US10385635B1 - Diffuser and solids collection and measurement system for use in conjunction with oil and gas wells - Google Patents

Diffuser and solids collection and measurement system for use in conjunction with oil and gas wells Download PDF

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US10385635B1
US10385635B1 US16/272,805 US201916272805A US10385635B1 US 10385635 B1 US10385635 B1 US 10385635B1 US 201916272805 A US201916272805 A US 201916272805A US 10385635 B1 US10385635 B1 US 10385635B1
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solids
baffle section
fluid
baffles
collection container
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Robert Alan Tucker
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Southpaw Fabrication
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Southpaw Fabrication
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    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B21/00Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
    • E21B21/06Arrangements for treating drilling fluids outside the borehole
    • E21B21/063Arrangements for treating drilling fluids outside the borehole by separating components
    • E21B21/065Separating solids from drilling fluids
    • E21B21/066Separating solids from drilling fluids with further treatment of the solids, e.g. for disposal
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B21/00Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
    • E21B21/06Arrangements for treating drilling fluids outside the borehole
    • E21B21/063Arrangements for treating drilling fluids outside the borehole by separating components
    • E21B21/065Separating solids from drilling fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0012Settling tanks making use of filters, e.g. by floating layers of particulate material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/003Sedimentation tanks provided with a plurality of compartments separated by a partition wall
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/0039Settling tanks provided with contact surfaces, e.g. baffles, particles
    • B01D21/0042Baffles or guide plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/2427The feed or discharge opening located at a distant position from the side walls
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/24Feed or discharge mechanisms for settling tanks
    • B01D21/245Discharge mechanisms for the sediments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/30Control equipment
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/35Arrangements for separating materials produced by the well specially adapted for separating solids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2221/00Applications of separation devices
    • B01D2221/04Separation devices for treating liquids from earth drilling, mining

Definitions

  • 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.
  • 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.
  • 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.
  • 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.
  • the principles of the present invention allow for an accurate measurement of the solids flowing out of a petroleum well under pressure.
  • 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;
  • FIG. 7 is a side view of the diffuser and solids collector system of FIG. 2A showing the weighing system in further detail.
  • 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 101 a - 101 c , corresponding water/solids separators 102 a - 102 f , valve manual manifolds 103 a - 103 c , four-phase separators 104 a - 104 c , solids tank 105 , and open top tank 106 .
  • the manifolds may be choke manifolds and the separators 2- or 3-phase separators.
  • Solids-bearing water from water/solids separators 102 a - 102 f and four phase separators 104 a - 104 c are passed to diffuser and solids collector system 100 .
  • 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.
  • 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 300 a - 300 c 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.
  • three (3) elongated internal rectangular baffles 400 a - 400 c are provided near the top of vertical baffle section 201 , along with two (2) slanted planar baffles 401 a - 401 b 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.
  • the number and location of vents 207 and fluid inlet 206 may also vary in alternate embodiments.
  • FIG. 5 A preferred configuration of horizontal baffle section 202 is shown in FIG. 5 .
  • four (4) baffles 500 a - 500 d extend upward from the angled side-sections 502 a - 502 b 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.
  • 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 601 a - 601 d are provided for discharging gas ( FIG. 6B ).
  • 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 .
  • hinged screen 600 is the closed position, pin 606 on hinged screen 600 slides into slot 607 of rotating latch 605 .
  • 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.

Abstract

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.

Description

CROSS-REFERENCE TO RELATED APPLICATION
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.
FIELD OF INVENTION
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.
BACKGROUND OF INVENTION
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.
SUMMARY OF INVENTION
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.
BRIEF DESCRIPTION OF DRAWINGS
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.
DETAILED DESCRIPTION OF THE INVENTION
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 101 a-101 c, corresponding water/solids separators 102 a-102 f, valve manual manifolds 103 a-103 c, four-phase separators 104 a-104 c, 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 102 a-102 f and four phase separators 104 a-104 c 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 300 a-300 c 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 400 a-400 c are provided near the top of vertical baffle section 201, along with two (2) slanted planar baffles 401 a-401 b 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 500 a-500 d extend upward from the angled side-sections 502 a-502 b 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 601 a-601 d 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.

Claims (20)

What is claimed is:
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.
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.
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.
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.
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