KR20060093086A - Catalyst and device for air cleaning - Google Patents

Catalyst and device for air cleaning Download PDF

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KR20060093086A
KR20060093086A KR1020060068916A KR20060068916A KR20060093086A KR 20060093086 A KR20060093086 A KR 20060093086A KR 1020060068916 A KR1020060068916 A KR 1020060068916A KR 20060068916 A KR20060068916 A KR 20060068916A KR 20060093086 A KR20060093086 A KR 20060093086A
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metal
catalyst
air
chloride
composite catalyst
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김문찬
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/88Handling or mounting catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86Catalytic processes
    • B01D53/8678Removing components of undefined structure
    • B01D53/8687Organic components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/10Noble metals or compounds thereof
    • B01D2255/102Platinum group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/207Transition metals
    • B01D2255/20707Titanium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

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Abstract

본 발명은 공기중의 산소와 수산화라디칼의 존재하에서 빛 에너지가 없어도 휘발성유기화합물과 포름알데히드등의 대기오염물질을 제거하는 특징을 가지는 이산화티탄을 복합 형태로 만든 촉매 및 이것을 사용한 공기정화 장치에 관한 것이다. 상기의 목적을 달성하기 위한 본 발명은 티타늄과 인 복합물질에, 마그네슘, 게르마늄중 하나이상의 금속과의 복합 촉매를 제조하여 빛이 없는 곳에서도 유기물 산화효과가 뛰어난 장점을 가지고 있다.The present invention relates to a catalyst made of a composite form of titanium dioxide having a characteristic of removing volatile organic compounds and air pollutants such as formaldehyde even in the presence of oxygen in the air and radicals of hydroxide, and an air purifier using the same. will be. The present invention for achieving the above object has the advantage of excellent oxidation effect of organic matter even in the absence of light by producing a composite catalyst of at least one metal of magnesium and germanium in the titanium and phosphorus composite material.

촉매, 공기정화, 활성탄 필터 Catalyst, Air Purification, Activated Carbon Filter

Description

공기정화용 촉매 및 장치{Catalyst and Device for Air Cleaning}Catalyst and Device for Air Purification {Catalyst and Device for Air Cleaning}

도 1은 가시광 촉매가 코팅된 부직포필터 또는 헤파필터, 가시광 촉매가 코팅된 입상활성탄필터 또는 섬유상활성탄필터, 흡입팬으로 구성된 공기정화장치를 나타낸 도1 is a non-woven filter or hepa filter coated with a visible light catalyst, a granular activated carbon filter or a fibrous activated carbon filter coated with a visible light catalyst, and an air purifying apparatus including a suction fan.

(도면의 주요부분에 대한 설명)(Explanation of main parts of drawing)

A : 오염된 공기A: contaminated air

B : 부직포필터 또는 헤파필터B: Nonwoven Filter or Hepa Filter

C : 입상 활성탄 필터, 또는 섬유상 활성탄 필터C: granular activated carbon filter, or fibrous activated carbon filter

D : 흡입팬D: suction fan

E : 깨끗한 공기E: clean air

본 발명은 산화티탄을 응용한 공기정화 촉매에 관한 것으로, 종래의 기술은 광촉매로 이산화티탄을 사용하고 용매로 물과 알콜류를 사용하여 자외선을 조사받아 광촉매 작용을 일으키게 하여왔다. 그러나 빛이 없는 곳에서는 전혀 광촉매효과를 나타내지 못하여 아직은 기술적으로 한계에 도달한 상태이다. 그리고 기존에는 광촉매 또는 가시광촉매를 사용하여 공기정화를 하였으나 오존발생과 빛에너지에 의한 온도 상승으로 공기를 정화하는데 많은 에너지와 부산물이 발생하였다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air purification catalyst using titanium oxide, and the related art uses titanium dioxide as a photocatalyst and water and alcohols as a solvent to irradiate ultraviolet rays to cause a photocatalytic action. However, in the absence of light, the photocatalytic effect has not been shown at all, and the technical limit is still reached. In the past, air purification was performed using photocatalysts or visible photocatalysts, but a lot of energy and by-products were generated to purify the air due to ozone generation and temperature rise due to light energy.

본 발명에서는 종래의 기술에 나타난 단점들을 제거하여, 빛이 없는 곳에서도 촉매 효과를 발현시켜, 공기중에 섞여있는 유해물질인 휘발성유기화합물과 포름알데히드등을 제거하는 공기정화 촉매 및 공기정화 장치를 제공하는데 있다.In the present invention, by removing the disadvantages shown in the prior art, by expressing the catalytic effect even in the absence of light, it provides an air purification catalyst and air purification apparatus to remove volatile organic compounds and formaldehyde, such as harmful substances mixed in the air It is.

본 발명에 사용되는 공기정화 촉매는 Ti 금속으로써 TiO2 분말에 인으로써 암모늄포스페이트 또는 인산을 함침시키고, 여기에 마그네슘 금속으로써 염화마그네슘이나 수산화마그네슘, 게르마늄 금속으로써 염화게르마늄이나 산화게르마늄중에서 1개 이상의 금속을 함침시켜 110℃에서 6시간 이상 건조시킨후 300℃ ∼ 500℃ 사이에서 2시간 이상 소성하여 Ti-P-M 복합 촉매를 만든다.여기서 M은 금속을 나타내며 Pt, Pd, Au중 하나 이상의 금속이다.The air purification catalyst used in the present invention is impregnated with ammonium phosphate or phosphoric acid by phosphorus in TiO 2 powder as Ti metal, and at least one metal in magnesium chloride or magnesium hydroxide as germanium metal or germanium chloride or germanium oxide as germanium metal. Impregnated and dried at 110 ° C. for at least 6 hours and then calcined at 300 ° C. to 500 ° C. for at least 2 hours to form a Ti-PM composite catalyst, wherein M represents a metal and is at least one of Pt, Pd and Au.

한편, 공기정화 촉매인 Ti-P-M 복합 촉매를 만들기 위하여 다른 방법으로는, Ti 금속으로써 TiCl4 또는 티타늄테트라이소프로폭사이드와 인으로써 암모늄포스페이트 또는 인산을 혼합하고, 여기에 마그네슘 금속으로써 염화마그네슘이나 수산화마그네슘, 게르마늄 금속으로써 염화게르마늄 중에서 1개 이상의 금속 화합물을 혼합하여 질산이나 황산 또는 염산 수용액상에서 60℃ ∼ 150℃에서 60rpm 이상으로 3시간 이상 교반하면서 졸겔법으로 제조하여 Ti-P-M 복합 촉매를 만든다. 여기서 M 은 금속을 나타내며 Pt, Pd, Au 중 하나 이상의 금속이다. Ti-P-M 복합 촉매에 사용된 물질의 비율은 Ti + P : M = 100 : 1에서 1 : 1 의 무게비로 혼합하여 사용하며, Ti : P = 10 : 1에서 1:10의 무게비로 혼합하여 사용한다. 상기의 물질들간의 무게비를 벗어나게 되면 촉매에서 촉매효과가 떨어져 공기정화 효과가 현저히 떨어진다.On the other hand, in order to make the Ti-PM composite catalyst as an air purification catalyst, another method is to mix TiCl 4 or titanium tetraisopropoxide as Ti metal and ammonium phosphate or phosphoric acid as phosphorus, and magnesium chloride or magnesium chloride as magnesium metal One or more metal compounds are mixed in germanium chloride as magnesium hydroxide and germanium metal and prepared by sol-gel method while stirring at 60 rpm or more at 60 ° C. to 150 ° C. for at least 3 hours in an aqueous solution of nitric acid or sulfuric acid or hydrochloric acid to form a Ti-PM composite catalyst. . Where M represents a metal and is at least one of Pt, Pd, Au. The ratio of the materials used in the Ti-PM composite catalyst is mixed by the weight ratio of Ti + P: M = 100: 1 to 1: 1, and mixed by the weight ratio of Ti: P = 10: 1 to 1:10. do. If the weight ratio between the above materials is out of the catalytic effect in the catalyst is lowered air purification effect is significantly reduced.

본 발명에 의한 장치는 오염된 도 1에서와 같이 오염된 공기(A)가 부직포필터 또는 헤파필터(B)를 통과하면서 분진이 제거되고, Ti-P-M 복합 촉매를 코팅한 입상 활성탄필터 또는 섬유상 활성탄 필터층(C)를 통과한후, 흡입팬(D)을 통과하여 미세분진이 제거되고, 휘발성유기화합물과 포름알데히드는 이산화탄소와 물로 바뀌며, 바이러스와 박테리아가 살균되어 깨끗한 공기(E)로 변하게 된다. 본 발명에 의한 장치는 공기청정기나 공기정화 공조시스템등에 사용될수 있으며, 이것을 응용한 공기정화 분야에 널리 사용될수 있다.In the apparatus according to the present invention, as the contaminated air (A) passes through the nonwoven fabric filter or the hepa filter (B), the dust is removed, and the granular activated carbon filter or the fibrous activated carbon coated with the Ti-PM composite catalyst as shown in FIG. After passing through the filter layer (C), the fine dust is removed by passing through the suction fan (D), volatile organic compounds and formaldehyde is converted to carbon dioxide and water, viruses and bacteria are sterilized and turned into clean air (E). The apparatus according to the present invention can be used in an air purifier or an air purifying air conditioning system and the like, and can be widely used in the field of air purification applying this.

다음의 실시예에 의하여 본 발명을 더 상세히 설명하는데 본 발명은 이들 실시예에만 한정되는 것은 아니다.The present invention is explained in more detail by the following examples, which are not intended to limit the present invention.

실시예1 에서 실시예4 까지와 비교예 1에서 4까지는 촉매 금속의 조합별로 본 발명의 장치를 사용하여 휘발성유기화합물로써 톨루엔과 포름알데히드, 살균력 성능으로 포도상구균의 제거 성능을 나타내었다.Examples 1 to 4 and Comparative Examples 1 to 4 showed the ability to remove Staphylococcus aureus by toluene, formaldehyde, and bactericidal activity as a volatile organic compound using a device of the present invention for each combination of catalyst metals.

표1은 본 발명의 장치를 사용하여, 가시광촉매의 구성성분과 휘발성유기화합물로써 톨루엔과 포름알데히드의 제거율과 살균력 성능으로 포도상구균의 제거율 및 분진의 제거율을 나타내었다. 공간속도는 50,000/hr 이었으며, 광원이 없는 암 실에서 사용하였고, 분진의 초기농도는 80㎍/㎥, 톨루엔의 초기농도는 100ppm, 포름알데히드는 초기농도를 50ppm으로 하였으며 2시간동안 본 발명의 공기정화기를 통과시킨후 제거율을 측정하였으며, 포도상구균은 본 발명의 장치를 통과한 공기를 24시간 동안 배양후 측정하였으며, KSM0146-2003의 Shake Flask Method 방법으로 시험하였다.Table 1 shows the removal rate of staphylococci and the dust removal rate of toluene and formaldehyde as a constituent and volatile organic compound of visible photocatalyst, and bactericidal performance. The space velocity was 50,000 / hr, and was used in a dark room without a light source. The initial concentration of dust was 80 µg / m 3, the initial concentration of toluene was 100 ppm, the formaldehyde was 50 ppm, and the air of the present invention was maintained for 2 hours. The removal rate was measured after passing through the clarifier. Staphylococcus was measured after incubation for 24 hours in the air passing through the apparatus of the present invention, was tested by the Shake Flask Method method of KSM0146-2003.

실시예 1)Example 1

Ti-P-M 복합촉매 성분이 Ti 금속으로써 TiO2 분말 10g에 인으로써 암모늄포스페이트 3g과 여기에 M 금속은 백금이며, 백금 금속으로써 염화백금 3g을 함침시켜 110℃에서 6시간 이상 건조시킨후 400℃ 에서 2시간동안 소성하여 Ti-P-Pt 복합 촉매를 만들고, 이것을 헤파필터층(B)와 입상활성탄 필터층(C)에 모두 코팅하였다. 본 발명에 사용되는 공기정화기는 도 1에 나타난것과 동일하며, 오염된 공기(A)로써 분진 80㎍/㎥, 톨루엔 100ppm, 포름알데히드 50ppm이 함유된 공기를 Ti-P-Pt 복합 촉매가 코팅된 헤파필터층(B)와 입상 활성탄필터층(C)를 차례로 통과한후,흡입팬(D)를 통과시켜, 포름알데히드와 톨루엔, 분진, 포도상구균의 제거율을 측정하였다.The Ti-PM composite catalyst component is Ti metal and 10 g of TiO 2 powder, so that 3 g of ammonium phosphate and M metal is platinum, and 3 g of platinum chloride is impregnated with platinum metal and dried at 110 ° C. for at least 6 hours, and then at 400 ° C. Firing for 2 hours to form a Ti-P-Pt composite catalyst, it was coated on both the HEPA filter layer (B) and granular activated carbon filter layer (C). The air purifier used in the present invention is the same as that shown in Figure 1, the air containing the contaminated air (A) dust containing 80㎛ / ㎥, 100ppm toluene, 50ppm formaldehyde Ti-P-Pt composite catalyst After passing through the HEPA filter layer (B) and the granular activated carbon filter layer (C) in turn, and passing through the suction fan (D), the removal rate of formaldehyde, toluene, dust, staphylococcus was measured.

이때, 오염된 공기의 유속은 공간속도를 50,000/hr 으로 하였으며, 암실에서 실험을 하였다.At this time, the flow rate of the contaminated air was a space velocity of 50,000 / hr, and the experiment in the dark room.

실시예 2)Example 2)

Ti-P-M 복합촉매 성분이 Ti 금속으로써 티타늄테트라이소프로폭사이드 10g과 인으로써 암모늄포스페이트 3g, M 금속은 백금이며, 백금 금속으로써 염화백금 3g을 혼합하여 질산 수용액상에서 90℃에서 60rpm 이상으로 3시간 동안 교반하면서 졸겔법으로 제조하여 Ti-P-Pt 복합 촉매를 만들고, 이것을 헤파필터층(B)와 입상활성탄 필터층(C)에 모두 코팅한것 외에는 실시예 1과 동일함The Ti-PM composite catalyst contains 10 g of titanium tetraisopropoxide as a Ti metal, 3 g of ammonium phosphate as phosphorus, and 3 g of M metal as platinum, and 3 g of platinum chloride as a platinum metal. It was prepared in the sol-gel method with stirring for a Ti-P-Pt composite catalyst, and the same as in Example 1 except that it was coated on both the HEPA filter layer (B) and the granular activated carbon filter layer (C).

실시예 3)Example 3

Ti-P-M 복합 촉매에서 M 금속 성분으로 Pt 대신 Pd 이며, Pd 금속으로써 염화팔라듐 3g을 사용한것 외에는 실시예1과 동일함In Ti-P-M composite catalyst, it is the same as that of Example 1 except for using Pd instead of Pt as M metal component and 3g of palladium chloride as Pd metal.

실시예 4)Example 4

Ti-P-M 복합 촉매에서 M 금속 성분으로 Pt 대신 Au 이며, Au 금속으로써 염화금 3g을 사용한것 외에는 실시예1과 동일함In Ti-P-M composite catalyst, it is Au instead of Pt as the M metal component, and is the same as Example 1 except that 3g of gold chloride is used as Au metal.

비교예 1)Comparative Example 1)

Ti-P 복합 촉매 성분이 Ti 금속으로써 TiO2 분말 10g에 인으로써 암모늄포스페이트 3g을 함침시켜 110℃에서 6시간 이상 건조시킨후 400℃ 에서 2시간동안 소성하여 Ti-P 복합 촉매를 만들고, 이것을 헤파필터층(B)와 입상활성탄 필터층(C)에 모두 코팅한것 외에는 실시예 1과 동일함.The Ti-P composite catalyst component was impregnated with 10 g of TiO 2 powder as Ti metal, impregnated with 3 g of ammonium phosphate, dried at 110 ° C. for at least 6 hours, and then calcined at 400 ° C. for 2 hours to form a Ti-P composite catalyst. The same as in Example 1 except that both the filter layer (B) and the granular activated carbon filter layer (C) were coated.

비교예 2)Comparative Example 2)

Ti-Pt 복합 촉매 성분이 Ti 금속으로써 TiO2 분말 10g에 백금 금속으로써 염화백금 3g을 함침시켜 110℃에서 6시간 이상 건조시킨후 400℃ 에서 2시간동안 소성하여 Ti-Pt 복합 촉매를 만들고, 이것을 헤파필터층(B)와 입상활성탄 필터층(C) 에 모두 코팅한것 외에는 실시예 1과 동일함.The Ti-Pt composite catalyst component was impregnated with 10 g of TiO 2 powder as Ti metal and 3 g of platinum chloride as platinum metal, dried at 110 ° C. for at least 6 hours, and calcined at 400 ° C. for 2 hours to form a Ti-Pt composite catalyst. The same as in Example 1 except that both the HEPA filter layer (B) and the granular activated carbon filter layer (C) were coated.

비교예 3)Comparative Example 3)

Ti-Pd 복합 촉매 성분이 Ti 금속으로써 티타늄테트라이소프로폭사이드 10g과 팔라듐 금속으로써 염화팔라듐 3g을 혼합하여 질산 수용액상에서 90℃에서 60rpm 이상으로 3시간 동안 교반하면서 졸겔법으로 제조하여 Ti-Pd 복합 촉매를 만들고, 이것을 헤파필터층(B)와 입상활성탄 필터층(C)에 모두 코팅한것 외에는 실시예 1과 동일함.The Ti-Pd composite catalyst component was prepared by the sol-gel method by mixing 10 g of titanium tetraisopropoxide as a Ti metal and 3 g of palladium chloride as a palladium metal and stirring at 90 ° C. or higher at 60 ° C. for 3 hours in an aqueous solution of nitric acid. A catalyst was prepared and coated in both the HEPA filter layer (B) and the granular activated carbon filter layer (C).

비교예 4)Comparative Example 4)

인 성분으로 암모늄포스페이트 10g에 Pt 금속으로써 염화백금 3g을 혼합하여 질산 수용액상에서 90℃에서 60rpm 이상으로 3시간 동안 교반하면서 P-Pt 촉매를 졸겔법으로 제조하여, 이것을 헤파필터층(B)와 입상활성탄 필터층(C)에 모두 코팅한것 외에는 실시예 1과 동일함.P-Pt catalyst was prepared by the sol-gel method by mixing 3 g of platinum chloride as a Pt metal with 10 g of ammonium phosphate as a phosphorus and stirring for 3 hours at 90 ° C. or more at 90 ° C. in a nitric acid solution. The same as in Example 1 except that all the coating on the filter layer (C).

표1. 가시광촉매의 구성성분과 톨루엔과 포름알데히드의 제거율과 분진 및 포도상구균의 제거율Table 1. Removal of Toluene and Formaldehyde and Removal of Dust and Staphylococcus

Figure 112006505851688-PAT00001
Figure 112006505851688-PAT00001

이상에서 상세히 설명한 바와 같이, 본 발명에 사용된 공기정화 촉매는 빛이 없는 곳에서도 유기물 산화 효과가 우수하며, 휘발성유기화합물이나 유기물을 빛이 없는 상온에서 산화시키는데 우수한 효과를 제공한다. 그리고 본 발명에 의한 장치로 후발성유기화합물 제거 및 살균력이 우수하여 공기정화능력이 탁월한 효과를 제공한다.As described in detail above, the air purification catalyst used in the present invention is excellent in the oxidation of organic matter even in the absence of light, and provides an excellent effect of oxidizing volatile organic compounds or organic matter at room temperature without light. And the device according to the present invention is excellent in the removal and sterilization of late-end organic compound provides an excellent air purification ability.

Claims (5)

Ti-P-M 복합 촉매로, 여기서 M은 금속을 나타내며 Pt, Pd, Au중 하나 이상의 금속인 것을 특징으로 하는 공기정화 촉매Ti-P-M composite catalyst, wherein M represents a metal and is an air purification catalyst characterized in that it is at least one metal of Pt, Pd, Au 제 1항에 있어서 Ti-P-M 복합 촉매에 사용된 물질의 비율은 Ti + P : M = 100 : 1에서 1 : 1 의 무게비로 혼합하여 사용하며, Ti : P = 10 : 1에서 1:10의 무게비로 혼합하여 사용하는 것을 특징으로 하는 공기정화 촉매The ratio of materials used in the Ti-PM composite catalyst of claim 1 is used by mixing in a weight ratio of Ti + P: M = 100: 1 to 1: 1, Ti: P = 10: 1 to 1:10 Air purification catalyst, characterized in that used by mixing in weight ratio Ti 금속으로써 TiO2 분말에 인 성분으로써 암모늄포스페이트 또는 인산을 함침시키고, 여기에 Pt 금속으로써 염화백금, 팔라듐 금속으로써 염화팔라듐, 금으로써 염화금 중에서 1개 이상의 금속을 함침시켜 110℃에서 6시간 이상 건조시킨후 300℃ ∼ 500℃ 사이에서 2시간 이상 소성하여 복합 촉매를 만드는 것을 특징으로 하는 공기정화 촉매 제조방법TiO 2 powder as Ti metal is impregnated with ammonium phosphate or phosphoric acid as phosphorus component, impregnated with at least one metal in platinum chloride as Pt metal, palladium chloride as palladium metal, gold as gold chloride and dried at 110 ° C for at least 6 hours. Method for producing an air purification catalyst characterized in that the composite catalyst is made by baking for 2 hours or more between 300 ℃ to 500 ℃ after Ti 금속으로써 TiCl4 또는 티타늄테트라이소프로폭사이드와 인 성분으로써 암모늄포스페이트 또는 인산을 혼합하고, 여기에 Pt 금속으로써 염화백금, 팔라듐 금속으로써 염화팔라듐, 금으로써 염화금 중에서 1개 이상의 금속을 혼합하여 질산이나 황산 또는 염산 수용액상에서 60℃ ∼ 150℃에서 60rpm 이상으로 3시간 이상 교반하면서 졸겔법으로 제조하는 것을 특징으로 하는 공기정화 촉매 제조방법TiCl 4 or titanium tetraisopropoxide as the Ti metal and ammonium phosphate or phosphoric acid as the phosphorus component are mixed, and one or more metals are mixed with platinum chloride as the Pt metal, palladium chloride as the palladium metal and gold chloride as the gold. A method for preparing an air purifying catalyst, characterized in that the sol-gel method is prepared by stirring at 60 rpm or more at 60 rpm in an aqueous solution of sulfuric acid or hydrochloric acid for at least 3 hours. 오염된 공기가 Ti-P-M 복합 촉매가 코팅된 부직포 필터 또는 헤파필터와 입상 활성탄필터 또는 섬유상 활성탄 필터층을 차례로 통과한후, 분진이 제거되고 휘발성유기화합물과 포름알데히드가 이산화탄소와 물로 바뀌며, 바이러스와 박테리아가 살균되어 깨끗한 공기로 바뀌는 것을 특징으로 하는 공기정화 장치로, 여기서 M은 금속을 나타내며 Pt, Pd, Au중 하나 이상의 금속인 것을 특징으로 한다.The contaminated air passes through the nonwoven filter or hepa filter coated with Ti-PM composite catalyst, and then the granular activated carbon filter or fibrous activated carbon filter layer, and then the dust is removed and the volatile organic compounds and formaldehyde are converted into carbon dioxide and water. Is a sterilized and changed to clean air, wherein M represents a metal and is characterized in that at least one metal of Pt, Pd, Au.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110508133A (en) * 2019-09-26 2019-11-29 崔小勤 Desulfurizing industrial fume denitration, dust removal integrated system and its process
CN115011109A (en) * 2022-07-26 2022-09-06 王卡 Antibacterial platinum photocatalyst negative ion activated carbon filter cotton and preparation method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110508133A (en) * 2019-09-26 2019-11-29 崔小勤 Desulfurizing industrial fume denitration, dust removal integrated system and its process
CN115011109A (en) * 2022-07-26 2022-09-06 王卡 Antibacterial platinum photocatalyst negative ion activated carbon filter cotton and preparation method thereof
CN115011109B (en) * 2022-07-26 2023-11-14 王卡 Preparation method of antibacterial platinum photocatalyst anion activated carbon filter cotton

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