A diffuser and solids collection system includes a first baffle section having an input for receiving from a petroleum well a fluid carrying solids and a first set of internal baffles for reducing a velocity of the fluid. A second baffle section in fluid communication with the first baffle section has a second set of internal baffles for further reducing the velocity of the fluid. A solids collection container separates the solids from the fluid received from the second baffle section. A weighing system, supported by the second baffle section and supporting the solids collection container, weighs the solids collected in the solids collection container.

Patent
   10385635
Priority
Jun 05 2018
Filed
Feb 11 2019
Issued
Aug 20 2019
Expiry
Feb 11 2039
Assg.orig
Entity
Small
6
14
currently ok
10. A solids measurement system for measuring solids discharged from a petroleum well comprising:
a vertical baffle section having an input for receiving from a petroleum well a fluid carrying solids and a set of vertically spaced internal baffles for reducing a velocity of the fluid;
a horizontal baffle section having a set of horizontally spaced internal baffles for reducing the velocity of the fluid discharged from the vertical baffle section;
a solids collection container for separating the solids from the fluid discharged from the horizontal baffle section; and
a weighing system for weighing the solids collected in the solids collection container.
20. A method of measuring solids discharged from a petroleum well comprising:
receiving from a petroleum well a fluid carrying solids;
reducing a velocity of the fluid with a vertical baffle section having a set of vertically spaced internal baffles;
reducing the velocity of the fluid discharged from the vertical baffle section with a horizontal baffle section having a set of horizontally spaced internal baffles;
separating the solids from the fluid discharged from the horizontal baffle section with a solids collection container supported by the horizontal baffle section; and
weighing the solids collected in the solids collection container with a weighing system supported by the horizontal baffle section.
1. A diffuser and solids collection system comprising:
a first baffle section having an input for receiving from a petroleum well a fluid carrying solids and a first set of internal baffles for reducing a velocity of the fluid;
a second baffle section in fluid communication with the first baffle section and having a second set of internal baffles for reducing the velocity of the fluid;
a solids collection container in fluid communication with the second baffle section for separating the solids from the fluid received from the second baffle section; and
a weighing system supported by the second baffle section and supporting the solids collection container for weighing the solids collected in the solids collection container.
2. The system of claim 1, wherein the first set of baffles of the first baffle section comprises a plurality of vertically spaced-apart baffles supported by sidewalls of the first baffle section.
3. The system of claim 2, wherein plurality of vertically spaced-apart baffles of the first baffle section comprise a first angled baffle extending downward from a first sidewall and a second angled baffle extending downward from a second opposing sidewall.
4. The system of claim 2, wherein the plurality of vertically spaced-apart baffles of the first baffle section comprise a plurality of laterally spaced apart vertically aligned baffles extending between first and second opposing sidewalls of first baffle section.
5. The system of claim 1, wherein the second set of baffles of the second baffle section comprises a plurality of laterally spaced baffles extending upward from a floor of the second baffle section.
6. The system of claim 5, wherein the plurality of laterally spaced baffles extending upward from a floor of the second baffle section comprise at least one baffle extending inward at an angle to a sidewall of the second baffle section.
7. The system of claim 5, wherein the plurality of laterally spaced baffles extending upward from a floor of the second baffle section comprise at least one baffle disposed substantially perpendicular to a sidewall of the second baffle section.
8. The system of claim 1, wherein the solids collection container comprises:
a hinged screen forming a bottom of the solids collection container; and
a latching mechanism for latching the hinged screen in a closed position during the collection of the solids and releasing the hinged screen to discharge the collected solids from the solids collection container.
9. The system of claim 1, wherein the weighing system comprises:
a support structure supported by an upper surface of the second baffle section;
a scale supported by the support structure; and
a coupling mechanism coupled to the scale and extending through apertures through upper and lower walls of the second baffle section to couple with the solids collections container.
11. The system of claim 10, wherein the solids collection container comprises:
a hinged screen forming a bottom of the solids collection container; and
a latching mechanism for latching the hinged screen in a closed position during the collection of the solids and releasing the hinged screen to discharge the collected solids from the solids collection container.
12. The system of claim 11, further comprising a filter material disposed across the hinged screen for separating the solids from the fluid.
13. The system of claim 10, wherein the weighing system comprises:
a support structure supported by an upper surface of the horizontal baffle section;
a scale supported by the support structure; and
a coupling mechanism coupled to the scale and extending through apertures through upper and lower walls of the horizontal baffle section to couple with the solids collections container.
14. The system of claim 13, wherein the coupling mechanism comprises a turnbuckle.
15. The system of claim 10, wherein the set of vertically spaced internal baffles of the vertical baffle section comprise at least one angled baffle extending downward from a sidewall of the vertical baffle section.
16. The system of claim 10, wherein the set of horizontally spaced internal baffles of the horizontal baffle section extend upward from a floor of the horizontal baffle section.
17. The system of claim 10, wherein at least part of the vertical baffle section is fabricated from steel.
18. The system of claim 10, wherein at least part of the horizontal baffle section is fabricated from steel.
19. The system of claim 10, wherein at least part of the solids collection container is fabricated from steel.

The present application claims the benefit of U.S. Provisional Patent Application Ser. No. 62/680,995, filed Jun. 5, 2018, which is incorporated herein in its entirety for all purposes.

The present invention relates in general to oil and gas operations and in particular to a diffuser and solids collection and measurement system for use in conjunction with oil and gas wells.

In a typical oil well, the oil, gas, water, and solids are produced at the wellhead and then separated. The oil, gas, and usable amounts of water are sent for sale or reuse. The solids, which may include solids such as fracing proppants (e.g., frac sand), are sent to a solids tank for recovery.

In many instances, the amount of solids being output from a given well or group of wells must be monitored. Current methods are based on rough estimates made by personnel observing the output being discharged into the tank. And while it would be advantageous to provide a more accurate and efficient method of determining the amount of solids being produced by a well, the nature of wellhead operations presents some significant challenges for achieving that goal. For example, the solids-bearing water is typically produced under pressure and is therefore discharged it at a high velocity.

The principles of the present invention are embodied in a diffuser and solids collector system that provides for the collection of solids discharged from a wellhead and the accurate measurement (e.g., weighing) of the collected solids.

One particular embodiment of these principles is a diffuser and solids collection system, which includes a first baffle section having an input for receiving from a petroleum well a fluid carrying solids and a first set of internal baffles for reducing a velocity of the fluid. A second baffle section in fluid communication with the first baffle section has a second set of internal baffles for further reducing the velocity of the fluid. A solids collection container separates the solids from the fluid received from the second baffle section. A weighing system, supported by the second baffle section and supporting the solids collection container, weighs the solids collected in the solids collection container.

Advantageously, the principles of the present invention allow for an accurate measurement of the solids flowing out of a petroleum well under pressure.

For a more complete understanding of the present invention, and the advantages thereof, reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which:

FIG. 1 depicts a representative petroleum well serviced by a diffuser and solids collector system according to the principles of the present invention;

FIG. 2A is a perspective view of an exemplary embodiment of the diffuser and solids collector system FIG. 1, embodying the principles of the present invention, and as installed over the solids collection tank of FIG. 1;

FIG. 2B is a side elevational view of the diffuser and solids collector system of FIG. 2A;

FIG. 3 is a perspective view of the diffuser and solids collector system of FIG. 2A;

FIG. 4A is partial cutaway end view of the diffuser and solids collector system of FIG. 2A showing the internal baffles of the vertical baffle section;

FIG. 4B is a cutaway top view of the diffuser and solids collector system of FIG. 2A showing the internal baffles of the vertical baffle section;

FIG. 5 is a cutaway top view of the diffuser and solids collector system of FIG. 2A showing the internal baffles of the horizontal baffle section;

FIG. 6A is a side view of the solids collection box of the diffuser and solids collector system of FIG. 2A;

FIG. 6B is a top view of the solids collection box of the diffuser and solids collector system of FIG. 2A without the bottom release handle in place;

FIG. 6C is a top view of the solids collection box of the diffuser and solids collector system of FIG. 2A with the bottom release handle in place;

FIG. 6D is a top perspective view of the solids collection box of diffuser and solids collector system of FIG. 2A showing the bottom release mechanism; and

FIG. 7 is a side view of the diffuser and solids collector system of FIG. 2A showing the weighing system in further detail.

The principles of the present invention and their advantages are best understood by referring to the illustrated embodiment depicted in FIGS. 1-7 of the drawings, in which like numbers designate like parts.

FIG. 1 is a diagram of an exemplary petroleum well system including a diffuser and solids collector system 100 embodying the present of the present invention. FIG. 1 shows three (3) petroleum production wells 101a-101c, corresponding water/solids separators 102a-102f, valve manual manifolds 103a-103c, four-phase separators 104a-104c, solids tank 105, and open top tank 106. In other systems, the manifolds may be choke manifolds and the separators 2- or 3-phase separators.

Solids-bearing water from water/solids separators 102a-102f and four phase separators 104a-104c are passed to diffuser and solids collector system 100. As discussed in further detail below, the water bearing solids, such as frac sand, are delivered diffusor and solids collection system 100, which reduces the fluid velocity, collects the solids, and allows the solids to be weighed. Once a desired amount of solids have been collected an weighed, they are discharged from diffuser and solids collector system 100 into solids tank 105.

FIG. 2A partially shows a preferred embodiment of diffuser and solids collection system 100 mounted on the solids tank 106 of FIG. 1. FIG. 2B shows the exterior of diffuser and solids collector system 100 in further detail. The illustrated embodiment includes a vertical baffle section 201, a horizontal baffle section 202, and a particulate (solids) collection box 203, which is supported by a scale 204 and pyramid support structure 205.

High-velocity solids-bearing water is received through an inlet 206 near the top a vertical baffle section 201 and passes through a series of internal baffles, discussed in further detail below. Additional baffles within contiguous horizontal baffle section 202 further reduce the fluid velocity.

After the reduction in fluid velocity, the solids-bearing water is discharged through an aperture in the base of horizontal baffle section 202 and into particulate collection box 203. Particulate collection box 203 includes filter material supported by a hinged screen on the base. The hinged screen is associated with a handle and release mechanism, which allow a lateral edge of the hinged screen to be released and the collected solids to be dumped into solids tank 105 below, once those solids have been weighed by scale 204.

FIG. 3 provides an alternate view of diffuser and solids collector system 100. Vertical baffle section 201 includes vents 207 on opposing sides for discharging gases accumulated during the diffusion process. The upper surface of the horizontal baffle section 202 includes an aperture through which a turnbuckle extends, as discussed below, to couple scale 204 with particulate collection box 203. Supports 302 at the four corners are provided for supporting diffuser and solids collector system 100 on the walls of solids tank 105 during use. Hinges 300a-300c allow a portion of the upper surface of horizontal baffle section 202 to swing open for internal access.

FIGS. 4A-4B show the preferred vertical baffle section 201 in further detail. As shown in FIGS. 4A and 4B, three (3) elongated internal rectangular baffles 400a-400c are provided near the top of vertical baffle section 201, along with two (2) slanted planar baffles 401a-401b extending from opposing sidewalls. (The principles of the present invention are not limited to this configuration, and in alternate embodiments, the number of rectangular and/or slanted baffles, as well as their positioning, may vary. In addition, the number and location of vents 207 and fluid inlet 206 may also vary in alternate embodiments.)

A preferred configuration of horizontal baffle section 202 is shown in FIG. 5. In the embodiment, four (4) baffles 500a-500d extend upward from the angled side-sections 502a-502b of the floor and at an angle to the horizontal baffle section 202 lateral sidewalls. A rectangular baffle 501 extends upward from the flat portion 503 of the floor and perpendicular to the lateral sidewalls. In alternate embodiments, the number and configuration of the baffles of the horizontal baffle section 202 may vary. Aperture 502 through the floor allows a turn buckle to extend through the interior of horizontal baffle section 202 for coupling particulate collection box 203 with scale 204, as well as to allow solid-bearing water to discharge into particulate collection box 203.

FIGS. 6A-6D illustrate the preferred configuration of particulate collection box 203. The bottom of the solids collection box is a hinged screen 600 as shown in FIG. 6A. A crossbar 602, as shown in FIG. 6B, provides structural support, as well as a grasping point for the turnbuckle hook. Four (4) vents 601a-601d are provided for discharging gas (FIG. 6B).

As shown in FIG. 6C, filter material 603 is disposed across hinged screen 600 for capturing solids as water is discharged through the bottom of particulate collection box 203 into solids tank 105. Once the solids have been collected and weighed, hinged screen 600 is released using the release mechanism of FIG. 6D.

The release mechanism includes a release handle 604 and a rotating latch 605, which includes a slot 607 for engaging a pin 606 extending from the free (non-hinged) side of hinged screen 600. Rotation of the latch around pivot point 608 is controlled by handle 604. When hinged screen 600 is the closed position, pin 606 on hinged screen 600 slides into slot 607 of rotating latch 605. To release hinged screen 600, and allow the free edge to fall, handle 604 is rotated such that latch 605 rotates away from pin 606 and pin 606 exits slot 607 in the latch 605.

The weighing system is shown in FIG. 7 for the preferred embodiment of diffuser and solids collector system 100. A pyramid support is disposed on the upper side of the horizontal baffle section. As discussed above, pyramid support 205 supports a scale 204. A turnbuckle 700, which is coupled to scale 704 by a hook 702, extends through aperture 301 on the upper surface of horizontal baffle section 202 and aperture 502 through the floor of horizontal baffle section 202. An opposing hook 701 couples to crossbar 602 of particle collection box 203. The solids captured by particulate collection box 203 and particulate collection box 203 itself are weighed together and the tare taken to determine the weight of the solids alone.

The primary components of diffuser and solids collector system 100 including vertical baffle section 201 and internal baffles 400 and 402, horizontal baffle section 202 and internal baffles 500 and 501, and particulate (solids) collection box 203, are preferably fabricated from steel. In alternate embodiments, other materials capable of withstanding the stresses from use of diffuser and solids collector system 100 in the petroleum fields may be used.

Although the invention has been described with reference to specific embodiments, these descriptions are not meant to be construed in a limiting sense. Various modifications of the disclosed embodiments, as well as alternative embodiments of the invention, will become apparent to persons skilled in the art upon reference to the description of the invention. It should be appreciated by those skilled in the art that the conception and the specific embodiment disclosed might be readily utilized as a basis for modifying or designing other structures for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.

It is therefore contemplated that the claims will cover any such modifications or embodiments that fall within the true scope of the invention.

Tucker, Robert Alan

Patent Priority Assignee Title
10905975, Nov 15 2018 Saudi Arabian Oil Company Removable trap stations for hydrocarbon flowlines
10914128, Jun 05 2018 Southpaw Fabrication Diffuser and solids collection and measurement system for use in conjunction with oil and gas wells
11524251, Nov 15 2018 Saudi Arabian Oil Company Removable trap stations for hydrocarbon flowlines
11555571, Feb 12 2020 Saudi Arabian Oil Company Automated flowline leak sealing system and method
11607628, Sep 17 2019 Chevron U.S.A. Inc.; CHEVRON U S A INC Systems and processes for automated sand separation
11911716, Jun 11 2018 ENERCORP ENGINEERED SOLUTIONS INC Fluid removal system for a blowdown vessel
Patent Priority Assignee Title
1190863,
3899926,
4247312, Feb 16 1979 C0NSOLIDATION COAL COMPANY; CONSOLIDATION COAL COMPANY, A CORP OF DE Drilling fluid circulation system
4878382, Nov 14 1987 Schlumberger Technology Corporation Method of monitoring the drilling operations by analyzing the circulating drilling mud
5106492, Dec 06 1990 Solar powered swimming pool skimmer
6410862, May 07 1998 Geoservices Equipements Device and method for measuring the flow rate of drill cuttings
6823238, Apr 14 1998 HUTCHISON HAYES PROCESS MANAGEMENT, LLC Selective apparatus and method for removing an undesirable cut from drilling fluid
7311818, Sep 28 2006 Water separation unit
7363829, Apr 20 2006 Drill cutting sampler
7964101, Jan 25 2006 Q'MAX Solutions Inc. Fluid treatment process
9610520, Jul 29 2013 CALX LIMITED Apparatus and method for treating slurries
20060096935,
20140014589,
GB2228215,
//
Executed onAssignorAssigneeConveyanceFrameReelDoc
Feb 11 2019Southpaw Fabrication(assignment on the face of the patent)
Feb 11 2019TUCKER, ROBERT ALANSouthpaw FabricationASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS 0482980219 pdf
Date Maintenance Fee Events
Feb 11 2019BIG: Entity status set to Undiscounted (note the period is included in the code).
Feb 28 2019SMAL: Entity status set to Small.
Apr 10 2023REM: Maintenance Fee Reminder Mailed.
Apr 28 2023M2551: Payment of Maintenance Fee, 4th Yr, Small Entity.
Apr 28 2023M2554: Surcharge for late Payment, Small Entity.


Date Maintenance Schedule
Aug 20 20224 years fee payment window open
Feb 20 20236 months grace period start (w surcharge)
Aug 20 2023patent expiry (for year 4)
Aug 20 20252 years to revive unintentionally abandoned end. (for year 4)
Aug 20 20268 years fee payment window open
Feb 20 20276 months grace period start (w surcharge)
Aug 20 2027patent expiry (for year 8)
Aug 20 20292 years to revive unintentionally abandoned end. (for year 8)
Aug 20 203012 years fee payment window open
Feb 20 20316 months grace period start (w surcharge)
Aug 20 2031patent expiry (for year 12)
Aug 20 20332 years to revive unintentionally abandoned end. (for year 12)