Process of mixing two compounds to chemically obtain a solid compound and an alkaline liquid solution

Abstract

The subject process relates generally to producing an aqueous solution through a simple but highly effective chemical reaction. The aqueous solution is composed of a blended solution with water and an added solubilizer for the chemical reaction. The results produce an ionic solid and an alkaline liquid solution which are useful commercial products, and various applications including but not limited to use as a CO.sub.2 capture solvent.

Claims

1. A process consisting of mixing only one of the blended solutions of calcium hydroxide and calcium carbonate with only one of the solubilizers of sodium phosphate and sodium carbonate, in a mixing tank with water to chemically produce only one of the ionic solids of calcium phosphate and calcium carbonate, and only one of the alkaline liquid solutions of sodium hydroxide and sodium carbonate.

2. The process of claim 1, wherein the only one of the blended solutions is calcium hydroxide and the only one of the solubilizers is one of sodium phosphate and sodium carbonate, to chemically produce only the ionic solid calcium phosphate, and only one of the alkaline liquid solutions of sodium hydroxide and sodium carbonate.

3. The process of claim 1, wherein the only one of the blended solutions is calcium carbonate and the only one of the solubilizers is sodium phosphate, to chemically produce only the ionic solid of calcium phosphate and only the alkaline liquid solution of sodium carbonate.

4. The process of claim 1, wherein the only one of the blended solutions is calcium hydroxide and the only one of the solubilizers is sodium carbonate, to chemically produce only the ionic solid of calcium carbonate and only the alkaline liquid solution of sodium hydroxide.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 is a partial flow chart and a partial diagrammatic representation of an embodiment of the subject concept;

(2) FIG. 1A is a partial flow chart and a partial diagrammatic representation of a more detailed concept from the embodiment of FIG. 1;

(3) FIG. 1B is a partial flow chart and a partial diagrammatic representation of another more detailed concept from the embodiment of FIG. 1;

(4) FIG. 1C is a partial flow chart and a partial diagrammatic representation of yet another more detailed concept from the embodiment of FIG. 1; and

(5) FIG. 1D is a partial flow chart and a partial diagrammatic representation of still another more detailed concept from the embodiment of FIG. 1.

DETAILED DESCRIPTION

(6) Referring to FIG. 1 of the drawings, a process 10 is provided. A solution mixing tank 12, containing water, receives one blended solution 14 for mixing with a solubilizer 16. As the two blended solutions 14,16 are mixed, a chemical reaction occurs therebetween. The chemical reaction in the mixing tank 12 creates an ionic solid 22 that is delivered by line 24 to an ionic solid tank 26 for commercial use. The chemical reaction also creates an alkaline liquid solution 28 that is delivered by line 30 to an alkaline liquid storage tank 32. It is recognized that the alkaline liquid solution in the liquid storage tank 32 could be used further as needed. As set forth, it is further recognized that several different blended solutions and solubilizers could be used in the embodiment of FIG. 1 without departing from the essence of the subject invention. Some desired inputs and outputs will be set forth hereafter with respect to the remaining Figs. Likewise, depending on the selected blended solution chosen to mix with the selected solubilizer desired ionic solids and alkaline liquid solutions will be produced. For example, some desired outputs will be calcium phosphate and calcium carbonate (ionic solids), and sodium hydroxide, sodium carbonate, potassium hydroxide, lithium hydroxide and potassium phosphate (alkaline liquid solutions).

(7) Referring to FIG. 1A, an embodiment is illustrated providing a solution mixing tank 12, containing water from a source of water 18, receives calcium hydroxide 36 (blended solution), and sodium phosphate 38 (solubilizer). The result of the chemical reaction between the calcium hydroxide 36 and the sodium phosphate 38 are calcium phosphate 40 (an ionic solid) and sodium hydroxide 42 (an alkaline liquid solution). The calcium phosphate 40 is now available for commercial use. Likewise, the sodium hydroxide 42 is available for additional processing or if desirable, it could be sold for commercial uses.

(8) Referring to FIG. 1B, another embodiment is illustrated providing a solution mixing tank 12, containing water from a source of water 18, receives a calcium carbonate 46 (blended solution), and a sodium phosphate 38 (solubilizer). The results of the chemical reaction between the calcium carbonate 46 and the sodium phosphate 38 creates calcium phosphate 40 (an ionic solid) and sodium carbonate 48 (alkaline liquid solution). The calcium phosphate 40 is now available for commercial use. Likewise, the sodium carbonate solution 48 is now available for additional processing or available for commercial uses.

(9) Referring to FIG. 1C, yet another embodiment is illustrated providing a solution mixing tank 12, containing water from a source of water 18, receives calcium hydroxide 36 (blended solution), and sodium carbonate solution 48 (solubilizer). The results of the chemical reaction between the calcium hydroxide solution 36 and the sodium carbonate solution 48 creates calcium carbonate 46 (an ionic solid) and a sodium hydroxide solution 42 (alkaline liquid solution). The calcium carbonate 46 is now available for commercial use. Likewise, the sodium hydroxide solution 42 is now available for additional processing or available for commercial uses.

(10) Kiln dust are predominately solid by-products generated during cement and lime kiln production operations. In both lime kiln dust (LKD) and cement kiln dust (CKD), various amounts of calcium oxide (CaO) and free lime are present. Depending on the collection location, calcium carbonate may also be present along with different types of oxides, such as, potassium oxide (K.sub.2O) and, magnesium oxide (MgO). These oxides also react with the sodium carbonate (Na.sub.2CO.sub.3) to produce additional sodium oxide (Na.sub.2O), which when mixed in water becomes sodium hydroxide (NaOH).

(11) The mixing of the solubilizer with the kiln dust in water, chemically produces calcium carbonate in addition to the alkaline solution. The calcium carbonate is one of the main material inputs necessary for the manufacture of cement and lime. By using kiln dust as a blended solution with or instead of calcium hydroxide, a lot of processing costs will be saved.

(12) Referring to FIG. 1D, still another embodiment is illustrated providing a source of water 18, calcium carbonate 46 (blended solution), and sodium sulfate 50 (solubilizer). The results of the chemical reaction between the calcium carbonate 46 and the sodium sulfate 50 creates calcium sulfate 54 (an ionic solid) and a sodium carbonate solution 48 (alkaline liquid solution). The calcium sulfate 54 and the sodium carbonate solution 48 may each be used in one of the current processes or sold for other commercial uses.

(13) By replacing the calcium carbonate 46 in mixing tank 12 (FIG. 1D) with a calcium hydroxide 36, different results are achieved, in that, the ionic solid is the same but the alkaline liquid solution is now a sodium hydroxide solution 42 (alkaline liquid solution).

(14) From a review of the above embodiments, there are numerous combinations of a blended solution mixed with a solubilizer to achieve various results for various uses.

INDUSTRIAL APPLICABILITY

(15) The subject process with the various examples provides simple, safe, cost-effective designs for producing the alkaline liquid solutions and ionic solid for use in the current or additional processes and/or sold for other commercial uses. The subject designs far exceed the other suppliers of these products in production cost effectiveness, more secure ways of storing the products, and in many applications, not needing to store the product but keep redirecting it for other application on site.

(16) With use of kiln dusts in the subject process, large volumes of kiln dust will not be stored in huge piles or used as land fill throughout the country. The Federal Highway Administration (FHA) reported that approximately 14.2 million tons of cement kiln dust (CKD) are produced annually and approximately 2 to 4 million tons of lime kiln dust (LKD) are generated each year in the United States. Most of this kiln dust is disposed of in landfills or stockpiles, with 100 million tons currently stockpiled throughout the country. Even though some of this kiln dust can be sold, the cement/lime industry still incurs high costs for handling the kiln dust. In some applications, the kiln dust could be used in another process as it is being generated

(17) Other embodiments as well as certain variations and modifications of the embodiments herein shown and described will obviously occur to those skilled in the art upon becoming familiar with the underlying concept. It is to be understood, therefore that the subject design, as claimed, may be practiced otherwise than as specifically set forth above.