Caustic soda (sodium hydroxide, NaOH) and caustic potash (potassium hydroxide, KOH) are chemicals used to control the pH of water-based drilling fluids. Approximately 33,000 to 45,000 tons of these chemicals are used annually in the drilling fluids industry. Both are corrosive materials, handling of which causes injuries in the drilling industry each year. As used hereinafter the term “caustic” shall mean caustic soda, caustic potash, or a mixture of both chemicals. Before being added to the drilling fluid, dry caustic is dissolved in water at the drilling rig site. This process gives off a great deal of heat and results in a highly corrosive solution. Traditional methods of handling caustic at the drilling rig site involve the risk of exposure to dry caustic and concentrated caustic solutions resulting in severe burns and irritation to the skin, lung, and eyes.
Caustic used in drilling fluids is typically supplied to the rig in dry form (flakes or beads) in 40 lb or 50 lb sacks. While dry caustic is sometimes added directly to the drilling fluid system, more frequently it is dissolved in water at the rig site and added to the drilling fluid in liquid form to ensure that it is rapidly and evenly mixed throughout the entire drilling fluid system.
Several problems are encountered when dealing with sacks of caustic. First, empty sacks containing the dry powder residue are either improperly disposed of in land fills, or are incinerated. Next, back injuries result from lifting heavy sacks (40-50 lbs each) to pour in a mixing barrel. The mixing process requires a full protective hazmat suit, and all unprotected personnel must leave immediate area during this process. As a result of the wearing of the hazmat suit, the mobility and vision of personnel is limited. In addition, personnel turnover due to hazardous exposure is high. Finally, use of sacks can result in a lack of quality control in uniform mixing to fluid ratios.
To this end, a need exists for an improved caustic mixing apparatus and method which isolates personal at a work site from exposure to hazardous materials. It is to such an apparatus and method that the inventive concepts disclosed herein are directed.
Referring now to the drawings, and particularly to
The hopper 12 is preferably a reusable, stainless steel transport container defining a chemical storage chamber. The hopper 12 can be selectively connected and disconnected from the conveyor assembly 16 (
As best shown in
The support skid 14 supports the mixing tank 18 and the conveyor assembly 36 (
Referring now to
The chemical mixer 10 is preferably automated to better ensure quality control through even delivery of caustic chemical to water. This results in lower costs due to appropriate level of chemical and ensures the well is not negatively impacted. To this end, conventional control systems such as a control assembly 69 may be utilized to synchronize the operation of the various components of the chemical mixer 10.
In use, the hopper 12 is filled with caustic at a remote, sealed location, and transported to the drilling rig site. At the drilling rig site, the hopper 12 is positioned on the platform 52 of the skid 14 such that the discharge conduit 34 is positioned in the first end 40 of the conveyor assembly 16 and connected to the conveyor assembly 16. A cycle is started by activating control assembly 69. A liquid fill valve 70 is caused to open and liquid is introduced into the mixing tank 18 via a conduit 71. The pump 60 starts withdrawing and reintroducing liquid into the mixing tank through the nozzle assembly 58 via a conduit 67 (
The mixing tank 18 may be of any size and dimension, but preferably is sized to accommodate an 8,000 foot well under normal application. Also, while the chemical mixer 10 has been described for use in the oil and gas industry, it should be appreciated that the chemical mixer may have application in other industries where there is a desire to eliminate the handling of reactive chemicals/fumes/gases or air containments which can irritate the human body. It should also be appreciated that the components of the chemical mixer 10 may be modified as to minimize explosion and/or fire safety risks as required by applicable industry safety standards. Such modifications may vary depending on the specific safety standards at a particular drilling rig site.
From the above description, it is clear that the inventive concepts expressed herein are well adapted to carry out the objects and to attain the advantages mentioned herein as well as those inherent in the inventive concepts expressed herein. While presently preferred embodiments of the inventive concepts disclosed herein have been described for purposes of this disclosure, it will be understood that numerous changes may be made which will readily suggest themselves to those skilled in the art and which are accomplished within the spirit of the inventive concepts disclosed and as defined in the appended claims.
This application claims benefit to U.S. Provisional Application No. 61/295,963, filed Jan. 18, 2010, and U.S. Provisional Application No. 61/236,629, filed Aug. 25, 2009, the entire contents of each being hereby incorporated herein by reference.
Number | Name | Date | Kind |
---|---|---|---|
3822056 | Hawes et al. | Jul 1974 | A |
4494345 | Peterson | Jan 1985 | A |
5303998 | Whitlatch et al. | Apr 1994 | A |
5823670 | Rushing et al. | Oct 1998 | A |
6796704 | Lott | Sep 2004 | B1 |
7401973 | Lott | Jul 2008 | B1 |
20030076737 | Grassi | Apr 2003 | A1 |
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International Search Report and the Written Opinion (PCT/US2010/046651); May 20, 2011. |
Number | Date | Country | |
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20110203699 A1 | Aug 2011 | US |
Number | Date | Country | |
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61295963 | Jan 2010 | US | |
61236629 | Aug 2009 | US |