Patent Application
20170095780
One embodiment relates generally to systems and methods for optimal mixing and distribution of two or more fluids, and more particularly, to systems and methods for optimal mixing and distribution of two or more fluids, including fracturing (frac) fluids and completion fluids, used in oil and gas operations.
In a variety of applications, the proper mixing and distribution of two or more fluids is a critical performance-affecting factor.
Many conventional manifold designs provide insufficient mixing and/or distribution of the subject fluids. For example, one conventional manifold design comprises a first pipe having inlets disposed thereon arranged in a first linear array pattern. The first pipe is connected via one or more conduits to a second pipe disposed substantially parallel to the first pipe, the second pipe having outlets disposed thereon arranged in a second linear array pattern. Fluids injected through the inlets travel through the first pipe to the connecting conduits and then into the second pipe where the fluid can then exit through the outlets. This flow path would ideally provide the means by which the injected fluids can thoroughly mix before exiting the manifold.
However, a typical scenario results in the fluid(s) injected through the outermost inlets of the first linear array pattern (i.e., the inlets disposed closest to the ends of the first pipe) being substantially absent from the outermost outlets of the second linear array pattern (i.e., the outlets disposed closest to the ends of the second pipe) positioned on the opposite side. A fluid injected through an inlet at one end of the first pipe is unlikely to travel in a flow path in which it will make it to an outlet at the opposite end of the second pipe.
While certain novel features of this invention shown and described below are pointed out in the annexed claims, the invention is not intended to be limited to the details specified, since a person of ordinary skill in the relevant art will understand that various omissions, modifications, substitutions and changes in the forms and details of the device illustrated and in its operation may be made without departing in any way from the spirit of the present invention. No feature of the invention is critical or essential unless it is expressly stated as being “critical” or “essential.”
The apparatus of the present invention solves the problems confronted in the art in a simple and straightforward manner. What is provided is a multi chamber mixing chamber method and apparatus.
One or more embodiments of the invention provide systems and methods for optimal mixing and distribution of two or more fluids.
The drawings constitute a part of this specification and include exemplary embodiments to the invention, which may be embodied in various forms.
For a further understanding of the nature, objects, and advantages of the present invention, reference should be had to the following detailed description, read in conjunction with the following drawings, wherein like reference numerals denote like elements and wherein:
Detailed descriptions of one or more preferred embodiments are provided herein. It is to be understood, however, that the present invention may be embodied in various forms. Therefore, specific details disclosed herein are not to be interpreted as limiting, but rather as a basis for the claims and as a representative basis for teaching one skilled in the art to employ the present invention in any appropriate system, structure or manner.
The multi-chamber manifold 100 comprises an elongate housing 104 having a first end 116a and a second end 120a. The ends 116a, 120a may be sealably capped with blocking end flanges 116b, 120b to prevent fluid from escaping therethrough. A plurality of fluid inlets 108a-108d maybe disposed along housing 104 in a first linear array pattern. Outermost fluid inlet 108a maybe disposed proximate the first end 116a and the first linear array pattern may extend towards the second end 120a. A plurality of fluid outlets 112a-112j may also be disposed along housing 104 in a second linear array pattern. Outermost fluid outlet 112a may be disposed proximate the second end 120a and the second linear array pattern may extend towards the first end 116a. Flow control valves (not shown) may be used to regulate fluid flow through the fluid inlets 108a-108d and the fluid outlets 112a-112j. In one embodiment, carbon steel may be used to construct the multi-chamber manifold 100. However, any material suitable for constructing a manifold for optimal mixing and distribution of two or more fluids may be used. While housing 104 is shown as having an annular cross-section, other configurations could be used in other embodiments.
Inlets 108a-108d may each be connected to one or more sources of fluid so that at least two different types of fluid may be fed or supplied to the multi-chamber manifold 100 for mixing and distribution. The fluids may include liquids and gases. In one embodiment, the fluids may comprise frac water blends obtained from a plurality of sources, or mixtures of frac fluids, chemical additives, and brines. Methods for facilitating the delivery of optimal volumes of a frac fluid containing optimal concentrations of one or more additives to a well bore are disclosed in United States Patent Publication No. 2010/0059226 A1, which is incorporated herein by reference in its entirety. Where a definition or use of a term in the incorporated reference is inconsistent or contrary to the definition of that term provided herein, the definition of that term provided herein applies and the definition of that term in the reference does not apply. The systems and methods of the present invention may be used to provide a homogeneous fluid blend for use in conjunction with the incorporated reference.
Referring now to
As shown in
The chamber separation structure 132 may comprise a horizontal chamber separation plate 136 defining a lower boundary of the vortex chamber 124 and one or more vertical chamber separation plates 140a, 140b defining lateral boundaries of the vortex chamber 124. The horizontal chamber separation plate 136 comprises side walls 144a, 144b that may be sealably coupled to the inner wall of housing 104. The one or more vertical chamber separation plates 140a, 140b may be oriented substantially perpendicular to the horizontal chamber separation plate 136. The one or more vertical chamber separation plates 140a, 140b may be disposed at and sealably coupled to the ends 148a, 148b of the horizontal chamber separation plate 136. In one embodiment, a portion of vertical chamber separation plate 140a may be shaped to conform to the geometry of the inner wall of housing 104 so as to create a sealed barrier, preventing the fluid mixture inside the vortex chamber 124 from flowing laterally in a direction towards the second end of housing 120a.
Inlets 108a-108d may protrude both outwardly and inwardly with respect to housing 104, each outward-inward protrusion combination forming an inlet nozzle defining a passage through which a fluid may be injected to the vortex chamber 124. The outwardly protruding portions 152a-152d of the inlet nozzles allow for fluids to commence its flow path into the multichamber manifold 100 such that the fluids flow substantially radial to housing 104. The inwardly protruding portions 156a-156d of the inlet nozzles are angled to affect an angular velocity on the fluids, projecting the fluids into the vortex chamber 124 in a manner causing the fluids to swirl rapidly about a center. This induced swirl, or vortex, provides turbulent flow that facilitates thorough mixing of the injected fluids, producing a substantially homogeneous blend. The specific angle of each inlet nozzle is determined based on the particular application.
The chamber separation structure 132 may further comprise a plurality of baffle plates 160a, 160b that extend upwardly from and substantially perpendicular to the horizontal chamber separation plate 136. As previously described, the inlet nozzles are angled to induce a vortex that facilitates the mixing of the injected fluids. The upwardly extending baffle plates 160a, 160b serve to guide the mixture of fluids through a gate 164 disposed between the upwardly extending baffle plates 160a, 160b, the gate 164 defining an opening in the horizontal chamber separation plate 136. The gate 164 directs the mixture of fluids to flow to the secondary mixing chamber 128.
One or more inlet nozzles may be disposed at either side of the upwardly extending baffle plates 160a, 160b. For example, in one embodiment, a first set of two inlet nozzles may be disposed at a lateral distance from upwardly extending baffle plate 160a, proximal to the first end 116a of housing 104. In this configuration, a second set of two inlet nozzles may also be disposed at a lateral distance from upwardly extending baffle plate 160b, distal to the first end 116a of housing 104 relative to first set of inlet nozzles. The inwardly protruding portions 156a-156d of the inlet nozzles may be angled upward relative to the horizontal chamber separation plate 136 and inward relative to the one or more vertical chamber separation plates 140a, 140b. Thus, the two sets of inlet nozzles may provide a mirror image trajectory of vectored fluid flow allowing the fluids to coincide and induce the vortex above the gate 164. Gravity causes substantially all of the fluid mixture to flow downwardly through gate 164, guided, in part, by upwardly extending baffles 160a, 160b.
The chamber separation structure 132 may further comprise an L-shaped baffle plate 168 connected to the bottom surface of the horizontal chamber separation plate 136 and disposed below the gate 164. Upon passing through gate 164, the fluid mixture encounters the L-shaped baffle plate 168, which guides the fluid mixture flow in a first direction towards the first end 116a of housing 104. The change in flow direction of the fluid mixture caused by the L-shaped baffle plate 168 may further enhance the mixture quality.
Another change in flow direction is caused by the fluid mixture encountering the first end 116a of housing 104, which forces the fluid mixture to flow in a second direction opposite the first direction. This change in flow direction may also further enhance the mixture quality. Moreover, as the fluid mixture flows in the second direction, it flows past the L-shaped baffle plate 168 towards the second end 120a of housing 104 where the fluid mixture can then be evenly distributed among fluid outlets 112a-112j.
Although
The multi-chamber manifold 100 illustrated in
One or more embodiments of the present invention relate to methods for enhanced mixing of fluids, as shown by the flow chart in
The methods further involve supplying two or more input fluids to the manifold through the fluid inlets of the manifold 502. The fluids may flow through inlet nozzles and into the vortex chamber. The fluid nozzles may be angled to induce a vortex in the vortex chamber 504. The vortex serves the purpose of stirring the input fluids for thorough mixing, producing a fluid mixture.
The fluid mixture may be directed downwards from the vortex chamber through a gate to a secondary mixing chamber 506 for further mixing. Baffles may be used to guide the flow path of the fluid mixture in various directions. The fluid mixture may be directed in a first direction towards a first end of the manifold 508. The fluid mixture may also be directed in a second direction opposite the first direction towards a second end of the manifold 510. Changing the direction of the fluid mixture flow path facilitates further mixing of the fluids.
The resulting homogeneous fluid blend may be distributed among the plurality of fluid outlets to discharge from the manifold 512. The destination of the fluid mixture after discharging from the manifold depends on the particular application. Fluid flow can be directed in its entirety to one destination or distributed either evenly or proportionally to multiple destinations.
It is to be understood that the invention is not to be limited or restricted to the specific examples or embodiments described herein, which are intended to assist a person skilled in the art in practicing the invention. For example, the number of fluids to be mixed, the number of inlets, the number of outlets, the number of spill over plates, and the number of chambers may vary according to the desired results of a particular application. Also, the dimensions of the various components of the multi-chamber manifold may be scaled to achieve the desired results of a particular application. Accordingly, numerous changes may be made to the details of procedures for accomplishing the desired results. These and other similar modifications will readily suggest themselves to those skilled in the art, and are intended to be encompassed within the spirit of the present invention disclosed herein and the scope of the appended claims.
The following is a list of reference numerals:
All measurements disclosed herein are at standard temperature and pressure, at sea level on Earth, unless indicated otherwise. All materials used or intended to be used in a human being are biocompatible, unless indicated otherwise.
It will be understood that each of the elements described above, or two or more together may also find a useful application in other types of methods differing from the type described above. Without further analysis, the foregoing will so fully reveal the gist of the present invention that others can, by applying current knowledge, readily adapt it for various applications without omitting features that, from the standpoint of prior art, fairly constitute essential characteristics of the generic or specific aspects of this invention set forth in the appended claims. The foregoing embodiments are presented by way of example only; the scope of the present invention is to be limited only by the following claims.
This is a continuation of U.S. patent application Ser. No. 14/869,070, filed on Sep. 29, 2015 (issuing as U.S. Pat. No. 9,457,326 on Oct. 4, 2016) which is a continuation of U.S. patent application Ser. No. 14/487,733, filed on Sep. 16, 2014 (issuing as U.S. Pat. No. 9,144,775 on Sep. 29, 2015), which is a continuation of U.S. patent application Ser. No. 13/458,526, filed Apr. 27, 2012 (issued as U.S. Pat. No. 8,834,016 on Sep. 16, 2014), which claims benefit of U.S. Provisional Patent Application Ser. No. 61/479,641, filed on Apr. 27, 2011, each of which is hereby incorporated herein by reference, and priority of each is hereby claimed. Priority of U.S. Provisional Patent Application Ser. No. 61/479,641, filed on Apr. 27, 2011, incorporated herein by reference, is hereby claimed.
| Number | Date | Country | |
|---|---|---|---|
| 61479641 | Apr 2011 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 14869070 | Sep 2015 | US |
| Child | 15284584 | US | |
| Parent | 14487733 | Sep 2014 | US |
| Child | 14869070 | US | |
| Parent | 13458526 | Apr 2012 | US |
| Child | 14487733 | US |
