SORBENT FOR REMOVING RADON, PRODUCTION METHOD FOR SAME, AND RADON REMOVAL METHOD USING SAME

Abstract

The present invention relates to a method of preparing an adsorbent for removing radon. The method includes (a) mixing a fluorine (F) compound and zeolite to produce a second mixture.

Claims

1. An adsorbent for removing radon containing zeolite bound to fluorine (F).

2. The adsorbent of claim 1, wherein the zeolite is natural zeolite.

3. A method of preparing an adsorbent for removing radon, comprising (a) mixing a fluorine (F) compound and zeolite to produce a second mixture.

4. The method of claim 3, wherein the zeolite is natural zeolite.

5. The method of claim 3, wherein the fluorine (F) compound is ammonium fluoride (NH.sub.4F).

6. The method of claim 3, further comprising (b) stirring the second mixture at a temperature of 60 to 100 C. for 2 to 4 hours.

7. The method of claim 6, further comprising: (c) after (b), cooling the second mixture to room temperature; and (d) after (c), drying the second mixture for 12 to 24 hours.

8. The method of claim 3, wherein the (a) includes: (a-1) mixing zeolite and ultrapure water to produce a first mixture; (a-2) stirring the first mixture at a temperature of 60 to 100 C. for 0.1 to 2 hours; and (a-3) after (a-2), mixing the fluorine (F) compound with the first mixture to produce the second mixture.

9. The method of claim 8, wherein in (a-3), the fluorine (F) compound is mixed with the first mixture through a plurality of times by a predetermined amount at a time to produce the second mixture.

10. The method of claim 8, wherein in (a-1), 30 to 50 mL of ultrapure water per 1 g of the zeolite is mixed.

11. A method of removing radon in water, comprising: (f) putting an adsorbent into water containing radon, wherein the adsorbent contains zeolite to which fluorine (F) is bound.

12. The method of claim 11, further comprising (g) after (f), adsorbing radon by the adsorbent for 10 to 70 hours.

13. The method of claim 12, wherein the water is groundwater.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0027] FIG. 1 is a diagram schematically illustrating a method of preparing an adsorbent for removing radon according to the present invention.

[0028] FIG. 2 is a diagram illustrating experimental results for radon removal efficiency of the adsorbent prepared by the preparing method according to the present invention and natural zeolite.

BEST MODE

[0029] Hereinafter, a method according to the present invention will be described in detail with reference to the accompanying drawings. Terms to be described below are defined in consideration of functions in the present invention and may be construed in different ways by the intention of users or practice. Therefore, these terms should be defined on the basis of the contents throughout the present specification.

[0030] 1. Method of Preparing Adsorbent

[0031] Referring to FIG. 1, a method of preparing an adsorbent for removing radon according to the present invention will be described.

[0032] The adsorbent for removing radon according to the present invention may be an adsorbent containing zeolite to which fluorine (F) is chemically bound.

[0033] A first mixture may be produced by mixing ultrapure water with zeolite in powder form for increasing a surface area. A second mixture may be produced by mixing a fluorine (F) compound with the first mixture.

[0034] Here, the zeolite may be any kind of zeolite, but may preferably be a natural zeolite. The fluorine compound may be any compound as long as it contains fluorine, but is preferably ammonium fluoride (NH.sub.4F).

[0035] After the above-described second mixture is stirred at a constant temperature for a constant time, precipitate is separated from the second mixture and dried to produce the zeolite to which the fluorine is bound.

[0036] A specific preparing experiment for preparing an adsorbent for removing radon will be described. [0037] (1) Put 5 g of powdered natural zeolite sieved to 150 m or less to increase the surface area into a 500 mL of polypropylene bottle. The first mixture is produced by mixing 200 mL of ultrapure water with the natural zeolite. [0038] (2) The first mixture is put in an oven and stirred at 80 C. for about 1 hour so that the zeolite is homogeneously mixed. [0039] (3) After step (2) above, while stirring, 50 mL of 1.33M ammonium fluoride (NH.sub.4F) is mixed by being slowly dropped by 1 mL each into the first mixture using a pipette for 1 hour to produce a second mixture. This is to ensure sufficient reaction by slowly mixing a small amount of ammonium fluoride. [0040] (4) After step (3) above, the second mixture produced in step (3) above is maintained at a temperature of 80 C. for about 3 hours while stirring is maintained. [0041] (5) Next, after stopping the stirring, the second mixture is taken out of the oven, sufficiently cooled until the temperature of the second mixture is lowered to a temperature similar to room temperature, and then dried for 12 to 24 hours. [0042] (6) Next, precipitate is separated from the second mixture using a filter paper having a pore diameter of 6 m. [0043] (7) The precipitate obtained from the second mixture is sufficiently dried to finally produce zeolite chemically bound to fluorine.

[0044] 2. Radon Removal Experiment

[0045] FIG. 2 is a graph comparing each radon removal efficiency in an experiment in which radon contained in groundwater is removed using simple natural zeolite and zeolite to which fluorine was chemically bound.

[0046] The experiment was conducted by putting 0.5 g each of the two adsorbents (natural zeolite and zeolite chemically bound to fluorine) into 15 mL of groundwater containing about 200 Bq/L of radon.

[0047] The radon removal efficiency was calculated using the difference between an initial radon concentration C.sub.0 in groundwater and a radon concentration C.sub.1 in groundwater after the adsorption experiment.

Radon removal efficiency (%)=(C.sub.0C.sub.1)/C.sub.0*100

[0048] Looking at the experimental results with reference to FIG. 2, after 24 hours, the radon removal efficiency of the natural zeolite is about 40%, whereas the radon removal efficiency of the zeolite chemically bound to the fluorine is 70%.

[0049] Looking at the radon removal efficiency according to the adsorption time, it can be seen that the adsorbent according to the present invention has significantly higher removal efficiency than the radon removal efficiency of the natural zeolite when the adsorption proceeds for about 10 to 70 hours. In particular, it shows remarkable radon removal efficiency for 10 to 50 hours.

[0050] In FIG. 2, FFNZ refers to the zeolite to which the fluorine is chemically bound.

[0051] Hereinabove, the present specification has been described with reference to the embodiments illustrated in the drawings so that those skilled in the art can easily understand and reproduce the present invention, but this is only exemplary, and those skilled in the art will understand that other embodiments equivalents variously modified from and equivalent to the embodiments of the present invention are possible. Therefore, the scope of protection of the present invention should be defined by the claims.