Solid-phase catalyst for decomposing hydrogen peroxide and method for producing same

Abstract

The present invention provides a solid-phase catalyst for decomposing hydrogen peroxide comprising a permanganate salt and a manganese (II) salt. The solid-phase catalyst stays a solid state in the form of nanoparticles at the time of hydrogen peroxide decomposition, and thus can be recovered for reuse and also has an excellent decomposition rate. In the method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to the present invention, a solid-phase catalyst is produced from a solution containing a permanganate salt, a manganese (II) salt, and an organic acid, so that the produced solid-phase catalyst is precipitated as a solid component even after a catalytic reaction, and thus is reusable and environmentally friendly, and cost reduction can be achieved through the simplification of a catalyst production technique.

Claims

1. A method for producing a solid-phase catalyst for decomposing hydrogen peroxide comprising the following steps: preparing an aqueous solution, comprising adding a permanganate salt, a manganese (II) salt and one or more organic acids selected from the group consisting of formic acid, acetic acid, oxalic acid, and citric acid to water (step 1); aging the aqueous solution of step 1 to form a solid-phase catalyst (step 2); and cleaning, drying and calcinating the solid-phase catalyst formed in step 2 (step 3).

2. The method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to claim 1, wherein the solid-phase catalyst is a heterogeneous catalyst of nanoparticles.

3. The method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to claim 1, wherein the permanganate salt is selected from the group consisting of potassium permanganate (KMnO.sub.4), zinc permanganate (Zn(MnO.sub.4).sub.2), calcium permanganate (Ca(MnO.sub.4).sub.2), silver permanganate (AgMnO.sub.4), sodium permanganate (NaMnO.sub.4), barium permanganate (Ba(MnO.sub.4).sub.2), magnesium permanganate (Mg(MnO.sub.4).sub.2), strontium permanganate (Sr(MnO.sub.4).sub.2), lithium permanganate (LiMnO.sub.4), cadmium permanganate (Cd(MnO.sub.4).sub.2), cesium permanganate (CsMnO.sub.4), and rubidium permanganate (RbMnO.sub.4).

4. The method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to claim 1, wherein the manganese (II) salt is one or more compounds selected from the group consisting of manganese acetate, manganese nitrate, manganese chloride, manganese acetylacetonate, manganese bromide, manganese carbonate, manganese fluoride, manganese iodide, and manganese sulfate.

5. The method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to claim 1, wherein the aging treatment in step 2 is performed with the sealed mixture in a dark room at room temperature at normal pressure for 580 hours.

6. The method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to claim 1, wherein the calcinating process in step 3 is performed in air or an inert gas atmosphere at 50350 C.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) The application of the preferred embodiments of the present invention is best understood with reference to the accompanying drawings, wherein:

(2) FIG. 1 is a graph illustrating the oxygen generation rate during the decomposition of hydrogen peroxide by the catalysts of Example 1, Comparative Example 1 and Comparative Example 2 according to the present invention.

(3) FIG. 2 is a set of photographs illustrating the comparison of the remaining catalyst and filtrate after the decomposition of hydrogen peroxide by the catalysts of Example 1, Comparative Example 1 and Comparative Example 2 according to the present invention.

BEST MODE

(4) Hereinafter, the present invention will be described in detail with reference to the following examples and experimental examples.

(5) However, the following examples and experimental examples are merely illustrative of the present invention, and the scope of the present invention is not limited by examples and experimental examples.

EXAMPLE 1

Preparation of a Solid-phase Catalyst for Decomposing Hydrogen Peroxide Treated with Acetic Acid

(6) Step 1: 10 ml of 1 M potassium permanganate and 30 ml of 1 M manganese (II) acetate were dissolved in 20 ml of distilled water, to which 99% acetic acid was additionally added. Then the mixture was stirred at room temperature for 10 minutes.

(7) Step 2: The mixture prepared in step 1 was tightly sealed, followed by aging in a dark room at room temperature under normal pressure for 72 hours.

(8) Step 3: The solid-phase catalyst produced in the mixture of step 2 was recovered, which was then washed with ml of ethanol and then dried in a 70 C. vacuum oven. Then, calcination was performed at 200 C., resulting in the preparation of a solid-phase catalyst for decomposing hydrogen peroxide.

EXAMPLE 2

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Formic Acid

(9) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 15 ml of 96% formic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

EXAMPLE 3

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Oxalic Acid

(10) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 8 ml of 3 M oxalic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

EXAMPLE 4

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Citric Acid

(11) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 8 ml of 12 M citric acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

COMPARATIVE EXAMPLE 1

Homogeneous Catalyst

(12) Potassium permanganate (KMnO.sub.4) manufactured by Junsei Co. (CAS No.: 7722-64-7, Lot No.: 2015C1513, Assay: min. 99.3%) was prepared.

COMPARATIVE EXAMPLE 2

Homogeneous Catalyst

(13) Manganese dioxide (MnO.sub.2) manufactured by Sigma-Aldrich Co. (CAS No.: 1313-13-9, 025-001-00-3 Lot No.: MKBS8414V, Assay: min. 99.99% (trace metal basis)) was prepared.

COMPARATIVE EXAMPLE 3

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Propionic Acid

(14) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 30 ml of 99% propionic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

COMPARATIVE EXAMPLE 4

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Butyric Acid

(15) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 40 ml of 99% butyric acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

(16) Hereinafter, the preferable embodiments of the present invention are described with the attached drawings. However, the embodiments of the present invention can be modified and altered in various ways and the present invention is not limited to the following illustration. It is well understood by those in the art who has the average knowledge on this field that the embodiments of the present invention are given to explain the present invention more precisely. Therefore, the shape and size of the elements in the drawings may be exaggerated for clarity of illustration and the elements indicated by the same mark in the drawings are the same elements. The factors showing similar function or activity are also indicated by the same mark in all the drawings. In addition, the inclusion of an element throughout the specification does not exclude other elements, but may include other elements, unless specifically stated otherwise.

(17) The present invention provides a solid-phase catalyst for decomposing hydrogen peroxide comprising a permanganate salt and a manganese (II) salt.

(18) Hereinafter, the solid-phase catalyst for decomposing hydrogen peroxide comprising a permanganate salt and a manganese (II) salt according to the present invention is described in more detail.

(19) Since the manganese-based catalyst, potassium permanganate (KMnO.sub.4), exists in a homogeneous form in an aqueous solution, it can induce a rapid decomposition reaction even in a low temperature region. However, after completion of the reaction, the catalyst component is uniformly dispersed in the aqueous solution, which is not easy to recover and may cause additional environmental problems. In the meantime, a solid-phase catalyst is generally precipitated in the aqueous solution after completion of the hydrogen peroxide decomposition with displaying layer separation, so that it can be recovered easily and can be reused. However, since the catalyst exists in a heterogeneous state in hydrogen peroxide, the decomposition reaction rate is slow.

(20) The solid-phase catalyst for decomposing hydrogen peroxide of the present invention has been improved to overcome the disadvantage of the homogeneous catalyst and the heterogeneous catalyst above. The solid-phase catalyst for decomposing hydrogen peroxide is produced by treating an organic acid, so that it can stay in the form of nanoparticles in hydrogen peroxide heterogeneously, indicating that the decomposition rate of hydrogen peroxide is accelerated and the recovery of the used catalyst is easy after completion of the decomposition reaction.

(21) The nanoparticle form can exist in the form of an aggregate of nanoparticles in which a permanganate salt and a manganese (II) salt are converted into manganese oxides.

(22) In the solid-phase catalyst for decomposing hydrogen peroxide comprising a permanganate salt and a manganese (II) salt according to the present invention, the permanganate salt is exemplified by potassium permanganate (KMnO.sub.4), zinc permanganate (Zn(MnO.sub.4).sub.2), calcium permanganate (CaMnO.sub.4), silver permanganate (AgMnO.sub.4), sodium permanganate (NaMnO.sub.4), barium permanganate (Br(MnO.sub.4).sub.2), magnesium permanganate (Mg(MnO.sub.4).sub.2), strontium permanganate (Sr(MnO.sub.4).sub.2), lithium permanganate (LiMnO.sub.4), cadmium permanganate (Cd(MnO.sub.4).sub.2), cesium permanganate (CsMnO.sub.4), and rubidium permanganate (RbMnO.sub.4), and is preferably potassium permanganate (KMnO.sub.4), but not always limited thereto.

(23) The manganese (II) salt herein is exemplified by manganese acetate, manganese nitrate, manganese chloride, manganese acetylacetonate, manganese bromide, manganese carbonate, manganese fluoride, manganese iodide and manganese sulfate, and is preferably manganese acetate, but not always limited thereto.

(24) In the course of the hydrogen peroxide decomposition using the solid-phase catalyst for decomposing hydrogen peroxide above, an exothermic reaction occurs in which water and oxygen gas are generated. The oxygen generation rate at this time is 8 L/min.Math.g22 L/min.Math.g, preferably 9 L/min.Math.g21 L/min.Math.g, and more preferably 10 L/min.Math.g20 L/min.Math.g.

(25) The present invention also provides a method for producing a solid-phase catalyst for decomposing hydrogen peroxide comprising the following steps:

(26) preparing an aqueous solution containing a permanganate salt, a manganese (II) salt and an organic acid (step 1);

(27) aging the aqueous solution of step 1 to form a solid-phase catalyst (step 2); and

(28) cleaning, drying and calcinating the solid-phase catalyst formed in step 2 (step 3).

(29) Hereinafter, the method for producing a solid-phase catalyst for decomposing hydrogen peroxide of the present invention is described in more detail step by step.

(30) First, in the method for producing a solid-phase catalyst for decomposing hydrogen peroxide of the present invention, step 1 is to prepare an aqueous solution comprising a permanganate salt, a manganese (II) salt and an organic acid.

(31) Step 1 is a pre-stage to form a solid-phase catalyst. In step 1, the permanganate and manganese (II) salts contained in the solid-phase catalyst are immersed in distilled water and mixed with the organic acid.

(32) The permanganate salt of step 1 is exemplified by potassium permanganate (KMnO.sub.4), zinc permanganate (Zn(MnO.sub.4).sub.2), calcium permanganate (CaMnO.sub.4), silver permanganate (AgMnO.sub.4), sodium permanganate (NaMnO.sub.4), barium permanganate (Br(MnO.sub.4).sub.2), magnesium permanganate (Mg(MnO.sub.4).sub.2), strontium permanganate (Sr(MnO.sub.4).sub.2), lithium permanganate (LiMnO.sub.4), cadmium permanganate (Cd(MnO.sub.4).sub.2), cesium permanganate (CsMnO.sub.4), and rubidium permanganate (RbMnO.sub.4), and is preferably potassium permanganate (KMnO.sub.4), but not always limited thereto.

(33) The manganese (II) salt of step 1 is exemplified by manganese acetate, manganese nitrate, manganese chloride, manganese acetylacetonate, manganese bromide, manganese carbonate, manganese fluoride, manganese iodide and manganese sulfate, and is preferably manganese acetate, but not always limited thereto.

(34) The organic acid of step 1 is selected from the group consisting of formic acid, acetic acid, oxalic acid and citric acid, but not always limited thereto.

(35) In the course of preparing the mixture of step 1, potassium permanganate (KMnO.sub.4) and manganese acetate can be used as the permanganate salt and the manganese (II) salt, and at this time the mixing weight ratio of potassium permanganate and manganese acetate is 1:11:5, preferably 1:21:4, and more preferably 1:2.81:3.6, but not always limited thereto.

(36) In addition, in the course of preparing the aqueous solution of step 1, the concentration of the organic acid is 50.0%99.9%, preferably 75.0%99.9%, and more preferably 90.0%99.9%, but not always limited thereto and any concentration range can be accepted as long as the condition facilitates the preparation of a catalyst that can stay as a solid state in hydrogen peroxide in the presence of the permanganate salt and the manganese (II) salt.

(37) Next, in the method for producing a solid-phase catalyst according to the present invention, step 2 is to form a solid-phase catalyst by aging the aqueous solution of step 1.

(38) In step 2, in order to form a catalyst staying in the form of a solid component during the catalytic reaction in hydrogen peroxide, the aqueous solution prepared in step 1 is aged.

(39) The aging treatment of step 2 is performed with the aqueous solution in a dark room at room temperature at normal pressure for 580 hours, preferably for 3575 hours, and more preferably for 6575 hours, but not always limited thereto.

(40) Next, in the method for producing a solid-phase catalyst according to the present invention, step 3 is to wash the solid-phase catalyst formed in step 2, followed by drying and calcinating thereof.

(41) In step 3, in order to produce the final solid-phase catalyst for decomposing hydrogen peroxide, the solid-phase catalyst formed in step 2 is recovered, washed, dried, and calcinated.

(42) The washing process in step 3 can be performed with distilled water, alcohol and acetone, but not always limited thereto.

(43) The drying process in step 3 can be performed at the temperature range between 50 C. and 110 C. at normal pressure or below.

(44) The calcinating process in step 3 can be performed in air or an inert gas atmosphere at 50350 C., preferably at 60330 C., and more preferably at 65300 C., but not always limited thereto.

(45) Further, the present invention provides an apparatus for the decomposition of hydrogen peroxide comprising the solid-phase catalyst for decomposing hydrogen peroxide.

(46) Hereinafter, the apparatus for the decomposition of hydrogen peroxide according to the present invention is described in more detail.

(47) The apparatus for the decomposition of hydrogen peroxide of the present invention contains a hydrogen peroxide storage tank; a reactor connected to the hydrogen peroxide storage tank and filled with the solid-phase catalyst for decomposing hydrogen peroxide; and an oxygen storage unit connected to the reactor and storing oxygen generated by the hydrogen peroxide decomposition reaction in the reactor.

(48) In the reactor of the apparatus for the decomposition of hydrogen peroxide of the present invention, the hydrogen peroxide introduced from the hydrogen peroxide storage tank is decomposed by the solid-phase catalyst for decomposing hydrogen peroxide charged in the reactor.

(49) At this time, the solid-phase catalyst for decomposing hydrogen peroxide can be recovered from water generated in the reactor after completion of the hydrogen peroxide decomposition reaction, and oxygen generated in the reaction can be stored in the oxygen storage unit.

(50) In addition, the present invention provides a method for the decomposition of hydrogen peroxide comprising the following steps:

(51) immersing the solid-phase catalyst for decomposing hydrogen peroxide in hydrogen peroxide to induce the decomposition of hydrogen peroxide into water and oxygen (step a); and

(52) recovering the solid-phase catalyst for decomposing hydrogen peroxide remaining after the catalytic reaction in step a (step b).

(53) Hereinafter, the method for the decomposition of hydrogen peroxide according to the present invention is described in more detail.

(54) First, in the method for the decomposition of hydrogen peroxide of the present invention, step a is to decompose hydrogen peroxide into water and oxygen by immersing the solid-phase catalyst for decomposing hydrogen peroxide in hydrogen peroxide.

(55) In step a, in order to decompose hydrogen peroxide into water and oxygen as shown in reaction formula 1 below, the said solid-phase catalyst is immersed in hydrogen peroxide.
2H.sub.2O.sub.2.fwdarw.2H.sub.2O+O.sub.2 <Reaction Formula 1>

(56) In step a, the concentration of hydrogen peroxide can be 5%50%, and the decomposition can be performed at a low temperature range between 1 C.50 C., but not always limited thereto.

(57) Next, in the method for the decomposition of hydrogen peroxide of the present invention, step b is to recover the used solid-phase catalyst for decomposing hydrogen peroxide remaining after the catalytic reaction of step a.

(58) In step b, the solid-phase catalyst for decomposing hydrogen peroxide remaining in water after the catalytic reaction can be recovered and reused.

(59) When the recovered solid-phase catalyst for decomposing hydrogen peroxide is reused, the catalyst still displays 70% to 90% of its original capacity.

(60) Practical and presently preferred embodiments of the present invention are illustrative as shown in the following Examples and Experimental Examples.

(61) However, it will be appreciated that those skilled in the art, on consideration of this disclosure, may make modifications and improvements within the spirit and scope of the present invention.

EXAMPLE 1

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Acetic Acid

(62) Step 1: 10 ml of 1 M potassium permanganate and 30 ml of 1 M manganese (II) acetate were dissolved in 20 ml of distilled water, to which 99% acetic acid was additionally added. Then the mixture was stirred at room temperature for 10 minutes.

(63) Step 2: The mixture prepared in step 1 was tightly sealed, followed by aging in a dark room at room temperature under normal pressure for 72 hours.

(64) Step 3: The solid-phase catalyst produced in the mixture of step 2 was recovered, which was then washed with 90 ml of ethanol and then dried in a 70 C. vacuum oven. Then, calcination was performed at 200 C., resulting in the preparation of a solid-phase catalyst for decomposing hydrogen peroxide.

EXAMPLE 2

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Formic Acid

(65) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 15 ml of 96% formic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

EXAMPLE 3

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Oxalic Acid

(66) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 8 ml of 3 M oxalic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

EXAMPLE 4

Preparation of a Solid-Phase Catalyst for Decomposing Hydrogen Peroxide Treated with Citric Acid

(67) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 8 ml of 12 M citric acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

COMPARATIVE EXAMPLE 1

Homogeneous Catalyst

(68) Potassium permanganate (KMnO.sub.4) manufactured by Junsei Co. (CAS No.: 7722-64-7, Lot No.: 2015C1513, Assay: min. 99.3%) was prepared.

COMPARATIVE EXAMPLE 2

Homogeneous Catalyst

(69) Manganese dioxide (MnO.sub.2) manufactured by Sigma-Aldrich Co. (CAS No.: 1313-13-9, 025-001-00-3 Lot No.: MKBS8414V, Assay: min. 99.99% (trace metal basis)) was prepared.

COMPARATIVE EXAMPLE 3

Preparation of a Solid-Phase Catalyst For Decomposing Hydrogen Peroxide Treated with Propionic Acid

(70) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 30 ml of 99% propionic acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

COMPARATIVE EXAMPLE 4

Preparation of a Solid-Phase Catalyst For Decomposing Hydrogen Peroxide Treated with Butyric Acid

(71) A solid-phase catalyst for decomposing hydrogen peroxide was prepared by the same manner as described in Example 1, except that 40 ml of 99% butyric acid was used instead of acetic acid as an organic acid in step 1 of Example 1.

EXPERIMENTAL EXAMPLE 1

Comparative Analysis of Crystallization

(72) To investigate the crystallization according to the type of the organic acid treated to the solid-phase catalyst for decomposing hydrogen peroxide, the solid-phase catalysts prepared in Examples 14, Comparative Example 3, and Comparative Example 4 were observed by the naked eye and the results are shown in Table 1 below.

(73) TABLE-US-00001 TABLE 1 Organic acids used in the catalyst Crystallization Example 1 Acetic acid Example 2 Formic acid Comparative Propionic acid X Example 3 Comparative Butyric acid X Example 4 Example 3 Oxalic acid Example 4 Citric acid

(74) As shown in Table 1, when propionic acid (Comparative Example 3) and butyric acid (Comparative Example 4) were used, a solid precipitate catalyst was not produced, while acetic acid, formic acid, oxalic acid and citric acid were used (Examples 14), a solid precipitate catalyst was generated.

EXPERIMENTAL EXAMPLE 2

Comparative Analysis of Oxygen Generation Rate

(75) To investigate the oxygen generation rate in the course of the decomposition of hydrogen peroxide by the solid-phase catalyst for decomposing hydrogen peroxide of the present invention, the catalysts of Example 1, Comparative Example 1 and Comparative Example 2 were immersed in 20 ml of 10% hydrogen peroxide at 2 C., followed by observation. The results are shown in Table 2 and FIG. 1.

(76) TABLE-US-00002 TABLE 2 Oxygen generation rate (L/min .Math. g) Example 1 15.4 Comparative Example 1 40.8 Comparative Example 2 0.7

(77) As shown in Table 2 and FIG. 1, the catalyst of Comparative Example 1, which is a potassium permanganate catalyst uniformly present in hydrogen peroxide, exhibited the highest oxygen generation rate of 40.8 L/min.Math.g, while the catalyst of Example 1 present in the form of solid distributed heterogeneously in hydrogen peroxide demonstrated the oxygen generation rate of 15.4 L/min.Math.g. The catalyst of Comparative Example 2 present in the form of solid distributed heterogeneously in hydrogen peroxide demonstrated the oxygen generation rate of 0.7 L/min.Math.g. Therefore, the solid-phase catalyst of Example 1 was confirmed to exhibit the most excellent oxygen generation rate.

(78) When the catalyst of Example 1 recovered after the decomposition of hydrogen peroxide was used, the oxygen generation rate was 12 L/min.Math.g, which was approximately 80% of the original catalyst capacity.

EXPERIMENTAL EXAMPLE 3

Analysis of Residual Solution after Decomposition of Hydrogen Peroxide

(79) To investigate the reactivity and pH of the residual solution remaining after the decomposition of hydrogen peroxide by using the solid-phase catalyst for decomposing hydrogen peroxide of the present invention, hydrogen peroxide was decomposed using the catalysts of Example 1, Comparative Example 1 and Comparative Example 2 and then pH of the residual solution was measured. Then, the residual solution was reacted with hydrogen peroxide. The results are shown in FIG. 2 and Table 3.

(80) TABLE-US-00003 TABLE 3 pH Reactivity to hydrogen (supernatant) peroxide (supernatant) Example 1 7 X Comparative 9 Example 1 Comparative 7 X Example 2

(81) As shown in Table 3 and FIG. 2, the catalyst of Comparative Example 1, which is a potassium permanganate catalyst uniformly present in hydrogen peroxide, showed basicity of pH 9 due to KOH generated by the hydrogen peroxide decomposition reaction. In the meantime, the catalyst of Example 1 present in the form of solid distributed heterogeneously in hydrogen peroxide showed pH 7 which is the same pH as pH of distilled water. Also, the catalyst of Comparative Example 2 present in the form of solid distributed heterogeneously in hydrogen peroxide showed pH 7.

(82) When hydrogen peroxide was additionally added to the residual solution containing the catalyst of Comparative Example 1, reaction was induced and the remaining catalyst component was confirmed. When hydrogen peroxide was additionally added to the residual solution containing the catalyst of Example 1 or Comparative Example 2 in which layer separation occurred, no additional reaction was induced.

(83) The hydrogen peroxide decomposition performance of the solid-phase catalyst for decomposing hydrogen peroxide of the present invention and the residual form after the hydrogen peroxide decomposition reaction were confirmed. Compared with the conventional solid-phase catalyst manganese dioxide, the hydrogen peroxide decomposition rate of the catalyst of the invention was significantly higher. In addition, the catalyst of the invention has an advantage of easy recovery after the decomposition reaction since it can stay as a solid phase.

INDUSTRIAL APPLICABILITY

(84) The present invention provides a solid-phase catalyst for decomposing hydrogen peroxide comprising a permanganate salt and a manganese (II) salt. The solid-phase catalyst stays a solid state in the form of nanoparticles at the time of hydrogen peroxide decomposition, and thus can be recovered for reuse and also has an excellent decomposition rate. In the method for producing a solid-phase catalyst for decomposing hydrogen peroxide according to the present invention, a solid-phase catalyst is produced from a solution containing a permanganate salt, a manganese (II) salt, and an organic acid, so that the produced solid-phase catalyst is precipitated as a solid component even after a catalytic reaction, and thus is reusable and environmentally friendly, and cost reduction can be achieved through the simplification of a catalyst production technique.