry is critical for the assessment of oil or gas reservoirs. For example, the fluid properties may be used for the proper management of oil and gas reservoirs including for instance production management and flow assurance. Fluid sampling and/or analysis may be performed during various phases of the exploration, development and production phases of a reservoir. Conventional tools are able to take a fluid sample from the well and bring it to surface where it is processed and analysed. For example, often times the phase behavior of the fluid may be studied using an analysis known in the industry as PVT analysis which measures, inter alia, the bubble point of the fluid as well as its wax, and asphaltene content. Also, compositional analysis of the fluid sample may be performed as well as analysis of its H2S, CO2, Hg, and heavy metal content. Also, well known are tools and methods for measuring the density and viscosity of the fluid its, water content, etc.
- More and more of these measurements are arranged to be performed downhole. This is because, generally, obtaining a correct estimation of fluid phase behavior requires that a sample with a pressure and temperature as close as possible to the conditions present at the wellhead be taken so that wax and asphaltenes do not precipitate out of the fluid. Fluid properties at the surface may differ from those present at the wellhead. Sampling of the fluid at the surface is therefore not a suitable option for the correct estimation of the fluid phase behavior in subsea oil or gas wells. However, the conditions prevalent in a subsea environment make access to a subsea fluid sample rather difficult.
- In a subsea oil or gas well installation, fluid flows from different well heads are often mixed through a series of manifolds. This poses an additional complication in the sampling and analysis of subsea wells. Sampling and analysis of the fluid flowing from each individual well would be preferred as it would provide a valuable understanding of the production capabilities and peculiarities of each well which in turn could be used for proper field management. Also, the properties of the fluid produced by subsea wells may change significantly over a short period of time. Thus, if the analysis of the samples that have been taken is done at a later time at a surface, the value of the data will be diminished.
- Various apparatus, methods and systems for sampling and analyzing well fluids have been identified previously. U.S. Pat. No. 6,435,279 discloses a method and apparatus for sampling fluids from an undersea wellbore utilizing a self-propelled underwater vehicle, and a collection and storage device. The '279 patent describes a method for sampling a fluid produced from a subsea well, the method comprising a remotely operated vehicle (ROV) having a collecting device for collecting a sample of fluid and a storage facility for the collected sample of fluid wherein said collecting device and storage facility are connected to the ROV. The collecting device is used to collect a sample from a subsea location, storing the sample in the ROV and then transferring it to a surface location.
- International patent applications WO 2008/087156, and WO 2006/096659 disclose various systems and methods for subsea sampling. The WO 2008/087156 patent application describes a subsea sampling and data collection device that is coupled to a flowline at a flowline installation. The WO 2008/087156 sampling and data collection device includes a sample collection system having a probe insertable into a flowline to collect a fluid sample. The WO 2008/087156 application is assigned to the same assignee as the present invention and it is hereby incorporated by reference for all purposes allowable under the law to the extent that its disclosure does not contradict with the present invention.
- An article entitled “Improved production sampling using the Framo multiphase flow meter” by Framo Engineering AS in October 1999 discusses a multiphase flow meter used in fluid sampling, including subsea with the aid of remotely operated vehicles (ROV).
- From the description above it is evident that for effective production and flow assurance management in subsea oil and gas reservoirs, there is a real need to obtain a good understanding of produced fluid on a well by well basis and to measure the variation of fluid properties from each of these wells with time. The present invention provides an improved apparatus and associated method that facilitate the sampling and the characterization of the fluids at a subsea environment, and as close as possible to each well head. The present invention and method also enable analysis of sampled fluid to occur on a real time basis and thus obtain accurate real time analysis data for well performance and management.
- A first aspect of this invention provides subsea apparatus for sampling and analysing fluid from a subsea fluid flowline proximate a subsea well, comprising:
-
- at least one housing located in close proximity to said subsea fluid flowline;
- at least one fluid sampling device located in the housing in fluid communication with a said subsea fluid flowline for obtaining a sample of fluid from the subsea fluid flowline;
- at least one fluid processing apparatus located in the housing in fluid communication with said subsea fluid flowline for receiving and processing a portion of the fluid flowing through said fluid flowline or in fluid communication with the fluid sampling device, for processing the sample of fluid obtained from the subsea fluid flowline for analysis, while keeping the sample of fluid at subsea conditions;
- a fluid analysis device located in the housing, the fluid analysis device being in fluid communication with the fluid processing device and/or with the fluid sampling device, the fluid analysis device being used for analysing said sample of fluid or the processed sample of fluid to generate data relating to a plurality of properties of said sample of fluid and communicating said data to a surface data processor or to at least one other subsea apparatus; and
- conveying means included in the housing for conveying the housing means from one subsea fluid flowline to another subsea fluid flowline or for conveying the housing to the surface.
- The fluid analysis data can be real time data, and this real time data is communicated to at least one electronic device which incorporates at least one software model used to provide information regarding the production of said subsea well. The software model may also used to provide predictions regarding the production of the well.
- In one form of the invention the fluid analysis data is used to control at least one piece of subsea equipment. The fluid processing apparatus separates the sample of fluid into at least a liquid and a gaseous phase, or mixes the sample of fluid with at least one other different fluid, or enriches the sample of fluid.
- In one form of the invention the fluid sampling device is in communication with the well fluid. The fluid sampling device may also be in communication with a fluid processing apparatus, the fluid processing apparatus being in communication with the well fluid.
- Further according to the invention, at least one data processing device may be locatable in the housing and may be in communication with the fluid analysing device. The data processing device processes data received from the fluid analysis device and communicates the data.
- The conveying means may be an attachment for a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV).
- The subsea apparatus may further comprise a plurality of housings which are connectable to each other in a modular fashion. The fluid analysis device of each housing may be in fluid communication with the fluid analysis device of another connected housing. In the same way, the fluid sampling device of each housing may be in fluid communication with the fluid sampling device of another fluid sampling device of a connected housing, and the data processing device of each housing may be in fluid communication with the data processing device of a connected housing.
- A second aspect of this invention provides a method of sampling and analysing fluid from a subsea well, the method comprising:
-
- locating at least one housing in close proximity to a subsea flowline proximate said subsea well, said housing comprising at least one fluid analysis device, at least one fluid processing apparatus and at least one fluid sampling device, the fluid sampling device being in fluid communication with said subsea flowline, the fluid processing apparatus being in fluid communication with said subsea flowline and/or with the fluid sampling device, the fluid analysis device being in fluid communication with the fluid processing device and/or with the fluid sampling device;
- obtaining a sample of fluid from the subsea flowline, and storing it in the fluid sampling device;
- transferring the sample of fluid to the processing device, and processing the sample of fluid with the processing device for analysis by the fluid analysis device, while keeping the sample of fluid at subsea conditions;
- transferring the sample of fluid from the processing device to the fluid analysis device;
- analysing the properties of the fluid with the fluid analysis device to obtain fluid analysis data subsea;
- communicating the fluid analysis data to at least one other subsea apparatus or to a surface data processor; and
- conveying the housing from said subsea fluid flowline to another subsea fluid flowline or to the surface.
- In one form of the invention the fluid sampling device is in fluid communication with a fluid processing apparatus, the fluid processing apparatus being in fluid communication with the well fluid flowing in the subsea flowline and the sample of fluid is obtained from the well fluid in the subsea flowline via the fluid processing apparatus. The fluid sampling device may also be in communication with a fluid processing apparatus that is in communication with the well fluid.
- Further according to the invention, at least one data processing device may be locatable in the housing and may be in fluid communication with the fluid analysis device, and which further comprises processing fluid analysis data received from the fluid analysis device by means of the data processing device and communicating the processed data to another apparatus or to the surface. The method may further include processing fluid data received from the fluid analysis device and communicating the data.
- The method may also comprise deploying one or more housings of the apparatus by means of a detachable subsea vehicle such as, for example, a remotely operated vehicle (ROV) or an autonomous underwater vehicle (AUV), the housings being connectable to each other.
- In a further form of the invention there may be a plurality of housings, and the method may further comprise connecting the plurality of housings to each other in a modular fashion, and wherein each fluid analysis device of each housing is in fluid communication with each other, and each fluid sampling device of each housing is in fluid communication with each other.
- Further aspects of the invention will be apparent from the following description.
-
FIG. 1 shows a schematic side view of a subsea apparatus for sampling and/or analysing fluid from a well according to one embodiment of the invention; -
FIGS. 2 shows a schematic side view of a housing of the subsea apparatus for sampling and analysing fluid from a well as shown inFIG. 1 , attached to a remotely operated vehicle (ROV); -
FIG. 3 shows a schematic side view of the subsea apparatus for sampling and/or analysing fluid attached to a fluid processing device indicating the flow direction through the components of the fluid processing device; -
FIG. 4 shows a diagrammatic view of a hydraulic sampling device of the subsea apparatus for sampling and/or analysing fluid from a well according to one embodiment of the invention; -
FIG. 5 a shows a diagrammatic view of a passive sampling device of the subsea apparatus for sampling and/or analysing fluid from a well according to another embodiment of the invention; -
FIG. 5 b shows a diagrammatic view of a passive sampling device of the subsea apparatus for sampling and/or analysing fluid from a well which uses venturi according to another embodiment of the invention; -
FIG. 6 shows a diagrammatic view of an active sampling device of the subsea apparatus for sampling and/or analysing fluid flow which uses a pump according to a further embodiment of the invention; -
FIGS. 7 a, 7 b and 7 c show a series of diagrammatic views of an adjustable inlet of a sampling device according to an embodiment of the invention; -
FIG. 8 shows a schematic layout of a fluid analyser of the subsea apparatus for analysing fluid from a well; -
FIG. 9 shows a schematic side view of a section of an in-line fluid analyser of the subsea apparatus for sampling and analysing fluid from a well according to one embodiment of the invention; -
FIG. 10 shows a schematic side view of a section of an in-line fluid analyser of the subsea apparatus for sampling and analysing fluid from a well which includes a phase behaviour fluid analyser according to another embodiment of the invention; -
FIGS. 11 , 11 a, 11 b and 11 c show schematic side view of a sampling bottle for low shock sampling with a piston inside the bottle of the subsea apparatus according to one embodiment of the invention; -
FIGS. 12 , 12 a, 12 b and 12 c show schematic side view of a sampling bottle for low shock sampling without a piston inside the bottle of the subsea apparatus according to one embodiment of the invention; -
FIG. 13 shows schematic view of a self retrievable sampling bottle apparatus of the subsea apparatus according to one embodiment of the invention; and -
FIG. 14 shows a schematic overview of a controller configuration used for the control of a number of subsea apparatuses according to one embodiment of the invention. - This subsea apparatus for analysing and/or sampling fluid from a well according to the invention is applicable to subsea installations or facilities in the oil and gas industry. In the drawings
FIG. 1 illustrates the basic layout of asubsea apparatus 10 for sampling and/or analysing fluid from a well according to the invention.Subsea apparatus 10 is located in close proximity to the wellhead of a well and includes a subseafluid processing device 12 for processing fluid samples obtained from the well. Thesubsea processing device 12 can be a phase separator, a phase accumulator, a boosting pump, a water treatment unit, chemical injector or an injection pump, depending on the application required. - The
subsea processing device 12 includes afluid sampling device 14. Thefluid sampling device 14 consists of a network of pipes connected to different sampling points in theprocessing device 12. Thefluid sampling device 14 can also include a distributor that can redirect the sampled fluid to different outlet. -
Subsea apparatus 10 further includes a remote operating device (ROV)docking station 16 which allows the docking and attachment of a remote operating device (ROV) 18 to thesubsea processing device 12. - As shown in
FIG. 1 , there is afluid interface 20 in communication with thesampling device 14 which is located below theROV docking station 16. Thefluid interface 20 allows a hydraulic connection between theROV 18 and theprocessing device 12, and thus fluid at well pressure can travel between them. This hydraulic connection can be initiated when theROV 18 is docked at the docking station and it can be disconnected when theROV 18 is removed. - A frame or
skid 22 could also be docked to the docking station with the help of anROV 18. As illustrated inFIG. 2 , theskid 22 is attached to theROV 18 with several instrumentation modules connected thereto. This will be further described below.Skid 22 can be docked to thedocking station 16 as theROV 18 approaches the installation. Theskid 22 can then be detached from theROV 18 through a specific skid/ROV interface 24 and it can then be left permanently on the installation ofapparatus 10. The skid/ROV interface 24 may be a fluid interface andskid 22 is in communication with thefluid interface 20. By using a hydraulic connection betweenskid 22 andfluid interface 20, the well fluid can be directed to theinstrumentation module 26 which is located on theskid 22. -
Skid 22 is designed so thatother skids 22 of a similar type can be connected to it. The design is modular so that theskids 22 can be configured and assembled in different orders, and then used for different purposes. -
Skid 22 can also be deployed using an autonomous under water vehicle AUV. In this case, theskid interface 24 may include instrumentation for the positioning of the AUV during docking. - An
instrumentation module 26 is located insideskid 22 and is connected to a controller/communication module 28.Instrumentation module 26 contains the fluid analyzer and it is used to perform fluid analysis and/or fluid sampling. It is connected to thefluid interface 20 and it can receive the fluid collected by thefluid sampling device 14. The type of analysis and the sampling sequence is managed by the controller/communication module 28. The controller/communication module 28 performs control either through a pre-defined sequence stored in the controller, from the surface with the use of a communication link, or in a completely automated mode with the use of the fluid analysis data obtained by the fluid analyzer ininstrumentation module 26. It is used to enable decisions to be made on how to process the sample of fluid. - There are various different possible schemes for the sampling which have been described previously in the art and these can easily be implemented in conjunction with this invention.
- The fluid analyzer in
instrumentation module 26 consists in a network of pipe connected to pumps, fluid properties sensors, sample chambers, fluid conditioners and injectors. This system is managed through the controller/communication module 28. - The fluid analysis data obtained by
apparatus 10 is used to control various types of subsea or surface equipment. This fluid analysis data is based on real time sample measurements obtained from the fluid sample that is obtained and also possibly analyzed at wellhead conditions. This real time fluid data may be communicated to an electronic device which incorporates at least one software model and this model may be used to provide information regarding the production of the well and to provide predictions regarding the production of the well. Thus information regarding reservoir assurance, or flow assurance management may be obtained through the processing of this fluid data. - Details will now be provided of further embodiments of the invention.
-
FIG. 3 illustrates an embodiment of the subsea apparatus for sampling and/or analysing fluid from a well according to the invention, which further includes aphase separator 30. - The
phase separator 30 which may be used is one of the typical examples of phase separators known in the art. Such a typical phase separator consists of apressure vessel 32 with an internal pipe drilled with radial holes. Thepressure vessel 32 includes afluid inlet 34 andfluid outlet 36. The direction of fluid flow is shown by arrows A inFIG. 3 . Thephase generator 30 was initially designed in the art as a device for fluid mixing purposes but it can also be used as a fluid separator. In the pressure vessel area, the fluid segregates depending on its density, with gas separating out on top and the liquid (oil and water) separating out at the bottom. As the fluid is forced through the central pipe (with holes), the phases are remixed, leading to a mixed fluid flow leaving at the outlet. -
Phase generator 30 allows liquid can be sampled at the bottom of the vessel while gas can be sampled at the top. -
FIG. 3 further shows aretrievable ROV 18 with askip 22 including a fluid sampling oranalysis module 26 to be used for fluid sampling, as well as askip 22 including a fluid sampling oranalysis module 26 to be used for fluid analysis, and then amulti-phase flow meter 38. - The hydraulic sampling device of
apparatus 10 is illustrated inFIGS. 5 and 6 . Fluid sampling can be done either through a passive or an active sampler. In the implementation of the invention shown inFIGS. 5 and 6 , the fluid sampling oranalysis module 26 has internal piping connecting theliquid sampling pipe 44 to thegas sampling pipe 46. It further includes aninlet pipe 40 to sample the fluid from the separator to the fluid analyzer inmodule 26 and anoutlet pipe 42 to re-inject the fluid to the separator or main fluid flow line after it has been analyzed. The direction of fluid flow is shown inFIGS. 5 a, 5 b and 6 by arrows B. -
Passive sampling devices 26 do not require any pump to sample the fluid as these devices are based on passive mechanisms. Two different possible implementations of passive sampling devices are shown inFIGS. 5 a and 5 b. InFIG. 5 b, the fluid movement inside the sampling tubes is generated using aventuri device 48. Theoutlet pipe 42 is connected toventuri device 48 which is located further down the fluid flow line. Theventuri device 48 generates a pressure difference that drives the fluid through the piping system and the fluid sampling oranalysis module 26 or from the inlet to the outlet. - In
FIG. 5 a, the fluid in the extraction line is dragged by the main flow in aperforated pipe 50. -
FIG. 6 describes an active sampler using apump 52 to generate the fluid flow from the inlet to the outlet. - In practice several different types of fluid sampling devices can be used. For example, in
FIGS. 5 and 6 , with the use of the proposed separator, it is possible to change the sampled liquid phase by adjusting the position of the inlet inside the phase separation chamber. The liquid phase of the fluid will accumulate at the bottom while the gas phase will accumulate at the top of the vessel. - One possibility is to have two or more inlet pipes 40.1 and 40.2 with different heights as is illustrated in
FIG. 7 a. If required, the flow from these sampling pipes could be directed to a manifold before being routed to the fluid sampling oranalysis module 26. - Another possibility which is described in
FIG. 7 b is to have a sampling pipe with an adjustable height that is adjustable with the use ofmechanical actuators 56. The height H may then be adjusted according to what is required. With time, the ratio between the different phases of fluid produced by the well changes. With such an adjustable sampling inlet, it is thus possible to adapt the sampling device to the changes in production conditions. -
FIG. 7 c describes an adjustable fluid sampling or analyzingmodule 26 which uses a series ofcontrollable valves 57 and 58 connected thereto to change the sampling point position. Thevalves 57 and 58 can be selectively closed. In the normal operation, allvalves 58 are closed except for the valve 57 which is at the level of the sampling point. The fluid flow is illustrated inFIG. 7 by arrows E. - In one embodiment of the invention there is a
universal skid 22 used for fluid sampling and analysis. Thisskid 22 includes thefluid interface 20, power/communication module 28, skid orROV interface 24, a local controller module and a fluid sampling oranalysis module 26. The local controller module controls the working of the sampling orfluid analysis module 26. - One feature of
apparatus 10 is its modularity.Apparatus 10 may be provided in different kinds of modules. Fluid, communication and skid or ROV interfaces are designed to be fully interoperable so that different kinds of modules ofapparatus 10 can be interconnected and configured in many different types of configurations. - Another feature of
apparatus 10 is that modules ofapparatus 10 includingskids 22 may be installed either on a temporary basis or on a semi-permanent basis. - Before any fluid sampling or fluid analysis operation starts, the
skids 22 are fully engaged in anROV 18 and connected to the various fluid interfaces. An individual module ofapparatus 10 comprising askid 22 and its attached equipment can be retrieved as required by anROV 18. - The fluid sampling or analyzing
device 26 which is mounted in askid 22 inapparatus 10 is shown in more detail inFIG. 8 . Thedevice 26 is enclosed in atool housing 59 and it includesfluid flow lines 60 connected together and guiding the fluid from an inlet to an outlet. Thedevice 26 further includespumps 62 which can move the fluid there through.Fluid conditioners 64 which are used to process the fluid and change properties such as the ratio between the different fluid phases, or the fluid pressure, volume or temperature are also included indevice 26.Fluid processing devices 12 may further include a separator, a mixer, and a PVT (pressure, volume and temperature) device. - In
device 26injectors 66 can be used to inject fluids which are different from the fluid which is flowing in aparticular flow line 60. The injected fluid can be used to generate an inhibitory chemical reaction with the sampled fluid or it can change the phase behavior of the fluid. Sample bottles orchambers 68 indevice 26 are used to take and store samples of the fluid inside aflow line 60.Fluid property sensors 70 are also shown located onflow lines 60 indevice 26. - In the drawings,
FIG. 9 illustrates an embodiment of the fluid sampling oranalysis device 26 ofapparatus 10 to be used for fluid analysis with one possible configuration ofsensors 70. In this embodiment,device 26 is in-line with the sampling piping. Various types ofsensors 70 are shown in the in-line configuration in afluid flow line 60. These sensors may be, for example, alamp 72 andspectrophotometer 74 arrangement, afluorescence detector 76, aresistivity sensor 78, an X-ray or gammaray density sensor 80, a pressure andtemperature gauge 82, a density orviscosity sensor 84, a vibratingwire 86, an in-line CO2 sensor 88, or an in-line H2S sensor 90. InFIG. 9 the fluid sample is shown to flow in either direction through theflow line 60. - The
fluorescence detector 76 can be used to, for example, detect traces of oil in water. This information can be useful for the assessment of subsea processing, for example, when water is separated from oil before being re-injected into the formation. - The
fluid resistivity sensor 78 can be used to detect water resistivity, which can be very useful information which can in turn be used to detect injection water breakthrough. Injection water used for reservoir stimulation will usually have a resistivity different from that of formation water. Water resistivity changes, therefore, can be correlated with injection water breakthrough. - The fluid sampling or
analysis device 26 can also include fluid conditioners. One possible fluid conditioner is a phase separator. This can be used for water or oil sampling. The main phase separator will give a liquid or gas separation. The phase separator within the fluid sampling oranalysis device 26 can therefore be used to separate the oil from the water if necessary. - Another sensor which may form part of
device 26 is a unit to “flash” the sample. Sample flashing consists of dropping the pressure of sample before injecting it with a specific sensor. This method is well known in the analysis of HP (high pressure) live oil samples by using gas chromatography. - The embodiment of
device 26 which is illustrated inFIG. 9 is suitable for different types of application. These could include, for example, NMR characterization for composition analysis or viscosity measurement, gas chromatography, mass spectroscopy, inductive coupled plasma chemical (ICP) analysis, electro-chemical sensors, or pH or ion concentration measurement in water phase using colorimetric methods. - In the drawings,
FIG. 10 illustrates a further embodiment ofapparatus 10 of the invention which includes a fluid sampling oranalysis device 26 to be used for fluid analysis that has a further possible configuration ofsensors 70.Device 26 in this embodiment can be used for several types of measurement.Device 26 includes two 92 and 94 that can be opened and closed in order to trap a fluid sample in between them. The volume of fluid in the piping system between the twoseal valves 92 and 94 forms a fluid circulation loop. The fluid in the circulation loop can be circulated with theseal valves circulation pump 96 andpump unit 103.Seal valve 98 is used to force the fluid flow through the circulation loop before 92 and 94 are closed.valves - A piston unit that is used to increase the volume trapped between the seal valves and consequently to reduce sample pressure. There is a pressure sensor connected to the circulation loop to monitor pressure changes as the piston is retracted. The piston is preferably retracted when the
circulation pump 96 is operating. The agitation created by the fluid moving helps to prevent a problem posed by fluid supersaturation. It is well-known in the art that estimation of bubble point requires some agitation as the pressure is changed. The circulation loop can include an ultrasonic transducer that will also generate agitation and this helps to prevent supersaturation. - A
scattering detector 100 sensor is used indevice 26 in order to detect bubbles or solid particles forming in afluid flow line 60. Thescattering detector 100 used is known in the art and is used to measure the attenuation of light as it passes through a cell. Formation of solid particles and gas bubbles will lead to an increase in the attenuation of light. This sensor is used to detect the fluid bubble point which indicates at which pressure gas starts to form in the flow line. Such sensors can be used to detect the gas condensate dew point, the fluid bubble point, gas bubble formation or the presence of solid particles. - A density and
viscosity sensor 84 may also be included indevice 26. It is used to measure the evolution of the parameters of density and viscosity against pressure. - An optical spectrometer (the
lamp 72 andspectrometer 74 arrangement) may also be included indevice 26 to measure fluid optical absorption at various wavelengths. The optical spectrometer, for example, can be used to estimate fluid composition by NIR spectroscopy. It is of particular interest for hydrocarbon analysis as the hydrocarbons have characteristic absorption peaks around [1600; 1800] nm. Spectral analysis in the visible range can also be used for monitoring asphaltene content of the fluid. -
Device 26 may also include acamera 102 which is used to monitor the condition of the fluid in the flow lines for the presence of bubbles or solid particles. In addition,device 26 may also enclose aUS transducer sensor 104. -
Device 26 may be enclosed in atemperature control unit 106. Thetemperature control unit 106 may enable the temperature of the fluid to be changed. In this way by combining pressure and temperature changes,device 26 can provide a comprehensive phase diagram for the fluid trapped in thefluid flow lines 60 of the device. -
Device 26 may be used in various downhole conditions and can be used in various applications such as, for example, the study of fluid phase diagrams (bubble point detection, wax or asphaltene onset, hydrate locus, etc), the study of fluid density and viscosity versus pressure, and the study of fluid composition. - Another important feature of the invention is the ability to sample fluid.
FIG. 11 gives a possible configuration for asampling bottle 108. The samplingbottles 108 ofapparatus 10 are configured for low shock sampling. Low shock sampling comprises filling abottle 108 with the sample with a controlled flow rate. The goal is to avoid fast pressure changes of the sample which could lead to phase transition before thebottle 108 is filled. - The
sampling bottle 108 can be implemented as follows: - A
cylindrical bottle 108 with apiston 110 defining two chamber spaces as it moves along the bottle's main axis. Thesample chamber 112 is located on one side ofpiston 110 is and thewater cushion chamber 114 is located on the other side ofpiston 110. -
Bottle 108 is connected to the fluid sampling line as shown inFIG. 11 . In the initial position before thebottle 108 is opened, shown inFIG. 11 a, the volume ofsample chamber 112 is minimal while thecushion water chamber 114 side is full. For sampling, thesolenoid valve 116 and thechoke valve 118 are opened. The rate of sampling can be controlled by thechoke 120. Thechoke 120 controls the fluid flow and therefore the fluid flow rate in thesample chamber 112. The sampling is completed once thepiston 110 reaches its final position on the other side of thebottle 108. Both thesolenoid valve 116 and thechoke 120 can be closed. Due to the controlled flow rate, the fluid is sampled with minimum pressure changes. - It will be noted that low shock sampling can also be done without the
piston 110 being in the bottle as shown inFIG. 12 c. In this case, thesampling bottle 108 must be flashed long enough to remove any of the initial filling water.FIG. 11 b illustratesbottle 108 during sampling. - Low shock sampling is a well known technique for downhole fluid sampling. Other possible variations of fluid sampling have also been described in the prior art.
- The fluid sampling can be controlled either from surface or it can be controlled through a predetermined sequence of actions to be taken on a periodic base.
- The combination of the fact that the fluid sampling or
analysis device 26 can be installed on a semi-permanent basis, the configuration of thesampling skid 22 and the possibility that sample can be obtained on a periodic basis, means that it is possible to sample the fluid without mobilizing anROV 18 with its support vessel.Device 26 can therefore perform time-lapsed sampling during the time it is installed on asubsea apparatus 10. With the proposed configuration, the sampling can be performed though period of time from a few months to a few years.Sample bottles 108 can be retrieved at the surface by using anROV 18 to pick up theskid 22 on which thesample bottles 108 are located. - A
sampling bottle 108 may also include atemperature control unit 122. Temperature control allows the sample temperature to be kept the same as when it was in the fluid flow of the well. It would avoid phase transition due to temperature changes. In practice, the sample will tend to cool when it is sent to thebottle 108. The temperature control system can consist of a simple electrical heating system wrapped around the bottle. - Another important feature of the invention is the ability of sampling
bottles 108 to be retrieved to the surface before theskid 22 is changed. Thebottle 108 may include means for energy storage, a positioning system and a propulsion mechanism. An embodiment of theapparatus 10 according to the invention which illustrates such a configuration of asample bottle 108 is shown inFIG. 13 . Thebottle 108 in this embodiment is filled with compressed gas. An inflatable structure such as aballoon 124 is connected to thebottle 108 that is filled with compressed gas. Theballoon 124 is connected to the compressed gas through asolenoid valve 116. - The
bottle 108 end fittings use male/femalehot stabs 107 that can be released through a command sent from the skid controller. Thebottle 108 is fixed to the skid chassis through a mechanical interface that can also be released by a command sent by the skid controller. Thebottle 108 also includes a localization system that can communicate with the surface. When thebottle 108 needs to be released a command is sent from the surface and this triggers the inflation of theballoon 124, as well as the release of the end fitting and mechanical interface. In addition this also activates alocalization beacon 126. Thebottle 108 is then buoyed to the surface. Once back at surface, thebottle 108 can be located and retrieved by asurface support vessel 128. - In
FIG. 4 of the drawings the fluid sampling section and the skids are shown to be in a modular configuration. Thefluid sampling device 26 is configured according to the configuration described inFIG. 5 a. Thedevice 26 includes two sampling lines located at different heights as is described inFIG. 7 a. The longer sampling line will sample liquid while the other shorter one will sample gas. Anextraction pipe 130 is common to thegas 44 andliquid 46 sampling pipes. They form two primary loops through which production fluid circulates. - The mechanical and hydraulic fluid interfaces are based on
standardized stab plates 134 including electrical and hydraulic connections, as well as 136 and 138. Thehydraulic valves valves 138 are closed when askid 22 is engaged on top of it. In all other circumstances the 136 and 138 are open. The mechanical interfaces of thevalves stab plates 134 and 136 and 138 are the same on top of the phase separator as they are on the skids 22. In this way thevalves skids 22 can be stacked in any configuration on top of theseparator 30. - The
136 and 138 are configured to connect thevalves fluid sampling lines 46 with theextraction line 130. As theskids 22 are connected one on top of another, thevalves 138 from the lower skids are closed while theupper valves 136 are opened. Thevalves 138 of thelower skid 22 are closed when the upper skid connects to it. This takes place after hydraulic connection is completed. The configuration of the 136 and 138 allows the liquid to circulate from thevalves separator 30 to theupper skid 22. - Fluid sampling and
analysis devices 26 are located between the samplingpipes 44 and theextraction pipes 130. There may be apump 132 associated with thesedevices 26 in order to circulate the fluid from thesampling line 44 to theextraction line 130. This configuration as shown inFIG. 4 allows for a fully modular configuration. - Another important feature of the invention is the use of subsea fluid analysis measurement by
apparatus 10 to be used to control subsea equipment. The information from theapparatus 10 can be used, for example to control subsea equipment in a fully automated mode, or to control subsea equipment from the surface using the information obtained fromapparatus 10. Different controllers/communication modules 28 are connected in a network configuration with, for example, an Ethernet architecture, which allows communication and control between the different skids 22. The information can either be sent to the surface or processed at seabed level for the direct management of the control of other subsea modules. - In a fully automated mode, the information obtained from the sensors is directly processed at the seabed and a decision is made at
subsea apparatus 10. The information can be used to optimize choke opening for example. Another possible example is the optimization of chemical or water injection and the optimization of phase separator operating conditions. The information can also be sent to the surface for human based interpretation and decision making. -
FIG. 14 shows one embodiment of thesubsea apparatus 10 and method according to the invention in which a template of fluid platforms are located on the seabed.FIG. 14 illustrates the flow of fluids from different wellheads which are mixed through sets of manifolds before being sent to the surface. Fluid platforms are shown placed between a wellhead and a manifold. This configuration enables the production fluid flow of each individual well to be characterized. - Another important feature of the
subsea apparatus 10 and method according to the invention is the ability to combine the measurements obtained from the fluid sensors ofdevices 26 inapparatus 10 with the measurements obtained from other sensors on the seabed. - One possibility is to combine fluid analysis results with multiphase flow meter measurement for flow assurance prediction. The measurement results can be fed to simulation software such as OLGA® to predict possible flow assurance problems along the subsea installation. For example, in a case where OLGA® is handling 1D dynamic simulation of fluid phase behavior along the subsea piping installation. It allows simulation from the wellhead to the surface. Critical inputs for this type of software are phase diagrams as well as the respective flow of each phase (water, oil and gas) of the fluid. A phase diagram of each phase can be obtained from a PVT sensor as illustrated in
FIG. 10 . - Another possibility is the use of composition measurement. A gas chromatograph could be installed on the fluid sampling or
analysis device 26 to be used for analysis so as to provide the detailed composition. Combined with equation of state this could provide a phase diagram for each phase. - The
apparatus 10 and method according to this invention in combination with multiphase flow meter data may be used to obtain real-time flow assurance prediction by feeding fluid properties directly into the software models that are used for this purpose. This would allow the control of subsea equipment to optimize production condition. - Flow assurance problems are likely to happen during installation shut-down, therefore, providing updated information on fluid behavior just before the shut-down would be able to help provide better management of the installation.
- Another possible application of the apparatus and method according to the invention is its use for the optimization of chemical injection. Many chemicals are injected at different points in a subsea installation to manage a flow assurance problem. By sampling the fluid at the injector output after the inhibitor is mixed with the production fluid, it is possible to assess the efficiency of the chemical treatment and optimize the quantity of chemical to be injected. For example, the measurements of a phase behavior analyzer can be used to assess the efficiency of the treatment. By comparing the phase behavior in real time, with the operation safety envelop, it is possible to optimize the volume or the type of chemical injected.
- The measurement from the fluid sampling or
analysis device 26 can also be used for a more accurate estimation of the flow rate from each of the different phases from a multiphase flowmeter. An important input parameter of a multiphase flow meter used in the oil and gas industry is the density of each phase. The fluid analysis device ofFIG. 9 could provide an estimation of the density of each phase that could be feedback in real-time to the multiphase flow meter for a more accurate estimation of individual flow rate. - In the subsea configuration of equipment illustrated in
FIG. 14 , the fluid flow from the different wellheads is mixed through the manifolds before being brought back to the surface. The problem of identifying the contribution of each well is known in the art as allocation. The fluids before mixing can come from different formations and from different pay zones. In addition, operators may sometimes share export lines. In terms of revenue sharing, allocation is extremely important. For allocation, fluid properties as well as flow rate must be considered. Further, in terms of fluid properties, from an allocation standpoint, the important parameters are H2S content, CO2 content as well as hydrocarbon phase composition. Therefore fluid analysis data obtained from theapparatus 10 could be used for real time correction of allocation calculation.
Claims (14)
1. Subsea apparatus for sampling and analysing fluid from a subsea fluid flowline proximate a subsea well, comprising:
at least one housing located in close proximity to said subsea fluid flowline;
at least one fluid sampling device located in the housing in fluid communication with a said subsea fluid flowline for obtaining a sample of fluid from the subsea fluid flowline;
at least one fluid processing apparatus located in the housing in fluid communication with said subsea fluid flowline for receiving and processing a portion of the fluid flowing through said fluid flowline or in fluid communication with the fluid sampling device, for processing the sample of fluid obtained from the subsea fluid flowline for analysis, while keeping the sample of fluid at subsea conditions;
a fluid analysis device located in the housing, the fluid analysis device being in fluid communication with the fluid processing device and/or with the fluid sampling device, the fluid analysis device being used for analysing said sample of fluid or the processed sample of fluid to generate data relating to a plurality of properties of said sample of fluid and communicating said data to a surface data processor or to at least one other subsea apparatus; and
conveying means included in the housing for conveying the housing means from one subsea fluid flowline to another subsea fluid flowline or for conveying the housing to the surface.
2. Subsea apparatus as in claim 1 , further comprising at least one electronic device which
incorporates at least one software model used to provide information regarding the production of said subsea well.
3. Subsea apparatus as in claim 1 , wherein the fluid analysis data is used to control at least one subsea piece of equipment.
4. Subsea apparatus as in claim I, wherein the fluid processing apparatus separates the sample of fluid into at least a liquid and a gaseous phase, or mixes the sample of fluid with at least one other different fluid, or enriches the sample of fluid.
5. Subsea apparatus as in claim 1 , wherein at least one data processing device is located in the housing and is in communication with the fluid analysis device.
6. Subsea apparatus as in claim 1 , wherein the conveying means is an attachment for a detachable subsea vehicle.
7. Subsea apparatus as in claim 6 , wherein the conveying means is an attachment for a remotely operated vehicle (ROV) and/or an autonomous underwater vehicle (AUV).
8. Subsea apparatus as in claim 1 , which comprises a plurality of fluid analysis devices which are connected to each other.
9. Subsea apparatus as in claim 1 , which comprises a plurality of housings connected to each other in a modular fashion located in close proximity to said subsea fluid flowline, and wherein each fluid analysis device of each housing is in fluid communication with each other, and each fluid sampling device of each housing is in fluid communication with each other.
10. A method of sampling and analysing fluid from a subsea well, the method comprising:
locating at least one housing in close proximity to a subsea flowline proximate said subsea well, said housing comprising at least one fluid analysis device, at least one fluid processing apparatus and at least one fluid sampling device, the fluid sampling device being in fluid communication with said subsea flowline, the fluid processing apparatus being in fluid communication with said subsea flowline and/or with the fluid sampling device, the fluid analysis device being in fluid communication with the fluid processing device and/or with the fluid sampling device;
obtaining a sample of fluid from the subsea flowline, and storing it in the fluid sampling device;
transferring the sample of fluid to the processing device, and processing the sample of fluid with the processing device for analysis by the fluid analysis device, while keeping the sample of fluid at subsea conditions;
transferring the sample of fluid from the processing device to the fluid analysis device;
analysing the properties of the fluid with the fluid analysis device to obtain fluid analysis data subsea;
communicating the fluid analysis data to at least one other subsea apparatus or to a surface data processor; and
conveying the housing from said subsea fluid flowline to another subsea fluid flowline or to the surface.
11. The method as in claim 10 , wherein the fluid sampling device is in fluid communication with a fluid processing apparatus, the fluid processing apparatus being in fluid communication with the well fluid flowing in the subsea flowline and the sample of fluid is obtained from the well fluid in the subsea flowline via the fluid processing apparatus.
12. The method as in claim 10 , wherein at least one data processing device is locatable in the housing and is in fluid communication with the fluid analysis device, and which further comprises processing fluid analysis data received from the fluid analysis device by means of the data processing device and communicating the processed data to another apparatus or to the surface.
13. The method as in claim 10 , wherein the conveying means is an attachment for a detachable subsea vehicle.
14. The method as in claim 10 , wherein there are a plurality of housings, and which further comprises connecting the plurality of housings to each other in a modular fashion, and wherein each fluid analysis device of each housing is in fluid communication with each other, and each fluid sampling device of each housing is in fluid communication with each other.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US12/642,299 US9074465B2 (en) | 2009-06-03 | 2009-12-18 | Methods for allocating commingled oil production |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB0810189.1 | 2008-06-04 | ||
| GB0810189.1A GB2460668B (en) | 2008-06-04 | 2008-06-04 | Subsea fluid sampling and analysis |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/642,299 Continuation-In-Part US9074465B2 (en) | 2009-06-03 | 2009-12-18 | Methods for allocating commingled oil production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20100059221A1 true US20100059221A1 (en) | 2010-03-11 |
Family
ID=39638145
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US12/477,190 Abandoned US20100059221A1 (en) | 2008-06-04 | 2009-06-03 | Subsea fluid sampling and analysis |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20100059221A1 (en) |
| GB (1) | GB2460668B (en) |
Cited By (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090288836A1 (en) * | 2008-05-21 | 2009-11-26 | Valkyrie Commissioning Services Inc. | Apparatus and Methods for Subsea Control System Testing |
| US20110224835A1 (en) * | 2009-06-03 | 2011-09-15 | Schlumberger Technology Corporation | Integrated flow assurance system |
| WO2012101133A3 (en) * | 2011-01-24 | 2013-01-03 | Services Petroliers Schlumberger | Apparatus for a fluid transport pipeline, related method and system |
| US20130025874A1 (en) * | 2011-07-30 | 2013-01-31 | Robert Saunders | System and method for sampling multiphase fluid at a production wellsite |
| WO2012107727A3 (en) * | 2011-02-09 | 2013-07-18 | Des Operations Limited | Well testing and production apparatus and method |
| WO2013130924A1 (en) * | 2012-03-02 | 2013-09-06 | Services Petroliers Schlumberger | Sampling separation module for subsea and/or surface application |
| US20130284443A1 (en) * | 2012-04-30 | 2013-10-31 | Cameron International Corporation | Sampling Assembly for a Well |
| EP2677115A1 (en) * | 2012-06-22 | 2013-12-25 | Openfield | A predictive flow assurance assessment method and system |
| US20140041446A1 (en) * | 2012-08-13 | 2014-02-13 | Cameron International Corporation | Apparatus and System for Passively Sampling Production Fluid from a Well |
| WO2014039959A1 (en) * | 2012-09-09 | 2014-03-13 | Schlumberger Technology Coroporation | Subsea sampling bottle and system and method of installing same |
| WO2013121212A3 (en) * | 2012-02-15 | 2014-07-10 | Dashstream Limited | Method and apparatus for oil and gas operations |
| US9045973B2 (en) | 2011-12-20 | 2015-06-02 | General Electric Company | System and method for monitoring down-hole fluids |
| US9068436B2 (en) | 2011-07-30 | 2015-06-30 | Onesubsea, Llc | Method and system for sampling multi-phase fluid at a production wellsite |
| US20160061004A1 (en) * | 2014-08-29 | 2016-03-03 | Schlumberger Technology Corporation | Autonomous flow control system and methodology |
| US20160215608A1 (en) * | 2015-01-27 | 2016-07-28 | Cameron International Corporation | Fluid monitoring systems and methods |
| US9441452B2 (en) | 2012-04-26 | 2016-09-13 | Ian Donald | Oilfield apparatus and methods of use |
| WO2016097717A3 (en) * | 2014-12-15 | 2016-09-15 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US9488748B2 (en) | 2011-05-11 | 2016-11-08 | Schlumberger Technology Corporation | System and method for generating fluid compensated downhole parameters |
| US9536122B2 (en) | 2014-11-04 | 2017-01-03 | General Electric Company | Disposable multivariable sensing devices having radio frequency based sensors |
| US9538657B2 (en) | 2012-06-29 | 2017-01-03 | General Electric Company | Resonant sensor and an associated sensing method |
| US9589686B2 (en) | 2006-11-16 | 2017-03-07 | General Electric Company | Apparatus for detecting contaminants in a liquid and a system for use thereof |
| US9611714B2 (en) | 2012-04-26 | 2017-04-04 | Ian Donald | Oilfield apparatus and methods of use |
| US9638653B2 (en) | 2010-11-09 | 2017-05-02 | General Electricity Company | Highly selective chemical and biological sensors |
| US9658178B2 (en) | 2012-09-28 | 2017-05-23 | General Electric Company | Sensor systems for measuring an interface level in a multi-phase fluid composition |
| US9689787B2 (en) | 2010-10-22 | 2017-06-27 | Seabox As | Technical system, method and use for online measuring and monitoring of the particle contents in a flow of injection water in an underwater line |
| US9746452B2 (en) | 2012-08-22 | 2017-08-29 | General Electric Company | Wireless system and method for measuring an operative condition of a machine |
| WO2017178830A1 (en) * | 2016-04-13 | 2017-10-19 | Ian Donald | Apparatus. systems and methods for sampling fluids |
| WO2019045177A1 (en) * | 2017-08-31 | 2019-03-07 | 한명석 | Hydrosphere monitoring system and hydrosphere monitoring device |
| US10267124B2 (en) | 2016-12-13 | 2019-04-23 | Chevron U.S.A. Inc. | Subsea live hydrocarbon fluid retrieval system and method |
| US10267145B2 (en) | 2014-10-17 | 2019-04-23 | Halliburton Energy Services, Inc. | Increasing borehole wall permeability to facilitate fluid sampling |
| EP3477042A1 (en) * | 2017-10-24 | 2019-05-01 | OneSubsea IP UK Limited | Fluid properties measurement using choke valve system |
| US10598650B2 (en) | 2012-08-22 | 2020-03-24 | General Electric Company | System and method for measuring an operative condition of a machine |
| US10684268B2 (en) | 2012-09-28 | 2020-06-16 | Bl Technologies, Inc. | Sensor systems for measuring an interface level in a multi-phase fluid composition |
| IT201900006068A1 (en) * | 2019-04-18 | 2020-10-18 | Saipem Spa | GROUP AND METHOD OF SAMPLING AND MEASUREMENT OF FLUIDS |
| US10895151B2 (en) | 2015-04-13 | 2021-01-19 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US10914698B2 (en) | 2006-11-16 | 2021-02-09 | General Electric Company | Sensing method and system |
| US20220034747A1 (en) * | 2018-12-03 | 2022-02-03 | Petróleo Brasileiro S.A. - Petrobras | System and method for detecting watertightness in the annular space of flexible lines |
| CN114109360A (en) * | 2021-11-16 | 2022-03-01 | 广州海洋地质调查局 | Active excitation type precise evaluation method for vertical content distribution of submarine hydrate reservoir |
| US20220090471A1 (en) * | 2019-01-30 | 2022-03-24 | Enpro Subsea Limited | Apparatus, Systems and Methods for Oil and Gas Operations |
| US12359542B2 (en) | 2021-05-12 | 2025-07-15 | Schlumberger Technology Corporation | Autonomous inflow control device system and method |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9074465B2 (en) * | 2009-06-03 | 2015-07-07 | Schlumberger Technology Corporation | Methods for allocating commingled oil production |
| US8770892B2 (en) * | 2010-10-27 | 2014-07-08 | Weatherford/Lamb, Inc. | Subsea recovery of swabbing chemicals |
| US9057252B2 (en) * | 2011-11-22 | 2015-06-16 | Vetco Gray Inc. | Product sampling system within subsea tree |
| US9880091B2 (en) | 2012-10-16 | 2018-01-30 | Statoil Petroleum As | Method and system for ultrasonic cavitation cleaning in liquid analysis systems |
| GB2557933B (en) * | 2016-12-16 | 2020-01-08 | Subsea 7 Ltd | Subsea garages for unmanned underwater vehicles |
Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3633667A (en) * | 1969-12-08 | 1972-01-11 | Deep Oil Technology Inc | Subsea wellhead system |
| US3636671A (en) * | 1970-07-06 | 1972-01-25 | Harry W Hollister | Access door assembly |
| US5189919A (en) * | 1991-04-29 | 1993-03-02 | Atlantic Richfield Company | Wellhead fluid sampler |
| US6234030B1 (en) * | 1998-08-28 | 2001-05-22 | Rosewood Equipment Company | Multiphase metering method for multiphase flow |
| US6435279B1 (en) * | 2000-04-10 | 2002-08-20 | Halliburton Energy Services, Inc. | Method and apparatus for sampling fluids from a wellbore |
| US20040134662A1 (en) * | 2002-01-31 | 2004-07-15 | Chitwood James E. | High power umbilicals for electric flowline immersion heating of produced hydrocarbons |
| US20040244982A1 (en) * | 2002-08-15 | 2004-12-09 | Chitwood James E. | Substantially neutrally buoyant and positively buoyant electrically heated flowlines for production of subsea hydrocarbons |
| US20050028974A1 (en) * | 2003-08-04 | 2005-02-10 | Pathfinder Energy Services, Inc. | Apparatus for obtaining high quality formation fluid samples |
| US20050028973A1 (en) * | 2003-08-04 | 2005-02-10 | Pathfinder Energy Services, Inc. | Pressure controlled fluid sampling apparatus and method |
| US20060108120A1 (en) * | 2004-11-22 | 2006-05-25 | Energy Equipment Corporation | Well production and multi-purpose intervention access hub |
| US20060272727A1 (en) * | 2005-06-06 | 2006-12-07 | Dinon John L | Insulated pipe and method for preparing same |
| US20070168170A1 (en) * | 2006-01-13 | 2007-07-19 | Jacob Thomas | Real time monitoring and control of thermal recovery operations for heavy oil reservoirs |
| US20070284108A1 (en) * | 2006-04-21 | 2007-12-13 | Roes Augustinus W M | Compositions produced using an in situ heat treatment process |
| US20080135254A1 (en) * | 2006-10-20 | 2008-06-12 | Vinegar Harold J | In situ heat treatment process utilizing a closed loop heating system |
| US20080135239A1 (en) * | 2006-12-12 | 2008-06-12 | Schlumberger Technology Corporation | Methods and Systems for Sampling Heavy Oil Reservoirs |
| US20080149343A1 (en) * | 2001-08-19 | 2008-06-26 | Chitwood James E | High power umbilicals for electric flowline immersion heating of produced hydrocarbons |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6763889B2 (en) * | 2000-08-14 | 2004-07-20 | Schlumberger Technology Corporation | Subsea intervention |
-
2008
- 2008-06-04 GB GB0810189.1A patent/GB2460668B/en active Active
-
2009
- 2009-06-03 US US12/477,190 patent/US20100059221A1/en not_active Abandoned
Patent Citations (36)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3633667A (en) * | 1969-12-08 | 1972-01-11 | Deep Oil Technology Inc | Subsea wellhead system |
| US3636671A (en) * | 1970-07-06 | 1972-01-25 | Harry W Hollister | Access door assembly |
| US5189919A (en) * | 1991-04-29 | 1993-03-02 | Atlantic Richfield Company | Wellhead fluid sampler |
| US6234030B1 (en) * | 1998-08-28 | 2001-05-22 | Rosewood Equipment Company | Multiphase metering method for multiphase flow |
| US6435279B1 (en) * | 2000-04-10 | 2002-08-20 | Halliburton Energy Services, Inc. | Method and apparatus for sampling fluids from a wellbore |
| US20080149343A1 (en) * | 2001-08-19 | 2008-06-26 | Chitwood James E | High power umbilicals for electric flowline immersion heating of produced hydrocarbons |
| US7032658B2 (en) * | 2002-01-31 | 2006-04-25 | Smart Drilling And Completion, Inc. | High power umbilicals for electric flowline immersion heating of produced hydrocarbons |
| US20040134662A1 (en) * | 2002-01-31 | 2004-07-15 | Chitwood James E. | High power umbilicals for electric flowline immersion heating of produced hydrocarbons |
| US7311151B2 (en) * | 2002-08-15 | 2007-12-25 | Smart Drilling And Completion, Inc. | Substantially neutrally buoyant and positively buoyant electrically heated flowlines for production of subsea hydrocarbons |
| US20040244982A1 (en) * | 2002-08-15 | 2004-12-09 | Chitwood James E. | Substantially neutrally buoyant and positively buoyant electrically heated flowlines for production of subsea hydrocarbons |
| US20050028974A1 (en) * | 2003-08-04 | 2005-02-10 | Pathfinder Energy Services, Inc. | Apparatus for obtaining high quality formation fluid samples |
| US7083009B2 (en) * | 2003-08-04 | 2006-08-01 | Pathfinder Energy Services, Inc. | Pressure controlled fluid sampling apparatus and method |
| US20050028973A1 (en) * | 2003-08-04 | 2005-02-10 | Pathfinder Energy Services, Inc. | Pressure controlled fluid sampling apparatus and method |
| US20060108120A1 (en) * | 2004-11-22 | 2006-05-25 | Energy Equipment Corporation | Well production and multi-purpose intervention access hub |
| US20060118308A1 (en) * | 2004-11-22 | 2006-06-08 | Energy Equipment Corporation | Dual bore well jumper |
| US7219740B2 (en) * | 2004-11-22 | 2007-05-22 | Energy Equipment Corporation | Well production and multi-purpose intervention access hub |
| US20060272727A1 (en) * | 2005-06-06 | 2006-12-07 | Dinon John L | Insulated pipe and method for preparing same |
| US20070168170A1 (en) * | 2006-01-13 | 2007-07-19 | Jacob Thomas | Real time monitoring and control of thermal recovery operations for heavy oil reservoirs |
| US20080035348A1 (en) * | 2006-04-21 | 2008-02-14 | Vitek John M | Temperature limited heaters using phase transformation of ferromagnetic material |
| US20080173450A1 (en) * | 2006-04-21 | 2008-07-24 | Bernard Goldberg | Time sequenced heating of multiple layers in a hydrocarbon containing formation |
| US20080035347A1 (en) * | 2006-04-21 | 2008-02-14 | Brady Michael P | Adjusting alloy compositions for selected properties in temperature limited heaters |
| US20070289733A1 (en) * | 2006-04-21 | 2007-12-20 | Hinson Richard A | Wellhead with non-ferromagnetic materials |
| US20080017380A1 (en) * | 2006-04-21 | 2008-01-24 | Vinegar Harold J | Non-ferromagnetic overburden casing |
| US20080173444A1 (en) * | 2006-04-21 | 2008-07-24 | Francis Marion Stone | Alternate energy source usage for in situ heat treatment processes |
| US20080174115A1 (en) * | 2006-04-21 | 2008-07-24 | Gene Richard Lambirth | Power systems utilizing the heat of produced formation fluid |
| US20080173449A1 (en) * | 2006-04-21 | 2008-07-24 | Thomas David Fowler | Sour gas injection for use with in situ heat treatment |
| US20070284108A1 (en) * | 2006-04-21 | 2007-12-13 | Roes Augustinus W M | Compositions produced using an in situ heat treatment process |
| US20080185147A1 (en) * | 2006-10-20 | 2008-08-07 | Vinegar Harold J | Wax barrier for use with in situ processes for treating formations |
| US20080142217A1 (en) * | 2006-10-20 | 2008-06-19 | Roelof Pieterson | Using geothermal energy to heat a portion of a formation for an in situ heat treatment process |
| US20080135244A1 (en) * | 2006-10-20 | 2008-06-12 | David Scott Miller | Heating hydrocarbon containing formations in a line drive staged process |
| US20080135254A1 (en) * | 2006-10-20 | 2008-06-12 | Vinegar Harold J | In situ heat treatment process utilizing a closed loop heating system |
| US20080217004A1 (en) * | 2006-10-20 | 2008-09-11 | De Rouffignac Eric Pierre | Heating hydrocarbon containing formations in a checkerboard pattern staged process |
| US20080217015A1 (en) * | 2006-10-20 | 2008-09-11 | Vinegar Harold J | Heating hydrocarbon containing formations in a spiral startup staged sequence |
| US20080217003A1 (en) * | 2006-10-20 | 2008-09-11 | Myron Ira Kuhlman | Gas injection to inhibit migration during an in situ heat treatment process |
| US20080135239A1 (en) * | 2006-12-12 | 2008-06-12 | Schlumberger Technology Corporation | Methods and Systems for Sampling Heavy Oil Reservoirs |
| US7464755B2 (en) * | 2006-12-12 | 2008-12-16 | Schlumberger Technology Corporation | Methods and systems for sampling heavy oil reservoirs |
Cited By (81)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9589686B2 (en) | 2006-11-16 | 2017-03-07 | General Electric Company | Apparatus for detecting contaminants in a liquid and a system for use thereof |
| US10914698B2 (en) | 2006-11-16 | 2021-02-09 | General Electric Company | Sensing method and system |
| US8430168B2 (en) * | 2008-05-21 | 2013-04-30 | Valkyrie Commissioning Services, Inc. | Apparatus and methods for subsea control system testing |
| US20090288836A1 (en) * | 2008-05-21 | 2009-11-26 | Valkyrie Commissioning Services Inc. | Apparatus and Methods for Subsea Control System Testing |
| US20110224835A1 (en) * | 2009-06-03 | 2011-09-15 | Schlumberger Technology Corporation | Integrated flow assurance system |
| US9689787B2 (en) | 2010-10-22 | 2017-06-27 | Seabox As | Technical system, method and use for online measuring and monitoring of the particle contents in a flow of injection water in an underwater line |
| US9638653B2 (en) | 2010-11-09 | 2017-05-02 | General Electricity Company | Highly selective chemical and biological sensors |
| US10408714B2 (en) | 2011-01-24 | 2019-09-10 | Framo Engineering As | Apparatus for a fluid transport pipeline, related method and system |
| WO2012101133A3 (en) * | 2011-01-24 | 2013-01-03 | Services Petroliers Schlumberger | Apparatus for a fluid transport pipeline, related method and system |
| CN103534438A (en) * | 2011-01-24 | 2014-01-22 | 普拉德研究及开发股份有限公司 | Apparatus for a fluid transport pipeline, related method and system |
| AU2012210633B2 (en) * | 2011-01-24 | 2016-03-17 | Framo Engineering As | Apparatus for a fluid transport pipeline, related method and system |
| US9702249B2 (en) * | 2011-02-09 | 2017-07-11 | Onesubsea Ip Uk Limited | Well testing and production apparatus and method |
| WO2012107727A3 (en) * | 2011-02-09 | 2013-07-18 | Des Operations Limited | Well testing and production apparatus and method |
| US20150184511A1 (en) * | 2011-02-09 | 2015-07-02 | Cameron Systems (Ireland) Limited | Well Testing and Production Apparatus and Method |
| US9488748B2 (en) | 2011-05-11 | 2016-11-08 | Schlumberger Technology Corporation | System and method for generating fluid compensated downhole parameters |
| US9068436B2 (en) | 2011-07-30 | 2015-06-30 | Onesubsea, Llc | Method and system for sampling multi-phase fluid at a production wellsite |
| US20130025874A1 (en) * | 2011-07-30 | 2013-01-31 | Robert Saunders | System and method for sampling multiphase fluid at a production wellsite |
| US9045973B2 (en) | 2011-12-20 | 2015-06-02 | General Electric Company | System and method for monitoring down-hole fluids |
| WO2013121212A3 (en) * | 2012-02-15 | 2014-07-10 | Dashstream Limited | Method and apparatus for oil and gas operations |
| AU2013220167B2 (en) * | 2012-02-15 | 2017-08-31 | Enpro Subsea Limited | Method and apparatus for oil and gas operations |
| US10174575B2 (en) * | 2012-02-15 | 2019-01-08 | Enpro Subsea Limited | Method and apparatus for oil and gas operations |
| AU2017268524B2 (en) * | 2012-02-15 | 2019-12-19 | Enpro Subsea Limited | Method and apparatus for oil and gas operations |
| US9618427B2 (en) | 2012-03-02 | 2017-04-11 | Schlumberger Technology Corporation | Sampling separation module for subsea or surface application |
| WO2013130924A1 (en) * | 2012-03-02 | 2013-09-06 | Services Petroliers Schlumberger | Sampling separation module for subsea and/or surface application |
| US9441452B2 (en) | 2012-04-26 | 2016-09-13 | Ian Donald | Oilfield apparatus and methods of use |
| US9611714B2 (en) | 2012-04-26 | 2017-04-04 | Ian Donald | Oilfield apparatus and methods of use |
| GB2521897B (en) * | 2012-04-30 | 2015-12-23 | Cameron Int Corp | Sampling Assembly for a well |
| GB2521897A (en) * | 2012-04-30 | 2015-07-08 | Cameron Int Corp | Sampling Assembly for a well |
| US20130284443A1 (en) * | 2012-04-30 | 2013-10-31 | Cameron International Corporation | Sampling Assembly for a Well |
| WO2013165747A1 (en) * | 2012-04-30 | 2013-11-07 | Cameron International Corporation | Sampling assembly for a well |
| US8991502B2 (en) * | 2012-04-30 | 2015-03-31 | Cameron International Corporation | Sampling assembly for a well |
| US9777555B2 (en) | 2012-06-22 | 2017-10-03 | Openfield | Predictive flow assurance assessment method and system |
| WO2013190093A3 (en) * | 2012-06-22 | 2014-06-19 | Openfield | A predictive flow assurance assessment method and system |
| EP2677115A1 (en) * | 2012-06-22 | 2013-12-25 | Openfield | A predictive flow assurance assessment method and system |
| WO2013190093A2 (en) | 2012-06-22 | 2013-12-27 | Openfield | A predictive flow assurance assessment method and system |
| US9538657B2 (en) | 2012-06-29 | 2017-01-03 | General Electric Company | Resonant sensor and an associated sensing method |
| GB2521294B (en) * | 2012-08-13 | 2019-11-20 | Cameron Int Corp | Apparatus and system for passively sampling production fluid from a well |
| GB2521294A (en) * | 2012-08-13 | 2015-06-17 | Cameron Int Corp | Apparatus and system for passively sampling production fluid from a well |
| US20140041446A1 (en) * | 2012-08-13 | 2014-02-13 | Cameron International Corporation | Apparatus and System for Passively Sampling Production Fluid from a Well |
| WO2014028228A1 (en) * | 2012-08-13 | 2014-02-20 | Cameron International Corporation | Apparatus and system for passively sampling production fluid from a well |
| US9551215B2 (en) * | 2012-08-13 | 2017-01-24 | Onesubsea Ip Uk Limited | Apparatus and system for passively sampling production fluid from a well |
| US9746452B2 (en) | 2012-08-22 | 2017-08-29 | General Electric Company | Wireless system and method for measuring an operative condition of a machine |
| US10598650B2 (en) | 2012-08-22 | 2020-03-24 | General Electric Company | System and method for measuring an operative condition of a machine |
| WO2014039959A1 (en) * | 2012-09-09 | 2014-03-13 | Schlumberger Technology Coroporation | Subsea sampling bottle and system and method of installing same |
| US9658178B2 (en) | 2012-09-28 | 2017-05-23 | General Electric Company | Sensor systems for measuring an interface level in a multi-phase fluid composition |
| US10684268B2 (en) | 2012-09-28 | 2020-06-16 | Bl Technologies, Inc. | Sensor systems for measuring an interface level in a multi-phase fluid composition |
| US9896906B2 (en) * | 2014-08-29 | 2018-02-20 | Schlumberger Technology Corporation | Autonomous flow control system and methodology |
| US20160061004A1 (en) * | 2014-08-29 | 2016-03-03 | Schlumberger Technology Corporation | Autonomous flow control system and methodology |
| US10267145B2 (en) | 2014-10-17 | 2019-04-23 | Halliburton Energy Services, Inc. | Increasing borehole wall permeability to facilitate fluid sampling |
| US9536122B2 (en) | 2014-11-04 | 2017-01-03 | General Electric Company | Disposable multivariable sensing devices having radio frequency based sensors |
| EP3412862A1 (en) * | 2014-12-15 | 2018-12-12 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| WO2016097717A3 (en) * | 2014-12-15 | 2016-09-15 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US11142984B2 (en) | 2014-12-15 | 2021-10-12 | Enpro Subsea Limited | Apparatus, systems and method for oil and gas operations |
| EP3789581A1 (en) * | 2014-12-15 | 2021-03-10 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US10480274B2 (en) | 2014-12-15 | 2019-11-19 | Enpro Subsea Limited | Apparatus, systems and method for oil and gas operations |
| EP3234303B1 (en) | 2014-12-15 | 2018-08-15 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US20160215608A1 (en) * | 2015-01-27 | 2016-07-28 | Cameron International Corporation | Fluid monitoring systems and methods |
| US10287869B2 (en) * | 2015-01-27 | 2019-05-14 | Cameron International Corporation | Fluid monitoring systems and methods |
| WO2016123252A1 (en) * | 2015-01-27 | 2016-08-04 | Cameron International Corporation | Fluid monitoring systems and methods |
| US10895151B2 (en) | 2015-04-13 | 2021-01-19 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| US10871424B2 (en) * | 2016-04-13 | 2020-12-22 | Enpro Subsea Limited | Apparatus, systems and methods for sampling fluids |
| WO2017178830A1 (en) * | 2016-04-13 | 2017-10-19 | Ian Donald | Apparatus. systems and methods for sampling fluids |
| GB2564983A (en) * | 2016-04-13 | 2019-01-30 | Enpro Subsea Ltd | Apparatus, systems and methods for sampling fluids |
| GB2564983B (en) * | 2016-04-13 | 2022-07-20 | Enpro Subsea Ltd | Apparatus, systems and methods for sampling fluids |
| AU2017250440B2 (en) * | 2016-04-13 | 2021-12-02 | Enpro Subsea Limited | Apparatus. systems and methods for sampling fluids |
| US10267124B2 (en) | 2016-12-13 | 2019-04-23 | Chevron U.S.A. Inc. | Subsea live hydrocarbon fluid retrieval system and method |
| KR20190024202A (en) * | 2017-08-31 | 2019-03-08 | 한명석 | Hydrosphere monitoring system and hydrosphere monitoring device |
| KR101982927B1 (en) * | 2017-08-31 | 2019-08-28 | 한명석 | Hydrosphere monitoring system and hydrosphere monitoring device |
| WO2019045177A1 (en) * | 2017-08-31 | 2019-03-07 | 한명석 | Hydrosphere monitoring system and hydrosphere monitoring device |
| US10502054B2 (en) | 2017-10-24 | 2019-12-10 | Onesubsea Ip Uk Limited | Fluid properties measurement using choke valve system |
| EP3477042A1 (en) * | 2017-10-24 | 2019-05-01 | OneSubsea IP UK Limited | Fluid properties measurement using choke valve system |
| US20220034747A1 (en) * | 2018-12-03 | 2022-02-03 | Petróleo Brasileiro S.A. - Petrobras | System and method for detecting watertightness in the annular space of flexible lines |
| US11940352B2 (en) * | 2018-12-03 | 2024-03-26 | Petróleo Brasileiro S.A.—Petrobras | System and method for detecting watertightness in the annular space of flexible lines |
| US20220090471A1 (en) * | 2019-01-30 | 2022-03-24 | Enpro Subsea Limited | Apparatus, Systems and Methods for Oil and Gas Operations |
| US11982161B2 (en) * | 2019-01-30 | 2024-05-14 | Enpro Subsea Limited | Apparatus, systems and methods for oil and gas operations |
| WO2020212932A1 (en) * | 2019-04-18 | 2020-10-22 | Saipem S.P.A. | Fluid sampling and measuring assembly and method |
| IT201900006068A1 (en) * | 2019-04-18 | 2020-10-18 | Saipem Spa | GROUP AND METHOD OF SAMPLING AND MEASUREMENT OF FLUIDS |
| US11952890B2 (en) | 2019-04-18 | 2024-04-09 | Saipem S.P.A. | Fluid sampling and measuring assembly and method |
| AU2020259398B2 (en) * | 2019-04-18 | 2025-11-13 | Saipem S.P.A. | Fluid sampling and measuring assembly and method |
| US12359542B2 (en) | 2021-05-12 | 2025-07-15 | Schlumberger Technology Corporation | Autonomous inflow control device system and method |
| CN114109360A (en) * | 2021-11-16 | 2022-03-01 | 广州海洋地质调查局 | Active excitation type precise evaluation method for vertical content distribution of submarine hydrate reservoir |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2460668B (en) | 2012-08-01 |
| GB2460668A (en) | 2009-12-09 |
| GB0810189D0 (en) | 2008-07-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US20100059221A1 (en) | Subsea fluid sampling and analysis | |
| US9322747B2 (en) | Isothermal subsea sampling system and method | |
| US9068436B2 (en) | Method and system for sampling multi-phase fluid at a production wellsite | |
| US8245572B2 (en) | System and method for analysis of well fluid samples | |
| US9702249B2 (en) | Well testing and production apparatus and method | |
| US8256283B2 (en) | Method of downhole characterization of formation fluids, measurement controller for downhole characterization of formation fluids, and apparatus for downhole characterization of formation fluids | |
| US20130025874A1 (en) | System and method for sampling multiphase fluid at a production wellsite | |
| BR102012029292B1 (en) | methods of cementing a tubular column in a well, an underwater well and a well that extends from a wellhead | |
| US11320347B1 (en) | Portable, high temperature, heavy oil well test unit with automatic multi sampling system | |
| EA024498B1 (en) | Fluid sampling assembly | |
| US11035231B2 (en) | Apparatus and methods for tools for collecting high quality reservoir samples | |
| US20090178797A1 (en) | Groundwater monitoring technologies applied to carbon dioxide sequestration | |
| US20090250214A1 (en) | Apparatus and method for collecting a downhole fluid | |
| US9926782B2 (en) | Automated fluid fraction sampling system | |
| US20090255672A1 (en) | Apparatus and method for obtaining formation samples | |
| US20180112527A1 (en) | Apparatus, systems and methods for oil and gas operations | |
| US12428960B2 (en) | Systems and methods for well testing | |
| Aghar et al. | The expanding scope of well testing | |
| WO2001077489A1 (en) | A method of conducting in situ measurements of properties of a reservoir fluid | |
| WO2012161588A1 (en) | Method and device for filling a submerged sample bottle | |
| EP1282760A1 (en) | A method of conducting in situ measurements of properties of a reservoir fluid |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: SCHLUMBERGER TECHNOLOGY CORPORATION,TEXAS Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:VANNUFFELEN, STEPHANE;VASQUES, RICARDO;YAMATE, TSUTOMU;AND OTHERS;SIGNING DATES FROM 20090713 TO 20090824;REEL/FRAME:023358/0004 |
|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |