KR101698588B1 - High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof - Google Patents

High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof Download PDF

Info

Publication number
KR101698588B1
KR101698588B1 KR1020150144329A KR20150144329A KR101698588B1 KR 101698588 B1 KR101698588 B1 KR 101698588B1 KR 1020150144329 A KR1020150144329 A KR 1020150144329A KR 20150144329 A KR20150144329 A KR 20150144329A KR 101698588 B1 KR101698588 B1 KR 101698588B1
Authority
KR
South Korea
Prior art keywords
reactor
odor
tio
odorous
colloidal
Prior art date
Application number
KR1020150144329A
Other languages
Korean (ko)
Inventor
제영숙
변기영
이병호
Original Assignee
제영숙
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 제영숙 filed Critical 제영숙
Priority to KR1020150144329A priority Critical patent/KR101698588B1/en
Application granted granted Critical
Publication of KR101698588B1 publication Critical patent/KR101698588B1/en

Links

Images

Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/16Disinfection, sterilisation or deodorisation of air using physical phenomena
    • A61L9/18Radiation
    • A61L9/20Ultra-violet radiation
    • A61L9/205Ultra-violet radiation using a photocatalyst or photosensitiser
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L9/00Disinfection, sterilisation or deodorisation of air
    • A61L9/01Deodorant compositions
    • A61L9/014Deodorant compositions containing sorbent material, e.g. activated carbon
    • 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
    • B01D53/02Separation 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 by adsorption, e.g. preparative gas chromatography
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/0203Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of metals not provided for in B01J20/04
    • B01J20/0225Compounds of Fe, Ru, Os, Co, Rh, Ir, Ni, Pd, Pt
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/06Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
    • B01J21/063Titanium; Oxides or hydroxides thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/002Catalysts characterised by their physical properties
    • B01J35/004Photocatalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/102Carbon
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/112Metals or metal compounds not provided for in B01D2253/104 or B01D2253/106
    • B01D2253/1122Metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/207Transition metals
    • B01D2255/20707Titanium

Abstract

The present invention relates to a device and a method capable of compositely treating odorous smells occurring from a sewage treating plant and an odorous smell contamination source. The device and the method according to the present invention can treat odorous smells at high efficiency by using a colloid-state TiO_2 optical catalyst obtained by remedying disadvantages of a conventional TiO_2 thin film coating system. The device according to the present invention comprises: a first reactor (1) for feeding a solution having a 10 nm particle size colloid TiO_2 (2) concentration of 15%, and having a UV lamp (3) capable of irradiating UV; and a second reactor (4) using activated carbon and iron powder as a filter. Through the device and the method for treating odorous smells by using a colloid-state TiO_2 solution for treating a high concentration of odorous materials, odorous materials are effectively removed compared to a conventional TiO_2 catalyst. Moreover, the device and the method can be semi-permanently used, so maintenance costs are low and a high concentration of odorous smells can be economically treated.

Description

콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법{High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof}TECHNICAL FIELD The present invention relates to a high-efficiency odor treatment apparatus using colloidal wet TiO2 reactor,

본 발명은 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법 관한 것으로서, 더욱 상세히는 하수처리장 및 악취 오염원에서 발생하는 악취를 복합처리할 수 있는 장치와 방법으로 기존의 TiO2 박막코팅 시스템에서 단점을 보완한 콜로이드 상태의 수용액 TiO2 광촉매를 이용하여 고효율로 악취를 처리할 수 있는 장치 및 방법에 관한 것이다.The present invention relates to an apparatus and a method for treating a high-efficiency odor using a colloidal-type wet TiO2 reactor, and more particularly, to an apparatus and a method for treating odors generated in a sewage treatment plant and a malodorous source, The present invention relates to an apparatus and a method for treating a malodor with high efficiency by using a supplemented colloidal aqueous solution TiO2 photocatalyst.

광촉매로서 사용되는 반도체는 가전자대(價電子端; Balance band), 전도대(傳導帶; Conduction band) 가 있고 그 에너지 준위의 차이를 밴드갭에너지(Bandgap energy)라고 한다. Semiconductors used as photocatalysts have a valance band and a conduction band, and the difference in energy level is called a bandgap energy.

광촉매 원리는 TiO2 표면에 TiO2 고유의 밴드갭 에너지에 해당하는 400nm 이하의 파장을 갖는 빛이 조사될 경우 가전자대에 있던 전자가 전도대로 여기(勵起)되고 가전자대에는 전자가 빠짐으로 인해 정공(正孔)이 생기면서 OH라디칼이나 O2-2라디칼이 형성되어 유기물질을 산화(분해)시키는 작용을 말한다.The photocatalytic principle is that when light having a wavelength of 400 nm or less, which corresponds to the band gap energy inherent in TiO 2, is irradiated on the surface of TiO 2, the electrons in the valence band are excited by the conduction band and electrons are removed from the valence band (OH) radicals and O2-2 radicals are formed and holes (organic molecules) are oxidized (decomposed).

TiO2 광촉매는 환경 친화적인 소재로서 아래와 같은 광분해 기작을 통해 대기 및 수질정화, 탈취, 살균의 의학적 치료 등 광범위한 용도를 가지고 있다.TiO2 photocatalyst is an environmentally friendly material and has a wide range of uses such as air treatment and purification, deodorization and medical treatment of sterilization through the following photolysis mechanism.

이산화티탄 촉매의 광분해 효과를 증진시키기 위하여 아나타제 결정상으로 제조하며, 5 내지 100㎚ 크기의 미립자 입자상과 이산화티탄 입자 내부에 중심 기공의 지름이 약 0.8㎚인 나노 크기의 기공을 형성시켜 유해가스 및 세균의 흡착, 탈착 기능을 부가하여, 광분해성을 크게 향상시킨 나노 크기의 기공을 갖는 다공성의 이산화티탄 광촉매와 이를 이용한 안료 제조방법이 개시되어 있다.In order to enhance the photodegradation effect of the titanium dioxide catalyst, nanoporous pores having a center pore diameter of about 0.8 nm are formed in the fine particle phase of 5 to 100 nm size and in the titanium dioxide particle, A porous titanium dioxide photocatalyst having nano-sized pores with greatly enhanced photodegradability, and a method for producing a pigment using the same.

대한민국 특허 제0324541호에는 이산화티타니아 광촉매와 광에너지를 활용하여 휘발성 유기물질(Volatile Organic Compound; VOC)을 처리할 수 있는 광촉매가 코팅된 충전물 충진형 튜브형 광화학반응장치로서, 태양에너지 또는 램프(lamp)로부터 조사되는 광에너지와 불균일계 반도체 광촉매를 활용하여 액체 상태는 물론 기체 상태로 존재하는 유독 유기물을 무해한 물질로 분해 처리하는 광화학반응시스템이 개시되어 있다.Korean Patent No. 0324541 discloses a filler-filled tubular photochemical reaction device coated with a photocatalyst capable of treating a volatile organic compound (VOC) using a titanium dioxide photocatalyst and light energy, Discloses a photochemical reaction system for decomposing and treating a toxic organic substance existing in a gaseous state as well as a liquid state into a harmless substance by utilizing a light energy and a heterogeneous semiconductor photocatalyst.

또한, 대한민국 특허 제0465923호에는 TiO2 광촉매 피복 비다공성 담체를 이용한 대기 및 수질 정화 장치 및 그 정화방법에 관한 것으로, 그 목적은 TiO2 광촉매 피복 비다공성 분체를 이용하여, 대기 및 수질 오염 물질을 저감시킬 수 있는 고효율 다용도 환경정화 장치 및 그 정화방법이 개시되어 있다.Korean Patent No. 0465923 describes an apparatus for purifying air and water using a TiO2 photocatalyst-coated nonporous carrier, and a purification method thereof. The object of the present invention is to reduce the air and water pollutants using a TiO2 photocatalyst-coated nonporous powder A high-efficiency multipurpose environmental purification apparatus and a purification method thereof.

그러나 상기 특허문헌에서 제조하고 있거나 이용되고 있는 TiO2 광촉매는 고 농도의 악취 제거 면에서 만족할만한 성과를 거두지 못하고 있다.However, the TiO2 photocatalyst produced or used in the above patent literature has not achieved satisfactory results in terms of high concentration of odor removal.

KR 등록특허 10-0324541KR Patent No. 10-0324541 KR 등록실용신안 20-0255688KR registered utility model 20-0255688 KR 공개특허특2000-0036695KR Patent Publication No. 2000-0036695 KR 등록특허 10-0581675KR Patent No. 10-0581675

이에 본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법은 통상의 광촉매(TiO2)에 비해서 콜로이드상의 TiO2 수용액을 이용하여 고농도의 악취 제거 성능이 우수한 TiO2 악취 처리장치 및 방법을 제공코자 하는 것이다.Accordingly, an apparatus and method for treating a high-efficiency odor using a colloidal-type wet TiO 2 reactor provided in the present invention provides a device and a method for treating a malodorous TiO 2 having a high concentration of malodor removing ability using a colloidal TiO 2 aqueous solution as compared with a conventional photocatalyst (TiO 2) I will do it.

본 발명은 고농도 악취 처리를 위하여 기존 박막 코팅을 통한 필터와 달리 sol-gel 상태의 다분산 콜로이드 상태의 TiO2 수용액을 UV에 노출시켜 고농도의 악취를 처리할 수 있도록 한 것을 특징으로 한다.The present invention is characterized in that unlike a conventional thin film coating filter for treatment of high concentration odor, a TiO2 aqueous solution of a sol-gel state polydisperse colloid is exposed to UV to treat a high concentration of odor.

이를 위해 본 발명은 10nm 입경의 콜로이드 TiO2 15% 농도의 용액이 주입되고, UV를 조사할 수 있는 UV램프를 갖는 1차 반응기와;To this end, the present invention relates to a process for preparing a UV-curable resin composition, comprising: a first reactor having a UV lamp capable of irradiating UV with a solution of colloidal TiO2 15%

필터로 아이론 파우더(iron powder)와 활성탄(active carbon)을 이용한 2차 반응기를 구비한 것을 특징으로 한다.And a secondary reactor using iron powder and active carbon as a filter.

본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법은 고농도의 악취물질을 처리시키는 콜로이드 상태의 TiO2 수용액을 이용한 악취처리 장치 및 방법으로 종래의 TiO2 촉매에 비해서 효과적으로 악취물질을 제거하고 있다. 또한 반영구적인 사용이 가능한 장치 및 방법으로 유지 보수비용이 낮아 경제적으로 고농도 악취를 처리할 수 있는 것이다.The apparatus and method for treating a high-efficiency odor using the colloidal-type wet TiO 2 reactor provided in the present invention effectively removes odor substances as compared with a conventional TiO 2 catalyst by using a colloid-treated TiO 2 aqueous solution for treating a high concentration of odor substances, . In addition, since the maintenance cost is low due to the semi-permanently usable apparatus and method, it is possible to economically treat the high concentration odor.

도 1은 본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법의 바람직한 일 실시예를 보인 블록 구성도
도 2는 본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법의 실험결과로 악취물질별 저감률을 보인 도표
BRIEF DESCRIPTION OF DRAWINGS FIG. 1 is a block diagram showing a preferred embodiment of an apparatus and a method for treating a high-efficiency odor using a colloidal-type wet TiO 2 reactor provided by the present invention;
FIG. 2 is a graph showing the reduction rate of odorous substances according to the results of an apparatus and a method for treating a high-efficiency odor using the colloidal-type wet TiO 2 reactor provided by the present invention

이하 본 발명에 첨부된 도면을 참조하여 본 발명을 상세히 설명하기로 한다. 우선, 도면들 중, 동일한 구성요소 또는 부품들은 가능한 한 동일한 참조부호를 나타내고 있음에 유의하여야 한다. 본 발명을 설명함에 있어, 관련된 공지기능 혹은 구성에 대한 구체적인 설명은 본 발명의 요지를 모호하지 않게 하기 위하여 생략한다.DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the accompanying drawings. First, it should be noted that, in the drawings, the same components or parts have the same reference numerals as much as possible. In the following description of the present invention, a detailed description of known functions and configurations incorporated herein will be omitted so as to avoid obscuring the subject matter of the present invention.

본 명세서에서 사용되는 정도의 용어 약, 실질적으로 등은 언급된 의미에 고유한 제조 및 물질 허용오차가 제시될 때 그 수치에서 또는 그 수치에 근접한 의미로 사용되고, 본 발명의 이해를 돕기 위해 정확하거나 절대적인 수치가 언급된 개시 내용을 비양심적인 침해자가 부당하게 이용하는 것을 방지하기 위해 사용된다.As used herein, the terms "substantially", "substantially", and the like are used herein to refer to a value in or near the numerical value when presenting manufacturing and material tolerances inherent in the meanings mentioned, Absolute numbers are used to prevent unauthorized exploitation by unauthorized intruders of the mentioned disclosure.

본 발명에서는 악취 처리를 위해 TiO2 광촉매를 약 10nm 이하로 줄여 수용액 상태로 만들어 sol-gel 형태의 콜로이드상의 형태로 전환하였으며, 기존의 TiO2와 달리 박막 코팅이 아닌 콜로이드 상에서의 촉매반응을 하도록 유도하여 장점으로는 콜로이드상의 TiO2 입자에서 광산화·환원 반응이 입자 표면에서 동시에 일어나며 입자 하나를 미세한 광전기화학 셀로 볼 수 있다.In the present invention, the TiO2 photocatalyst is reduced to about 10 nm or less to convert it into an aqueous solution state and converted into a sol-gel type colloid-like form. In contrast to the conventional TiO2, , Photo-oxidation and reduction reactions occur simultaneously on the surface of the colloidal TiO2 particles, and one particle can be seen as a fine photo-electrochemical cell.

콜로이드상의 광촉매의 결정 입자 크기를 반경 약 10nm 이하로 줄이면 전하이동체(charge carrier)는 양자역학적으로 마치 상자 안에 갇힌 압자(particle-in-a-box)처럼 행동하게 되는 특이한 현상이 관찰된다.When the crystal size of the colloidal-phase photocatalyst is reduced to a radius of about 10 nm or less, the charge carrier is observed to behave like a particle-in-a-box in a quantum mechanical manner.

이런 양자 효과로 말미암아 밴드 간격이 증가하게 되고 band edge가 이동하여 보다 높은 산화 환원 전위를 형성하게 된다. 양자크기로 만들어진 콜로이드상의 광촉매는 광반응의 속도제한단계(rate limiting step)가 전하전이 반응일 경우 광효율(photo efficient)을 향상시킨다.This quantum effect increases the band gap and moves the band edge to form a higher redox potential. A colloidal-like photocatalyst made of quantum size improves photo efficiency when the rate limiting step of the photoreaction is a charge transfer reaction.

본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법은 1차와 2차 반응기로 구성되는 TiO2 악취 처리 장치 및 방법으로, 1차 반응기에서 TiO2(약 10 nm 입경) 15% 농도의 TiO2 콜로이드 용액을 주입하고 UV램프를 통해 UV를 조사토록 한다.An apparatus and method for treating a high-efficiency odor using a colloidal-type wet TiO2 reactor provided in the present invention is a device and a method for treating a malodor of TiO2 composed of a primary and a secondary reactor. In the first reactor, TiO2 (about 10 nm in particle size) Of TiO2 colloid solution is injected and UV is irradiated through UV lamp.

이 과정에서 발생하는 OH 라디컬과 악취가 반응하여 악취물질을 산화·환원 반응을 통한 악취를 제어한다.The OH radicals and odors generated in this process react to control the odor through the oxidation / reduction reaction of odor materials.

콜로이드상의 TiO2 용액에 악취를 폭기 시킴과 동시에 오존(O3)을 주입하여 콜로이드상의 TiO2가 부유하는 과정에서 광산화 반응부의 253.7nm와 380nm의 파장을 동시에 방사하는 UV램프에 직접적으로 노출시켜 반응을 할 수 있는 접촉면적 증대를 통한 1차반응기의 반응균일화하여 악취 처리를 극대화 한다.In the course of colloidal TiO2 floating, ozone (O3) is injected into the colloidal TiO2 solution while the odor is augmented and the reaction can be carried out by directly exposing to the UV lamp which radiates the wavelength of 253.7nm and 380nm of the photo- The reaction of the first reactor is made uniform by increasing the contact area, thereby maximizing the processing of the offensive odor.

2차 반응기에서는 1차 반응기에서 제어하지 못한 미량의 악취 및 기타 대기오염물질을 제거하는 필터로 아이론 파우더 및 활성탄을 이용한 것을 특징으로 한다.The second reactor is characterized by using iron powder and activated carbon as a filter for removing a small amount of odor and other air pollutants that are not controlled in the first reactor.

도 1은 본 발명에서 제공하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치의 바람직한 일 실시예를 보인 전체 블록 구성도이다.1 is an overall block diagram showing a preferred embodiment of a high-efficiency odor treatment apparatus using the colloidal-type wet TiO2 reactor provided in the present invention.

도시한 바와 같이 본 발명의 악취 처리 장치는 1차 반응기(1)와 2차 반응기(4)로 크게 이루어진다.As shown in the drawings, the malodor treatment apparatus of the present invention is largely composed of a first reactor 1 and a second reactor 4.

상기 1차 반응기(1)는 악취와 오존(O3)이 각 1m/min 의 유속으로 유입되도록 하며, 1차 반응기(1) 내에는 sol-gel 상태의 콜로이드 TiO2(2)가 UV램프(3)와 반응토록 한다.In the first reactor 1, a colloid TiO 2 (2) in the sol-gel state is introduced into the UV lamp 3 (3) in the first reactor 1, so that odor and ozone (O 3 ) ).

상기 1차 반응기(1)의 용적은 가로 20cm, 세로20cm,, 높이 200cm로 하며, 콜로이드 TiO2(2) 수용액 용량은 4L로 한다.The volume of the first reactor (1) is 20 cm in width, 20 cm in length, 200 cm in height, and the capacity of the colloidal TiO 2 (2) aqueous solution is 4 L.

1차 반응기(1)에 설치되는 UV램프는 253.7nm와 380nm의 파장을 발생시킨다.The UV lamp installed in the first reactor (1) generates wavelengths of 253.7 nm and 380 nm.

2차 반응기(4)는 1차 반응기(1)에서 배출된 가스가 유입되어 잔류하는 대기오염 물질 및 악취물질을 최종적으로 제어하게 된다. The secondary reactor 4 finally controls the remaining air pollutants and odorous substances introduced into the first reactor 1.

상기 2차 반응기(4)의 용적은 가로 20cm, 세로20cm,, 높이 200cm로 하며, 2차 반응기(4) 내부에는 아이론 파우더 또는 활성탄(Activated carbon)이 500g 투입된다.The second reactor 4 has a volume of 20 cm, a length of 20 cm, and a height of 200 cm. In the second reactor 4, 500 g of iron powder or activated carbon is charged.

(실험예)(Experimental Example)

본 발명의 악취 처리장치를 사용하여 악취 처리 과정을 다음과 같이 실험하였다.The odor treatment process was performed as follows using the malodor treatment apparatus of the present invention.

1) TiO2 콜로이드 합성과정 (Synthetic process of TiO2 colloid)1) Synthetic process of TiO2 colloid

Ti(OBu)4와 acetylacetone (AcAc)를 1:4 몰 비율로 실온에서 잠시 동안 교반 한 후 1 부탄올 30ml를 용액을 추가 희석하고, 15분 동안 교반시킨 후 질산 수용액을 첨가하였다. 콜로이드 분산은 투명 졸에 60 ℃ 온도로 유지하여 하루동안 숙성시켰다.Ti (OBu) 4 and acetylacetone (AcAc) were stirred in a 1: 4 molar ratio at room temperature for a while, 30 ml of 1-butanol was further diluted, stirred for 15 minutes, and an aqueous nitric acid solution was added. The colloidal dispersion was kept in a transparent sol at a temperature of 60 캜 for aging for one day.

2) 콜로이드 TiO2 반응2) Colloidal TiO2 reaction

악취 물질을 1차 반응기에 1m/min 유속으로 유입시키며 이와 더불어 오존도 같은 유량으로 주입한다.The odorous substance is introduced into the first reactor at a flow rate of 1 m / min and the ozone is injected at the same flow rate.

악취 유입시 아래 방향에서 주입하여 자동 폭기 상태로 버블 형태의 콜로이드 TiO2와 반응시켜 접촉면적을 최적화 하며, UV램프(3)의 UV에서 광촉매의 산화 환원 반응이 콜로이드 각 입자에서 일어나 악취를 제어한다.When the odor is introduced, it is injected from the downward direction to optimize the contact area by reacting with the bubble type colloid TiO2 in the state of automatic aeration, and the redox reaction of the photocatalyst occurs in the UV of the UV lamp (3).

3) 악취 측정 및 검출3) Odor measurement and detection

㉠ 1차 반응기에서 나온 악취가스를 알데하이드는 DNPH(2,4-dinitrophenylhydazine) 카트리지를 이용하여 포집하고 HPLC(High Performance Liquid Chromatography)를 이용하여 분석하며, 휘발성 유기화합물인 VOCs(Volatile organic compounds)는 Tenac tube를 이용하여 포집 및 GC/MS(Gas Chromatography/Mass Spectrometry)를 이용하여 분석한다.The volatile organic compounds (VOCs), which are volatile organic compounds, are collected by using Tenac (2,4-dinitrophenylhydrazine) cartridges and analyzed by HPLC (High Performance Liquid Chromatography) and analyzed by GC / MS (Gas Chromatography / Mass Spectrometry).

또한 2차 반응기를 통과한 가스 역시 ㉠의 실험법을 반복하여 측정 분석 후 악취물질의 농도를 1차 반응기와 비교하여 제거율을 산출 하였다.In addition, the gas passing through the second reactor was also tested repeatedly, and the removal rate was calculated by comparing the concentration of the odorous substance with that of the first reactor after the measurement and analysis.

상기 실험예에 사용된 TiO2 악취처리시스템 specification은 다음과 같다.The specification of the TiO2 malodor processing system used in the above experimental example is as follows.

가) 광촉매 반응의 실험 조건A) Experimental conditions of photocatalytic reaction

a. 광촉매 반응기 용적(ℓ) 16~24  a. Photocatalytic reactor volume (ℓ) 16 ~ 24

b. 광촉매 중량(g) 14~24  b. Photocatalyst weight (g) 14 ~ 24

c. 반응물 농도(ppm) 알데하이드류 10~30ppm(w/v)  c. Reactant Concentration (ppm) Aldehydes 10 - 30 ppm (w / v)

VOCs류 100~300ppm(w/v) VOCs Type 100 ~ 300ppm (w / v)

d. 악취처리 유량(유입 악취 유량): 3m3/mind. Odor treatment flow rate (incoming odor flow rate): 3m 3 / min

e. 적정 처리 악취 농도e. Properly treated odor concentration

ㄱ. 알데하이드류 : 1m/min 유속으로 처리시 100% 제거A. Aldehydes: 100% removal at 1m / min flow rate

ㄴ. VOCs류 : 1m/min 유속으로 처리시 100% 제거 N. VOCs: 100% removal at 1m / min flow rate

도 2는 본 발명의 실험결과를 악취물질별 저감률을 보인 도표로 악취물질인 알데하이드류와 휘발성유기화합물이 1차반응기(1)를 거친 결과 60% 이상 저감되며 2차반응기(4)를 거치고 나면 악취물질이 불검출(N.D:not detected) 되는 것을 알 수 있다. FIG. 2 is a graph showing the reduction rate of the odorous substances according to the test results of the present invention. The aldehydes and the volatile organic compounds, which are malodorous substances, are reduced by 60% or more as a result of passing through the first reactor 1 and passed through the second reactor 4 It can be seen that odorous substances are not detected (ND).

이상과 같이 구성될 수 있는 본 발명의 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치 및 방법은 고농도의 악취물질을 처리시키는 콜로이드 상태의 TiO2 수용액을 이용한 악취를 처리할 수 있도록 한 것으로서, 기존의 TiO2 촉매에 비해서 효과적으로 악취물질을 제거할 수 있으며, 반영구적인 사용이 가능하고, 유지 보수비용이 낮아 경제적으로 고농도 악취를 처리할 수 있는 것이다.The apparatus and method for treating a high-efficiency odor using the colloidal-type wet TiO 2 reactor of the present invention, which can be configured as described above, are capable of treating odor using a colloidal TiO 2 aqueous solution for treating a high concentration of malodorous substances. It is possible to effectively remove odorous substances as compared with catalysts, semi-permanent use is possible, and maintenance cost is low, so that high-concentration odor can be economically treated.

이상에서 설명한 본 발명의 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 시스템은 전술한 실시예 및 첨부된 도면에 의해 한정되는 것이 아니고, 본 발명의 기술적 사상을 벗어나지 않는 범위 내에서 여러 가지 치환, 변형 및 변경이 가능함은 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자에게 있어서 명백할 것이다.The above-described high-efficiency odor treatment system using the colloidal wet TiO 2 reactor of the present invention is not limited to the above-described embodiments and the accompanying drawings, and various substitutions, modifications, and changes may be made without departing from the technical spirit of the present invention. It will be apparent to those skilled in the art that changes may be made in the present invention.

1: 1차 반응기 2: (sol-gel 상태의)콜로이드 TiO2
3: UV램프 4: 2차 반응기
1: primary reactor 2: colloidal TiO2 (in sol-gel state)
3: UV lamp 4: Secondary reactor

Claims (2)

10nm 입경의 콜로이드 TiO2(2) 15% 농도의 용액이 주입되고, UV를 조사할 수 있는 UV램프(3)를 갖는 1차 반응기(1)와;
필터로 아이론 파우더 및 활성탄을 이용한 2차 반응기(4)를 구비한 것을 특징으로 하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 장치.
(1) having a UV lamp (3) into which a solution of 15% colloidal TiO2 (2) having a 10 nm particle diameter is injected and can be irradiated with UV;
And a second reactor (4) using iron powder and activated carbon as a filter. The apparatus for treating a high-efficiency odor using a colloidal-type wet TiO2 reactor.
1차 반응기에 10nm의 콜로이드상의 TiO2 15% 농도의 용액을 주입하고 UV램프를 통해 UV를 조사하는 과정과;
상기 과정에서 발생하는 OH 라디컬과 악취가 반응하여 악취물질을 산화·환원 반응을 통한 악취를 제어하는 과정과;
상기 콜로이드상의 TiO2 용액에 악취를 폭기 시킴과 동시에 오존(O3)을 주입하여 콜로이드상의 TiO2가 부유하는 과정에서 광산화 반응부의 253.7nm와 380nm의 파장을 동시에 방사하는 UV램프에 직접적으로 노출시켜 악취 처리를 행하는 과정과;
상기 1차 반응기를 통과한 가스 중의 미량의 악취 및 기타 대기오염물질을 제거하기 위해 필터로 아이론 파우더 또는 활성탄을 사용한 2차 반응기를 통해 처리할 수 있도록 한 것을 특징으로 하는 콜로이드형 습식 TiO2 반응기를 이용한 고효율 악취처리 방법.
Injecting a solution of 15% concentration of TiO2 on colloidal 10 nm in the primary reactor and irradiating UV through a UV lamp;
Controlling the odor through the oxidation / reduction reaction of the odorous substance by reacting the OH radicals and the odor generated in the process;
The odor is aerated to the colloidal TiO 2 solution and the ozone (O 3) is injected to expose the colloid-like TiO 2 to the UV lamp which simultaneously emits the wavelengths of 253.7 nm and 380 nm of the photo-oxidation reaction part, A process of doing;
Characterized in that it is treated through a second reactor using iron powder or activated carbon as a filter in order to remove trace odor and other atmospheric pollutants in the gas passing through the first reactor. High - efficiency odor treatment method.
KR1020150144329A 2015-10-15 2015-10-15 High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof KR101698588B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020150144329A KR101698588B1 (en) 2015-10-15 2015-10-15 High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020150144329A KR101698588B1 (en) 2015-10-15 2015-10-15 High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof

Publications (1)

Publication Number Publication Date
KR101698588B1 true KR101698588B1 (en) 2017-01-23

Family

ID=57989827

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020150144329A KR101698588B1 (en) 2015-10-15 2015-10-15 High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof

Country Status (1)

Country Link
KR (1) KR101698588B1 (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20000036695A (en) 2000-03-25 2000-07-05 임한진 Wet appartus use of removed the smell using the photocatalysis
KR200255688Y1 (en) 2001-08-28 2001-12-13 (주) 빛과환경 Hybrid Sterilizing and Deodorizing Equipment Using Photocatalysts and Combustion Catalysts
KR100324541B1 (en) 1999-05-17 2002-02-16 손재익 VOC treatment system with photocatalytic tubular reactors packed with Ti02-coated packing materials and its utilization
KR20030083972A (en) * 2002-04-24 2003-11-01 한국지질자원연구원 Apparatus and method for environmental purification by using TiO2 photocatalyst coated non-porous carriers
KR20050047045A (en) * 2005-04-07 2005-05-19 주식회사 과학기술분석센타 Hybrid processing method for deodorization and the system therefor adopted real-time controller
KR100581675B1 (en) 2004-07-13 2006-05-22 레인보우스케이프주식회사 Deodorization apparatus of foul smell gas
JP2010075879A (en) * 2008-09-26 2010-04-08 Cs Engineering:Kk Method of deodorizing exhaust
US20110159109A1 (en) * 2008-09-02 2011-06-30 Drexel University Titania dispersion and method for making

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100324541B1 (en) 1999-05-17 2002-02-16 손재익 VOC treatment system with photocatalytic tubular reactors packed with Ti02-coated packing materials and its utilization
KR20000036695A (en) 2000-03-25 2000-07-05 임한진 Wet appartus use of removed the smell using the photocatalysis
KR200255688Y1 (en) 2001-08-28 2001-12-13 (주) 빛과환경 Hybrid Sterilizing and Deodorizing Equipment Using Photocatalysts and Combustion Catalysts
KR20030083972A (en) * 2002-04-24 2003-11-01 한국지질자원연구원 Apparatus and method for environmental purification by using TiO2 photocatalyst coated non-porous carriers
KR100581675B1 (en) 2004-07-13 2006-05-22 레인보우스케이프주식회사 Deodorization apparatus of foul smell gas
KR20050047045A (en) * 2005-04-07 2005-05-19 주식회사 과학기술분석센타 Hybrid processing method for deodorization and the system therefor adopted real-time controller
US20110159109A1 (en) * 2008-09-02 2011-06-30 Drexel University Titania dispersion and method for making
JP2010075879A (en) * 2008-09-26 2010-04-08 Cs Engineering:Kk Method of deodorizing exhaust

Similar Documents

Publication Publication Date Title
Weon et al. TiO2 nanotubes with open channels as deactivation-resistant photocatalyst for the degradation of volatile organic compounds
Keller et al. Photocatalytic oxidation of butyl acetate in vapor phase on TiO2, Pt/TiO2 and WO3/TiO2 catalysts
Mahmoodi et al. Kinetics of heterogeneous photocatalytic degradation of reactive dyes in an immobilized TiO2 photocatalytic reactor
Qourzal et al. Photodegradation of 2-naphthol in water by artificial light illumination using TiO2 photocatalyst: Identification of intermediates and the reaction pathway
Habibi et al. Photocatalytic degradation of some organic sulfides as environmental pollutants using titanium dioxide suspension
KR101334970B1 (en) Photocatalyst material, method for decomposition of organic material, interior member, air purification device, and appatarus for preparation of oxidizing agent
Kormali et al. Photocatalysis by polyoxometallates and TiO2: a comparative study
Kumar et al. Photocatalysis by nanoparticles of titanium dioxide for drinking water purification: a conceptual and state-of-art review
JP2009078211A (en) Photocatalyst
Hajaghazadeh et al. Heterogeneous photocatalytic oxidation of methyl ethyl ketone under UV-A light in an LED-fluidized bed reactor
Wang et al. Electrospun cerium-based TiO2 nanofibers for photocatalytic oxidation of elemental mercury in coal combustion flue gas
KR20140134990A (en) A water treatment system including porous alumina membranes immobilized photocatalysts, operating method thereof, and purifying method of wastewater using thereby
Liang et al. Photo-catalytic degradation of volatile organic compounds (VOCs) over titanium dioxide thin film
Jędrzejczyk et al. Wide band gap Ga 2 O 3 as efficient UV-C photocatalyst for gas-phase degradation applications
JP2005270734A (en) Photocatalyst composite and organic substance converting method using the same
Mojir Shaibani et al. Photocatalytic BiFeO 3 nanofibrous mats for effective water treatment
Chen et al. Enhanced photocatalytic degradation of atrazine by platinized titanium dioxide under 352 nm irradiation
KR101698588B1 (en) High -efficiency odor treatment apparatus using coloid wet type Ti02 reactor and method thereof
KR101173445B1 (en) Photocatalyst composition and manufacturing method thereof for offensive odor treatment
Malinowska et al. Titania aerogels: Preparation and photocatalytic tests
Algubury Study the activity of titanium dioxide nanoparticle using orange G dye
Dona et al. The effect of dosage on the photocatalytic degradation of organic pollutants
Qourzal et al. Photodegradation of 2-naphthol using nanocrystalline TiO2
Pitchaimuthu et al. Enhanced photocatalytic activity of CeO2 using β-cyclodextrin on visible light assisted decoloration of methylene blue
Ahmed et al. Quantum yield of formaldehyde formation from methanol in the presence of TiO2 and platinized TiO2 photocatalysts

Legal Events

Date Code Title Description
E701 Decision to grant or registration of patent right
GRNT Written decision to grant