In oilfield environments, treatment of particles (e.g., cuttings) from drilling fluid must be reduced in size for them be able to be pumped into hydraulically induced fractures. Conventionally, the size of the particles as they come out of the drilling process is in a range of 0-30 mm. The size has to be reduced to a size below 300 microns, which is a size reduction ratio of 1:100. Such reduction is typically done with degradation centrifugal pumps or roller and hammer mills, which have either one or two shafts.
Conventional hammer mills can grind particles down to a certain particle size, but then get inefficient the finer the particles are. This leads to a build-up of particles in the milling circuit, which leads to high abrasion on the milling tools, high energy consumption, and equipment failure.
The foregoing and other features of the present disclosure will become more fully apparent from the following description and appended claims, taken in conjunction with the accompanying drawings. Understanding that these drawings depict several embodiments in accordance with the disclosure and are, therefore, not to be considered limiting of its scope, the disclosure will be described with additional specificity and detail through use of the accompanying drawings.
In the drawings:
In the following detailed description, reference is made to the accompanying drawings, which form a part hereof. In the drawings, similar symbols identify similar components, unless context dictates otherwise. The illustrative embodiments described in the detailed description and drawings are not meant to be limiting and are for explanatory purposes. Other embodiments may be utilized, and other changes may be made, without departing from the spirit or scope of the subject matter presented herein. It will be readily understood that the aspects of the present disclosure, as generally described herein, and illustrated in the drawings, may be arranged, substituted, combined, and designed in a wide variety of different configurations, each of which are explicitly contemplated and made part of this disclosure.
This disclosure is drawn to systems, devices, apparatuses, and/or methods, related to milling particles in drilling fluid. Specifically, the disclosed systems, devices, apparatuses, and/or methods relate to milling particles in drilling fluid using multiple milling techniques.
Example system 100 may receive drilling fluid including particles from an inlet 110. Inlet 110 may direct the drilling fluid including particles into first mill 120. A first motor 125 may be coupled to first mill 120 such that first motor 125 drives first mill 120. As first motor 125 causes first mill 120 to operate, first mill 120 may grind the particles. As first mill 120 grinds the particles, the particles' diameter is reduced, and at least some of the particles may be transferred to second mill 140. When the diameter of the particles in first mill 120 is smaller than gaps in diaphragm 130, the particles may exit first mill 120 to second mill 140 via diaphragm 130.
Second motor 145 may be coupled to second mill 140 such that second motor 145 drives second mill 140. As second motor 145 causes second mill 140 to operate, second mill 140 may grind particles. As second mill 140 grinds the particles, the particles' diameter is further reduced, and at least some of the particles may be transferred to an outlet 140 through an outlet diaphragm. When the diameter of the particles in second mill 140 is smaller than gaps in the outlet diaphragm, the particles may exit second mill 140 to outlet 150.
Operation of example system 100 may be controlled by an operator via a control panel. Some example control panels may receive input to control operation of the first mill and/or the second mill. Additionally, some example control panels may include error conditions and/or monitoring services to notify an operator of system statuses.
In some examples, first mill 120 may be a hammer mill and second mill 140 may be a pearl mill. In some examples, the hammer mill may be horizontally oriented. In some examples, the pearl mill may be horizontally oriented. In some examples, first motor 125 and second motor 145 may be any type of motor, including a direct drive engine or a gear drive engine.
Hammer mill 620 may include an access door 621 portion that allows an operator to open the side of hammer mill 620. Access door 621 may include a hinge 624 coupled to a portion of hammer mill 620.
Hammer mill 620 may include a hinged portion that allows an operator to open the top of hammer mill 620. This hinged portion may include a hinge coupled to a rear portion of hammer mill 620.
Hammer mill 620 may be a rotary mill that grinds particles using impact force(s). Hammer mill 620 may be coupled to a motor 625 such that motor 625 causes hammer mill 620 to operate. Specifically, motor 625 may be coupled to and rotate a shaft 626 within hammer mill 620. Impact tool(s) 627 may be removably coupled to shaft 626.
In some examples, each impact tool 627 may include a rotor 628. In some examples, a tool head 629 may be removably coupled to each rotor 628. Tool head 629 may be independently coupled to rotor 628 and may be separately removable and/or replaceable. In some examples, rotor 628 may include multiple arms extending away from shaft 626. In some examples, a tool head 629 may be removably coupled to the end of each arm.
In some examples, impact tools 627 and/or tool heads 629 may be of tungsten carbide or other suitable material.
In some examples, hammer mill 620 may include liner(s) 623 coupled to the interior of hammer mill 620. In some examples, liner(s) 623 may be removable from hammer mill 620 in multiple pieces or as a single component.
Example system 600 may receive drilling fluid including particles from an inlet 610. Inlet 610 may direct the drilling fluid including particles into hammer mill 620. Motor 625 causes hammer mill 620 to operate to grind the particles. As hammer mill 620 grinds the particles, the particles' diameter is reduced, and at least some of the particles may be transferred to pearl mill 640. When the diameter of the particles in hammer mill 620 is smaller than gaps in diaphragm 630, the particles may exit hammer mill 620 to pearl mill 640 via diaphragm 630.
Pearl mill 840 may include an access door 841 portion that allows an operator to open the side of pearl mill 840. Access door 841 may include a hinge 824 coupled to a portion of pearl mill 840.
Pearl mill 840 may include a hinged portion 843 that allows an operator to open the front of pearl mill 840. Hinged portion 843 may include a hinge 842 coupled to a lower portion of pearl mill 840.
Pearl mill 840 may be a rotary mill that grinds particles primarily using friction. Pearl mill 840 may be coupled to a motor 845 such that motor 845 causes pearl mill 840 to operate. Specifically, motor 845 may be coupled to and rotate a shaft 846 within pearl mill 840. Rotation tool(s) 847 may be removably coupled to shaft 846.
In some examples, pearl mill 840 may include liner(s) coupled to the interior of pearl mill 840. In some examples, liner(s) may be removable from pearl mill 840 in multiple pieces or as a single component.
Pearl mill 840 may receive the drilling fluid including particles from hammer mill via diaphragm 830. Motor 845 causes pearl mill 840 to operate to grind the particles. As pearl mill 840 rotates, the particles may contact grinding media, the rotation tool(s), and/or liner(s). Such contact acts to grind the particles, and the particles' diameter is reduced (even further than in the hammer mill). In some examples, grinding media may include ceramic grinding media or other suitable grinding material. At least some of the particles may be transferred through outlet diaphragm to outlet 850. When the diameter of the particles in pearl mill 840 is smaller than gaps in outlet diaphragm, the particles may exit pearl mill 840 to outlet 850 via outlet diaphragm.
In some examples, example method 1100 may also include, prior to friction grinding, transferring only the particles having a reduced diameter from the first chamber to the second chamber. In some examples, example method 1100 may also include, after friction grinding, transferring only the particles having a further reduced diameter from the second chamber to an outlet. In some examples, transferring particles from a first mill to a second mill may occur based on fluid pressure of the drilling fluid in the first mill.
While various aspects and embodiments have been disclosed herein, other aspects and embodiments will be apparent to those skilled in the art. The various aspects and embodiments disclosed herein are for purposes of illustration and are not intended to be limiting, with the true scope and spirit being indicated by the following claims.
Number | Name | Date | Kind |
---|---|---|---|
2260826 | Booge | Oct 1941 | A |
3910507 | Okada et al. | Oct 1975 | A |
5375779 | Ephraim | Dec 1994 | A |
5551639 | Artemjev et al. | Sep 1996 | A |
5655720 | Hixon et al. | Aug 1997 | A |
6453584 | Buckner | Sep 2002 | B1 |
7374115 | Geiger et al. | May 2008 | B2 |
20020033278 | Reddoch | Mar 2002 | A1 |
20080099591 | Cerra et al. | May 2008 | A1 |
20120234952 | Nordell | Sep 2012 | A1 |
Entry |
---|
International Search Report and Written Opinion for corresponding PCT Application No. PCT/US2014/012423 dated Apr. 29, 2014, 14 pages. |
Number | Date | Country | |
---|---|---|---|
20140209717 A1 | Jul 2014 | US |