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OwnerDaniel Kappes, Terence Albert +1inventors
InventorsDaniel Kappes, Terence Albert, Dennis Anderson
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The present invention is a process to react limestone with sulfate and/or sulfuric acid solutions and/or other solutions containing sulfates, in order to neutralize the solutions and precipitate the sulfates, in such a way that the limestone is used with an efficiency that makes the use of limestone economic. This reaction is most often used in the environmental cleanup of mine and industrial wastes, however it may be used in other industrial applications. In previously existing technology, the reaction is typically done in agitated tanks containing a slurry of the solution mixed with lime or limestone, or in percolating beds of crushed limestone. Typically the reaction of limestone in such systems is very slow and inefficient, so that normally the use of limestone is precluded—it is instead necessary to utilize lime (calcium oxide or hydroxide). In the present invention, the limestone is reacted with the solution continuously, in a high intensity reactor, which is designed to provide a high-energy input and continuous renewal of the limestone surface. The technology and methodology are a new and novel approach that earlier researchers and engineering applications did not use and the new technology is not obvious or describes in prior art or practice.
1) The process of reacting an acidic or high-dissolved-solids solution with limestone whereby the reaction takes place in a high intensity reactor which continually renews and impacts the surfaces of the limestone particles, in order to affect a rapid reaction rate and an efficient utilization of the limestone.
4) The two stage process of reacting an acidic solution with limestone in a high intensity reactor in order to affect a rapid reaction rate, an efficient utilization of limestone, and a partial rectification of the solution, followed by a second stage whereby the solution and/or the limestone slurry is contacted with hydrated or quick lime (usually in a stirred tank reactor) to complete the rectification of the solution.
5) The processes of steps 1 through 4, in which the solution is a dilute, slightly acidic sulfate solution of the type commonly encountered in environmental discharge streams from mines and process plants.
6) The processes of steps 1 through 5, in which either the limestone or lime slurry, or the combined slurry, is partially thickened, and a dense slurry stream is recycled to either the first or second stage reactors, with the purposes of completing the utilization of the reagents, and of nucleating the resulting product so that it filters and/or settles more rapidly than a non-nucleated product.
7) The process of achieving solution rectification by any of the steps 1 through 6, followed by filtering or settling the slurry to remove the solids from the liquids, followed by discharging the liquids in an environmentally acceptable manner and disposing of the solids in an acceptable solids disposal facility.
8) The process of achieving solution rectification by any of the steps 1 through 6, that is enhanced by aeration or oxidation within the reactor as the acid neutralization process is ongoing.
9) The process of steps 1 through 6 as they are applied in conjunction with other processes, or as part of a larger processing system.
10) The process of steps 1 through 6 as they are applied in conjunction with the addition of other chemicals to enhance the reaction, or to conduct unrelated reactions simultaneously.
Dependencies are inferred from the claim text.