FIELD OF THE INVENTION
[0001] The present invention relates to an injection device for injecting a fluid to a target
location, such as into a downhole location.
BACKGROUND TO THE INVENTION
[0002] Many industries require fluids to be delivered, or injected, from a source to a target
location. For example, in the oil and gas industry many well completions include a
means of injecting chemicals into the wellbore at a point in the completion for the
purposes of corrosion reduction, scale reduction, hydrate reduction, well stimulation,
a variety of optimisation strategies or the like. It is highly desirable to be able
to control the rate of injection, and in typical applications the preference is to
permit a relatively constant rate of injection to be achieved, irrespective of and
pressure fluctuations within the system. Injection may also be required at other locations,
such as into the wellbore, associated formation, annulus and the like. Injection could
also be required at a subsea location, such as at a Christmas tree, flow line, jumper,
manifold, wing line or the like. Some other examples of injection in the oil and gas
industry include downhole injection of a fluid to assist production.
US Patent Document 3,125,113 A discloses a valve for a gas lift system which shows some of the features of the injection
valve of the invention.
[0003] A typical wellbore completion installation with injection capabilities is diagrammatically
illustrated in Figure 1. The wellbore, generally identified by reference numeral 10,
comprises a casing string 12 located within a drilled bore 14 which extends from surface
16 to intercept a hydrocarbon bearing formation 18. A lower annulus area 20 defined
between the casing 12 and bore 14 may be filled with cement 22 for purposes of support
and sealing. A production tubing string 24 extends into the casing 12 from a wellhead
26 and production tree 28. A lower end of the production tubing string 24 is sealed
against the casing 12 with a production packer 30 to isolate a producing zone 32.
A number of perforations 34 are established through the casing 12 and cement 22 to
establish fluid communication between the casing 12 and the formation 18. Hydrocarbons
may then be permitted to flow into the casing 12 at the producing zone 32 and then
into the production tubing 24 via inlet 36 to be produced to surface. Artificial lift
equipment, such as an electric submersible pump (ESP) 37 may optionally be installed
inline with the production tubing 24 as part of the completion to assist production
to surface. The production tree 28 may provide the necessary pressure barriers and
provides a production outlet 38 from which produced hydrocarbons may be delivered
to a production facility (not shown), for example.
[0004] A small bore injection line or conduit 40, which is often referred to as a capillary
line, runs alongside the production tubing 24 from a surface located injection fluid
source 42 to a downhole target location, which in the illustrated example is a lower
end of the production tubing 24, below the ESP 37. The production tubing 24 may include
an optional injection mandrel 44. An injection pump 46 is located at a topside location
to facilitate injection of the injection fluid 42.
[0005] An injection valve 48 is located in a lower region of the injection line 40 and functions
to permit fluid injection into the production tubing 24, in some cases preferentially
at a constant injection rate, while preventing reverse flow back into the injection
line 40. Known valves for such purposes include an injection check valve, such as
illustrated in Figure 2. In this example the check valve 48 includes a housing 50
with an inlet 52 for communicating with the injection line 40 and an outlet 54 for
communicating with the production tubing 24. A poppet member 56 (other similar members
such as pistons and balls are also known) is mounted in the housing 50 and is biased
by a spring 58 towards a closed position in which the poppet 56 sealingly engages
a seat 60 to prevent flow through the housing 50. To permit injection the fluid pressure
at the inlet 52 must establish a downward force on the poppet 56 which exceeds the
combined force of the spring 58 and the pressure at the outlet 54, which act in the
opposing direction. Accordingly, in normal flow conditions the inlet pressure will
be a fixed differential above the outlet pressure by a magnitude dictated primarily
by the force of the spring 58, and also by any back-pressure created at the inlet
by the effect of the poppet 56 and seat defining a flow restriction. An exemplary
graphical representation of the effects of varying the inlet or outlet pressures is
provided in Figure 3. As shown, irrespective of pressure fluctuations at the outlet
54, the inlet pressure 62 will always be a fixed value above the outlet pressure 64
by a differential 66 which is defined primarily by the spring 58.
[0006] In chemical injection there is always a hydrostatic pressure gradient present in
the injection line 40. This pressure gradient is a function of the density of the
fluid and the true vertical height of the well known as the TVD (True Vertical Depth).
As depth increases, the hydrostatic pressure will linearly increase, such that the
maximum hydrostatic pressure will act at the inlet 52 of the injection valve 48. This
hydrostatic pressure will act in a direction to open the valve poppet member 56 against
the combined resistance of the spring 58 and the pressure at the valve outlet 54,
which will be largely equal to the pressure within the production tubing 24 at the
point of injection. There may be circumstances where the hydrostatic pressure force
acting at the valve inlet 52 exceeds the resistance provided by the valve outlet pressure
and the spring 58, for example where large hydrostatic pressures exist in deeper wells,
and/or where relatively low wellbore pressures exist, for example due to operation
of the ESP 37. In such circumstances the result can be the undesirable flow or cascading
of injection fluid into the target location. This effect may be termed "hydrostatic
fall-through".
[0007] If unchecked such hydrostatic fall-through will occur until the hydrostatic pressure
within the injection line 40 is in equilibrium with the target location pressure and
the resistance provided by the valve spring 58. If the injection fluid is not continuously
replenished, or not replenished as quickly as the injection fluid cascades through
the valve 48, then the result will be the creation of low, vacuum or near vacuum pressures
in the upper region of the injection line 40. Such a vacuum may present the injection
line 40 to adverse mechanical forces and stresses, such as radial collapse forces.
Furthermore, the established vacuum may be defined by a pressure which is lower than
the vapour pressure of the injection fluid, thus causing the injection fluid to boil.
This may be compounded by the effect of the increased temperatures associated with
wellbore environments. The consequence of vacuum occurrence in chemical injection
lines is that the original fluid may not be able to retain its intended state and
the fluid carrier will boil off. This has the potential of many adverse effects, such
as solid depositing, viscosity change, crystal formation, waxing, partial or full
solidification, and generally changes within the fluid causing loss of effectiveness
of the injection chemical, and the like.
[0008] To provide a numerical example, for an injection line which has a TVD of 1420 meters
with an injection fluid having a density of 1050 kg/m
3, the hydrostatic pressure (calculated by the product of fluid density, gravity and
TVD) acting at the inlet 52 of the valve 48 will be in the region of 146 bar. If the
pressure in the production tubing 24 at the point of injection is 95 bar, and assuming
that the valve spring 58 and other flow resistance is equivalent to providing 2 bar
of pressure resistance, then this creates a pressure differential across the valve
of 49 bar. Accordingly, due to the tendency for the system to seek equilibrium the
injection fluid within the injection line 40 will cascade through the valve 48 until
the height of injection fluid establishes a hydrostatic pressure at the valve inlet
52 which is in equilibrium with the pressure in the production tubing plus other resistance,
which in the present example will be 97 bar. Thus, a hydrostatic pressure of 97 bar
at the valve inlet 52 will require the injection fluid to cascade to define a height
of around 942 metres. This will therefore leave the upper 478 meters of the injection
line 40 under vacuum conditions, which is graphically illustrated in Figure 4.
[0009] Such hydrostatic fall-through may be addressed by increasing the spring force rating
of the spring 58. This will function to increase the resistance to flow through the
valve 48, such that a greater pressure differential between valve inlet 52 and outlet
54 can be accommodated before the onset of hydrostatic fall-through. A graphical example
of the use of a more powerful valve spring is illustrated in Figure 5. As in the previous
graphical example of Figure 3, the effect of the spring is such that irrespective
of pressure fluctuations at the valve outlet 54, the inlet pressure 70 will always
be a fixed value above the outlet pressure 72 by the differential 68. In this exemplary
case a differential of around 80 bar is established by a more powerful spring, and
such a spring would prevent the occurrence of hydrostatic fall-through in the specific
numerical example provided above.
[0010] However, the size of a valve spring may be limited by the size of the injection valve
and available space to accommodate deployment and installation of such a valve. Further,
in circumstances where very large pressure differentials exist, the required size
of a valve spring may be impossible to accommodate within the valve.
[0011] In addition to establishing a desired pressure differential across a valve using
a spring, it is also known in the art to utilise the effect of a flow restriction
within a valve to establish a desired backpressure within the injection line 40. Also,
such a flow restriction may be variable to ensure a consistent injection flow rate
can be achieved irrespective of the pressure differential.
[0012] As described above, in known injection valves a fixed differential between valve
inlet and outlet is provided. Thus, the expectation and desire is that the valve inlet
pressure will track any variations in the outlet pressure by the fixed differential.
The intention of this is to prevent hydrostatic fall-through, and to facilitate a
relatively constant injection rate. However, in certain circumstances, for example
where the outlet pressure should drop, for example due to activation of an ESP, it
has been observed that there is an unexpected sudden rush of injection fluid through
the valve. This is contrary to expectation, which is that a substantially continuous
injection rate should be achieved by self-adjustment of the valve to maintain the
fixed pressure differential between inlet and outlet. Further, such a sudden rush
of injection fluid through the valve may cause damage to the valve.
[0013] Furthermore, in the exemplary completion system shown in Figure 1 an optional ESP
37 is provided, wherein the injection fluid is injected upstream, or on the inlet
side of the ESP 37. The injection fluid may function to inhibit scale and the like
within the ESP 37, to condition the production fluids to permit more efficient pumping,
for example by reducing the viscosity of the production fluids, and the like. In this
respect, when the ESP 37 is activated the pressure at the pump inlet, and thus at
the injection location will fall. As described above, the injection valve 48 should
permit this fall in pressure to be accommodated and ensure that the injection line
pressure is maintained at a fixed differential above the target location pressure,
and self-adjusts to ensure a consistent flow rate of injection fluid.
[0014] Expected, and indeed desired pressure profiles at the inlet and outlet of the ESP
37, and at the inlet 52 of the valve 48 is graphically illustrated in Figure 6. In
this respect, as the ESP 37 is activated the pump inlet pressure 74 should fall, and
the pump outlet pressure 76 should rise, until a steady state running condition is
preferably achieved. In view of the fixed pressure differential provided by the valve
48, illustrated by line 78 in Figure 6, the inlet pressure 80 of the valve 48 will
be maintained at a fixed value above the inlet pressure 74 of the pump 37, and will
thus define a substantially equivalent pressure profile, albeit at a fixed differential
higher.
[0015] However, despite the expectation and desire for the pump inlet and outlet pressures
to reach a steady state shortly after activation of the ESP 37, the present inventor
has observed that in practice this may not be the case. For example, during fluid
injection, such as injection of a diluent to modify the viscosity of the production
fluids, the pressure profiles observed may be more accurately depicted in Figure 7
- it should be noted that Figure 7 represents a generalisation of the observations
made by the applicant. In this respect, when the ESP 37 is activated the pump inlet
pressure 82 falls, and the pump outlet pressure 84 rises, with the inlet pressure
86 tracking above the pump inlet pressure 82 by the magnitude of the fixed differential
88, as expected. However, it has been observed that the pump inlet and outlet pressures
82, 84 may not achieve the expected and desired steady state, and as illustrated in
Figure 7 these pressures may fluctuate for an extended period following activation
of the ESP 37. In this respect the observation is that pump inlet pressure 82 may
fall while outlet pressure 84 rises, followed by an increase in inlet pressure 82
and corresponding fall in outlet pressure 84, with the cycle repeating. Further, as
the valve inlet pressure 86 tracks above the pump inlet pressure 82 by the fixed differential
88 then this also fluctuates, and as a consequence so, too, does the injection fluid
pressure 90 at the surface. Such pressure fluctuations can cyclically load the completion
equipment, such as the ESP 37, surface pump 46, injection line 40 and the like, which
may have a detrimental effect, for example by fatiguing the equipment, by establishing
greatly interrupted and irregular production, reducing the lifetime of the completion
equipment requiring more frequent workover and servicing, requiring a greater monitoring
and reducing the understanding about the effectiveness of the fluid being injected,
perhaps leading to increased fluid injection in attempts to counter the effects of
this observation of pressure fluctuations.
[0016] A greater understanding of the causes of such observations, and any solutions to
address such causes, is desired.
SUMMARY OF THE INVENTION
[0017] The invention is defined by independent claims. Furthermore, the embodiments of the
invention are those defined by the dependent claims.
[0018] Aspects of the present invention relate to an injection device for use in injecting
a fluid into a target location. Such an injection device may include a housing having
an inlet for communication with an injection line or source of injection fluid, an
outlet for communication with a target injection location, and a reference pressure
port for communicating with a source of reference pressure, wherein the reference
pressure port is isolated from the outlet. A valve member may be mounted within the
housing. The injection device may be configured such that fluid pressures at the inlet
and reference pressure port act to cause said valve member to move within the housing
to vary flow between the inlet and the outlet. In some embodiments the injection device
may include a sealing arrangement which permits pressures at the inlet and reference
pressure port to move the valve member. Such a sealing arrangement may optionally
function to control the effect of fluid pressure at the outlet acting on the valve
member. In some embodiments the sealing arrangement may optionally function to substantially
eliminate the effect of fluid pressure at the outlet acting on the valve member.
[0019] Aspects of the present invention also relate to a method for injecting a fluid into
a target location. Such a method may comprise communicating an inlet of an injection
device to a source of injection fluid, and communicating an outlet of the injection
device to a target location. The method may further comprise permitting a valve member
mounted within the injection device to be moved by action of pressure at the inlet
of the device and by pressure acting at a reference port of the device which is isolated
form the outlet. Such movement of the valve member may function to vary flow between
the inlet and the outlet
[0020] Such an injection device and method seeks to address certain unforeseen problems
and observations which are contrary to expectation in injection processes. In this
respect, through diligent investigations and research the present inventor has discovered
certain reasons for such observations and problems. For example, in some cases problems
in known injection valves may be attributed to the fact that such valves function
to modify valve inlet pressure based almost exclusively on the valve outlet pressure,
which is understood to be largely equal to the pressure at the injection location,
which in certain cases may be subject to large variations. Such problems may be mitigated
in the present invention by permitting the valve member of the injection device to
be moved by action of a fluid pressure provided at a reference pressure port which
is isolated from the outlet of the housing. In certain embodiments the effect of outlet
pressure may be substantially eliminated in the present invention.
[0021] As noted above, previously known injection valves principally operate by modifying
valve inlet pressure based on valve outlet pressure. As such, in the event of a variation
in outlet pressure, inlet pressure should be varied accordingly. However, in some
instances an unexpected surge of flow through the valve occurs when the outlet pressure
varies. The present inventor has attributed this observation to the compressibility
of the fluid being injected, and in particular to the requirement for a volumetric
change in a fluid to occur in the event of a pressure change.
[0022] More specifically, fluids are often considered to be incompressible. This, however,
is only true to a limited extent and when high pressures are applied to fluids they
do compress. Therefore if the pressure of an injection fluid at the inlet of a valve
is required to fall, for example, a volume of fluid must be dissipated in order for
this to occur. The valve inlet will be coupled to a source of injection fluid, and
in some cases extremely long injection conduits will be utilised for this purpose,
for example in downhole applications. As such, the volume of the injection fluid within
an injection conduit may be significant, such that the volume of fluid to be dissipated
in order to permit the pressure fall may also be significant. This fluid can only
be dissipated through the injection valve. No matter how efficient the injection valve
is at maintaining a differential pressure and tracking a change in outlet pressures,
the valve will have to dissipate this volume of fluid to accommodate the fall in inlet
pressure. It has been found the volumes of fluid that require dissipation due to pressure
fall, for example, as may be found as a pump, such as an electric submersible pump
(ESP), is activated to reduce pressure presented to an injection valve or device outlet,
are more than is often thought.
[0023] Conversely, it has been observed that following the dissipation of fluid in the injection
line, as ESP inlet pressure falls, the ESP inlet pressure may then be seen to rise.
In order to facilitate a continuing delivery of chemical through the injection valve,
its inlet pressure must be increased. As fluid is delivered to increase inject line
pressure flow is consumed by the fluid compressibility and enlargement of the injection
line, thus causing a cessation or reduction of fluid flow through the injection valve.
Thus creating a fall in flow following a surge of flow. This can lead to a cyclic
repetition of a rise and surge of flow followed by a fall and loss of flow.
[0024] Although a general situation has been suggested above in which pressure variations
occur at a target location by use of an ESP, this may not always be the case, and
such pressure variations may occur due to many reasons.
[0025] In addition to the compressibility of the fluid, any associated injection conduit
may enlarge under internal pressure. This means its internal volume will increase
thus requiring more fluid to be introduced in order to reach a required pressure.
Therefore in order for the injection conduit to fall in pressure the volume of fluid
entrained at its starting pressure must be fully dissipated in order to reach a lower
pressure. This fluid volume dissipation therefore results in a significant rise, or
surge of flow through the injection valve as the inlet pressure falls.
[0026] According to a first aspect of the present invention there is provided an injection
device for use in injecting a fluid into a target location, comprising:
a housing defining an inlet for communicating with a source of injection fluid, an
outlet for communicating with a target injection location, and a separate reference
port for communicating with a reference pressure source;
a first valve member mounted within the housing;
a second valve member mounted within the housing and defining a flow path therethrough
to facilitate fluid communication between the inlet and outlet of the housing; and
a sealing arrangement provided between the second valve member and the housing and
configured such that fluid pressure at the housing inlet and housing reference port
apply a force on the second valve member to cause said second valve member to move
relative to the first valve member and vary flow between the inlet and the outlet.
[0027] In use, the effect of the reference pressure acting on the sealing arrangement may
contribute to movement of the second valve member. As such, the effect of the reference
pressure may function to control movement of the second valve member and thus control
flow through the valve. Such an arrangement may permit the second valve member to
be controlled without reliance, or with a reduced reliance, on pressure at the housing
outlet, which may be substantially equivalent to pressure at the target injection
location, as is the case in prior art devices.
[0028] The sealing arrangement may be configured to substantially confine any flow between
the inlet and the outlet to the flow path of the second valve member. That is, the
sealing arrangement may be such that flow between the inlet and outlet of the housing
may only be achieved through the flow path of the second valve member.
[0029] For the purposes of clarity, pressure acting at the inlet of the housing may be defined
as inlet pressure, pressure acting at the outlet of the housing may be defined as
outlet pressure, and pressure acting at the reference pressure port may be defined
as reference pressure.
[0030] The sealing arrangement may be directly mounted between the second valve member and
the housing. For example, the sealing arrangement may directly engage the second valve
member and the housing.
[0031] The sealing arrangement may be indirectly mounted between the second valve member
and the housing. For example, the sealing arrangement may indirectly engage at least
one of the second valve member and the housing. In one embodiment an intermediate
component may be provided between the sealing arrangement and at least one of the
second valve member and the housing.
[0032] A portion of the sealing arrangement may be in communication with the inlet of the
housing such that inlet pressure may establish a force on the second valve member
in a first direction. A portion of the sealing arrangement may be in communication
with the reference pressure port of the housing such that reference pressure may establish
a force on the second valve member in a second direction. The second direction may
be opposite to the first direction. In such an arrangement the forces generated by
the effect of pressures at the inlet and reference pressure port may result in a net
movement of the second valve member to thus vary flow between the inlet and the outlet.
[0033] The sealing arrangement may be configured such that movement of the second valve
member is achieved in accordance with a pressure differential between inlet and reference
pressures. The sealing arrangement may be configured to establish a preferential bias
of forces applied by action of inlet and reference pressures.
[0034] The sealing arrangement may define a sealing area between the second valve member
and the housing. The sealing area may determine the magnitude of a force applied on
the second valve member upon exposure to various pressures.
[0035] In one embodiment the sealing arrangement may define an inlet sealing area configured
to be exposed to inlet pressure, and a reference sealing area configured to be exposed
to reference pressure. A ratio of the inlet and reference sealing areas may affect
a net force generated on the second valve member by the inlet and reference pressures.
[0036] The inlet and reference sealing areas may be substantially equal. In such an arrangement
a net force applied on the second valve member may be a function of a pressure differential
between the inlet and reference pressures.
[0037] The inlet and reference sealing areas may by different. In such an arrangement a
force bias on the second valve member may be applied by the sealing arrangement by
action of the inlet and reference pressures. That is, a net force applied on the second
valve member may be a function of both a differential of inlet and reference sealing
areas and a differential between the inlet and reference pressures.
[0038] The injection device may be configured such that inlet pressure establishes a force
on the valve member to cause said valve member to move in a direction to increase
flow, for example initiate flow, between the inlet and the outlet of the housing.
The injection device may be configured such that reference pressure establishes a
force on the valve member to cause said valve member to move in a direction to decrease
flow, for example to prevent flow, between the inlet and the outlet of the housing.
[0039] A portion of the sealing arrangement may be in communication with the outlet of the
housing. The sealing arrangement may be configured to control the effect of the outlet
pressure on the second valve member.
[0040] In one embodiment the sealing arrangement may be configured to substantially eliminate
the effect of outlet pressure on the valve member. In such an embodiment the sealing
arrangement may be configured such that the effect of outlet pressure does not establish
or significantly minimises any net force on the second valve member. Such an arrangement
may remove or eliminate any reliance on outlet pressure to control movement of the
second valve member. This may contribute to addressing problems associated with prior
art devices where variations in outlet pressure may have a detrimental effect on operation
of the injection device.
[0041] The sealing arrangement may be configured such that outlet pressure may establish
first and second substantially equal and opposite forces on the second valve member,
such that any net force is substantially minimised.
[0042] The sealing arrangement may be configured such to permit the outlet pressure to provide
a desired bias force on the second valve member. In such an arrangement any effect
of outlet pressure may be utilised in a desired way, for example to bias the second
valve member to move in a desired direction.
[0043] The sealing arrangement may define first and second outlet sealing areas between
the second valve member and the housing, wherein each of the first and second outlet
sealing areas is configured to be exposed to outlet pressure. The first and second
sealing areas may be configured to permit outlet pressure to generate a force on the
second valve member in opposite directions.
[0044] In one embodiment the first and second outlet sealing areas may be substantially
equal. In such an arrangement the effect of outlet pressure acting on the first and
second outlet areas may be cancelled out, such that no or minimal net force is applied
on the second valve member by outlet pressure.
[0045] In one embodiment the first and second outlet sealing areas may be different. In
such an arrangement the effect of the same outlet pressure acting on the first and
second outlet areas may present a net force acting in one direction, and thus the
outlet pressure may act to apply this bias force on the second valve member in this
one direction.
[0046] The sealing arrangement may comprise one or more seal members. The sealing arrangement
may comprise one or more of sliding seal members, o-rings, bellows seals, diaphragm
seals piston rings or the like.
[0047] The sealing arrangement may include first and second seal assemblies which extend
between the second valve member and the housing.
[0048] The first seal assembly may comprise one or more seal members.
[0049] The second seal assembly may comprise one or more seal members.
[0050] The first seal assembly may be configured to isolate the housing inlet from the housing
outlet, such that fluid communication between the inlet and the outlet is permitted
only through the flow path in the second valve member.
[0051] The second seal assembly may be configured to isolate the housing outlet from the
housing reference port.
[0052] The first seal assembly may define an inlet sealing area configured to be exposed
to inlet pressure.
[0053] The first seal assembly may define a first outlet sealing area configured to be exposed
to outlet pressure.
[0054] The second seal assembly may define a reference sealing area configured to be exposed
to reference pressure.
[0055] The second seal assembly may define a second outlet sealing area configured to be
exposed to outlet pressure.
[0056] The inlet, reference and first and second outlet sealing areas may be as defined
above.
[0057] The device may comprise a biasing arrangement configured to bias the second valve
member in a desired direction. The biasing arrangement may be configured to bias the
second valve member to move in a direction to decrease flow between the inlet and
the outlet, for example to close the injection device. The biasing arrangement may
be selected to provide a desired biasing force.
[0058] The second valve member may be configured to be actuated to move in a direction to
decrease flow by a combination of biasing force from a biasing arrangement and the
action of reference pressure. The second valve member may be configured to be actuated
to move in a direction to increase flow by the action of inlet pressure.
[0059] The biasing arrangement may be configured to establish a force on the second valve
member to permit a desired pressure differential within the injection device to be
achieved. For example, the biasing arrangement may permit or require the injection
pressure to be maintained at a fixed pressure differential above the reference pressure,
by a magnitude associated with the force applied by the biasing arrangement.
[0060] The biasing arrangement may comprise one or more springs, such as a coil spring,
wave spring, flat spring, disk spring, Belleville spring or the like. The biasing
arrangement may comprise a deformable member capable of elastic recovery, such as
an elastic body subject to deformation, for example compression.
[0061] The biasing arrangement may be adjustable.
[0062] The second valve member may comprise a profile to permit engagement with the biasing
arrangement, such as an annular rib, one or more pins, or the like. The biasing arrangement
may directly engage the second valve member. The biasing arrangement may indirectly
engage the second valve member, for example via an intermediate component such as
a plate member or the like.
[0063] The injection device may be configured for use in any application, such as in any
application where a fluid is required to be injected into a target location, such
as in the oil and gas industry, chemical processing industry, manufacturing industry
or the like.
[0064] The injection device may be configured for use in injection into a wellbore target
location. The target location may be associated with wellbore equipment or infrastructure.
The target location may be associated with downhole tubing or equipment, such as production
tubing, casing or liner tubing, drill pipe, coiled tubing or the like.
[0065] The injection device may be configured for use in injection into a separate flow
line. Such a separate flowline may include a pressure varying device, such as a pump
assembly, for example an electric submersible pump (ESP) assembly. In one embodiment
the injection device may be configured for use in injection of a fluid into a flow
line at a location which is upstream of a pressure varying device. In such an arrangement
the target injection location may be located on an inlet side of such a pressure varying
device, and as such the target location may be subject to pressure variations established
by operation of the pressure varying device. Thus, the injection device of the present
invention may assist to minimise any detrimental effect by virtue of the variations
at the target injection location.
[0066] The inlet fluid pressure at the inlet of the housing may be at least partially defined
by fluid pressure within an associated injection line and/or an associated source
of injection fluid. The outlet fluid pressure may be at least partially defined by
fluid pressure at an associated target location.
[0067] The reference pressure may be selected to be any desired pressure. In some embodiments
the reference pressure may be selected to be lower than the inlet pressure.
[0068] The reference pressure may be configured to define a minimal pressure, such as atmospheric
or less than atmospheric. Such an arrangement may minimise the effect of the reference
pressure of applying a force on the second valve member. This arrangement may be selected
when, for example, the effect of the outlet pressure is minimised or negated by the
form of the sealing arrangement, such that variation in flow through the injection
device is controlled largely by inlet pressure, and the presence of any associated
biasing arrangement acting on the second valve member.
[0069] The reference pressure port may be configured for communication with any desired
source of reference pressure. The source of reference pressure may exclude the target
location. Such exclusion of the target location may minimise reliance on the outlet
pressure or target location pressure on operation of the device. This may assist to
minimise any effects of volumetric expansion, or even contraction, of fluid positioned
on the inlet side of the housing, for example within an associated injection line.
[0070] The reference pressure port may be configured for communication with a local source
of reference pressure. In one embodiment the reference pressure port may be configured
for communication with a source of reference pressure which is incorporated within
the injection device, for example formed within the housing of the injection device.
Such a local source of reference pressure may be configured to provide a fixed reference
pressure. In some embodiments a local source of reference pressure may be variable.
[0071] The reference pressure port may be configured for communication with a source of
reference pressure at a remote location. In some embodiments where the injection device
is utilised for injection into a downhole target location, the source of reference
pressure may be provided at surface level and/or at a separate downhole location.
[0072] In one embodiment the outlet of the housing is configured to communicate with a target
location which is positioned on one side of a pressure varying device, and the reference
pressure port is configured to communicate with a location which is positioned on
an opposite side of the pressure varying device. The pressure varying device may comprise
a pump, such as an ESP. The pressure varying device may comprise a choke.
[0073] In one embodiment the outlet of the housing is configured to communicate with an
inlet of a pump assembly, and the reference pressure port is configured to communicate
with an outlet of the same pump assembly. Such an arrangement may be utilised where
the pump assembly is used within a wellbore, such as to provide artificial lift to
produced fluid, to pressurise fluids for injection into a surrounding formation or
the like. In such an arrangement, the effect of any significant pressure variation,
in particular a significant pressure decrease, experienced at the reference pressure
port (i.e., the pump outlet) is minimised, and as such the effect of possible volumetric
expansion or the like within fluid located on the inlet side of the injection device
is also minimised.
[0074] The reference pressure applied at the reference pressure port may be user variable.
Such an arrangement may permit a user to tune or vary the use of the injection device
to accommodate particular operation conditions, such as the density of the fluid being
injected and the like.
[0075] The first and second valve members may cooperate to define a restriction to flow.
This may establish a back pressure in the inlet side assisting to maintain the inlet
pressure above the outlet pressure. This arrangement may assist to prevent hydrostatic
fall-through of an injection fluid. The degree of separation between the first and
second valve members may be adjustable to adjust the restriction to flow. The degree
of separation may be adjusted automatically to maintain the inlet pressure above outlet
pressure. Such automatic adjustment may be achieved by the desire for the injection
device to continuously satisfy force equilibrium. In such a case force equilibrium
may permit the desired pressure differential to be maintained.
[0076] The first and second valve members may be engageable. Such engagement may permit
the first valve member to seal the flow path in the second valve member. The second
valve member may be moveable within the housing to become separated form the first
valve member, to thus permit flow through the flow path. The degree of separation
between the first and second valve members may define a restriction to flow through
the injection device, which may function to define a back-pressure within the inlet
side of the injection device.
[0077] The first valve member may be fixed relative to the housing, such that movement of
the second valve member is required to vary flow.
[0078] The first valve member may be defined by an integral part of the housing.
[0079] The first valve member may be defined by a component which is separate from the housing.
The first valve member may be permitted to move within the housing. Permitting both
the first and second valve members to move within the housing may provide advantages
in terms of improving sealing between the first and second valve members when engaged.
For example, when engaged the first valve member may be biased against the second
member by inlet fluid pressure to assist sealing therebetween.
[0080] The use of inlet pressure to assist sealing may permit improved sealing to be achieved
upon engagement of the first and second valve members minimising the risk of leakage
therebetween. This in turn may, in some applications, minimise the possibility of
an associated injection line in communication with the housing inlet being exposed
to vacuum or negative pressure conditions, for example due to hydrostatic fall-through.
[0081] The second valve member may be configured to support the first valve member when
engaged therewith. In such an arrangement movement of the second valve member when
engaged with the first valve member will result in movement of both members. This
arrangement may permit the valve members to retain the flow path in the second valve
member closed in the event of such collective movement of the valve members. This
may assist to regulate or minimise the effects of spurious or undesired pressure fluctuations
which may otherwise cause inadvertent disengagement of the members. Such undesired
pressure fluctuations may be transitory or fleeting and not intended to represent
operational pressure fluctuations. For example, transitory pressure fluctuations may
be created by flow surges.
[0082] The first valve member may be located on the inlet side of the second valve member.
[0083] Each valve member may define an engagement surface configured to be mutually engaged
to prevent flow through the injection device. Each engagement surface may define a
sealing surface.
[0084] The first and second valve members may define a seal area at the region of engagement.
When the first and second valve members are engaged inlet fluid pressure may act on
one side, which may be defined as an upstream side of the seal area. The bias force
acting on the first valve member may therefore be a function of the seal area and
the inlet pressure. Outlet fluid pressure may act on an opposite side of the seal
area, which may be defined as a downstream side. The outlet pressure may define a
force acting on the first valve member which is a function of the seal area and the
outlet pressure. In this arrangement the first valve assembly may be biased by the
effect of a pressure differential between inlet and outlet pressures.
[0085] The apparatus may comprise a limiting arrangement configured to limit or restrict
movement of the first valve member. The limiting arrangement may be configured to
limit movement of the first valve member during opening of the valve assembly. The
limiting arrangement may be arranged to limit movement of the first valve member at
a point of limitation and permit the second valve member to move beyond the point
of limitation and to become disengaged from the first valve member. The limiting arrangement
may be fixed relative to the housing.
[0086] The limiting arrangement may comprise a tether.
[0087] The limiting arrangement may comprise a land region configured to be engaged by the
first valve member when at a point of limitation.
[0088] The limiting arrangement may comprise a no-go. The limiting arrangement may comprise
a shoulder arrangement. The limiting arrangement may comprise an elongate member.
The elongate member may extend through the second valve member.
[0089] The first valve member may be biased by a biasing arrangement in a desired direction.
The biasing arrangement associated with the first valve member may be configured to
bias said member in a direction towards engagement with the second valve member. Such
a biasing arrangement may assist sealing between the valve members when engaged. The
biasing arrangement associated with the first valve member may comprise one or more
springs, such as a coil spring, wave spring, flat spring or the like. The biasing
arrangement may comprise a deformable member capable of elastic recovery, such as
an elastic body subject to deformation, for example compression.
[0090] One of the first and second valve members may define a valve seat member and the
other of the first and second members may define a valve body member. The valve seat
member may define a valve seat which is engaged by the valve body member.
[0091] The valve body member may comprise a pin. The valve body member may comprise a ball.
The valve body member may comprise a disk, plug, plunger or the like.
[0092] The injection device may comprise a pressure rated frangible arrangement configured
to rupture upon exposure to a predetermined pressure. The frangible arrangement may
be located within the housing. The frangible arrangement may be located on the inlet
or upstream side of the second valve member. The frangible arrangement may be configured
to isolate at least the second valve member from inlet pressure until required. The
frangible arrangement may comprise a burst disk arrangement, rupture cartridge or
the like.
[0093] The injection device may comprise a surge protection arrangement configured to provide
protection against surging flow within or through the housing. Such surging flow may
be caused by a particular pump duty cycle, rupturing of a frangible arrangement or
the like. The surge protection arrangement may be configured to provide protection
to the valve assembly. The surge protection arrangement may be located within the
housing. The surge protection arrangement may be located on the inlet or upstream
side of the second valve member.
[0094] The surge protection arrangement may comprise a component defining a flow path, wherein
the flow path is restricted in the event of surging flow. The flow path may be restricted
by being partially or fully closed. The surge protection arrangement may be biased
towards a condition in which the flow path is open, and moved against said bias during
surging flow. The magnitude of the bias may define the surge rating of the surge protection
arrangement. The surge protection arrangement may comprise a spring configured to
bias the surge protection arrangement towards a condition in which the flow path is
open.
[0095] The injection device may comprise a filter arrangement configured to filter injection
fluid. The filter arrangement may be mounted within the housing. The filter arrangement
may be located on the inlet or upstream side of the second valve member.
[0096] The injection device may comprise at least one check valve configured to prevent
flow through the injection device in a direction from the outlet to the inlet. Such
an arrangement may eliminate the risk of flow reversal, for example in the event of
outlet pressure exceeding inlet pressure. At least one check valve may be located
on an outlet or downstream side of the second valve member. At least one check valve
may be located on an inlet or upstream side of the second valve member. At least one
check valve may be located within the second valve member, for example within the
flow path of the second valve member. At least one check valve may be mounted within
the housing of the injection device. At least one check valve may be provided separately
and secured to the housing of the injection device, for example via a suitable conduit
or the like.
[0097] The housing may be defined by a unitary component. The housing may be defined by
multiple components coupled together.
[0098] The inlet and outlets of the housing may be arranged in-line with each other.
[0099] The inlet may be arranged on one end location of the housing and the outlet may be
arranged on one side of the housing.
[0100] The injection device may form part of an injection system. The injection system may
comprise multiple injection devices. At least one of the multiple injection devices
may be provided in accordance with any aspect of the present invention. An injection
device according to any aspect of the present invention may be used in combination
with any other injection device. In one embodiment the injection device may be used
in series with a further injection device. For example, two or more injection devices
may be arranged in series within a common injection line.
[0101] At least an injection device which is arranged to communicate directly with a target
location may be provided in accordance with the present invention. Such an injection
device may be considered to be a final stage injection device. Other associated injection
devices which are located upstream of a final stage injection device may or may not
be provided in accordance with the present invention. For example, an injection device
located upstream of a final stage injection device may modify inlet pressure to said
upstream injection device based on outlet pressure of said injection device.
[0102] Where multiple injection devices are arranged in series within an injection line,
the devices may operate to divide any required pressure differential between the injection
line and ultimate injection location into stages. This may reduce the required pressure
drop across an individual injection device, which may provide advantages. For example,
in some cases an injection fluid may have behavioural problems when passed over an
injection device at a high differential pressure. Such problems may include cavitation,
depositing of solids or a change in the state of the injection fluid, which may lead
to reduced effectiveness, such as chemical effectiveness, of the injection fluid.
Accordingly, by use of multiple injection devices arranged in series, the differential
pressure presented across each device may be restricted or reduced, and in particular
to levels which are advantageously lower than any threshold where problems may occur
within the injection fluid. Such an advantageous use of more than one injection valve
in series may also be achieved while still providing the effect of avoiding low, vacuum
or near vacuum pressures within the injection line.
[0103] The injection device may be configured for use in combination with one or more other
injection devices arranged in parallel. In such an arrangement multiple injection
devices may be arranged for injection of a fluid from a common injection fluid source
into multiple different locations.
[0104] The injection device may be configured to be coupled within fluid tubing. The injection
device may be configured to be located at a downhole location. The injection device
may be configured to be located within downhole tubing. The injection device may be
configured to be located in an annulus surrounding downhole tubing. The injection
device may be configured to be located within a pocket formed in downhole tubing.
The injection device may be configured to be located at a subsea location. The injection
device may be configured to be located at a surface location.
[0105] The injection device may be configured to be permanently installed within an injection
system. The injection device may be configured to be temporarily installed within
an injection system. In one embodiment the injection device may be configured to be
deployed and/or retrieved by an elongate member, such as by wireline, coiled tubing
or the like.
[0106] The injection device may be for use with any suitable injection fluid. Such an injection
fluid may comprise a chemical. Such an injection fluid may comprise any one of, for
example, a scale inhibitor, corrosion inhibitor, pH modified, viscosity modified,
diluent, water, oil, acid or the like. It will be appreciated by those of skill in
the art that any injection fluid may be utilised with the injection device of the
present invention.
[0107] The injection device may be configured to inject a fluid into a subterranean formation,
for example for sequestration of a fluid, to assist with production of fluids from
the formation, to support the surrounding subterranean geology, or the like.
[0108] The injection device may be configured for use in injecting a fluid into any location
of any flow line or flow process, such as at any location of a flow line extending
from a subterranean formation to a surface location.
[0109] According to a second aspect of the present invention there is provided a method
for injecting a fluid into a target location, comprising:
communicating an injection fluid to an inlet of a housing of an injection device;
communicating an outlet of the housing to a target location;
communicating a reference port of the housing to a source of reference pressure;
causing a second valve member to move relative to a first valve member by exposure
to pressure at the inlet of the housing and pressure at the reference pressure port
of the housing, wherein such movement permits flow through a flow path of the valve
member to be adjusted.
[0110] According to a third aspect of the present invention there is provided a pumping
system comprising:
a flow line;
a pump associated with the flow line and defining an inlet side and an outlet side;
an injection device according to the first aspect, wherein the outlet of the injection
device housing is in communication with the flow line on an inlet side of the pump.
[0111] In one embodiment the reference pressure port of the injection device housing may
be in communication with the flow line on an outlet side of the pump.
[0112] The reference pressure port may be in communication with a remote source of reference
pressure.
[0113] The reference pressure port may be in communication with a local source of reference
pressure, for example provided by a pressure reservoir within the housing of the injection
device.
[0114] According to an example not forming part of the claimed invention there is provided
an injection device for injecting a fluid into a target location, comprising:
a housing defining an inlet for communicating with a source of injection fluid, an
outlet for communicating with a target injection location, and a separate reference
port for communicating with a reference pressure source which excludes the target
injection location;
a valve member mounted within the housing and defining a flow path therethrough to
facilitate fluid communication between the inlet and outlet of the housing, wherein
the valve member is moveable within the housing by exposure to fluid pressure at the
housing inlet and fluid pressure at the housing reference pressure port to vary flow
between the inlet and the outlet.
[0115] According to an example not forming part of the claimed invention there is provided
an injection device for use in injecting a fluid into a target location, comprising:
a housing including an inlet chamber for communicating with an injection line, an
outlet chamber for communicating with a target location, and a reference chamber for
communicating with a reference pressure source;
a valve member mounted within the housing and defining a valve flow path to facilitate
fluid communication between the inlet and outlet chambers;
a first seal assembly provided between the valve member and the housing and isolating
the inlet chamber from the outlet chamber such that a pressure differential between
the inlet and outlet chambers acting over the first seal assembly will establish a
force on the valve member; and
a second seal assembly provided between the valve member and the housing and isolating
the reference chamber from the outlet chamber such that a pressure differential between
the reference chamber and the outlet chamber acting over the second seal assembly
will establish a force on the valve member,
wherein the valve member is permitted to move within the housing in accordance with
the pressure forces applied via the first and second seal assemblies to vary flow
through the valve flow path between the inlet and the outlet chambers.
[0116] According to an example not forming part of the claimed invention there is provided
an injection system for injecting a fluid into a target location, comprising:
an injection line in communication with a source of injection fluid;
an injection device coupled to the injection line and comprising:
a housing defining an inlet coupled to the injection line, an outlet for communicating
with a target injection location, and a separate reference port for communicating
with a reference pressure source;
a first valve member mounted within the housing;
a second valve member mounted within the housing and defining a flow path therethrough
to facilitate fluid communication between the inlet and outlet of the housing; and
a sealing arrangement provided between the second valve member and the housing and
configured such that fluid pressure at the housing inlet and housing reference port
apply a force on the second valve member to cause said second valve member to move
relative to the first valve member and vary flow between the inlet and the outlet.
[0117] The injection device may define a first injection device and the injection system
may comprise a second injection device located upstream of the first injection device.
In such an arrangement the second injection device may comprise an outlet in communication
with the inlet of the first injection device.
[0118] The provision of a second injection device within the injection system may permit
a pressure differential between an injection line and a target location to be divided
into stages, which may be advantageous in certain circumstances.
[0119] The second injection device may be configured similarly to the first injection device.
For example, the second injection device may permit movement of an associated valve
member by exposure to a reference pressure which is isolated from an outlet pressure.
[0120] The second injection device may be configured differently from the first injection
device.
[0121] The second injection device may comprise a housing defining an inlet coupled to the
injection line and an outlet for communicating with the inlet of the first injection
device. The second injection device may comprise a first valve member mounted within
the housing. The second injection device may comprise a second valve member mounted
within the housing and defining a flow path therethrough to facilitate fluid communication
between the inlet and outlet of the housing. The first and second valve members may
move relative to each other to vary flow through the flow path of the second valve
member, and thus also through the second injection device.
[0122] The second injection device may comprise a sealing arrangement provided between the
second valve member and the housing and configured such that fluid pressure at the
housing inlet and housing outlet may apply a force on the second valve member to cause
said second valve member to move relative to the first valve member and vary flow
between the inlet and the outlet.
[0123] According to an example not forming part of the claimed invention there is provided
a method for creating an injection system, comprising:
determining a required pressure differential between an injection line and a target
injection location which maintains the injection line at a positive pressure;
determining an operational threshold pressure differential of an injection fluid;
determining a required number of discrete pressure reduction stages within the injection
line to provide the required pressure differential between the injection line and
target location while maintaining each pressure reduction stage below the operational
threshold pressure differential of the injection fluid; and
installing a number of injection devices within an injection line to correspond to
the determined number of discrete pressure reduction stages.
[0124] In such an arrangement an injection line may be created which includes a number of
injection devices to provide a required number of discrete pressure differentials
each below the operational threshold pressure differential of an associated injection
fluid, yet which collectively maintain the injection line in a positive pressure.
[0125] The injection devices may be located at any location along the length of the injection
line.
[0126] The pressure within the injection line may be associated, at least partly, with hydrostatic
pressure.
[0127] At least one injection device may be provided in accordance with any other aspect.
[0128] Other aspects may relate to the use of the injection device according to any previous
aspect, for example in a wellbore injection system, in a downhole pumping system,
or the like.
[0129] Other aspects may relate to a completion system for a wellbore, such as a wellbore
associated with the exploration and production of hydrocarbons.
[0130] It should be understood that the features defined in relation to one aspect may be
applied to any other aspect.
BRIEF DESCRIPTION OF THE DRAWINGS
[0131] These and other aspects of the present invention will now be described, by way of
example only, with reference to the accompanying drawings, in which:
Figure 1 is a diagrammatic illustration of a typical wellbore system which includes
injection capabilities;
Figure 2 is a diagrammatic representation of a known injection valve arrangement;
Figure 3 is a diagrammatic illustration of inlet and outlet pressure profiles of the
injection valve of Figure 2;
Figure 4 graphically represents the effects of hydrostatic fall-through within a capillary
or injection line;
Figure 5 provides an illustration of inlet and outlet pressure profiles of the injection
device of Figure 2, with the use of a more powerful spring;
Figures 6 and 7 illustrate, respectively, expected and actual pressure profiles of
the inlet and outlet pressures of a downhole pump, and of the inlet pressure of an
associate injection valve;
Figure 8 is a cross-sectional view of an injection device in accordance with one embodiment
of the present invention;
Figure 9 is a cross-sectional view of an injection device in accordance with an alternative
embodiment of the present invention;
Figure 10 provides an exemplary pressure plot of the use of an injection device according
to the present invention, in which a reference pressure from an outlet of a downhole
pump is utilised;
Figure 11 provides an exemplary pressure plot of the use of an injection device according
to the present invention, in which a reference pressure from a remote location, such
as a surface location, is utilised;
Figure 12 is a cross-sectional view of an injection device according to an alternative
embodiment of the present invention;
Figure 13 is an exemplary pressure plot of the use of the injection device of Figure
12;
Figures 14 to 18 are cross-sectional views of an injection device in accordance with
respective alternative embodiments of the present invention;
Figure 19 is a diagrammatic representation of a downhole injection system in accordance
with an embodiment of the present invention; and
Figure 20 is an exemplary pressure plot of the injection system of Figure 19.
DETAILED DESCRIPTION OF THE DRAWINGS
[0132] The present invention relates to an injection device which may be used in multiple
applications. However, for exemplary purposes some specific embodiments of an injection
device have been illustrated in the drawings, and described below, with a potential
application within a wellbore system, such as a wellbore system for the extraction
of oil and/or gas form a subterranean reservoir.
[0133] Figure 1, which has also been described above, provides an illustration of a wellbore
completion installation, generally identified by reference numeral 10, with injection
capabilities via injection valve 48. A known injection valve 48 is illustrated in
Figure 2, which has already been described above. Furthermore, it has been explained
above that although with the use of such a known injection valve 48 the expected pressure
behaviour within an injection system, which is reflected in Figure 6, may not actually
be achieved, and in fact a more accurate representation of reality is provided in
Figure 7. In this particular example, which involves the use of a downhole pump, such
as an ESP 37 (Figure 7), upon activation the pump 37, inlet and outlet pressures might
continue to fluctuate for extended periods, and may not reach a desired steady state
condition. It is believed by the present inventor that such extended periods of fluctuation
is caused by unsteady rates of injection via the injection valve 48 which is initiated
by a sudden rush of injection fluid through the valve shortly after initial activation
of the pump 37. Through diligent investigation and research performed by the present
inventor it is considered that such a rush of fluid through the valve is caused by
the compressibility of the injection fluid, as described below in detail. However,
in general terms, the present inventor believes that as known injection valves require
the valve inlet pressure to track above valve outlet pressure, then in the event of
a relatively quick pressure change at the valve outlet, for example by activation
of a pump, then the fluid in the injection line acting at the valve inlet will require
to undergo a volumetric change to accommodate the required change in pressure. This
volumetric change will cause the rush through the valve, and destabilise the system.
[0134] A common injection or capillary control line size currently used for chemical injection
is 9.5 mm (3/8") OD tube. Also, many wells are completed with "deviation" where the
well may be drilled off at progressive angles to increase its reach from a central
commencement location. Therefore a well may possess a true vertical depth of, for
example, 2000 metres but in fact be far more in its true deviated or Measured Depth
(Md).
[0135] The normal internal volume of such a control line can be summarised at varying measured
depths as follows:
| |
Capillary Line Length - metre |
| Length - m |
1000 |
2000 |
3000 |
4000 |
| Volume - L |
39.4 |
78.9 |
118.3 |
157.8 |
[0136] Fluids are often considered to be incompressible. This is only true to a limited
extent and when high pressures are applied to fluids they do compress. This is a fluid
property that is a function of the compressibility of the fluid which may also change
with temperature and pressure.
[0137] Therefore if the capillary line 40 (Figure 1) is at a given pressure which then is
required to fall, a volume of fluid must be dissipated in order for this to occur.
This fluid can only be dissipated through the injection valve 48. No matter how efficient
the injection valve 48 is at maintaining a differential pressure and tracks a change
in outlet pressures, the valve will have to dissipate this volume of fluid to accommodate
a change in capillary line pressure. It has been found the volumes of fluid that require
dissipation are more than is often thought.
[0138] In addition to the compressibility of the fluid, the capillary line 40 itself will
enlarge under internal pressure. This means its internal volume will increase thus
requiring more fluid to be introduced in order to reach a required pressure. Therefore,
in order for the capillary line 40 to fall in pressure the volume of fluid entrained
at its starting pressure must be fully dissipated in order to reach a lower pressure.
This fluid volume dissipation therefore results in a significant rise, or surge of
flow through the injection valve 48 as the capillary line pressure falls.
[0139] This may occur as the ESP 37 is brought online causing the ESP inlet pressure and
therefore the valve outlet pressure to fall. As the injection valve 48 attempts to
maintain a fixed differential from its inlet to outlet it allows the increased flow
to occur through itself. This rise in flow may be very significant and constitute
a flow surge through the injection valve 48. This has another detrimental effect where
the injection valve 48 can be overwhelmed and once the flow surge has passed the valve
may fall in its resistance pressure and struggle to retrieve a fixed value above its
outlet pressure. In doing this the capillary line 40 must gain in pressure before
it can reach a value to overcome the valve resistance pressure and continue to flow
again.
[0140] The flow may therefore fluctuate, starting with a flow spike followed by a fall in
flow, a stop in flow and then a slow recovery of flow until flow is normalised again.
[0141] A significant consequence of this is that flow of chemical to the ESP 37 is not of
a fixed value and is inconsistent. In this respect certain chemicals are used, called
diluents, to reduce heavy oil viscosity or density to aid in production. A surge of
chemical or diluent flow may overdose the chemical or diluent resulting in a lighter
fluid for the ESP 37 to pump followed by a fall in chemical flow which increases fluid
weight causing a reduction in ESP 37 pumping efficiency.
[0142] The ESP 37 therefore is seen to increase flow then suffer a reduction in efficiency.
This is generally illustrated in Figure 7 in which the ESP outlet pressure 84 is seen
to rise as its inlet 82 falls but then suffers a decrease in efficiency where its
outlet 84 falls again as the inlet 82 rises while the injection valve pressure 86
is seen to track the ESP inlet pressure 82. This is due to firstly the surge of chemical
or diluent and then the fall in chemical or diluent flow.
[0143] Another effect of this variation in pressures due to the rise and fall of valve outlet
pressure is that the surface injection pressure 90 (a fixed value above the valve
outlet pressure by the valve resistance pressure minus the capillary line hydrostatic
pressure) will also vary which could create loading on surface injection pump equipment
42.
[0144] The consequences of this cycling of load on the ESP 37 is considered to be, as a
minimum, greatly interrupted and inconstant production, greater cycle load on the
ESP 37 leading to reduced lifetime requiring the well be worked over to service the
ESP 37, greater monitoring and a lack of understanding about the effectiveness of
the chemical or diluent input leading to increased chemical or diluent input in attempts
to counter the problem.
[0145] It is also possible that the surge effect through the injection valve 48 could cause
damage to its ability to provide a back pressure. This could lead to a fall in resistance
ultimately allowing a vacuum to occur in the control line 40 which itself creates
risk of blockage, corrosion etc.
[0146] In view of such issues identified by, the inventor as developed an injection device
which seeks to address these problems. An embodiment of such an injection device will
now be described with reference to Figure 8.
[0147] The injection device, which is generally identified by reference numeral 100 includes
a housing 102 defining an inlet 104, outlet 106 and a reference pressure port 108.
The inlet 104 is configured to be in communication with a source of injection fluid
110, for example via an injection line (not shown). The outlet 106 is configured to
be in communication with a target location 112, such as a downhole location. The reference
pressure port 108 is configured to be in communication with a source of reference
pressure 114.
[0148] The device 100 further includes a first valve member 116 which in the present embodiment
is rigidly secured to the housing 102. A second valve member 118 is moveably mounted
within the housing 102 and defines a flow path 120 extending therethrough to facilitate
fluid communication between the inlet 104 and outlet 106. As will be described in
further detail below, the second valve member 118 is permitted to move in accordance
with inlet and reference pressures to vary flow between the inlet 104 and outlet 106.
[0149] The first and second valve members 116, 118 are configured to be engaged and define
a sealed area 122 therebetween, such that when the first and second valve members
116, 118 are engaged flow through the flow path 120 is prevented. However, when the
second valve member 118 is moved the valve members 116, 118 become disengaged such
that flow is permitted. Also, when the first and second valve members 116, 118 are
disengaged the gap defined therebetween may create a flow restriction and movement
of the second valve member 118 may vary this flow restriction to assist to vary flow
of injection fluid through the device 100.
[0150] The device 100 further comprises a biasing spring 101, in this case a coil spring,
which acts on the second valve member 118 to bias this in an upward direction (relative
to the orientation of Figure 8), towards engagement with the first valve member 116.
Thus, spring 101 effectively operates to bias the second valve member 118 towards
a closed position.
[0151] The device 100 further comprises a sealing arrangement 122 which includes first and
second sealing assemblies 124, 126 extending between the second valve member 116 and
the housing 102. The first sealing assembly 124 provides isolation between the inlet
104 and the outlet 106, such that flow between the inlet and outlet must be achieved
via the flow path 120 in the second valve member 118. Further, the second sealing
assembly 126 isolates the outlet 106 from the reference pressure port 108.
[0152] The first sealing assembly 124 is exposed to inlet fluid pressure, such that said
inlet fluid pressure will establish a force on the second valve member 118 in a downward
direction (relative to the orientation of Figure 8). Further, the second sealing assembly
126 is exposed to reference pressure such that said reference pressure will establish
a force on the second valve member 118 in an upward direction (again, relative to
the orientation of Figure 8). Accordingly, a net force will be applied on the second
valve member 118 by the action of the inlet and reference pressures, and in particular
in accordance with a pressure differential between the inlet and outlet pressures.
[0153] In the present embodiment the first and second sealing assemblies 124, 126 define
equivalent seal areas, and as such there is no effect on any seal area differential,
although in other embodiments such a seal area differential may be provided.
[0154] Furthermore, both the first and second sealing assemblies 124, 126 are exposed to
outlet fluid pressure. Also, as the first and second sealing assemblies 124, 126 define
equivalent seal areas then the effect of the outlet pressure will be cancelled, and
no net force will be created by outlet pressure. It should be noted, however, that
in other alternative embodiments a seal area differential may be provided to establish
a bias force generated by outlet pressure.
[0155] Accordingly, in the present embodiment the outlet pressure, which will largely be
defined by pressure at the target location 112, will not have any effect on the operation
of the device 100. This may therefore avoid those problems identified above which
stem from possible variations in outlet pressure resulting in a sudden surge through
an injection device.
[0156] In use, for flow through the device 100 to be established, the force applied on the
second valve member 118 by the inlet pressure must exceed to combined force applied
by the reference pressure and the spring 101. In this way, the inlet pressure may
be presented at a pressure which is greater than the reference pressure by the appropriate
equivalent pressure generated by the spring 101, in addition to any backpressure created
by the restriction to flow between the first and second valve members 116, 118.
[0157] The device 100 may be used in conjunction with any desired source of reference pressure
114. In particular, the effects and advantages of the present invention may be achieved
where the source of reference pressure 114 excludes the target location 112.
[0158] An alternative embodiment of an injection device, in this case generally identified
by reference numeral 200, is shown in Figure 9, reference to which is now made. Device
200 is similar to device 100 of Figure 8, and as such like features share like reference
numerals, incremented by 100. Further, the operation of the device 200 is largely
similar to device 100, and as such only the difference in structure and operation
will be described with reference to device 200.
[0159] In this respect device 200 also includes a housing 202 defining an inlet 204, outlet
206 and reference pressure port 208, with first and second valve members 216, 218
mounted within the housing 202. A sealing arrangement 222 comprising first and second
sealing assemblies 224, 226 is positioned between the second valve member 218 and
the housing, and functions, as before, to provide a desired force bias on the second
valve member 218 by action of inlet and reference pressures.
[0160] In the present embodiment, however, the first valve member 216 is not rigidly secured
to the housing 202, but is instead also permitted to move within the housing 202.
In particular, the first valve member 216 is provided in the form of a pin which is
mounted on a spring 130 which acts to bias said valve member 216 into engagement with
the second valve member 218 to close the flow path 220 in said second valve member
218. Accordingly, when the first and second valve members 216, 218 are engaged, movement
of the second valve member 218, for example by action of the various pressures and
the second valve member bias spring 201, will also cause movement of the first valve
member 216.
[0161] The housing 201 further comprises a limit arrangement in the form of an annular lip
132, and the second valve member 216 includes a corresponding circumferential rib
134. When the first and second valve members 216, are engaged, with the annular lip
132 and circumferential rib 134 disengaged, inlet fluid pressure will act over the
seal area 222 between the engaged valve members 216, 218, which will have the effect
of pressing said members together. This arrangement therefore permits inlet pressure
to be utilised to improve the seal between the valve members when engaged.
[0162] However, when the appropriate pressure forces applied at the inlet is sufficient
to move the second valve member downwardly, the circumferential rib 134 of the first
valve member 216 will eventually engage the annular lip 132, such that continued downward
movement of the second valve member 218 will cause disengagement of the valve members,
thus establishing flow between the inlet 204 and outlet 206.
[0163] Also shown in the present embodiment is a check valve assembly 136 located at the
outlet 206 of the housing, and which functions to prevent backflow from the target
location 212 into the device. Although the check valve assembly 136 is shown mounted
in an integrated part of the housing 202, a separate check valve assembly may instead
be provided and secured relative to the outlet 206 of the housing 202.
[0164] As defined above, it is possible to use any desired source of reference pressure,
perhaps with the exception of pressure at the target location. For example, in one
exemplary use, the injection device may be used in the wellbore completion arrangement
10 first shown in Figure 1, reference to which is again made, wherein the injection
valve 48 in Figure 1 may be replaced with the device according to any embodiment of
the invention. In such an exemplary use the target location is on the inlet or suction
side of an ESP 37. As noted above, problems have been discovered in prior art systems
which also use this target location to vary the pressure within the associated injection
line 40. However, in the present exemplary use the reference pressure may be provided
from the outlet or delivery side of the ESP. A graphical representation of the various
pressure profiles associated with such an exemplary use of the present invention is
illustrated in Figure 10.
[0165] As illustrated, when a pump (where use) such as an ESP is activated the inlet pressure
140 will fall, and the outlet pressure 141 will rise. As the device utilises this
outlet pressure 141 as a reference pressure, this results in the inlet pressure 143
of the device defines the same pressure profile, albeit at a differential higher provided
by the effect of the spring acting against the second valve member in addition to
the effect of any back pressure created by flow through the device. As illustrated
also in Figure 10, the pressure differential 146 between the inlet and outlet of the
device is no longer fixed, which differs from the prior art. Also, the surface pressure
146 defines a similar profile to that of the pump outlet pressure 142. As is clear
from Figure 10, the pump is considered to reach a desired steady state condition,
without any problems occurring due to cascading of fluid through the device.
[0166] In an alternative exemplary use, the device may be arranged such that the reference
pressure is provided from a source, for example at surface level, which permits the
reference pressure to be varied. The associated pressure profiles of an associated
ESP and of the device is illustrated in Figure 11. In this respect, when the pump
is activated the inlet pressure 150 falls. At this stage the reference pressure 151
is fixed at a first value, and as such the inlet pressure 152 of the device is initially
constant at a first value, which will be a fixed differential above reference pressure
151. If at some point a change in reference pressure is required, for example due
to a change in density of injection fluid, then this may be readily achieved, irrespective
of the pump inlet pressure. In the exemplary embodiment the change involves an increase
in reference pressure 151 (initiated around time interval 6), such that the inlet
pressure 152 is seen to increase to a second, higher level.
[0167] A further alternative embodiment of an injection device, in this case generally identified
by reference numeral 300, is shown in Figure 12. Device 300 is similar to device 200
shown in Figure 9, and as such like features share like reference numerals, incremented
by 100. For brevity, only differences between the embodiments in Figures 9 and 12
will be highlighted. In this respect, device 300 includes bellows type first and second
sealing assemblies 324, 326 which form the sealing arrangement. Further, the device
300 comprises an integrated reference pressure reservoir 160 which contains an internal
reference pressure which acts at the reference port 308. Thus, the second valve member
318 is affected by the pressure within this reservoir 160.
[0168] Further, the second valve member 318 includes a lower pin 142 which engages a plate
144, which in turn is acted on by the bias spring 301, which in this case is a disk
spring, mounted within the reservoir 160.
[0169] In this present embodiment the device 300 does not necessarily require the presence
of any external source of reference pressure, which may provide significant advantages
in terms of permitting a simplified system to be utilised. Furthermore, in certain
cases the pressure within the reservoir may define a minimal pressure, such that the
effect of any active pressure is essentially negligible, such that any force applied
to move the second valve member 318 upwardly is achieve primarily by the spring 301.
[0170] A pressure plot associated with the device 300 of Figure 12 is shown in Figure 13,
in this case again assuming that the device is arranged to inject a fluid into the
inlet side of an ESP, such as ESP 37 of Figure 1. Referring to Figure 13, as a pump
(where used) such as an ESP is activated pump inlet pressure 162 falls. However, as
the reference pressure within reservoir 160 is constant, a constant valve inlet pressure
164 and surface pressure 166 will be achieved, with the pressure differential 168
between the device inlet 304 and outlet 306 varying.
[0171] An injection device according to the present invention may be embodied in a number
of ways, and a selection of further example embodiments are presented in Figures 14
to 18, reference to which will now be made. For brevity only particular differences
between the embodiments will be identified.
[0172] Injection device 400 of Figure 14 is generally similar to device 200 of Figure 9,
and as such like features share like reference numerals, incremented by 200. Device
400 includes bellows type sealing assemblies 424, 426 which form the sealing arrangement
422.
[0173] Injection device 500 of Figure 15 is generally similar to device 200 of Figure 9
, and as such like features share like reference numerals, incremented by 300. Device
500 includes bellows sealing assemblies 524, 526 which form the sealing arrangement
522. Further, the second valve member 516 includes an extension pin 170 which is engaged
by a plate 172 which in turn is engaged by bias spring 501.
[0174] Injection device 600 of Figure 16 is generally similar to device 200 of Figure 9
, and as such like features share like reference numerals, incremented by 400. Device
600 includes bellows sealing assemblies 624, 626 which form the sealing arrangement
622. Further, the second valve member 616 includes an extension pin 174 which is engaged
by a plate 176 which in turn is engaged by bias spring 601.
[0175] Furthermore, the second valve member 616 includes a ball member which cooperates
with the second valve member 618. A support stalk 178 extends through the flow path
620 of the second valve member 618 and functions to limit movement of the ball of
the first valve member 616.
[0176] Injection device 700 of Figure 17 is generally similar to device 300 of Figure 12,
and as such like features share like reference numerals, incremented by 400. In this
embodiment the first valve member 716 includes a profiled pin 180 which extends upwardly
therefrom and is received within an annular chamber 182. the pin 180 and chamber 182
cooperate to limit movement of the second valve member 716 to permit disengagement
from the second valve member 718.
[0177] Injection device 800 of Figure 18 is generally similar to device 300 of Figure 12,
and as such like features share like reference numerals, incremented by 500. In device
800 the outlet 806 is provided inline with the inlet 804. This is achieved by providing
a flow path 186 around the reservoir chamber 660. Further, device 800 includes a check
valve assembly 190 in communication with the outlet 806.
[0178] In some cases the required differential resistance pressure required where an ESP
is set to a very high Total Vertical Depth (TVD) and the ESP will draw to extremely
low pressures may be very high. This is by way of a capillary line hydrostatic being
large due to the great depth (TVD) and the ESP drawing to an exceptionally low pressure
for the purposes of enhanced production, for example. In such cases the fluid being
injected may have behavioural problems when passed over the injection device at a
high differential pressure. Such problems may include cavitation, depositing of solids
or a change in the state of the injection fluid which may lead to reduced effectiveness,
such as chemical effectiveness.
[0179] The present inventor therefore considers it to be desirable that in some situations
a differential pressure be reduced to levels that are under the thresholds where such
issues may occur with the injection fluid. This reduction in differential pressure,
however, may not be readily achieved in conventional prior art systems as the requirement
still exists that the overall resistance within the injection device must be large
enough to ensure there is no vacuum in the capillary injection line.
[0180] To address this, an injection device according to the present invention (such as
in any embodiment described above) may be installed at a lower point of injection
but in addition to this a second (or third etc.) injection valve may be installed
at a higher point in the injection line, for example at any higher point in the injection
line. Such an arrangement is illustrated in Figure 19, reference to which is now made.
In this respect, Figure 19 provides a diagrammatic illustration of a wellbore system,
generally identified by reference numeral 910, which includes injection capabilities
and is largely similar to the system 10 of Figure 1. As such, like features share
like reference numerals incremented by 900. Thus, wellbore system 910 includes a casing
string 912 located within a drilled bore 914 which extends from surface 916 to intercept
a hydrocarbon bearing formation 918. A lower annulus area 920 may be filled with cement
922 for purposes of support and sealing. A production tubing string 924 extends from
a wellhead 926 and production tree 928. A lower end of the production tubing string
924 is sealed against the casing 912 with a production packer 930 to isolate a producing
zone 932. A number of perforations 934 are established through the casing 912 and
cement 922 to establish fluid communication between the casing 912 and the formation
918. Hydrocarbons may then be permitted to flow into the casing 912 at the producing
zone 932 and then into the production tubing 924 via inlet 936 to be produced to surface.
Artificial lift equipment, such as an ESP 937 may optionally be installed inline with
the production tubing 924 as part of the completion to assist production to surface.
The production tree 928 may provide the necessary pressure barriers and provides a
production outlet 938 from which produced hydrocarbons may be delivered to a production
facility (not shown), for example.
[0181] A small bore injection line or conduit 940, which is often referred to as a capillary
line, runs alongside the production tubing 924 from a surface located injection fluid
source 942 to a downhole target location, which in the illustrated example is a lower
end of the production tubing 924, below the ESP 937. The production tubing 924 may
include an optional injection mandrel 944. An injection pump 946 is located at a topside
location to facilitate injection of the injection fluid 942.
[0182] A first injection valve 948 is located at the lower end of the injection line 940
in proximity to the location of injection. This injection valve 948 may be provided
in accordance with any embodiment of the present invention. A second injection valve
949 is coupled to the injection line 940 at a location which is upstream of the first
injection valve 948. The second injection valve 949 may be provided in accordance
with any embodiment of the present invention. The second injection valve 949 may be
provided in accordance with any known or conventional injection valve, such as a conventional
backpressure injection valve which may modify its inlet pressure based on its outlet
pressure.
[0183] With the example arrangement shown in Figure 19, the overall required differential
pressure may be broken into two stages, thus ensuring that the differential pressure
occurring at any one of the injection valves 948, 949 is reduced ensuring the injection
fluid is not subjected to high shear rates through the device under high differential
pressures.
[0184] This installation mode may be generally illustrated in the below example where a
very high setting depth (TVD) is required for the ESP 937 which is intended to run
at a very low intake pressure. The injection line 940 is installed with a conventional
back pressure injection device (the second injection device 949) at approximately
50% of its TVD and an injection device (the first injection device 948) at the ESP
intake depth (full TVD). If a single back pressure device is used it would be required
to have a minimum back pressure resistance of 314 bar. However, if we assume in the
present illustration that the injection fluid has been found to suffer degradation
of properties if passed through a differential of more than 180 bar, then this required
pressure differential of 314 bar will have an adverse effect on the injection fluid.
Therefore two stages are employed with an upper device 949 and a lower device 948.
[0185] A process of designing or selecting the from of an appropriate injection system in
the present illustration is set out in the table below:
| Total Vertical Capillary Line Height (TVD) - metres |
3050 |
| Determine Capillary Hydrostatic Pressure |
| Specific Gravity of Injected Fluid |
1.050 |
| Density of Fluid - kg/m3 |
1050.00 |
| TOTAL Capillary Line Hydrostatic pressure - bar |
314.2 |
| Identify Chemical Differential Limitations |
| Maximum Allowable Differential - bar |
180.0 |
| Is Allowable Dp greater than required Dp ? |
NO |
| Required Stages of Resistance |
2 |
| Determine Upper and Lower Stage Conditions |
| Minimum ESP Inlet Pressure - bar |
86.0 |
| Lower Device Resistance Pressure - bar |
150.0 |
| Lower Device Inlet Pressure - bar |
236.0 |
| Installation Depth of Upper Stage (TVD) - metre |
1480.0 |
| % of Overall TVD for Installation of Upper Stage - % |
49% |
| Capillary line height from lower to upper stage (TVD) - m |
1570.0 |
| Hydrostatic Pressure in line from lower to upper Stage - bar |
161.8 |
| Upper Stage Device outlet Pressure - bar |
74.2 |
| Upper Device Resistance Pressure - bar |
100.0 |
| Upper Device Inlet Pressure - bar |
174.2 |
| Hydrostatic Pressure in line from upper Stage to Surface - bar |
152.5 |
| Surface Injection Pressure - bar |
21.8 |
[0186] Although in the example above the upper device is located at approximately 50% of
the TVD, this is only exemplary, and any suitable depth may be utilised. This is illustrated
in the further example below, in which the upper device is located at an further example
depth of 71% of TVD.
| Determine Upper and Lower Stage Conditions |
| Minimum ESP Inlet Pressure - bar |
86.0 |
| Lower Device Resistance Pressure - bar |
150.0 |
| Lower Device Inlet Pressure - bar |
236.0 |
| Installation Depth of Upper Stage (TVD) - metre |
2180.0 |
| % of Overall TVD for Installation of Upper Stage - % |
71% |
| Capillary line height from lower to upper stage (TVD) - m |
870.0 |
| Hydrostatic Pressure in line from lower to upper Stage - bar |
89.6 |
| Upper Stage Device outlet Pressure - bar |
146.4 |
| Upper Device Resistance Pressure - bar |
100.0 |
| Upper Device Inlet Pressure - bar |
246.4 |
| Hydrostatic Pressure in line from upper Stage to Surface - bar |
224.6 |
| Surface Injection Pressure - bar |
21.8 |
[0187] Therefore by using two stages (upper and lower) each with appropriate differential
settings of 100 and 150 bar respectively, the overall resistance is provided and the
full injection line is maintained in a positive pressure thus avoiding vacuum fall
out conditions and ensuring the injection fluid is passed through differential pressures
beneath its property change threshold of 180 bar.
[0188] The first example provided above may be further illustrated in Figure 20, which is
a pressure plot along the length of the injection line showing the individual pressure
drop effect of the first and second injection devices 948, 949.
[0189] It should be understood that the embodiments described herein are merely exemplary
and that various modifications may be made thereto without departing from the scope
of the invention. For example, various embodiments have been described above, and
it should be recognised that further embodiments are possible in which the features
of some of the illustrated embodiments may be applied to others. Thus, any combination
of the illustrated features may be possible.
[0190] Further, in the example of Figure 19, any number of injection devices may be utilised
to provide the desired stages of pressure drop along the length of the injection line.
1. Bohrlochinjektionsvorrichtung (100) zur Verwendung beim Injizieren eines Fluids in
eine Bohrloch-Zielstelle (112), umfassend:
ein Gehäuse (102), das einen Einlass (104) zur Verbindung mit einer Injektionsfluidquelle
(110), einen Auslass (106) zur Verbindung mit einer Zieleinspritzstelle (112) und
einen separaten Referenzanschluss (108) zur Verbindung mit einer Referenzdruckquelle
(114) festlegt;
ein erstes Ventilelement (116), das innerhalb des Gehäuses (102) angebracht ist;
ein zweites Ventilelement (118), das innerhalb des Gehäuses (102) angebracht ist und
einen Strömungsweg (120) definiert, um eine Fluidverbindung zwischen dem Einlass (104)
und dem Auslass (106) des Gehäuses (102) zu ermöglichen, wobei das zweite Ventilelement
(118) innerhalb des Gehäuses (102) beweglich zwischen einer offenen Stellung, in der
das erste und das zweite Ventilelement (116, 118) außer Eingriff sind, um eine Fluidverbindung
zwischen dem Einlass (104) und dem Auslass (106) des Gehäuses (102) durch den Strömungsweg
zu ermöglichen, und einer geschlossenen Stellung angebracht ist, in der das erste
und das zweite Ventilelement (116, 118) in Eingriff sind, wodurch eine Fluidverbindung
zwischen dem Einlass (104) und dem Auslass (106) des Gehäuses durch den Strömungsweg
verhindert wird;
eine Vorspannanordnung, die auf das zweite Ventilelement (118) wirkt, um das zweite
Ventilelement (118) in Richtung der geschlossenen Stellung vorzuspannen, um einen
Durchfluss zwischen dem Einlass (104) und dem Auslass (106) zu verringern; und
eine Dichtungsanordnung (122), die zwischen dem zweiten Ventilelement (118) und dem
Gehäuse (102) vorhanden und dazu eingerichtet ist, dass ein Fluiddruck am Gehäuseeinlass
(104) und am Gehäusereferenzanschluss (108) eine Kraft auf das zweite Ventilelement
(118) ausübt, um das zweite Ventilelement (118) dazu zu veranlassen, sich relativ
zum ersten Ventilelement (116) zu bewegen und einen Durchfluss zwischen dem Einlass
(104) und dem Auslass (106) zu verändern, wobei zur Erleichterung einer Bewegung zwischen
dem zweiten Ventilelement (118) und dem ersten Ventilelement (116) der Fluiddruck
am Gehäuseeinlass die kombinierte Kraft des Gehäusereferenzanschlussdrucks und der
Vorspannanordnung übersteigen muss, so dass die Stellung des zweiten Ventilelements
(118) in Übereinstimmung mit einer Druckdifferenz zwischen Einlass- und Referenzdruck
erreicht wird.
2. Bohrlochinjektionsvorrichtung (100) nach Anspruch 1, wobei ein Teil der Dichtungsanordnung
(122) mit dem Einlass (104) des Gehäuses (102) solchermaßen in Verbindung steht, dass
ein Einlassdruck eine Kraft auf das zweite Ventilelement (118) in einer ersten Richtung
aufbauen kann, und ein Teil der Dichtungsanordnung (122) mit dem Referenzdruckanschluss
(108) des Gehäuses (102) solchermaßen in Verbindung steht, dass ein Referenzdruck
eine Kraft auf das zweite Ventilelement (118) in einer zweiten Richtung aufbauen kann,
die der ersten Richtung entgegengesetzt ist, und/oder wobei die Dichtungsanordnung
(122) so konfiguriert ist, dass eine Bewegung des zweiten Ventilelements (118) in
Übereinstimmung mit einer Druckdifferenz zwischen Einlass- und Referenzdruck erreicht
wird.
3. Bohrlochinjektionsvorrichtung (100) nach Anspruch 1 oder 2, wobei die Dichtungsanordnung
(122) einen Einlassdichtungsbereich, der dazu eingerichtet ist, einem Einlassdruck
ausgesetzt zu sein, und einen Referenzdichtungsbereich definiert, der dazu eingerichtet
ist, einem Referenzdruck ausgesetzt zu sein, wobei optional der Einlass- und der Referenzdichtungsbereich
im Wesentlichen gleich sind, oder wobei optional der Einlass- und der Referenzdichtungsbereich
unterschiedlich sind, um eine Kraftvorspannung auf das zweite Ventilelement durch
eine Wirkung des Einlass- und des Referenzdrucks zu erzeugen.
4. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
die Bohrlochinjektionsvorrichtung (100) dazu eingerichtet ist, dass der Einlassdruck
eine Kraft auf das zweite Ventilelement (118) erzeugt, um das zweite Ventilelement
(118) dazu zu veranlassen, sich in eine Richtung zur Erhöhung des Durchflusses zu
bewegen, und der Referenzdruck eine Kraft auf das zweite Ventilelement (118) erzeugt,
um das zweite Ventilelement (118) dazu zu veranlassen, sich in eine Richtung zur Verringerung
des Durchflusses zu bewegen.
5. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
ein Teil der Dichtungsanordnung (122) mit dem Auslass (106) des Gehäuses (102) in
Verbindung steht, wobei die Dichtungsanordnung (122) optional dazu eingerichtet ist,
die Wirkung des Auslassdrucks auf das zweite Ventilelement (118) im Wesentlichen zu
eliminieren, und/oder wobei die Dichtungsanordnung (122) dazu eingerichtet ist, dass
der Auslassdruck eine erste und eine zweite im Wesentlichen gleichgroße und entgegengesetzte
Kraft auf das zweite Ventilelement (118) ausübt, so dass jede Nettokraft im Wesentlichen
minimiert ist, oder wobei optional die Dichtungsanordnung (122) dazu eingerichtet
ist, dem Auslassdruck zu erlauben, eine gewünschte Vorspannkraft auf das zweite Ventilelement
(118) auszuüben.
6. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
die Dichtungsanordnung (122) erste und zweite Auslassdichtungsbereiche zwischen dem
zweiten Ventilelement (118) und dem Gehäuse (102) definiert und jeder der ersten und
zweiten Auslassdichtungsbereiche dazu eingerichtet ist, dem Auslassdruck ausgesetzt
zu sein, wobei optional die ersten und zweiten Dichtungsbereiche dazu eingerichtet
sind, dem Auslassdruck zu erlauben, eine Kraft auf das zweite Ventilelement (118)
in entgegengesetzten Richtungen auszuüben, wobei optional die ersten und zweiten Auslassdichtungsbereiche
im Wesentlichen gleich sind oder wobei optional die ersten und zweiten Auslassdichtungsbereiche
unterschiedlich sind.
7. Bohrlochinjektionsgerät (100) nach einem der vorhergehenden Ansprüche, wobei die Dichtungsanordnung
(122) erste und zweite Dichtungsbaugruppen (124, 126) umfasst, die sich zwischen dem
zweiten Ventilelement (118) und dem Gehäuse (102) erstrecken, wobei optional jede
der ersten und zweiten Dichtungsbaugruppen (124, 126) ein oder mehrere Dichtungselemente
umfasst, wobei optional die erste Dichtungsbaugruppe (124) den Gehäuseeinlass (104)
vom Gehäuseauslass (106) isoliert, so dass eine Fluidverbindung zwischen dem Einlass
(104) und dem Auslass (106) durch den Strömungsweg (120) im zweiten Ventilelement
geleitet wird, wobei optional die zweite Dichtungsbaugruppe (126) den Gehäuseauslass
(106) vom Gehäusereferenzausschluss (108) isoliert, wobei optional die erste Dichtungsbaugruppe
(124) einen Einlassdichtungsbereich definiert, der in der Vorrichtung (100) dazu angeordnet
ist, dem Einlassdruck ausgesetzt zu sein, wobei optional die erste Dichtungsbaugruppe
(124) einen ersten Auslassdichtungsbereich definiert, der in der Vorrichtung (100)
dazu angeordnet ist, dem Auslassdruck ausgesetzt zu sein, wobei optional die zweite
Dichtungsanordnung (126) einen Referenzdichtungsbereich definiert, der in der Vorrichtung
(100) dazu angeordnet ist, einem Referenzdruck ausgesetzt zu sein, wobei optional
die zweite Dichtungsanordnung (126) einen zweiten Auslassdichtungsbereich definiert,
der in der Vorrichtung (100) dazu angeordnet ist, einem Auslassdruck ausgesetzt zu
sein.
8. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, umfassend
eine Vorspannanordnung, die dazu eingerichtet ist, das zweite Ventilelement (118)
in eine gewünschte Richtung vorzuspannen.
9. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
im Gebrauch der Einlassfluiddruck am Einlass (104) des Gehäuses (102) zumindest teilweise
durch einen Fluiddruck innerhalb einer zugehörigen Injektionsleitung und/oder einer
zugehörigen Injektionsfluidquelle (110) definiert ist und der Auslassfluiddruck zumindest
teilweise durch einen Fluiddruck an einem zugehörigen Bohrlochzielort (112) definiert
ist und/oder wobei der Referenzdruck atmosphärisch oder geringer als atmosphärisch
ist.
10. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
der Referenzdruckanschluss (108) für eine Verbindung mit einer Referenzdruckquelle
(114) konfiguriert ist, mit Ausnahme eines Referenzdrucks von der Bohrlochzielposition
(112).
11. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
der Auslass (106) des Gehäuses (102) dazu eingerichtet ist, mit einem Bohrlochzielort
(112) in Verbindung zu stehen, der auf einer Seite einer Druckänderungsvorrichtung
angeordnet ist, und der Referenzdruckanschluss (108) dazu eingerichtet ist, mit einem
Ort in Verbindung zu stehen, der auf einer gegenüberliegenden Seite der Druckänderungsvorrichtung
angeordnet ist, wobei die Druckänderungsvorrichtung optional eine Pumpe umfasst.
12. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
der Auslass (106) des Gehäuses (102) dazu eingerichtet ist, mit einem Einlass einer
Pumpenbaugruppe in Verbindung zu stehen, und der Referenzdruckanschluss (108) dazu
eingerichtet ist, mit einem Auslass derselben Pumpenbaugruppe in Verbindung zu stehen,
und/oder wobei der am Referenzdruckanschluss (108) angelegte Referenzdruck vom Benutzer
einstellbar ist.
13. Bohrlochinjektionsvorrichtung (100) nach einem der vorhergehenden Ansprüche, wobei
das erste Ventilelement (116) relativ zum Gehäuse (102) fixiert ist, so dass eine
Bewegung des zweiten Ventilelements (118) erforderlich ist, um den Durchfluss zu variieren,
oder wobei das erste Ventilelement (116) durch ein vom Gehäuse (102) getrenntes Bauteil
definiert ist und das erste Ventilelement (116) sich innerhalb des Gehäuses (102)
bewegen kann.
14. Verfahren zum Einspritzen eines Fluids in einen Bohrlochzielort (112), umfassend:
Zuführen eines Injektionsfluids zu einem Einlass (104) eines Gehäuses (102) einer
Bohrlochinjektionsvorrichtung (100), die ein erstes Ventilelement (116) und ein zweites
Ventilelement (118) aufweist;
Vorspannen des zweiten Ventilelements (114) in Richtung des ersten Ventilelements
(116);
Verbinden eines Auslasses (106) des Gehäuses (102) mit einem Bohrlochzielort (112);
Verbinden eines Referenzanschlusses (108) des Gehäuses (102) mit einer Referenzdruckquelle
(114);
Veranlassen, dass sich ein zweites Ventilelement (118) relativ zu einem ersten Ventilelement
(116) bewegt, indem es einem Druck am Einlass (104) des Gehäuses (102) ausgesetzt
wird, wobei eine solche Bewegung nur nach Überwinden eines kombinierten Drucks der
Vorspannung und des Drucks am Referenzdruckanschluss (108) des Gehäuses (102) auftritt,
wobei eine solche Bewegung es ermöglicht, einen Durchfluss durch einen Strömungsweg
(120) des Ventilelements (118) einzustellen.
15. Pumpsystem, umfassend:
eine Strömungsleitung;
eine Pumpe, die mit der Strömungsleitung verbunden ist und eine Einlassseite und eine
Auslassseite definiert;
eine Bohrlochinjektionsvorrichtung (100) nach einem der Ansprüche 1 bis 13, wobei
der Auslass (106) des Bohrlochinjektionsvorrichtungsgehäuses (102) mit der Strömungsleitung
an einer Einlassseite der Pumpe in Verbindung steht, wobei ein Referenzdruckanschluss
des Injektionsvorrichtungsgehäuses mit der Strömungsleitung an einer Auslassseite
der Pumpe in Verbindung steht.