KR20010018330A - Fabrication of catalyst for removal of dioxin - Google Patents

Fabrication of catalyst for removal of dioxin Download PDF

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Publication number
KR20010018330A
KR20010018330A KR1019990034240A KR19990034240A KR20010018330A KR 20010018330 A KR20010018330 A KR 20010018330A KR 1019990034240 A KR1019990034240 A KR 1019990034240A KR 19990034240 A KR19990034240 A KR 19990034240A KR 20010018330 A KR20010018330 A KR 20010018330A
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South Korea
Prior art keywords
catalyst
dioxin
removal
carrier
reagent
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KR1019990034240A
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Korean (ko)
Inventor
정태섭
이민호
김경수
김종국
윤동주
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정태섭
주식회사 하이엔텍
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Priority to KR1019990034240A priority Critical patent/KR20010018330A/en
Publication of KR20010018330A publication Critical patent/KR20010018330A/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/28Molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0201Impregnation
    • B01J37/0213Preparation of the impregnating solution
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08Heat treatment

Abstract

PURPOSE: Disclosed is a preparation method of catalyst for removing dioxin. The used catalyst is composed of molybdenum and vanadium species and these ingredients are coated on the surface of honeycomb substrate. CONSTITUTION: V2O5 and (MH4)6Mo7O24·4H2O are dissolved with respective proper ratios to get a slurry solution. And then the prepared compound is coated on the surface of honeycomb monolith and calcined at 400-500deg.C for 5 hours.

Description

다이옥신 제거용 촉매 제조{Fabrication of catalyst for removal of dioxin}Fabrication of catalyst for dioxin removal {Fabrication of catalyst for removal of dioxin}

본 발명은 다이옥신(dioxin) 제거용 Mo-V계 촉매를 제조하는 방법에 관한 것으로 기존의 Al2O3, SiO2및 MgO로 구성된 하니컴(honey comb)을 이용하여 Mo 및 V을 피복시켜 다이옥신 제거용 촉매를 제조하는 방법에 관한 것이다.The present invention relates to a method for preparing a Mo-V-based catalyst for dioxin removal, and removes dioxin by coating Mo and V using a honey comb composed of Al 2 O 3 , SiO 2, and MgO. It relates to a method for producing a catalyst for.

일반적으로 소각장에서 발생되는 다이옥신 처리는 연소 process, 집진 process, 처리 process로 나누며, 연소실에서 연소분위기 조성 즉, 850℃이상 체류시간 2초 이상으로 유지하여 폐기물에 포함가능성이 있는 다이옥신을 안정적으로 분해하고 다이옥신 재생성을 방지하기 위해 200℃로 냉각하고 그래도 생성된 다이옥신은 반건식 세정장치를 통과하여 lime과 활성탄에 의해 흡착제거한다. 다이옥신 제거 방법으로는 촉매분해, 광분해, 소각 열분해, 오존분해, 화학적 분해, 물리화학적 분해, 생물학적인 분해 방법 등이 있다.In general, dioxin treatment generated in incinerator is divided into combustion process, dust collection process, and treatment process.The composition of the combustion atmosphere in the combustion chamber, that is, the retention time of more than 850 ℃ and the retention time of 2 seconds or more, stably decomposes dioxin that may be included in the waste. In order to prevent dioxin regeneration, it is cooled to 200 ° C. and the dioxin produced is still adsorbed and removed by lime and activated carbon through a semi-dry cleaning device. Dioxin removal methods include catalytic decomposition, photolysis, incineration pyrolysis, ozone decomposition, chemical decomposition, physicochemical decomposition, and biological decomposition.

촉매를 이용한 다이옥신 분해방법은 다이옥신을 함유한 가스와 공기를 촉매층에 흘러보내 산화분해시켜 다이옥신을 제거하는 방법이다. 촉매로는 금속산화물(V2O5, TiO2, WO3등) 및 귀금속(Pt, Pd)이 사용되어 있으며 분해효율을 높이기 위해 Pt, Pd 등을 TiO2나 SiO2등에 담지시켜 사용하기도 한다. 광분해는 빛을 이용하여 화학결합을 파괴시키는 방법으로 특정파장의 빛을 조사하면 빛 에너지에 의해 화학물질이 분해된다. 다이옥신 광분해는 자외선 파장이 가장 효과적으로 알려져 있다. 이는 실제 어느정도나 분해되는가를 추정하기가 어렵다. 비산재 중의 다이옥신 분해방법으로는 소각과 열분해 방법이 있다. 소각법은 고온에서의 산화분해 반응을 이용하기 때문에 비산재와 공기를 충분히 접촉시켜야 하므로 비산재는 유기물 함량이 낮아서 발열량이 적기 때문에 보조연료를 사용해야 할 필요성이 있다. 또한 완전연소를 위해서는 연소실 내의 온도분포, 산소농도, 체류시간 등을 적절히 제어해야한다. 화학적 분해 및 물리화학적 분해방법은 열과 압력을 이용하여 다이옥신을 분해시키는 방법으로 초임계유체를 이용한 수중의 다이옥신 분해방법으로 초임계계수와 산소를 완전히 혼합하면 유기물의 산화속도가 커지며, 유기염소계 용제의 산화분해처리가 검토되고 있는 실정이다.Dioxin decomposition using a catalyst is a method of removing dioxins by oxidatively decomposing gas and air containing dioxins through a catalyst layer. Metal oxides (V 2 O 5 , TiO 2 , WO 3, etc.) and precious metals (Pt, Pd) are used as catalysts, and Pt, Pd, etc. may be supported by TiO 2 , SiO 2, etc. to increase decomposition efficiency. . Photolysis is a method of breaking chemical bonds using light. When light of a specific wavelength is irradiated, chemicals are decomposed by light energy. Dioxin photolysis is most effectively known as the ultraviolet wavelength. It is difficult to estimate how much it actually decomposes. Dioxin decomposition methods in fly ash include incineration and pyrolysis methods. Since incineration requires oxidative decomposition at high temperatures, the fly ash must be sufficiently in contact with the air, so the fly ash has a low organic matter content and thus generates a low calorific value. Therefore, it is necessary to use auxiliary fuel. In addition, for complete combustion, it is necessary to properly control the temperature distribution, oxygen concentration, and residence time in the combustion chamber. Chemical decomposition and physicochemical decomposition methods are used to decompose dioxins using heat and pressure. Dioxins in water using supercritical fluids are completely mixed with supercritical water and oxygen, and the oxidation rate of organic compounds increases. Oxidative decomposition treatment is under consideration.

이러한 다이옥신 제거방법 중 촉매를 이용한 제거는 제거효율을 높이기 위한 촉매의 개발이 우선과제이다.Among the dioxins removal methods, the removal of the catalysts is a priority for developing catalysts to increase the removal efficiency.

본 발명은 상기의 방법 중에서 촉매를 이용하여 다이옥신을 분해시키기 위한 다이옥신(dioxin) 제거용 Mo-V계 촉매를 제조하는 방법에 관한 것으로 도시 쓰레기소각로에서 다이옥신류의 생성과 대기로의 방출을 최소화하기 위해 기존의 Al2O3, SiO2및 MgO로 구성된 하니컴(honey comb)을 이용하여 Mo 및 V을 피복시켜 다이옥신 제거용 촉매를 제조하는 방법에 관한 것으로 다이옥신의 제거 효율을 높이기 위한 것이다.The present invention relates to a method for producing a dioxin-removing Mo-V-based catalyst for decomposing dioxins using the catalyst among the above methods, to minimize the production of dioxins and emission to the atmosphere in urban waste incinerators. In order to improve the removal efficiency of dioxin, the present invention relates to a method for preparing a catalyst for dioxin removal by coating Mo and V using honeycomb composed of conventional Al 2 O 3 , SiO 2, and MgO.

촉매를 이용한 다이옥신 분해방법은 다이옥신을 함유한 가스와 공기를 촉매층에 흘러보내 산화분해시켜 다이옥신을 제거하는 방법이다.Dioxin decomposition using a catalyst is a method of removing dioxins by oxidatively decomposing gas and air containing dioxins through a catalyst layer.

이 발명은 위의 기술적 과제를 해결하기 위해 Al2O3, SiO2및 MgO로 구성된 하니컴(honey comb)을 이용하여 촉매를 제조하고자 오산화 바나듐(V2O5)과 몰리브덴산암모늄((NH4)6Mo7O24·4H2O)를 적정 비율로 혼합 용해하여 담체 함침용 시약을 제조하는 단계, 상기 시약을 온욕상에서 하니컴(honey comb)담체를 함침시키고 서서히 교반하면서 증발 건조시켜 용해된 시약을 충분히 담체에 흡수시키는 단계, 상기의 건조된 담체를 100℃/1hr의 승온속도로 400∼500℃에서 5시간 유지하면서 소성시켜 촉매를 제조 단계로 이루어진 것이 특징이 있다. 이러한 촉매를 이용한 다이옥신 제거는 높은 효율성을 가지고 있다.The present invention is to solve the above technical problem to prepare a catalyst using a honey comb consisting of Al 2 O 3 , SiO 2 and MgO (vanadium pentoxide (V 2 O 5 ) and ammonium molybdate ((NH 4 6 Mo 7 O 24 · 4H 2 O) mixed dissolution in an appropriate ratio to prepare a carrier impregnation reagent, the reagent was dissolved by impregnating the honey comb carrier in a warm bath and evaporated to dryness with gentle stirring It is characterized by consisting of a step of sufficiently absorbing the carrier, the dried carrier is calcined while maintaining at 400 ~ 500 ℃ for 5 hours at a temperature rising rate of 100 ℃ / 1hr. Dioxin removal using such a catalyst has high efficiency.

이상에서 상술한 바와 같이 본 발명은 도시 쓰레기 소각로에서의 다이옥신류의 생성을 최소화하고 대기로의 배출을 억제하기 위해서 소각로의 후 연소 영역에서 가장 문제시되는 다이옥신을 제거하려는 목적으로 기존의 하니컴 형태에 Mo 및 V를 피복시켜 제거율을 극대화하여 전세계적으로 첨예한 사회문제로 대두되고 있으며, 인체 및 생물체 내에 축적되기 쉽고, 발암성을 가진 강한 독성의 다이옥신 제거의 효율을 높이는 효과가 있다.As described above, the present invention provides Mo in the existing honeycomb form for the purpose of removing dioxin, which is the most problematic in the post-combustion zone of the incinerator, in order to minimize the production of dioxins in the municipal waste incinerator and to suppress the discharge to the atmosphere. And by coating V and maximizing the removal rate is emerging as a sharp social problem around the world, it is easy to accumulate in the human body and living organisms, it is effective to increase the efficiency of toxic dioxins removal of carcinogenicity.

Claims (1)

다이옥신(dioxin) 제거용 Mo-V계 촉매 제조 방법에 있어서,In the manufacturing method of Mo-V-based catalyst for dioxin removal, 상기의 촉매를 제조하고자 오산화 바나듐(V2O5)과 몰리브덴산 암모늄((NH4)6Mo7O24·4H2O)를 적정 비율로 혼합 용해하여 담체 함침용 시약을 제조하는 단계,Preparing a catalyst impregnation reagent by mixing and dissolving vanadium pentoxide (V 2 O 5 ) and ammonium molybdate ((NH 4 ) 6 Mo 7 O 24 .4H 2 O) in an appropriate ratio to prepare the catalyst, 상기 시약을 온욕상에서 하니컴(honey comb)담체를 함침시키고 서서히 교반하면서 증발 건조시켜 용해된 시약을 충분히 담체에 흡수시키는 단계,Impregnating the reagent with a honey comb carrier in a warm bath and evaporating to dryness with gentle stirring to sufficiently absorb the dissolved reagent into the carrier, 상기의 건조된 담체를 100℃/1hr의 승온속도로 400∼500℃에서 5시간 유지하면서 소성시켜 촉매를 제조하는 방법.Method of preparing a catalyst by baking the dried carrier while maintaining at 400 ~ 500 ℃ 5 hours at a temperature increase rate of 100 ℃ / 1hr.
KR1019990034240A 1999-08-18 1999-08-18 Fabrication of catalyst for removal of dioxin KR20010018330A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100332224B1 (en) * 2000-01-31 2002-04-12 조성종 Oxidation Catalyst for Emission Control of Dioxin in Flue Gas, method of preparing and using the same
KR20030095912A (en) * 2002-06-15 2003-12-24 (주)하이엔텍 The catalyst for removing injuriousness gas and manufacturing method of the same
KR102079475B1 (en) 2019-07-29 2020-02-20 노한길 Fabrication method of SCR catalyst for removal of dioxin

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08318135A (en) * 1995-03-20 1996-12-03 Mitsubishi Chem Corp Method for decomposing chlorinated organic compound
JPH09103646A (en) * 1995-08-08 1997-04-22 Ebara Corp Method and apparatus for treating combustion exhaust gas
WO1999005329A1 (en) * 1997-07-24 1999-02-04 Siemens Aktiengesellschaft Method for operating a sintering plant, and sintering plant

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08318135A (en) * 1995-03-20 1996-12-03 Mitsubishi Chem Corp Method for decomposing chlorinated organic compound
JPH09103646A (en) * 1995-08-08 1997-04-22 Ebara Corp Method and apparatus for treating combustion exhaust gas
EP0787521A1 (en) * 1995-08-08 1997-08-06 Ebara Corporation Method and apparatus for treating combustion exhaust gases
WO1999005329A1 (en) * 1997-07-24 1999-02-04 Siemens Aktiengesellschaft Method for operating a sintering plant, and sintering plant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100332224B1 (en) * 2000-01-31 2002-04-12 조성종 Oxidation Catalyst for Emission Control of Dioxin in Flue Gas, method of preparing and using the same
KR20030095912A (en) * 2002-06-15 2003-12-24 (주)하이엔텍 The catalyst for removing injuriousness gas and manufacturing method of the same
KR102079475B1 (en) 2019-07-29 2020-02-20 노한길 Fabrication method of SCR catalyst for removal of dioxin

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