METHOD FOR PREPARING INORGANIC COMPOUND USING DESULFURIZATION GYPSUM FOR REDUCING GREENHOUSE GAS EMISSIONS

Abstract

The present invention relates to a method for preparing an inorganic compound using desulfurization gypsum for reducing greenhouse gas emissions, and, more specifically, to a method for preparing an inorganic compound, in which calcium sulfate and calcium carbonate, which have various uses as construction materials and the like, can be prepared using, as raw material, desulfurization gypsum which, being a recycled resource, is industrial waste, and an extraction agent, and the extraction agent can be reused after separation, and thus, compared to existing processes, greenhouse gases and manufacturing costs can be remarkably reduced.

Claims

1. A method for producing inorganic compounds using desulfurization gypsum comprising an anhydrous gypsum powder manufacturing step of filtering a mixture of desulfurized gypsum, eluent and water to separate the filtrate and anhydrous gypsum cake, and drying the separated anhydrous gypsum cake; and a calcium carbonate powder manufacturing step of supplying a carbon dioxide-containing gas to the filtrate separated in the anhydrous gypsum powder manufacturing step, filtering the mixture to separate it into a calcium carbonate cake and an eluent solution, and drying the separated calcium carbonate cake, wherein the eluent solution separated in the calcium carbonate powder manufacturing step is reused by supplying it to the anhydrous gypsum powder manufacturing step.

2. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the desulfurized gypsum is prepared in a CFBC boiler and comprises 40 to 60% by weight of CaSO.sub.4 and 25 to 45% by weight of CaO.

3. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the eluent is selected from the group consisting of NH.sub.4Cl, NH.sub.4NO.sub.3 and combinations thereof.

4. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the weight ratio of desulfurization gypsum and water is 1:5 to 1:45 in the anhydrous gypsum powder manufacturing step.

5. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the weight ratio of desulfurization gypsum and eluent is 1:0.7 to 1:2 in the anhydrous gypsum powder manufacturing step.

6. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the carbon dioxide-containing gas is an exhaust gas of a circulating fluidized bed combustion boiler.

7. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the anhydrous gypsum powder manufacturing step is performed at 20? C. to 30? C. for 2 to 10 hours.

8. The method for producing inorganic compounds using desulfurization gypsum according to claim 1, wherein the calcium carbonate powder manufacturing step is performed at 20? C. to 30? C. for 1 to 5 hours.

Description

BRIEF DESCRIPTION OF THE FIGURES

[0014] FIG. 1 schematically shows the process of Example 1, which is a method for producing an inorganic compound of the present invention.

[0015] FIG. 2 schematically shows the process of the Comparative Example of the present invention corresponding to the prior art.

[0016] FIG. 3 shows the result of X-ray diffraction analysis of the anhydrous gypsum powder obtained in Examples 1 and 2.

[0017] FIG. 4 shows the result of X-ray diffraction analysis confirming that Vaterite-type PCC was obtained in Examples 1 and 2.

[0018] FIG. 5 shows the result of X-ray diffraction analysis of inorganic compounds (anhydrous gypsum powder and PCC) obtained in the Comparative Example.

[0019] FIG. 6 shows the result of SEM analysis of PCC obtained in Example 1.

[0020] FIG. 7 shows the result of SEM analysis of PCC obtained in the Comparative Example.

CONCRETE MODE FOR CARRYING OUT THE INVENTION

[0021] The present invention is explained in more detail below.

[0022] The method for producing inorganic compounds using desulfurization gypsum of the present invention comprises an anhydrous gypsum powder manufacturing step of filtering a mixture of desulfurized gypsum, eluent and water to separate the filtrate and anhydrous gypsum cake, and drying the separated anhydrous gypsum cake; and a calcium carbonate powder manufacturing step of supplying a carbon dioxide-containing gas to the filtrate separated in the anhydrous gypsum powder manufacturing step, filtering the mixture to separate it into a calcium carbonate cake and an eluent solution, and drying the separated calcium carbonate cake, wherein the eluent solution separated in the calcium carbonate powder manufacturing step is reused by supplying it to the anhydrous gypsum powder manufacturing step.

[0023] In the present specification, the anhydrous gypsum powder manufacturing step may be referred to as the first step, and the calcium carbonate powder manufacturing step may be referred to as the second step.

[0024] The method for producing inorganic compounds using desulfurization gypsum of the present invention comprises the anhydrous gypsum powder manufacturing step of filtering a mixture of desulfurized gypsum, eluent and water to separate the filtrate and anhydrous gypsum cake, and drying the separated anhydrous gypsum cake.

[0025] CaO in desulfurization gypsum (CaOCaSO.sub.4) is hydrated and dissolved in water and separated from CaSO.sub.4, but the degree is low, so an eluent that can promote dissolution is injected. As the eluting agent, various components as described below may be used, and in one embodiment, NH.sub.4Cl may be used. The reaction at this time is as follows. [0026] CaSO.sub.4.Math.CaO(s)+2NH.sub.4Cl(aq).fwdarw.CaSO.sub.4(s)+CaCl.sub.2)(aq)+2NH.sub.3(aq)+H.sub.2O(I)

[0027] In one embodiment of the present invention, CaSO.sub.4(s), CaCl.sub.2(aq), 2NH.sub.3(aq) and H.sub.2O(I) may exist in the mixture of desulfurization gypsum, eluent and water due to the above reaction. Since CaCl.sub.2) has a higher solubility in water than Ca(OH).sub.2 generated when no separate eluent is added (i.e., when only desulfurization gypsum and water are mixed), a small amount of water can be used to elute CaO and separate it from anhydrous gypsum.

[0028] The desulfurization gypsum used in the present invention is manufactured for the purpose of removing sulfur oxides generated in a circulating fluidized bed boiler (CFBC boiler), its raw material is limestone, and the desulfurization reaction path in the CFBC boiler is as follows. [0029] 1st. CaCO.sub.3.fwdarw.CaO+CO.sub.2 (850?900? C.) [0030] 2nd. CaO+SO.sub.2+1/2O.sub.2+CaSO.sub.4

[0031] The desulfurization gypsum (CaOCaSO.sub.4) used in the present invention may comprise 40 to 60% by weight of CaSO.sub.4 and 25 to 45% by weight of CaO. In the second step of the desulfurization reaction, the CaO conversion rate is about 50%, and precipitated calcium carbonate is produced using unreacted CaO present in the desulfurization gypsum, and other components can be used as anhydrous gypsum products.

[0032] The eluent used in the anhydrous gypsum powder manufacturing step may be one selected from the group consisting of NH.sub.4Cl, sodium boride, urea, NH.sub.4NO.sub.3 and combinations thereoffor example, NH.sub.4Cl.

[0033] In the anhydrous gypsum powder manufacturing step, the weight ratio of desulfurization gypsum and water may be 1:5 to 1:45for example, 1:5 to 1:40, 1:6 to 1:30 or 1:8 to 1:20. If the amount of water compared to desulfurization gypsum is lower than the above ratio, the amount of dissolution of CaO in the desulfurization gypsum is insignificant, so the quality (purity) of anhydrous gypsum and the amount of calcium carbonate produced may decrease. Conversely, if the content of water is greater than the above ratio, it is difficult to obtain additional effects.

[0034] In the anhydrous gypsum powder manufacturing step, the weight ratio of desulfurization gypsum and eluent may be 1:0.7 to 1:2for example, 1:0.75 to 1:1.8 or 1:0.8 to 1:1.5. If the amount of eluent compared to desulfurization gypsum is lower than the above ratio, the amount of dissolution of CaO in the desulfurization gypsum is insignificant, so the quality (purity) of anhydrous gypsum and the amount of calcium carbonate produced may decrease. Conversely, if the content of eluent is greater than the above ratio, it is difficult to obtain additional effects.

[0035] In the anhydrous gypsum powder manufacturing step, anhydrous gypsum powder may be prepared by drying the separated anhydrous gypsum cake. Manufactured anhydrous gypsum can be used as a building material, fertilizer, etc. through washing and drying processes.

[0036] The anhydrous gypsum powder manufacturing step may be performed at 20? C. to 30? C.for example, room temperaturefor 2 to 10 hoursfor example, 2 to 8 hours or 2 to 6 hours.

[0037] The method for producing inorganic compounds using desulfurization gypsum of the present invention comprises a calcium carbonate powder manufacturing step of supplying a carbon dioxide-containing gas to the filtrate separated in the anhydrous gypsum powder manufacturing step, filtering the mixture to separate it into a calcium carbonate cake and an eluent solution, and drying the separated calcium carbonate cake.

[0038] The filtrate separated in the anhydrous gypsum powder manufacturing step may contain CaCl.sub.2) and NH.sub.3 due to the reaction between CaO separated from the desulfurization gypsum and the eluent. In one embodiment, when a carbon dioxide-containing gas is supplied to the filtrate from which CaO is eluted (calcium is eluted in the form of CaCl.sub.2)) to give carbon dioxide, CaCl.sub.2) is precipitated as CaCO.sub.3 (PCC), and NH.sub.3 (aq.) and Cl.sup.? combines to form NH.sub.4Cl. [0039] CaCl.sub.2(aq)+2NH.sub.3(aq)+2H.sub.2O(I)+CO.sub.2(g).fwdarw.CaCO.sub.3(s)+2NH.sub.4Cl(aq)+H.sub.2O(I)

[0040] In the calcium carbonate powder manufacturing step, the mixture can be separated into calcium carbonate cake and eluent solution, and the separated eluent solution can be reused by supplying the solution to the anhydrous gypsum manufacturing step. In one embodiment, the eluent may be NH.sub.4Cl, and may be used for eluting CaO in desulfurization gypsum by supplying it to the anhydrous gypsum powder manufacturing step, thereby reducing process costs due to the use of the eluent.

[0041] The carbon dioxide-containing gas used in the calcium carbonate powder manufacturing step is not particularly limited, and for example, exhaust gas from a circulating fluidized bed combustion boiler or 100% carbon dioxide gas can be used. Although not particularly limited, the carbon dioxide-containing gas may be supplied at 100 to 500 ml/min.

[0042] In the calcium carbonate powder manufacturing step, after separating the calcium carbonate cake and the eluent solution, the eluent is supplied to the anhydrous gypsum powder manufacturing step, and the separated calcium carbonate cake is dried to prepare calcium carbonate powder. The produced calcium carbonate may be precipitated calcium carbonate (PCC), which, unlike limestone, has high whiteness and small particle size, and is used as a functional agent in various industries.

[0043] The calcium carbonate powder manufacturing step may be performed at 20? C. to 30? C.for example, at room temperaturefor 1 to 5 hoursfor example, 1 to 4 hours or 1 to 3 hours.

[0044] The present invention is explained in more detail through the following Examples and Comparative Examples. However, the scope of the present invention is not limited thereby in any manner.

EXAMPLES

Example 1, Example 2 and Comparative Example

[0045] In the configuration shown in Table 1 below, a method for producing inorganic compound using the desulfurization gypsum of the present invention was performed (Step 1: anhydrous gypsum powder manufacturing step, Step 2: calcium carbonate powder manufacturing step).

[0046] Example 1 uses the eluent for the first time, Example 2 uses the eluate separated from the reaction of Step 2 of Example 1, and the Comparative Example uses only desulfurization gypsum and water without using a separate eluent.

[0047] The process of Example 1, which is a method for producing the inorganic compound of the present invention and the process of the Comparative Example are schematically shown in FIGS. 1 and 2, respectively.

TABLE-US-00001 TABLE 1 Step 1: CaO elution Raw materials (g) Added Step 2: PCC manufacturing Desulfurization Deionized ratio of Supplied Categories gypsum NH.sub.4Cl water Ca.sup.2+:2Cl.sup.? Time Temperature CO.sup.2 Time Temperature Example 1 60 51 600 1:2 4 h Room 100%, 1 h 20 m Room temperature 200 ml/min temperature Example 2 60 Using the eluate separated from the 4 h Room 100%, 1 h 20 m Room reaction of Step 2 of Example 1 temperature 200 ml/min temperature Comparative 12 0 600 1:0 15 h Room 100%, 6 h 00 m Room Example temperature 200 ml/min temperature

[0048] The X-ray diffraction analysis results of the inorganic compounds obtained in Examples 1 and 2that is, anhydrous gypsum powder and calcium carbonate (PCC)are shown in FIGS. 3 and 4, respectively.

[0049] From FIG. 3, it was confirmed that the anhydrous gypsum after the first step of Example 1 was produced in a form in which CaO and Ca(OH).sub.2 components were removed compared to the raw material desulfurization gypsum. In addition, in Example 2, it was confirmed that the reused eluent elutes CaO and Ca(OH).sub.2 components in the desulfurization gypsum, which is the raw material, in the same way as in Example 1. This can be said to prove the effectiveness of the reuse of the eluent in the method for producing inorganic compounds using the desulfurization gypsum of the present invention.

[0050] In addition, the results of X-ray diffraction analysis confirming that calcium carbonate in the form of vaterite (PCC) was obtained in Examples 1 and 2 are shown in FIG. 4. It was confirmed that vaterite-type PCC was synthesized by adding carbon dioxide to the filtrate in the second step of Example 1, and PCC of the same type (vaterite) as Example 1 was synthesized in Example 2 in which the process was performed by reusing the eluent of Example 1. This can also be said to prove the effectiveness of the reuse of the eluent in the method for producing inorganic compounds using the desulfurization gypsum of the present invention.

[0051] Meanwhile, the X-ray diffraction analysis result of the inorganic compounds (anhydrous gypsum powder and PCC) obtained in the Comparative Example is shown in FIG. 5. In the Comparative Example, in order to dissolve CaO in the desulfurization gypsum, a large amount of water (solvent) was used in the Step 1 process compared to the Examples and sufficient reaction time was given, but it was confirmed that CaO remained in a hydrated form in the anhydrous gypsum. In addition, it was confirmed that PCC in the form of calcite was synthesized in the step 2 process differently from the Examples.

[0052] FIG. 6 shows the SEM analysis result of PCC obtained in Example 1, and FIG. 7 shows the SEM analysis result of PCC obtained in the Comparative Example. It can be confirmed that the PCC obtained in Example 1 is vaterite particles and the PCC obtained in the Comparative Example is calcite particles. As can be seen in FIG. 6, vaterite particles have a spherical shape unlike calcite particles, and have the advantage of increasing strength and improving economic efficiency while maintaining the flexibility of rubber when used as a rubber additive. On the other hand, as can be seen in FIG. 7, calcite particles are mainly in the form of hexagons, and have angles, so they have little flexibility compared to vaterite particles.