WO2015154160A1 - Appareil de dessablage et son procédé d'utilisation - Google Patents

Appareil de dessablage et son procédé d'utilisation Download PDF

Info

Publication number
WO2015154160A1
WO2015154160A1 PCT/CA2014/050712 CA2014050712W WO2015154160A1 WO 2015154160 A1 WO2015154160 A1 WO 2015154160A1 CA 2014050712 W CA2014050712 W CA 2014050712W WO 2015154160 A1 WO2015154160 A1 WO 2015154160A1
Authority
WO
WIPO (PCT)
Prior art keywords
vessel
particulates
fluid
freeboard
inclination angle
Prior art date
Application number
PCT/CA2014/050712
Other languages
English (en)
Inventor
Christopher HEMSTOCK
Original Assignee
Specialized Desanders Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Specialized Desanders Inc. filed Critical Specialized Desanders Inc.
Priority to AU2014390648A priority Critical patent/AU2014390648B2/en
Priority to BR112016023136-8A priority patent/BR112016023136B1/pt
Priority to SG11201608009YA priority patent/SG11201608009YA/en
Publication of WO2015154160A1 publication Critical patent/WO2015154160A1/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2494—Feed or discharge mechanisms for settling tanks provided with means for the removal of gas, e.g. noxious gas, air
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0015—Controlling the inclination of settling devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0087—Settling tanks provided with means for ensuring a special flow pattern, e.g. even inflow or outflow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D21/00—Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24—Feed or discharge mechanisms for settling tanks
    • B01D21/2405—Feed mechanisms for settling tanks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2221/00—Applications of separation devices
    • B01D2221/04—Separation devices for treating liquids from earth drilling, mining
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/02—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity

Definitions

  • the present disclosure generally relates to an apparatus and a method for removing particulates from multiphase fluid streams, and in particular, relates to an apparatus and a method for removing sands from multiphase fluid streams produced from an oil or gas well while minimizing the abrasion to the equipment involved.
  • Erosion of the production equipment is severe enough to cause catastrophic failure.
  • High fluid stream velocities are typical and are even purposefully designed for elutriating particles up the well and to the surface.
  • An erosive failure of this nature can become a serious safety and environmental issue for the well operator.
  • a failure such as a breach of high pressure piping or equipment releasee uncontrolled high velocity flow of fluid which is hazardous to service personnel. Releasing such fluid to the environment is damaging to the environment resulting in expensive cleanup and loss of production. Repair costs are also high.
  • a pressurized tank (“P-Tank”) is placed on the wellsite and the well is allowed to produce fluid and particulates.
  • the fluid stream is produced from a wellhead and into a P-Tank until sand production ceases.
  • the large size of the P-Tank usually restricts the maximum operating pressure of the vessel to something in the order of 1,000 - 2,100 kPa. In the case of a gas well, this requires some pressure control to be placed on the well to protect the P-Tank.
  • a pressure reduction usually is associated with an increase in gas velocity which in turn makes sand-laden wellhead effluent much more abrasive and places the pressure controlling choke at risk of failure.
  • Another problem associated with this type of desanding technique is that it is only a temporary solution. If the well continues to make sand, the solution becomes prohibitively expensive. In most situations with this kind of temporary solution, the gas vapors are not conserved and sold as a commercial product
  • Another known system includes employing filters to remove particulates.
  • a common design is to have a number of fiber-mesh filter bags placed inside a pressure vessel. The density of the filter bag fiber-mesh is matched to the anticipated size of the particulates. Filter bags are generally not effective in the removal of particulates in a multiphase condition. Usually multiphase flow in the oil and gas operations is unstable. Large slugs of fluid followed by a gas mist are common.
  • a desander having an elongate, horizontal vessel with an inlet at one end and an outlet at the other end.
  • the outlet separated from the inlet by a downcomer flow barrier, such as a wasi, adjacent the vessel's outlet or exit.
  • the weir forms, and maintains, an upper freeboard portion having a cross-sectional area which is greater that of the field piping from whence the fluid stream emanates for encouraging water and particulates to fall out of the freeboard portion.
  • Water and particulates accumulate along a belly portion. The accumulation of particulates is along a substantial length of the elongate vessel increasing the difficulty of periodic manual removal of such accumulating using scraper rods and the like.
  • Desanding apparatus is provided which is placed adjacent to a well's wellhead for intercepting a fluid stream flow before prior to entry to equipment including piping, separators, valves, chokes and downstream equipment
  • the fluid stream can contain a variety of phases including liquid, gas and solids.
  • a pressure vessel is inserted in the flowsteam by insertion into high velocity field piping extending from the wellhead.
  • the vessel contains an upper freeboard portion having a cross-sectional area which is greater that of the field piping from whence the fluid stream emanates.
  • the freeboard portion is maintained through control of the angle of the desander, obviating the need for a downcomer of Applicant's own prior art horizontal desanders.
  • a desanding system receives a gas stream containing entrained liquid and particulates.
  • the system comprises a vessel, elongated along a longitudinal axis and inclined from a horizontal at a non-zero inclination angle.
  • the vessel has a fluid inlet, adjacent an upper end for discharging the gas stream into the vessel at an inlet velocity, and a fluid outlet, spaced along the longitudinal axis from, and lower than, the fluid inlet
  • the vessel further has a gas/liquid interface at the fluid outlet, a belly storage portion formed below the interface, and a freeboard portion formed adjacent an upper portion of the vessel above the interface.
  • the freeboard portion has a freeboard cross-sectional area which diminishes from the fluid inlet to the fluid outlet, wherein a freeboard velocity, adjacent the fluid inlet is less than the inlet velocity, the freeboard velocity being such that the entrained liquids and particulates fall out of the gas stream for collecting in the belly storage portion.
  • a desanded gas stream flows out of the freeboard portion and out the fluid outlet, being free of a substantial portion of the particulates.
  • a vessel of an embodiment of the present invention is incorporated in a desanding system to replace existing prior connective piping for a wellhead, the vessel being supported using structure to align the vessel with the wellhead piping and downstream equipment
  • the desander's fluid inlet and fluid outlet associated with the inclined world of the desander are adapted to connect to the orthogonal world of the connective piping.
  • a method for desanding a fluid stream emanating from a wellhead and containing gas and entrained liquid and particulates, comprises providing an elongated vessel having a longitudinal axis which is inclined from the horizontal.
  • the vessel has a fluid inlet adjacent an first end of the vessel and a fluid outlet spaced along the longitudinal axis from the fluid inlet; inclining the vessel at angle from a horizontal at a non-zero inclination angle so that the fluid outlet is lower that the fluid inlet for forming a freeboard portion above the fluid outlet
  • the fluid stream is discharging from the fluid inlet, into the vessel and substantially parallel to the longitudinal axis for establishing a liquid interface in a belly portion of the vessel, the belly portion and being formed below the fluid outlet Liquid and particulates are being directed along a trajectory in the freeboard portion of the vessel to intercept a substantial portion of the particulates at the liquid interface for storage in the belly portion.
  • a desanded gas stream is recovered at the fluid outlet which is substantially free of part
  • the inlet can be parallel or non-parallel with the longitudinal axis for enabling a trajectory to intercept the gas/liquid interface.
  • the fluid stream can be introduced through a replaceable nozzle.
  • the fluid inlet can be curved to align the inlet from the inclined desander and orthogonal piping from a wellhead.
  • a vessel having a distal end and a proximal end for removing particulates from a multiple-phase fluid stream containing gas, entrained liquid and particulates
  • the vessel comprising: a volume having a diverging bounding wall, a distal base, and an apex; the diverging bounding wall having a top wall at a first inclination angle and a bottom wall at a second inclination angle; the second inclination angle at a greater angle than the first inclination angle; a fluid inlet interface at the apex for receiving said fluid stream into the volume of the vessel; a fluid outlet on the top of the top wall, spaced from the fluid inlet interface; a horizontally extending freeboard interface separating a freeboard portion formed adjacent an upper portion of the vessel above the interface and a belly portion therebetow, the belly portion being bounded at its bottom by the bottom wall, the freeboard portion forming a freeboard cross-sectional area for a freeboard velocity of the fluid
  • the second inclination angle may be greater than the angle of repose of settled particulates.
  • the top inclination angle may be inclusively between 2 and 20 degrees.
  • the cross-sectional shape of the proximal base may be circular.
  • the central axis may be perpendicular to the plane of the distal base. In some other embodiments, the central axis may be oblique to the distal base.
  • the vessel may further comprise a lower discharge from the belly portion for discharging liquid and collected particulates.
  • the discharge further comprises: an inlet valve adjacent and fluldly connected to the discharge; a particulate accumulation chamber; and a discharge valve, wherein the particulate accumulation chamber is sandwiched between the inlet valve and the discharge valve.
  • the fluid inlet interface has a discharge end, and the discharge end is oriented for discharging the gas stream into the freeboard at an angle equal to the top inclination angle.
  • the fluid inlet interface may further comprise a replaceable nozzle having a discharge end oriented for discharging the gas stream into the freeboard.
  • the replaceable nozzle may be connected to the fluid inlet interface at a flange.
  • the desanding system receives a gas stream emanating from a wellhead and the fluid inlet interface further comprises a receiving end for receiving the gas stream, the receiving end being orthogonal to the wellhead.
  • the top inclination angle is variable for varying fluid stream conditions. In some other embodiments, the bottom inclination angle is variable for particulate stream conditions.
  • a method for desanding a fluid stream emanating from a wellhead comprising: providing an elongated vessel extending from a proximal end downwardly towards a distal end and having a diverging bounding wall to define a top inclination angle and a bottom inclination angle larger than the top inclination angle; injecting, at a first fluid velocity, the fluid stream into the vessel from the proximal end at about the first inclination angle; directing, at a second fluid velocity slower than said first fluid velocity, said fluid stream along an elongated flow path in the vessel from the proximal end towards the distal end to allow an effective amount of the entrained liquid and particulates fall out of the fluid stream and move into a belly portion; collecting desanded gas in a freeboard portion, said freeboard portion being above the belly portion and being separated therefrom by a gas/liquid interface; and discharging the
  • the method further comprises collecting desanded liquid from the belly portion and discharging, from the belly portion, the desanded liquid with the discharged gas at the distal end.
  • Figure 1 is a cross-sectional side view of Applicants prior art elongated horizontal desander illustrating downcomer flow barrier, fluid streams, falling trajectory of particulates, and accumulations of separated liquid, particulates and particulate-free fluid discharge;
  • Figure 2 is a cross-sectional view of an embodiment of a tilted or inclined desander
  • Figures 3A and 3B are perspective representations of the volumes of the belly portion and freeboard portions of the inclined desander of Fig. 2;
  • Figure 4 is a cross-sectional view of another embodiment of an inclined desander having a greater inclination angle than that of Fig.2;
  • Figure 5 is a cross sectional view of a curved fluid inlet, square to the desander, and having a long radius angular transition elbow between orthogonal piping and the inclined desander;
  • Figure 6 is a representation of an inclined desander illustrating parameters for an example 36 inch diameter desander having a horizontal fluid inlet;
  • Figure 7 is a cross-sectional view of a desander having a tilted conical vessel, according to another embodiment DETAILED DESCRIPTION
  • a desander is typically inserted between or as a replacement for existing piping such as connecting piping between a wellhead and downstream equipment such as multiphase separators.
  • a prior art horizontal desander comprises a cylindrical pressure vessel 11 having a substantially horizontal axis A, a first fluid inlet end 12 adapted for connection to the fluid stream F.
  • the fluid stream F typically comprises a variety of phases including gas G, some liquid L and entrained particulates such as sand S.
  • the fluid stream F containing sand S enters through the inlet end 12 and is received by a freeboard portion 13.
  • the freeboard area is set by a downcomer flow barrier 14. Accordingly, the velocity of the fluid stream F slows to a point below the entrainment or elutriation velocity of at least a portion of the particulates S in the fluid stream.
  • an inclined desander 20 are free of the prior art flow barrier and, through tilting or inclination of the vessel, maximize freeboard upon entry of the flow stream, and reduce liquid flow rates for maximizing settling conditions therein and retention of captured particulates S. Variability of the inclination angle o enables a measure of variability between the respective freeboard and liquid-storing belly portion for adjusting performance.
  • the desander 20 comprises a vessel 22 having an axis A oriented at an acute angle o to the horizontal H.
  • the desander 20 has a fluid inlet 24 at an upper end 25 for receiving a fluid stream F typically comprising a variety of phases including gas G, some liquid L and entrained particulates such as sand S.
  • the fluid inlet 24 is oriented parallel to a longitudinal axis A of the vessel 22.
  • a fluid outlet 26 is located along a top 28 of the vessel 22, and spaced from the fluid inlet 24.
  • a gas/liquid interface 32 forms extending horizontally from about the fluid outlet 26.
  • a belly portion 40 is formed below the interface 32 for containing liquid L and particulates S.
  • a freeboard portion 44 is formed above the interface 32.
  • the fluid inlet 24 discharges into the freeboard 44.
  • Particulate trajectory can be manipulated by positioning and orienting a discharge end 29 of the fluid inlet 24.
  • the discharge 29 of the inlet 24 can be aligned parallel to the vessel axis A.
  • the inlet 24 or discharge 29 can be oriented in other orientations including above the inclined axis A, or below the axis A.
  • the interface 32 is a generally obround, gas/liquid interface between the belly and freeboard portions 40, 44.
  • the obround interface 32 has a distal end 33 adjacent the fluid outlet 26 and a proximal end 34, the location of which is intermediate the fluid outlet 26 and fluid inlet 24 and varies with liquid level and inclination angle o.
  • the trajectory of the fluid stream F, from inlet 24, converges with the interface 32.
  • the trajectory for dropping sand S and liquid L into the belly portion 40 is foreshortened, reducing drop out time.
  • the vessel 22 is long enough to space the fluid inlet 24 sufficiently from the interface 32 to minimize turbulence of the liquid L in the belly portion 40, that spacing being dependent upon various design factors including vessel inclination angle o, inlet fluid stream velocity and characteristics.
  • the maximum level of the interface 32 is controlled at the distal end 33, set by eventual liquid entrainment and discharge at the fluid outlet 26.
  • Gas G discharges at the fluid outlet 26.
  • any oil and other liquids are re- entrained with the gas G exiting at fluid outlet 26.
  • Particulates S continue to be captured in the belly portion 40 until its volumetric capacity is reached.
  • Connective piping 46 between conventional wellhead and downstream equipment, is typically in rectilinear or orthogonal arrangements.
  • the angle o of the desander 20 introduces coupling or connection challenges.
  • the connective piping 46 is generally horizontal or vertical and incorporation of the inclined desander 20 requires an adjustment made at the fluid inlet 24 and fluid outlet 26.
  • the fluid outlet 26 can be fit to the top 28 of the vessel 22 at angle a, orienting the outlet 26 vertically and thereby obviating the need for an angular transition.
  • the desander 20 is shown diagrammatically split at the interface 32 for illustrating the incrementally increasing volume of the belly portion 40 below and the incrementally decreasing volume of freeboard portion 44, increasing and decreasing as referenced to the feed stream F.
  • the freeboard portion 44 demonstrates a cross-sectional area which diminishes from the fluid inlet 24 to the fluid outlet 26.
  • a freeboard velocity at the fluid inlet 24 is such that the entrained liquids L and particulates S fall out of the fluid stream F and collect in the storage belly portion 40.
  • the cross-sectional area of the freeboard portion 44, adjacent the fluid inlet 24, is at its greatest for achieving the lowest average inlet velocity for maximum drop out efficiency for particulates S and liquids L
  • the velocity reduction upon discharge is significantly greater than that of Applicants prior art horizontal desander. Particulate removal is accomplished while minimizing the portion of the vessel allocated to the freeboard portion 44, maximizing the efficiency of that freeboard portion for particulate drop out, and resulting in a greater allocation of the overall portion of the vessel to the belly portion 40 for storage.
  • Velocity in the freeboard portion 44 increases after a substantial portion of the particulates S have already deposited in the belly portion 40.
  • the cross-sectional area of the belly portion 40 increases towards the fluid outlet 26 and the velocity of liquids accumulating therein diminishes.
  • particulates accumulate and flow downvessel at an angle of repose.
  • the accumulation of liquid L and particulates S establishes a downward flow in the belly portion, and as the particulates accumulate and limit the free flow of the liquid L in the belly portion 40, the liquid velocity begins to increase, drawing more particulates S down vessel.
  • the inclination angle o can be adjusted, shown here as an increased angle over that of Fig. 2.
  • the trajectory of the feed stream impinges the interface 32 at less acute angle, impinges the interface 32 sooner and enables selection of shorter vessels 22 and greater particulate removal efficiency.
  • Inclination angles o can be adjusted, for a given length of vessel 22, between fluid inlet 24 and fluid outlet 26, to accommodate gas G and liquid L content in the feed fluid stream F. Inclination angles o would generally be in the range of about 2 degrees to about 20 degrees.
  • the shallowest operating angle o is limited by the minimum requirement for a minimum freeboard 44 cross- sectional area adjacent the inlet 24 once the interface 32 builds to about the fluid outlet 26.
  • the steepest operating angle o is limited by the requirement for a minimum storage capacity in the belly portion 40.
  • the minimum inclination angle would be the condition where the inlet 24 is entirely in the gas phase of the freeboard portion 44 and the gas phase at the discharge is of zero height
  • the maximum inclination angle would be the condition where the inlet 24 is well above the gas/liquid interface allowing substantial freeboard to handle slug flow. Angles above 45 degrees limit the performance of desander considerably since the residence time of the liquid phase in the belly portion 40 is reduced.
  • the fluid inlet 24, exposed to entrained particulates S in the fluid stream, is subject to greatest risk of erosion.
  • the inlet 24 can be integrated with the vessel 22, one can also provide an inlet 24 or discharge 29 that is replaceable for ease of maintenance. Options include accepting eventual wear and shutdown of the desander 20 for replacement of an integrated inlet 24; modifying the material or configuration of the inlet 24 to prolong service life, or using replaceable discharge of nozzle for minimizing turnaround time.
  • one approach is to make the discharge 29 replaceable including incorporating features of a replaceable nozzle as set forth in Applicant's Patent CA 2,535,215 issued May 8, 2008.
  • a replaceable nozzle 50 can be fit to a compatible coupling at the upper end 25 of the vessel 22.
  • replaceable nozzle 50 comprises the discharge 29, and a threaded connection or nozzle flange 29i, for connection to a compatible threacled connection or flange 24i at the inlet 24 of the vessel 22.
  • the orientation of the discharge is dependent on the coupling 24i, 29i and arrangement of the discharge relative thereto.
  • the replaceable nozzle 50 includes a connecting piping coupling, such as a connective flange 47i for connecting to the piping 47.
  • the nozzle 50 can incorporate a curved portion 51 , such as a long radius elbow, transition between the orthogonal world of the connecting piping and the inclined axis A of the vessel 22. That curved portion 51 can be integrated with the inlet 24, nozzle 50 or located in advance thereof, such as in a transition pup joint
  • Prior art desanders 10 such as that described in US 6,983,852 to Applicant, for different feed fluid streams F, might include one typical standard vessel 11 having a nominal 0.3 m (12 inch) diameter by 3.048 m (10 feet) long and another vessel 11 having 0.3 m (12 inch) diameter by 6.096 m (20 feet) long, both of which are fitted with a downcomer weir to set the freeboard portion.
  • the prior art downcomer flow barrier such as a weir
  • the prior art downcomer flow barrier can be eliminated by providing similar 0.3 m (12 inch) diameter vessels 22 and tilting the upper end 30 of the new desander 20 at about twice the prior art weir height so as to form the interface 32 at the fluid outlet 26.
  • a 20 foot long inclined vessel 22 would only need to be inclined about 1 ⁇ 2 the angle o of the 10 foot long inclined vessel 22. Performance can be adjusted by varying the angle.
  • An example of an inclined desander 20 includes that sized to receive a fluid stream F of 50 m 3 /d, bearing particulates S having an average size of 150 urn.
  • the fluid stream typically includes sufficient liquid to accumulate in the belly portion.
  • the fluid stream F is discharged to vessel 22, having a 0.3 m (1 foot) diameter and 3.048 m (10 feet) long.
  • a typical pressure of the fluid stream F is about 7000 kPa (1015 psia).
  • the freeboard volume is 0.10 m 3 and the belly portion is 0.486 m 3
  • the resulting belly portion capacity is about 502 kg of liquid and sand particulates.
  • an inclined desander 20 illustrates some additional optional characteristics including a fluid inlet 24 oriented horizontally, the inlet being directly connectable to orthogonal connection piping.
  • the discharge 29 is oriented at an angle to the longitudinal axis A, in this case in a generally horizontal plane, which is angled upwardly from axis A.
  • the initially horizontal trajectory of a substantial portion of the feed stream falls off before engaging the vessel 22.
  • the inlet 24 can be square to the connective pipe as, in this embodiment, the vessel 22 is of sufficient diameter, such as 36 inches, to permit inlet placement in the freeboard 44 while the trajectory is such that it minimizes or avoids vessel wall involvement.
  • a horizontal spacing between the inlet 24 and inside wall of the vessel 22 is about 1.5 feet
  • Removal of accumulated particulates is conducted periodically with the vessel 22 shut in, adjacent the inlet 24 and outlet 26, and depressurized. Conveniently, access can be through a pressure-rated access closure and port at the lower end 42, as the angle of repose and flow in the belly portion carries particulates thereto.
  • a suitable closure is shown in Fig. 1 of the prior art and in Fig. 6 as adapted to the inclined desander 20.
  • the vessel 22 is supported sufficiently high of the ground or otherwise positioned for angular access thereto, such as with scrapers and the like.
  • a pressure vessel, hemispherical head-form of closure 60 can be pivoted from the vessel 22 and counterweighted to dose flush to the inclined cylindrical end of the vessel 22.
  • a gantry 62 assists in manipulation of the head for access to the belly portion 40.
  • the illustrated vessel 22 includes an eccentric end 64 at the lower end 42, to reduce the diameter of the vessel 22 downstream of the fluid outlet 26.
  • Advantages of reducing the vessel diameter at the lower end 42 include adapting to a smaller, more easily manageable or standard form of dean out
  • the deanout is a pressure-rated closure 60 supported upon gantry 62.
  • a 36 inch vessel having 33 inch internal diameter, is indined at 4 degrees.
  • the cylindrical portion of the vessel is about 20 feet long with a 3 foot long eccentric portion, redudng the diameter from 3 to about 18 inches for fitting an 18 inch dean out
  • Conventional pressure safety valves and other gas phase related devices and instrumentation, not shown, are reliably located in the freeboard portion 44 between the fluid outlet 26 and the upper end 25.
  • Fig. 7 shows a cross-sectional view of a desander 100, according to an alternative embodiment
  • the desander 100 comprises a tilted vessel 102 coupled to a particulate collection structure 180.
  • the desander 100 does not require a flow barrier.
  • the vessel defines an elongate, enclosing volume having a surface or diverging bounding wall terminated at opposing ends; a proximal end accommodating a flow inlet, and distal end.
  • a portion of the bounding wall is oriented as a top wall and a portion of which is oriented as a bottom wall.
  • the top wall is tilted downwardly in the direction of flow at a first angle of inclination.
  • the bottom wall is also tiled downwardly in the direction of flow.
  • the slope of the bottom wall is divergent from the top wall so as to have a second angle of inclination that is greater than that of the top wall.
  • a conical vessel can be a circular cone having an axis extending from the apex to the base and a surface thereabout, the axis of which is angled so that the top wall has the downward and first angle of inclination.
  • a right conical vessel has a circular cross-section; however, non-circular cross- sections are contemplated including elliptical, obround and polygonal.
  • One skilled in the art would have to account for the use of non-conventional shapes when considering pressure boundaries or use a conventional pressure boundary with non pressure bearing internals of the proposed shapes.
  • the desander 100 maximizes the effectiveness of the freeboard portion, and reduces liquid flow rates to optimize settling conditions therein and improve retention of captured particulates S.
  • components described as proximal and distal as related to their proximity to the inlet are described as proximal and distal as related to their proximity to the inlet.
  • a conical body 104 extending from a lower, distal end 106 tapering to an upper, proximal end 108 with a central axis 110 upwardly slanting from a horizontal line (not shown).
  • the vessel is a right circular conical frustum having a circular distal base 112 at the lower, distal end 106 perpendicular to the central axis 110, a geometric surface comprising a conical wall 114 shown axially symmetrical to the central axis 110, and an apex 116 at the upper, proximal end 108.
  • apex 116 is truncated for installation of connecting hardware such as flanges.
  • the vessel 102 is characterized by a first acute top inclination angle a defined by a top wall 118 of the body 104 and a horizontal line 120, and a second, bottom inclination angle ⁇ defined by the bottom wall 122 of the body 104 and a horizontal line 124.
  • the top inclination angle a is selected for forming the freeboard portion of the vessel
  • the bottom inclination angle ⁇ is selected for forming a belly portion that minimizes sand deposition and instead encourages a mobile sand dune for migration of settled particulates to a sump at the bottom of the vessel and subsequent transferring to a sand accumulator.
  • the relationship between the top and bottom inclination angles a and ⁇ , the diameter of the circular distal base 112, the diameter of the circular truncated apex 116 and the length (i.e., the distance between the distal base 112 and the truncated apex 116) of the vessel 102 is:
  • ⁇ Arctan( (D_distal - D_proximal) /2 / L) ) x 2 + ⁇ , where Arctan() represents the arctangent function, D_distal represents the diameter of the circular distal base 112, D_proximal represents the diameter of the circular truncated apex 116, and L represents the length of the vessel 102 measured along the central axis 110. Therefore, the vessel 102 may be customized in design by selecting a proper vessel length, diameter of the circular distal base 112, ratio of the diameter of the circular distal base 112 to that of the circular truncated apex 116, and top inclination angle a to meet a process performance requirement
  • the vessel 102 comprises a fluid inlet interface 140 at the upper proximal end 108 and a fluid outlet 142 located on the top side of the vessel in proximity with the distal end 106 and spaced from the fluid inlet interface 140.
  • the fluid inlet interface 140 comprises a receiving end 144 outside the vessel 102 for receiving a fluid stream F typically comprising a variety of phases including gas G, some liquid L and entrained particulates such as sand S, and a discharge end 146 inside the vessel 102 for discharging the received multiphase fluid stream F into the vessel at an inlet velocity.
  • the position and orientation of the discharge end 146 determine the particulate trajectory.
  • the discharge end 146 is oriented such that the received fluid F is injected into the vessel along a direction 148 parallel to the top wall 118.
  • the discharge end 146 may alternatively be oriented in other orientations, e.g., an angle smaller or larger than that of the top wall 118, depending on the design.
  • a gas/liquid interface 160 forms extending horizontally in the vessel 102 from about the fluid outlet 142.
  • the gas/liquid interface 160 is a generally elliptic, gas and liquid interface having a distal end 166 adjacent the fluid outlet 142 and a proximal end 168, the location of which is determined by the lower end of the fluid outlet 142 and the top inclination angle a.
  • a freeboard portion 164 is formed above the gas/liquid interface 160.
  • a belly portion 162 is formed below the gas/liquid interface 160 for containing liquid L and particulates S. The belly portion 162 has a large volume as the diameter of the vessel 102 increases towards the distal end 106.
  • a fluid stream discharged from the fluid inlet interface 140 travels along an elongated flow path from the fluid inlet interface 140 to the fluid outlet 142.
  • the freeboard portion 164 has a cross-sectional area greater than that of the fluid inlet interface 140, the fluid velocity in the freeboard portion adjacent the fluid inlet interface 140, is less than that in the inlet, and particulates cannot be maintained in suspension.
  • the trajectory for dropping sand S and liquid L into the belly portion 162 is foreshortened, reducing drop out time.
  • the vessel 102 is of sufficient length to space the fluid inlet 140 sufficiently from the gas/liquid interface 160 to minimize turbulence of the liquid L in the belly portion 162, that spacing being dependent upon various design factors including vessel top inclination angle a, bottom inclination angle ⁇ , inlet fluid stream velocity and characteristics.
  • the level of the gas/liquid interface 160 is controlled by the fluid outlet 142 in proximity with the distal end 106, set by eventual liquid entrainment and discharge at the fluid outlet 142.
  • the fluid outlet 142 In steady state, when the liquid level reaches the fluid outlet 142, any oil and other liquid is re- entrained with the gas G exiting at fluid outlet 142.
  • the fluid stream discharged from the fluid outlet 142 has about the same gas/liquid ratio as the stream received at the inlet 140. In other words a mass balance is established in that discharged liquid matches incoming liquid.
  • Particulates S continue to be captured in the belly portion 162, creating an unstable sand bank.
  • the particulates form a sand bank on the lower portion of the vessel 102.
  • the bottom inclination angle ⁇ of the vessel 102 is selected to be steep enough, e.g., to be about or larger than the angle of repose of a bank of wet particulates.
  • the sand and liquid migrate towards the bottom of the vessel 102 via a lower discharge 172 into the particulate collection structure 180, and fall through the open valves 182 into the sand accumulation chamber 184.
  • the liquid discharged from the fluid outlet 142 will, on occasion, be less than that in the incoming liquid by the amount removed with the particulates.
  • At least particulates are collected and discharged from the belly portion.
  • particulates and liquid are collected in the belly portion and are periodically or continuously discharged therefrom.
  • liquid is discharged with desanded gas from the freeboard portion at the distal end at the fluid outlet 142.
  • the fluid inlet 140 and the fluid outlet 142 are connected to the connective pipes of a conventional wellhead and downstream equipment (not shown), respectively.
  • the receiving end 144 of the fluid inlet interface is typically orthogonal to the wellhead.
  • the fluid outlet 142 is configured in a vertical orientation and thereby obviates the need for an angular transition.
  • the fluid inlet 140 being exposed to entrained particulates S in the fluid stream F, is subject to significant risk of erosion, and has to be properly designed to ensure the regular use of the desander 100.
  • Methods described above e.g., using appropriate material or configuration to prolong its service life, regularly replacing the wom-out fluid inlet, and/or using a replaceable discharge of nozzle, may be used in various embodiments.
  • a replaceable nozzle as shown in Fig. 5 that has a discharge end with an inclination angle a and a horizontal receiving end is used for coupling to the horizontal connective pipe (not shown).
  • Velocity in the freeboard portion 164 increases after a substantial portion of the particulates S have already deposited in the belly portion 162.
  • the cross-sectional area of the belly portion 162 increases towards the fluid outlet 142, and the velocity of liquids accumulating therein diminishes.
  • particulates accumulate and flow down the vessel 102 at an angle of repose.
  • the accumulation of liquid L and particulates S establishes a downward flow in the belly portion 162, and as the particulates accumulate and limit the free flow of the liquid L in the belly portion 162, the liquid velocity begins to increase, drawing more particulates S down vessel.
  • the bottom inclination angle ⁇ is greater than the angle of repose of a bank of wet particulates, the sand will migrate towards the particulate collection structure 180.
  • the top inclination angle a may be selected to meet the requirement of accommodating gas G and liquid L content in the feed fluid stream F.
  • the smallest top inclination angle a is limited by the minimum requirement for a minimum freeboard 164 cross-sectional area adjacent the inlet 140 once the gas/liquid interface 160 builds to about the fluid outlet 142.
  • the largest top inclination angle a is limited by the requirement for a minimum freeboard gas capacity to accommodate particulate removal of any sand S in the gaseous phase G of the incoming fluid stream F.
  • the minimum top inclination angle a is the minimum inclination angle of the top wall 118 that ensures the inlet 24 be entirely in the freeboard 164 when the gas/liquid interface 160 reaches the bottom of the fluid outlet 142.
  • the maximum top inclination angle a is the inclination angle of the top wall 118 at which the inlet 140 is well above the gas/liquid interface 160 allowing substantial freeboard to handle slug flow.
  • the trajectory of the injected fluid stream F impinges the gas/liquid interface 160 at less acute angle, impinges the gas/liquid interface 160 sooner and allows the use of shorter vessels 102 and greater particulate removal efficiency.
  • the top inclination angle a is preferably selected from the range of about 2 degrees to about 20 degrees.
  • the bottom inclination angle ⁇ may be selected to be great than or equal to the estimated angle of repose of a wet sand bank to facilitate smooth particulates drop-off.
  • the bottom inclination angle ⁇ is larger than the top inclination angle a.
  • the conical shape vessel 102 is determined after the length of the vessel 102, the top and bottom inclination angles a and ⁇ are selected.
  • a desander 100 comprises a conical shape vessel 102 having a circular distal base of diameter 0.91 meter (36 inches), a circular truncated apex of diameter 0.154 meter (i.e., 6 inches) and a length of 3.05 meters (i.e., 10 feet).
  • the vessel is tilted such that the bottom inclination angle ⁇ is 35 degree.
  • the vessel 102 comprises a lower discharge 172 coupled to the particulate collection structure 180 to allow particulates and liquid to migrate thereto.
  • the particulate collection structure 180 comprises a sand accumulation chamber 184 sandwiched between an inlet valve 182 and a discharge valve 186.
  • the inlet valve 182 is connected to the vessel 102 on top thereof and to the sand accumulation chamber 184 therebelow, and the sand accumulation chamber 184 is in turn connected to the discharge valve 186 therebelow.
  • the particulate collection structure 180 also comprises a particulate detector 188, e.g., an ultrasonic sand detector, to detect particulate accumulation in the sand accumulation chamber 184.
  • the inlet valve 182 may be set to the open position and the discharge valve 186 set to the closed position in normal operation to allow the sand accumulation chamber 184 to collect particulates and liquid from the vessel 102.
  • the removal of accumulated particulates can be conducted periodically with the vessel 102 being pressurized and in operation.
  • the valves 182 and 186 are controlled automatically by the particulate detector 188 to periodically open and dose.
  • an interlock is used to prevent the inlet and discharge valves from being open at the same time.
  • the valve 182, between the vessel 102 and the sand accumulation chamber 184 is normally open except at the time of particulate removal, allowing particulates to fall into the accumulator.
  • the discharge valve 186 is normally closed except at the time of particulate removal.
  • valve 182 is first closed. Valve 186 is then opened allowing the particulates contained in the sand accumulation chamber 184 to exit Usually, valve 186 is opened only for a short period of time sufficient to allow the volume of the sand accumulation chamber 184 to be evacuated. After removing particulates from the sand accumulation chamber 184, valve 186 is closed and valve 182 is then reopened to allow particulates in the particulate drop out the vessel 102 to migrate into the sand accumulation chamber 184.
  • the belly portion 162 of the vessel has sufficient space to store particulates inside the vessel 102 during the particulates-removing process, and the volume of the sand accumulation chamber 184 is sufficiently large to discharge enough particulates within a cleaning cycle so as not to cause a backup of particulates into valve 182 thereby preventing the valve to dose.
  • Both valves 182 and 186 are required to have service rated for abrasive slurries.
  • valve 182 can be left open.
  • Valve 186 is opened only for a short period of time, sufficient to allow the volume of the sand accumulation chamber 184 to be evacuated.
  • the vessel 102 is supported by supporting structure to maintain the vessel 102 in its vertical orientation.
  • the top inclination angle of the vessel 102 is adjustable at the time of installation.
  • the fluid inlet 140 and outlet 142 are rendered orthogonal. After installation, the orientation of the vessel 102, the receiving end 144 of the inlet 140, the fluid outlet 142 and the particulate collection structure 180 is then fixed for operation.
  • the support structure comprises an inclination adjustment structure for adjusting the inclination angle of the vessel 102 to adapt to fluid stream conditions and or particulate stream conditions.
  • the support structure may comprise a first support anchor pivotably coupled to the vessel 102 at a position near the distal end thereof, and a second support anchor pivotably coupled to the vessel 102 at a position near the truncated apex thereof.
  • the height of the first and/or second support anchors is adjustable such that the inclination angle of the vessel may be adjusted by adjusting the height of the first and/or second support anchors.
  • the fluid outlet 142 and the particulate collection structure 180 may be pivotable within a predefined range of angle to allow a generally orthogonal orientation under any suitable inclination angle of the vessel 102.
  • the inlet 140 may also be pivotaWe within a predefined range of angle such that the orientation of the receiving end 144 thereof may be adjusted to adapt to the orientation of the vessel.
  • a set of inlets 140 are provided to allow users to choose an inlet 140 suitable for an orientation-adjusted vessel 102 and install it thereon.
  • a particulate detector 188 is used for detecting particulate accumulation in the sand accumulation chamber 184
  • a timer may alternatively be used to periodically control valves 182 and 186 to remove particulates from the sand accumulation chamber 184.
  • no particulate detector or time is used, and the valves 182 and 186 are manually controlled to remove particulates from the sand accumulation chamber 184.
  • the vessel 102 is a tilted, right circular conical frustum
  • the vessel 102 may be an oblique circular frustum such that the circular distal base located at the lower, distal end of the vessel is not perpendicular to the central axis.
  • the vessel 102 tapers from the distal end to a smaller, truncated apex at the proximal end
  • the vessel 102 has a constant diameter from the distal end to the proximal end.
  • the particulate collection structure 180 may alternatively comprise different components.
  • the particulate collection structure 180 may be a simple sand sump having no valve.
  • the desanding devices in the embodiments described above are made of suitable material for the environment, fluid and pressures, such as steel or the like, with specifications satisfying relevant safety code requirements.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

L'invention concerne un système de dessablage comprenant une cuve allongée qui est inclinée selon un angle d'inclinaison non nul. La cuve possède une extrémité supérieure qui bascule vers le bas en direction d'une extrémité distale, et comprend une paroi de délimitation divergente de manière qu'une paroi supérieure possédant un premier angle d'inclinaison et une paroi inférieure possédant un second angle d'inclinaison supérieur au premier angle d'inclinaison soient définies. Une interface d'entrée de fluide à l'extrémité supérieure de la cuve décharge un courant gazeux contenant les liquides et matières particulaires entraînés, dans une partie de revanche adjacente à la paroi supérieure au-dessus d'une interface gaz-liquide formée au-dessous de la sortie de fluide. Une section transversale de la partie de revanche provoque la précipitation des liquides et matières particulaires qu'ils contiennent pour la collecte dans une partie de stockage ventrale formée au-dessous de l'interface. Un courant gazeux dessablé, débarrassé d'une partie importante des matières particulaires est retiré de la cuve par une sortie de fluide adjacente à la base distale.
PCT/CA2014/050712 2014-04-11 2014-07-29 Appareil de dessablage et son procédé d'utilisation WO2015154160A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
AU2014390648A AU2014390648B2 (en) 2014-04-11 2014-07-29 A desanding apparatus and a method of using same
BR112016023136-8A BR112016023136B1 (pt) 2014-04-11 2014-07-29 Aparelho de desarenação e método de uso do mesmo
SG11201608009YA SG11201608009YA (en) 2014-04-11 2014-07-29 A desanding apparatus and a method of using same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2,848,738 2014-04-11
CA2848738A CA2848738C (fr) 2014-04-11 2014-04-11 Un appareil de dessablage et une methode d'utilisation dudit appareil

Publications (1)

Publication Number Publication Date
WO2015154160A1 true WO2015154160A1 (fr) 2015-10-15

Family

ID=54287038

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CA2014/050712 WO2015154160A1 (fr) 2014-04-11 2014-07-29 Appareil de dessablage et son procédé d'utilisation

Country Status (6)

Country Link
AU (1) AU2014390648B2 (fr)
BR (1) BR112016023136B1 (fr)
CA (1) CA2848738C (fr)
MY (1) MY174765A (fr)
SG (1) SG11201608009YA (fr)
WO (1) WO2015154160A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11173427B2 (en) 2017-09-25 2021-11-16 Sand Separation Technologies Inc. Device for separating solids from a fluid stream
US11839884B2 (en) 2018-09-06 2023-12-12 Sand Separation Technologies Inc. Counterflow vortex breaker

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2646150A1 (fr) * 2007-12-12 2009-06-12 Occidental Oil And Gas Holding Corporation Separation du sable des fluides produits par un puits
WO2010034325A1 (fr) * 2008-09-24 2010-04-01 Statoilhydro Asa Séparateur gaz-liquide
US7785400B1 (en) * 2009-06-30 2010-08-31 Sand Separators LLC Spherical sand separators

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2646150A1 (fr) * 2007-12-12 2009-06-12 Occidental Oil And Gas Holding Corporation Separation du sable des fluides produits par un puits
WO2010034325A1 (fr) * 2008-09-24 2010-04-01 Statoilhydro Asa Séparateur gaz-liquide
US7785400B1 (en) * 2009-06-30 2010-08-31 Sand Separators LLC Spherical sand separators

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11173427B2 (en) 2017-09-25 2021-11-16 Sand Separation Technologies Inc. Device for separating solids from a fluid stream
US11839884B2 (en) 2018-09-06 2023-12-12 Sand Separation Technologies Inc. Counterflow vortex breaker

Also Published As

Publication number Publication date
MY174765A (en) 2020-05-13
AU2014390648A1 (en) 2016-10-13
BR112016023136B1 (pt) 2022-04-19
BR112016023136A2 (fr) 2017-08-15
CA2848738A1 (fr) 2015-10-11
AU2014390648B2 (en) 2019-05-23
SG11201608009YA (en) 2016-10-28
CA2848738C (fr) 2016-10-18

Similar Documents

Publication Publication Date Title
US8945256B2 (en) Desanding apparatus and system
US9861921B2 (en) Desanding apparatus and a method of using the same
US9909405B2 (en) Desanding apparatus and a method of using same
US9938812B2 (en) Desanding apparatus and a method of using same
US9327214B2 (en) Desanding apparatus and a method of using same
US11035216B2 (en) Gravity desanding apparatus with filter polisher
US7383958B2 (en) Desanding apparatus and system
AU2014390648B2 (en) A desanding apparatus and a method of using same
CA2433741C (fr) Dispositif et systeme de dessablage
EP3226998B1 (fr) Appareil de dessablage et son procédé d'utilisation
NZ724583A (en) A desanding apparatus and a method of using same
NZ704897A (en) A desanding apparatus and system
NZ704897B2 (en) A desanding apparatus and system
NZ721282B2 (en) A desanding apparatus and a method of using the same

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 139450140003008239

Country of ref document: IR

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14889023

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: IDP00201606870

Country of ref document: ID

ENP Entry into the national phase

Ref document number: 2014390648

Country of ref document: AU

Date of ref document: 20140729

Kind code of ref document: A

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112016023136

Country of ref document: BR

122 Ep: pct application non-entry in european phase

Ref document number: 14889023

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 112016023136

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20161004