GB2467792A - Fluid injection apparatus and method - Google Patents
Fluid injection apparatus and method Download PDFInfo
- Publication number
- GB2467792A GB2467792A GB0902585A GB0902585A GB2467792A GB 2467792 A GB2467792 A GB 2467792A GB 0902585 A GB0902585 A GB 0902585A GB 0902585 A GB0902585 A GB 0902585A GB 2467792 A GB2467792 A GB 2467792A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fluid
- injection
- additive
- injection apparatus
- line
- 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.)
- Granted
Links
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B37/00—Methods or apparatus for cleaning boreholes or wells
- E21B37/06—Methods or apparatus for cleaning boreholes or wells using chemical means for preventing, limiting or eliminating the deposition of paraffins or like substances
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17D—PIPE-LINE SYSTEMS; PIPE-LINES
- F17D3/00—Arrangements for supervising or controlling working operations
- F17D3/12—Arrangements for supervising or controlling working operations for injecting a composition into the line
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01F—MEASURING VOLUME, VOLUME FLOW, MASS FLOW OR LIQUID LEVEL; METERING BY VOLUME
- G01F11/00—Apparatus requiring external operation adapted at each repeated and identical operation to measure and separate a predetermined volume of fluid or fluent solid material from a supply or container, without regard to weight, and to deliver it
Abstract
An apparatus for selectively injecting an additive fluid into a process fluid comprises an additive fluid supply line 13 having a pump 12. It also has an injection line 11 for delivering additive fluid to the process fluid, and a directional control valve 25 in the injection line operable between an open position in which it permits flow of the additive fluid in the injection line and a closed position in which it interrupts flow. The apparatus further includes a control means 18 for selecting a pulse rate for the directional control valve to control the flow rate of the additive fluid in the injection line. The pulse rate may be selected in response to a parameter of the additive, such as pressure or viscosity. The injector may be used to ensure that formation fluid flowing through a well is not inhibited by solidification of paraffin wax.
Description
FLUID INJECTION APPARATUS AND METHOD
The present invention relates to fluid injection apparatus and a method for selectively injecting an additive fluid into a process fluid.
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process fluid flowing through a well andlor pipeline with a chemical additive on a continuous or intermittent basis in order to ensure that the well continues to operate efficiently. For example, methanol or another suitable substance may be injected to inhibit the solidification of paraffin wax on the walls of the well or pipeline as this serves to restrict the process flow and may serve to inhibit the operation of valves within the pipeline. Other examples include hydrate, scale or corrosion inhibitors.
Injection of the chemical additive may be required at a variable rate depending on the flow conditions or pressure within the well or pipeline and a slow injection rate is often necessary to inhibit wax or hydrate formation.
In sub-sea applications the injection apparatus must be reliable as access for cleaning, repair or maintenance is difficult.
It is known to use a variable pump to control the chemical injection rate. One example of this is a hydraulically actuated diaphragm pump available from Milton Roy. Such a pump is typically operated by a controller or, alternatively, a solenoid and a plunger is displaced in a cylinder to displace hydraulic fluid on one side of a diaphragm. This serves to deflect the diaphragm which, in turn, displaces the chemical such that it is injected into the process flow.
In an alternative approach that is used in particular for slow flow rates, a pressure compensated flow valve injects the chemical at a consistent flow rate irrespective of upstream or downstream pressure changes. The variable inlet flow is incident on a first side of a piston and passes through a bleed path in the piston. The bleed path has an orifice so as to generate a pressure drop across the piston. The resultant force moves the piston against a biasing spring and a variable throttle, part of which is formed on the piston serves to maintain a constant outlet flow regardless of the inlet flow rate. In some applications it has been found that such valves are not particularly accurate. Moreover, they rely on delivering the chemical through small orifices or flow paths which have a tendency to become blocked by contaminants.
Since such valves are often situated sub sea it is a difficult process to get access to them for cleaning purposes. Multi-plate filter baffles have been employed to address this problem but these also have a tendency to become clogged with contaminants and restrict the flow.
Ti c. .-n, nl.ianf,-f' thin;n,,antinn tin nh,,intci rir rnitirtntc. th nhnro nnrl It 10 (211 LiLJJLSJL Lit tII'..i}J1�.0�..I1l. IIIVLIILI'..JIi i.J LJ(JVIUL'.d Lit lllltt5UtL L!1�.. UUt.JV� (211(1 other, disadvantages. U is also an object of the present invention to provide for improved, or alternative, fluid injection apparatus.
According a first aspect of the present invention there is provided fluid injection apparatus for selectively injecting an additive fluid into a process fluid at a given location comprising: an additive fluid supply line having a pump for pumping the additive fluid; at least one injection line for delivering additive fluid to the process fluid at the given location; a directional control valve in the injection line operable between an open position in which it permits flow of the additive fluid in the injection line and a closed position in which it interrupts the flow; a controller for sending a pulsed control signal at a selected pulse rate to the directional control valve to control the flow rate of the additive fluid in the injection line.
The apparatus of the present invention provides for a relatively simple, reliable and accurate way of modulating the flow rate of fluid. The pulse rate effectively controls the flow rate of the fluid in the injection line and can be used to deliver fluid accurately at a wide range of flow rates The controller may be configured to vary the pulse rate in response to at least one parameter of the additive fluid which may be, for example, a detected pressure difference between the additive fluid in the supply line and the injection line. In order to determine the pressure difference a pressure sensor may be provided in the supply line and similarly a pressure sensor may be provided in the injection line. In each case the pressure sensors may transmit signals representative of the sensed pressure to the controller. In addition, or alternatively, the variation in pulse rate may be dependent on the viscosity of the fluid.
The pulsed control signal may be an electrical signal or, alternatively, it may be a pneumatic or hydraulic signal for a pilot inlet of the directional control valve. In the case of an electrical signal the directional control valve may be solenoid-operated.
The controller may be a programmable logic controller. It may store a look-up table in memory for determining the pulse rate based on the sensed pressure difference.
There may be a fluid additive fluid reservoir connected to the supply line. The pump may have an inlet in flow communication with an outlet of the reservoir.
The pump may be configured to maintain a constant supply line pressure and may be driven by a variable speed motor with an inverter drive. The inverter drive is preferably controlled by the controller.
There may be provided at least one fluid damper in the supply line and/or in the injection line.
There may be provided a plurality of injection lines each with its directional control valve. The directional control valves may be controlled so as to provide different flow rates in each of the injection lines.
According to a second method of the present invention there is provided a method for selectively injecting an additive fluid into a process fluid comprising: delivering an additive fluid from a supply line to at least one injection line for onward delivery to the process fluid; operating a directional control valve in the injection line in a pulsed manner between an open position to permits flow of the additive fluid in the injection line and a closed position in order to interrupts the flow; selecting a pulse rate for the directional control valve to control the flow rate of the additive fluid in the injection line.
The pulse rate is selected in response to at least one parameter of the additive fluid such as, for example, a pressure difference in the additive fluid between the supply line and injection line. Account may also be taken of other inherent fluid parameters such as, for example, viscosity.
A specific embodiment of the invention will now be described, by way of example only, with reference to the accompanying drawings, in which: Figure 1 is a schematic circuit diagram of a chemical injection control system in accordance with the present invention; and Figure 2 is a graph showing exemplary solenoid calibration curves in the form of a plot of flow rate against solenoid control pulses per minute.
Referring now to figure 1, a chemical fluid additive for injection into a well, pipeline or the like is stored in a reservoir 10 and delivered to a plurality of injection lines I I a, 11 b, II c etc.. A hydraulic pump 12 delivers the fluid to a supply line 13 for onward transmission to the injection lines ha, lib, lic etc. The pump 12 has an inlet 14 connected to an outlet 15 01 the reservoir 10 and is driven by a variable speed motor 1 6 with an inverter drive 1 7 that is operated under the control of a programmable logic controller (PLC) 18.
The supply line 13 is fitted with a first pressure sensor 20 for determining the fluid pressure leaving the pump 12. The pressure reading is converted into an electrical signal that is transmitted to the PLC 1 8. Immediately downstream of the first pressure sensor 20 there is a damper accumulator 21 for damping significant pressure fluctuations in the fluid and a filter 22 for removing contaminants before the fluid is injected into the well or pipeline. The plurality of injection lines 11 a, b, c are connected to a point downstream of the filter 22 and each such injection line has a calibrated fixed orifice 23, a second pressure sensor 24 and a directional control valve 25.
The second pressure sensor 24 operates in the same manner as the first sensor and sends an electrical signal representative of the pressure in the respective injection line ha, b, c, etc. to the PLC 18. Each fixed orifice 23 is calibrated accurately at a particular set point such that for a given pressure drop (determined by the difference in readings between the first and second pressure sensors 20, 24) across the orifice the flow rate through the orifice 23 is known.
Each of the directional control valves 25 is a solenoid-controlled, two-position, two-port, spring return valve with the operation of the solenoid being controlled by electrical signal sent from the PLC 18 along the line indicated by reference number 26. Each valve 25 is depicted in its normally closed position (to which it is biased by the return spring) where it blocks the respective injection line 11 a, b, c but is moved to the open position by the solenoid upon receipt of a control signal from the PLC 18. The signal delivered to the solenoid is pulsed so as to actuate the valve 25 between on and off positions. The pulse rate selected is dependent on the desired flow rate and the pressure drop (Dp) between the upstream supply line 13 and the downstream injection line 11 a,b, or c etc. as determined from the pressure sensor 20, 23 readings. The PLC uses empirical data to modulate the pulse rate to achieve the desired flow rate in the injection line. This data is shown in the form of a graph in figure 2. The graph is effectively stored as a look-up table in a memory associated with the PLC 18. In figure 2 there is shown a number of plots of fluid flow rate Q in litres per minute (x axis) against the pU1SC ratc (pulses per minute), each plOt being for a different pressure drop (Dp) represented in bar. It will be appreciated that the graphs will vary for different viscosities of the chemical being injected.
It will be appreciated that any number of injection lines may be provided depending on the number of wells. Each line may be operated with a different flow rate. in the exemplary embodiment shown in figure 2 five injection lines 1 la-I le are shown but any number may be provided. In the figure only the first and second injection lines 1 la and 1 lb are shown with directional control valves 25 -the valves and other components being omitted from the subsequent injection lines lic to lie for clarity.
The upstream pressure is maintained substantially constant by the motor and inverter control.
The configuration allows a single upstream supply line 13 to be provided on shore or on a platform or floating vessel with the multiple injections lines lla-e etc. being provided sub sea. Alternatively the injection lines may also be on shore or otherwise above the sea.
It is will be appreciated by one of ordinary skill in the art that the invention has been described by way of example only, and that the invention itself is defined by the claims. Numerous modifications and variations may be made to the exemplary design described above without departing from the scope of the invention as defined in the claims. For example, the solenoid of each directional control valve need not necessarily be controlled by pulsed electrical signals. In an alternative arrangement the solenoid is replaced by a piloting piston device that is provided with pulsed pressure signals (e.g. pneumatic) provided by a suitable controller. Furthermore, the data stored in the PLC 18 for determining the appropriate pulse rate may be other than empirical.
The described and illustrated embodiments are to be considered as illustrative and not restrictive in character, it being understood that only the. preferred embodiments have been shown and described and that all changes and modifications that come within the scope of the inventions as defined in the claims are desired to be protected. It should be understood that while the use of words such as "preferable", "preferably", "preferred" or "more preferred" in the description suggest that a feature so described may be desirable, it may nevertheless not be necessary and cmbodimcnts lacking such a feature may be contemplated as within the scope of the invention as defined in the appended claims. In relation to the claims, it is intended that when words such as "a," "an," "at least one," or "at least one portion" are used to preface a feature there is no intention to limit the claim to only one such feature unless specifically stated to the contrary in the claim. When the language "at least a portion" and/or "a portion" is used the item can include a portion and/or the entire item unless specifically stated to the contrary.
Claims (18)
- CLAIMSFluid injection apparatus for selectively injecting an additive fluid into a process fluid at a given location comprising: an additive fluid supply line having a pump for pumping the additivc fluid; at least one injection line for delivering additive fluid to the process fluid at the given location; a directional control valve in the injection line operable between an open position in which it permits flow of the additive fluid in the injection line and a closed position in which it interrupts the flow; a controller for sending a pulsed control signal at a selected pulse rate to the directional control valve to control the flow rate of the additive fluid in the injection line.
- 2. Fluid injection apparatus according to claim 1, wherein the controller is configured to vary the pulse rate in response to at least one parameter of the additive fluid.
- 3. Fluid injection apparatus according to claim 2, wherein the at least one parameter is a detected pressure difference between the additive fluid in the supply line and the injection line.
- 4. Fluid injection apparatus according to claim 2, wherein the at least one parameter is the viscosity of the additive fluid.
- 5. Fluid injection apparatus according to any one of claims 1 to 4, wherein the pulsed control signal is an electrical signal.
- 6. Fluid injection apparatus according to claim 5, wherein the directional control valve is solenoid-operated.
- 7. Fluid injection apparatus according to any preceding claim, wherein the controller is a programmable logic controller.
- 8. Fluid injection apparatus according to any preceding claim, further comprising an additive fluid reservoir connected to thc supply line.
- 9. Fluid injection apparatus according to any preceding claim, wherein the pump is configured to maintain a constant supply line pressure.
- 10. Fluid injection apparatus according to claim 9, wherein the pump is driven by a variable speed motor with an inverter drive.
- 11. Fluid injection apparatus according to claim 9, wherein the inverter drive is controlled by the controller.
- 12. Fluid injection apparatus according to any preceding claim, wherein there is provided at least one fluid damper in the supply line.
- 13. Fluid injection apparatus according to any preceding claim, wherein there is provided at least one fluid damper in the injection line.
- 14. Fluid injection apparatus according to any preceding claim, wherein there is provided at least one pressure sensor in the supply line or the injection line.
- 15. Fluid injection apparatus according to any preceding claim, wherein there is provided a plurality of injection lines each with a directional control valve.
- 16. A method for selectively injecting an additive fluid into a process fluid comprising: delivering an additive fluid from a supply line to at least one injection line for onward delivery to the process fluid; operating a directional control valve in the injection line in a pulsed manner between an open position to permit flow of the additive fluid in the injection line and a closed position in order to interrupt the flow; selecting a pulse rate for the directional control valve to control the flow rate of the additive fluid in the injection line.
- 1 7. A method according to claim 1 5, wherein the pulse rate is selected in response to at least one parameter of the additive fluid.
- 1 8. A method according to claim 16, wherein the at least parameter is a pressure difference in the additive fluid between the supply line and injection line.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0902585A GB2467792B (en) | 2009-02-17 | 2009-02-17 | Fluid injection apparatus and method |
PCT/GB2010/000269 WO2010094911A2 (en) | 2009-02-17 | 2010-02-15 | Fluid injection apparatus and method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0902585A GB2467792B (en) | 2009-02-17 | 2009-02-17 | Fluid injection apparatus and method |
Publications (3)
Publication Number | Publication Date |
---|---|
GB0902585D0 GB0902585D0 (en) | 2009-04-01 |
GB2467792A true GB2467792A (en) | 2010-08-18 |
GB2467792B GB2467792B (en) | 2013-05-08 |
Family
ID=40548285
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB0902585A Expired - Fee Related GB2467792B (en) | 2009-02-17 | 2009-02-17 | Fluid injection apparatus and method |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB2467792B (en) |
WO (1) | WO2010094911A2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104141474B (en) * | 2014-08-01 | 2016-08-24 | 陈志军 | Environment-friendly type Oil/gas Well medicine adding vehicle and method of work thereof |
CN104847307B (en) * | 2015-05-26 | 2017-10-13 | 中国石油集团渤海石油装备制造有限公司 | A kind of well-washing wax-cleaning car LNG pretreatment units and its processing method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5209300A (en) * | 1992-02-04 | 1993-05-11 | Ayres Robert N | Pressure regulated chemical injection system |
US5517593A (en) * | 1990-10-01 | 1996-05-14 | John Nenniger | Control system for well stimulation apparatus with response time temperature rise used in determining heater control temperature setpoint |
WO2004016904A1 (en) * | 2002-08-14 | 2004-02-26 | Baker Hughes Incorporated | Subsea chemical injection unit for additive injection and monitoring system for oilfield operations |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4007755A (en) * | 1974-01-18 | 1977-02-15 | Sun Oil Company Of Pennsylvania | Component injection system |
US7389787B2 (en) * | 1998-12-21 | 2008-06-24 | Baker Hughes Incorporated | Closed loop additive injection and monitoring system for oilfield operations |
US7318476B2 (en) * | 2004-11-16 | 2008-01-15 | Ayres Robert M | Automatic chemical treatment system with integral flush fluid dispenser |
US20090095351A1 (en) * | 2007-07-16 | 2009-04-16 | Boss Packaging Inc. | Pipeline additive control device and method |
-
2009
- 2009-02-17 GB GB0902585A patent/GB2467792B/en not_active Expired - Fee Related
-
2010
- 2010-02-15 WO PCT/GB2010/000269 patent/WO2010094911A2/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5517593A (en) * | 1990-10-01 | 1996-05-14 | John Nenniger | Control system for well stimulation apparatus with response time temperature rise used in determining heater control temperature setpoint |
US5209300A (en) * | 1992-02-04 | 1993-05-11 | Ayres Robert N | Pressure regulated chemical injection system |
WO2004016904A1 (en) * | 2002-08-14 | 2004-02-26 | Baker Hughes Incorporated | Subsea chemical injection unit for additive injection and monitoring system for oilfield operations |
Also Published As
Publication number | Publication date |
---|---|
WO2010094911A2 (en) | 2010-08-26 |
GB0902585D0 (en) | 2009-04-01 |
WO2010094911A3 (en) | 2010-10-21 |
GB2467792B (en) | 2013-05-08 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 20200217 |