US20130299523A1

US20130299523A1 - Proportional controlled orifice for metering granular material

Info

Publication number: US20130299523A1
Application number: US13/468,473
Authority: US
Inventors: Chad A. Fisher
Original assignee: Halliburton Energy Services Inc
Current assignee: Halliburton Energy Services Inc
Priority date: 2012-05-10
Filing date: 2012-05-10
Publication date: 2013-11-14
Also published as: WO2013169598A1; AU2013259914A1; EP2847499A1; CA2873245A1

Abstract

Disclosed herein is a gate valve design with a proportionally controlled orifice area. The moving element of the gate is shaped to cooperate with a fixed element so that as the gate opens, the open orifice area changes geometrically.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS

Not applicable.

STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT

Not applicable.

REFERENCE TO A MICROFICHE APPENDIX

Not applicable.

BACKGROUND

It is common in the drilling, completion and servicing of subterranean wells to utilize large volumes of mixtures of components in both solid and fluid form. Examples of these mixtures include drilling, fracturing, and other well treatment mixtures. Fracturing mixtures include solid materials called proppants. Proppants are solid particles mixed in dry form with fracturing fluid to hold fractures open after a hydraulic fracturing treatment. In addition to naturally occurring sand grains, man-made or specially engineered proppants, such as resin-coated sand or high-strength ceramic materials like sintered bauxite, may also be used. As used herein, the term “dry particulate material” is used to refer to particulate materials which cannot be pumped or handled as a fluid. To be effective for their purposes, some mixtures require that components be mixed in precise quantities. In view of logistics and the volumes required, it is impractical to first measure quantities of the solids and liquids and then mix them together as a batch. Typically, mixing is accomplished, while adding the components to a mixing chamber and proportion control of the components is performed, using valves.
Dry solid materials are commonly mixed by conveying them to a container, typically a hopper, where they are fed by gravity into the mixing chamber. It is common in the industry to use augers to meter dry solid material from bins and hoppers into the mixing chamber. Sliding gate valves have been used but suffers from the disadvantages described herein. As used herein, the term “sliding gate valve” is used to refer to a valve having a planar or wedge shaped a valve element that moves into and out of the flow path and cooperates with a fixed seat to meter flow through the valve orifice. In a gate valve, the area defined between the valve and its seat is sometimes called an “orifice.” Sliding gate valves can be controlled (opened and closed) manually or by electrical or fluid actuators.
The ratio of the smallest dimension of an orifice is critical to the jamming probability caused by material bridging. The combination of the orifice area (size) and the critical dimension (smallest orifice dimension) contribute to the flow rate of material through the orifice. Typical sliding gate valves used to control the flow of materials have quadrilateral-shaped orifices. These gate valves are simple and easy to use to meter material flow by sliding the valve element into or out of the flow path to adjust the orifice size.
In these existing gate valves, the width of the orifice is a fixed dimension and, as the valve opens, a quadrilateral orifice is created. Accordingly, these gate valves will have a large orifice area, compared to the smallest dimension of the orifice as the gate opens. Once the gate valve is open far enough to exceed the distance at which bridging occurs or far enough to diminish the entry effects of the minimum optimum dimension, the total, open area of the orifice allows more material to pass than is desired. Accordingly, these gate valves cannot accurately meter small flow rates.
In these existing gate valves, small movements of the valve element cause proportionally large changes in orifice size. These gate valves do not provide fine metering control.
Accordingly, there is a need for metering equipment that provides fine flow rate control, especially at lower flow rates where jamming can occur.

SUMMARY

Disclosed herein is a gate valve with an orifice that varies in two dimensions as the valve element is moved. In one sliding gate valve embodiment, the gate valve orifice is quadrilateral shaped and varies in both width and length as the valve element is moved. In another circle orifice gate valve embodiment, a plurality of valve elements are mounted to pivot into and out of the flow to vary the orifice size in both length and width dimensions.

BRIEF DESCRIPTION OF THE DRAWINGS

For a more complete understanding of the present disclosure and the advantages thereof, reference is now made to the following brief description, taken in connection with the accompanying drawings and detailed description:

FIG. 1 is a schematic view, illustrating a typical particulate material supply system for use drilling, completion operations on a well according to the disclosure of the present invention;

FIG. 2 is a top plan view of a prior art sliding gate valve, illustrating the valve in the closed position;

FIG. 3 is a cross-sectional view of the prior art valve illustrated in FIG. 2 taken along line 2-2, looking in the direction of the arrows;

FIG. 4 is a top plan view of the orifice portion of a sliding gate valve, illustrated in the closed position according to the present invention;

FIG. 5 is a top plan view of the orifice portion of the sliding gate valve of FIG. 4 illustrated in the partially opened or metering position according to the present invention;

FIG. 6 is a top plan view of the orifice portion of the circle orifice gate valve, illustrated in the fully open position according to the present invention; and

FIG. 7 is a top plan view of the orifice portion of the circle orifice gate valve of FIG. 6, illustrated in the partially closed or metering position according to the present invention.

DETAILED DESCRIPTION OF THE EMBODIMENTS

In the drawings and description that follow, like parts are typically marked throughout the specification and drawings with the same or similar reference letters and numerals. The drawing figures are not necessarily to scale. Certain features of the invention may be shown exaggerated in scale or in somewhat schematic form and some details of conventional elements may not be shown in the interest of clarity and conciseness.
The various characteristics mentioned above, as well as other features and characteristics described in more detail below, will be readily apparent to those skilled in the art with the aid of this disclosure, upon reading the following detailed description of the embodiments and by referring to the accompanying drawings.
Disclosed herein are solid particulate material supply and metering systems for oil well services, using an improved sliding gate valves. More specifically, gate valves are positioned to control the gravity flow of dry solid particulate material into a mixing chamber where the particulate is mixed in proportion with other components, including liquid components. The sliding gate valve of the present invention is characterized by being able to accurately meter the gravity flow of dry particulate materials and, in particular, to accurately meter small quantities of dry solid materials.
Referring to FIG. 1, there is illustrated one embodiment of a material supply and metering system 10 for use in preparing mixtures for use in gas well servicing and drilling. System 10 comprises a hopper 12 for containing a quantity of dry particulate material, such as a proppant. A conveyor 14 is typically used to load hopper 12. The particulate material flows by gravity through the valve 16 to a mixer 18. The valve 16 is typically a sliding gate valve which is used to meter the flow of material into the mixer 18. One or more fluid components are supplied to the mixer 18 from a tag 22 through a fluid pump 20. A supply pump 24, in the form of a positive displacement pump, provides particulate fluid mixture to the well 26.
A sliding gate valve 16 of conventional construction is illustrated in FIGS. 2 and 3 in the slightly open position. Valve 16 comprises a frame 30 having with the feed opening and a flange surrounding the opening that is suitable for attachment of the valve 16 to the bottom of the hopper 12. The quadrilateral-shaped frame 30 surrounds the feed opening and supports a valve seat 32. The valve element 34 comprises a sliding plate which, when the valve is opened, cooperates with the valve seat 32 to define the valve orifice 38. As will be appreciated, as the valve element 34 is moved in the direction of arrow 40 out of feed opening, a quadrilateral-shaped orifice 38 is formed. For purposes of description, the width dimension (W) of the orifice is defined transverse to the valve element's direction of movement, as illustrated by arrow 40. The orifice length dimension (L) is defined parallel to the direction of movement 40. In a rectangular orifice, the area (A) is computed by multiplying the length by the width.
An actuator assembly 36 is connected to the valve element 34. The actuator assembly 36 is operably associated with the valve element 34 to selectively move it into and out of the feed opening. Actuator assembly 36 is an electrically powered actuator 42 that can be operated to control the position of the valve element 34.
When metering of relatively smaller quantities of material, the orifice area A of the valve will be small. As illustrated in FIG. 2, as the valve opens, a rectangular orifice is formed with a length (L) that is multiples less than the width (W). At smaller areas, the length of the orifice is the critical, smallest dimension and is more likely to experience material bridging. Once the gate valve is open far enough to exceed the critical length distance (L) at which bridging occurs (and to diminish the entry effects), the total, open area of the orifice allows more material to pass than is desired. Accordingly, because of bridging, these conventional gate valves cannot meter relatively small flow rates.
Referring to FIGS. 4 and 5, an embodiment of a sliding sleeve gate valve 116 is illustrated. In FIG. 4, the valve is illustrated in the closed position, and in FIG. 5, the valve is illustrated in the partially open position. The valve seat 132 is in the form of a plate, positioned in the feed opening. The seat 132 has a right-angled, triangular-shaped opening 133, formed there through which particulate material can flow when the valve is open. The valve element 134 is mounted to slide in the direction of arrow 140 with respect to the seat 132. As illustrated, the valve element 134 has a right-angled, triangular-shaped cutout portion 135.
In operation, as the valve element 134 moves in the direction of arrow 140, the triangular cutouts 133 and 135 will begin to overlap, forming a quadrilateral-shaped orifice 138. In the preferred embodiment, orifice 138 is substantially square shaped, with equal length sides. The orifice area (A) is defined by the square of any one side. It is envisioned, however, that depending on the shapes of the triangular cutouts, the orifice can take on different shapes and proportions. As the valve element 134 moves in the direction of arrow 140, the lengths of the four sides (S) defining the orifice 138 all increase equally and the length (L) of the orifice becomes greater in the same amount as the width (W). In orifices of the same area (flow rate), the smallest or critical dimension of a square-shaped orifice is greater than the smallest dimension of a rectangular shaped orifice. This allows the sliding gate valve embodiment illustrated in FIG. 5 to operate at lower flow rates than other quadrilateral orifice shapes.
As illustrated in FIG. 5, when the triangular cutouts overlap slightly, orifice 138 is formed with a small cross-section area but with no one dimension substantially smaller than the other dimensions. In the FIG. 5 embodiment, the gate valve orifice 138 is quadrilateral shaped and varies both width and length as the valve element is moved.
In an alternative embodiment, a particulate material gate valve 216 is illustrated in FIGS. 6 and 7. In FIG. 6, valve 216 is shown in the completely open condition. In FIG. 7, valve 216 is shown in the partially open or metering position. In this embodiment, valve 216 is in the form of a circle orifice gate valve. Valve 216 comprises an annular seat 232 that surrounds a circular particulate material feed opening.
A plurality of adjacent pedals-shaped valve elements 234 are mounted to pivot into and out of the material feed opening. In the illustrated embodiment, six separate elements are shown, however, more or less elements could be utilized. In the illustrated embodiment, each of the valve elements 234 comprise a flat plate. The valve elements 234 are formed with arcuate or curved, interior facing edges 235, however, it is envisioned that the interior edges could be defined by one or more straight lines or other shapes. The valve elements 234 are illustrated in FIG. 6, positioned out of the feed opening and under the seat 232. The valve elements 234 are mounted to rotate about pivots 239. An actuator (not illustrated) is operably connected to the valve elements 234 to rotate the elements in the forward and reverse directions of arrow 240.
As illustrated in FIG. 7, as the valve elements move in the direction of arrow 240, the cross-sectional area of the orifice 238 becomes smaller. When it is desired to meter a small quantities of particulate materials through the valve 216, the orifice 238 formed by the valve elements 234. In the preferred embodiment, the elements define an orifice that is roughly polygon shaped. The more valve elements are present in the valve, the more the orifice approximates a circle. As will be appreciated, as the shape approaches a circular shape, the orifice surface effects would be reduced. As in the above-described embodiment, this shape of the orifice 238 is conducive to reducing bridging of the particulate material at lower flow rates.
According to a particular feature of the present invention, the valve embodiments illustrated and described herein can be utilized in the system illustrated in FIG. 1 to meter small quantities of particulate materials, while reducing material bridging and jamming.
At least one embodiment is disclosed and variations, combinations, and/or modifications of the embodiment(s) and/or features of the embodiment(s) made by a person having ordinary skill in the art are within the scope of the disclosure. Alternative embodiments that result from combining, integrating, and/or omitting features of the embodiment(s) are also within the scope of the disclosure. Use of broader terms, such as “comprises,” “includes,” and “having,” should be understood to provide support for narrower terms, such as “consisting of,” “consisting essentially of,” and “comprised substantially of.” Accordingly, the scope of protection is not limited by the description set out above but is defined by the claims that follow, that scope including all equivalents of the subject matter of the claims. Each and every claim is incorporated as further disclosure into the specification, and the claims are embodiment(s) of the present invention.

Claims

What is claimed is:

1. A system for metering particulate material, comprising:

a container of dry particulate material, having a gravity-fed discharge;

a gate valve positioned in the discharge to control the flow of material from the container, the gate valve comprising a seat and at least one valve element movable out of the closed position to define a material feed orifice through which material is fed by gravity, the orifice being formed between the seat and valve element to vary in both length and width during at least a portion of the valve element movement.

2. The system according to claim 1, wherein the orifice has a polygonal-shaped cross section area.

3. The system according to claim 1, wherein the orifice area is quadrilateral shaped.

4. The system according to claim 1, wherein the orifice area is square shaped

5. The system according to claim 1, wherein the valve element has a triangular, cross-section shaped cutout area, extending through the valve element.

6. The system according to claim 1, wherein the valve seat has a triangular-shaped opening.

7. The system according to claim 6, wherein, the valve seat opening is in the shape of a right-angle triangle.

8. The system according to claim 1, wherein, the valve element has a triangular-shaped opening.

9. The system according to claim 8, wherein, the valve element opening is in the shape of a right-angle triangle.

10. A system for metering particulate material, comprising:

a container of dry particulate material having a gravity fed discharge; and

a gate valve position in the discharge to control the flow of material from the container, the gate valve comprising a seat and at least one movable valve element, at least one of the valve seat and valve element having a triangular-shaped opening, the valve element mounted to move out of a closed position where the triangular-shaped opening defines a material feed orifice through which material is fed by gravity.

11. The system of claim 10, wherein both of the valve element and seat have triangular-shaped openings.

12. The valve of claim 10, wherein the orifice is quadrilateral shaped.

13. The valve of claim 10, wherein the triangular-shaped opening is a right-angled triangle.

14. The valve of claim 11, wherein both triangular-shaped openings are right-angled triangles.

15. A method for metering the flow of particulate material by gravity from a discharge opening in a container, comprising the steps of:

positioning a sliding gate valve, comprising a seat and a valve element in the discharge opening;

selectively moving the valve with respect to the seat to form an orifice that varies in both length and width as the seat moves; and

flowing material through the orifice.

16. The method of claim 15, wherein the gate valve positioning step comprises positioning a sliding gate valve with a triangular opening in at least one of the seat and valve element and wherein the opening forms at least a portion of the orifice.

17. The method of claim 15, wherein the positioning step comprises positioning a sliding gate valve, having triangular openings formed in both the seat and valve element, and wherein the openings form at least a portion of the orifice.

18. The method of claim 15, wherein the orifice form step comprises forming a polygonal-shaped opening.

19. The method of claim 15, wherein the orifice form step comprises forming a quadrilateral-shaped opening.

20. The method of claim 15, wherein the orifice form step comprises forming a square-shaped opening.