KR20120097605A - Honeycomb catalyst device - Google Patents

Honeycomb catalyst device Download PDF

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KR20120097605A
KR20120097605A KR1020110016910A KR20110016910A KR20120097605A KR 20120097605 A KR20120097605 A KR 20120097605A KR 1020110016910 A KR1020110016910 A KR 1020110016910A KR 20110016910 A KR20110016910 A KR 20110016910A KR 20120097605 A KR20120097605 A KR 20120097605A
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South Korea
Prior art keywords
catalyst block
catalyst
hole
block
base
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KR1020110016910A
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Korean (ko)
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류민웅
정영신
류원형
박용민
김권택
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(주)엔티시
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Priority to KR1020110016910A priority Critical patent/KR20120097605A/en
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418—Honeycomb filters
    • B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
    • B01D46/2482—Thickness, height, width, length or diameter
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418—Honeycomb filters
    • B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
    • B01D46/2486—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure characterised by the shapes or configurations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2418—Honeycomb filters
    • B01D46/2451—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure
    • B01D46/2486—Honeycomb filters characterized by the geometrical structure, shape, pattern or configuration or parameters related to the geometry of the structure characterised by the shapes or configurations
    • B01D46/2496—Circular
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/38—Removing components of undefined structure
    • B01D53/44—Organic components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708—Volatile organic compounds V.O.C.'s

Abstract

PURPOSE: A honeycomb catalyst apparatus is provided to easily separate and replace a catalyst block and minimize waste as cutting of the catalyst block is not needed. CONSTITUTION: A honeycomb catalyst apparatus(150) includes a base part, a catalyst block(157), and a supporting part(155). The base part divides the inner part of a target gas transferring part into an upper part and a lower part along the transferring direction of target gas. A through hole is formed at the base part and connects the upper part and the lower part. The catalyst block is installed at the base part to purify the target gas through the through hole. The supporting part supports the catalyst block in the base part such that the catalyst block can detachably combine with the base part.

Description

허니컴 촉매장치 {Honeycomb catalyst device}Honeycomb catalyst device

본 발명은 허니컴 촉매장치에 관한 것으로서, 더욱 상세하게는 허니컴 촉매의 설치 및 재활용이 용이한 허니컴 촉매장치에 관한 것이다.The present invention relates to a honeycomb catalyst device, and more particularly, to a honeycomb catalyst device for easy installation and recycling of a honeycomb catalyst.

일반적으로, 촉매 담체는 가스 중의 오염 성분, 특히, 배기가스 중의 입자상 물질(PM)을 흡착, 정화 처리하는데 많이 이용되고 있다. 통상, 엔진에서 배기 매니폴드를 통해 배출되는 배기가스는 배기 파이프를 거쳐 촉매 변환기로 도입되어 정화되고, 머플러를 통과하면서 소음이 감소된 후 대기 중으로 방출된다. 촉매 변환기는 매연여과장치 (DFT; Diesel Particulate Filter)의 일종으로 배기가스 중의 오염 물질을 처리하는 역할을 한다. 촉매담체는 촉매 변환기 내부에 설치되어 배기가스 중의 입자상 물질을 포집, 정화하는데 많이 이용되고 있다. In general, catalyst carriers are widely used to adsorb and purify pollutants in gas, particularly particulate matter (PM) in exhaust gas. Typically, the exhaust gas from the engine through the exhaust manifold is introduced into the catalytic converter through the exhaust pipe to be purified, and after being passed through the muffler, the noise is reduced and then released into the atmosphere. Catalytic converters are a type of diesel particulate filter (DFT) that treat pollutants in exhaust gases. The catalyst carrier is installed inside the catalytic converter and is widely used for collecting and purifying particulate matter in exhaust gas.

촉매 담체에는, 구성상의 특징에 따라, 펠릿형, 허니컴형, 금속 와이어형이 있다. 본 발명의 명세서에서 다루어지는 것은 허니컴 촉매 담체이다.The catalyst carrier is in the form of pellet, honeycomb, or metal wire, depending on the characteristics of the configuration. Addressed in the present specification are honeycomb catalyst carriers.

종래의 허니컴 촉매 담체 구조물은 복수개의 촉매블럭들을 육면체의 반응기 내에 삽입 설치하여 형성하는 것이 일반적이었다. 반응기는 배기가스가 통과하는 이동로 상에 설치되며 배기가스의 연통이 가능하도록 상면과 하면이 개방되어 있는 형태를 이루는게 일반적이었다. Conventional honeycomb catalyst carrier structures are generally formed by inserting a plurality of catalyst blocks into a hexahedral reactor. The reactor was generally installed on a moving path through which exhaust gas passes, and the upper and lower surfaces thereof were opened to enable communication of the exhaust gas.

상술한 촉매블럭들의 경우에는 상하부가 개방된 육면체의 반응기에 충진되며 촉매블럭들 사이에 처리가스가 촉매블럭을 통과하지 않고 지나갈 수 있는 이격공간이 형성되지 않게 하기 위해서 사각 또는 팔각기둥으로 제작하여 각각의 촉매블럭들을 상호 밀착설치해야 하였다. In the case of the catalyst blocks described above, the upper and lower portions of the catalyst blocks are filled in a hexahedral reactor, and each of the catalyst blocks is manufactured in a square or octagonal column so as not to form a space for the processing gas to pass without passing through the catalyst block. Of catalyst blocks had to be installed in close contact with each other.

따라서 원통형의 촉매블럭의 경우에는 각기둥 형태가 되도록 절단하는 절단작업을 거쳐야 하였으며, 절단과정에서 유실되는 촉매의 양이 많아 낭비가 심한 문제점이 있었다. Therefore, in the case of the cylindrical catalyst block, the cutting operation was to be cut to form a columnar shape, and the amount of catalyst lost during the cutting process was largely a wasteful problem.

본 발명은 상기 문제점을 해결하기 위해 창출된 것으로서, 원통형의 허니컴 촉매블럭을 재가공 없이 사용할 수 있으며 하우징에 설치 및 해체가 용이하게 형성된 허니컴 촉매장치를 제공하는데 그 목적이 있다.The present invention has been made to solve the above problems, and an object of the present invention is to provide a honeycomb catalyst device in which a cylindrical honeycomb catalyst block can be used without reworking and is easily installed and dismantled in a housing.

상기 목적을 달성하기 위한 본 발명에 따른 허니컴 촉매장치는 처리대상 가스가 이동하는 이송부의 내부를 상기 처리가스가 이동하는 방향을 따라 상하로 구획하며, 구획된 상부와 하부를 상호 연통시키는 관통홀이 형성된 베이스부와, 상기 관통홀을 통해 통과하는 처리대상 가스를 정화하도록 상기 베이스부에 설치되는 촉매블럭과, 상기 촉매블럭이 상기 베이스부에 착탈 가능하게 결합되도록 상기 베이스부에 촉매블럭을 지지시키는 지지부를 구비한다.The honeycomb catalyst device according to the present invention for achieving the above object is to partition the inside of the conveying unit to move the processing target gas up and down along the direction in which the processing gas moves, the through hole for communicating the partitioned top and bottom mutually A base block formed, a catalyst block installed in the base unit to purify the gas to be processed through the through hole, and a catalyst block supported by the base unit such that the catalyst block is detachably coupled to the base unit. It has a support.

상기 촉매블럭은 원통형으로 형성되고, 상기 지지부는 상하로 관통된 중공 원통형으로 형성되어 하단 외주면이 상기 관통홀에 끼워지거나 상기 관통홀의 상부에 위치하도록 상기 베이스부의 상면에 안착되게 결합되며, 상기 중공은 상기 촉매블럭의 외경에 대응하는 내경으로 상기 지지부의 상단으로부터 하방으로 소정길이 연장되는 상부구간과, 상기 상부구간의 하단으로부터 하방으로 연장되되 상기 상부구간에 비해 상대적으로 직경이 작고 상기 관통홀과 연통되어 있는 하부구간으로 이루어지는 것이 바람직하다.The catalyst block is formed in a cylindrical shape, the support portion is formed in a hollow cylindrical penetrating up and down is coupled to be seated on the upper surface of the base portion so that the lower outer peripheral surface is fitted into the through hole or located above the through hole. An upper section extending a predetermined length downward from an upper end of the support portion with an inner diameter corresponding to an outer diameter of the catalyst block, and extending downward from a lower end of the upper section, the diameter being relatively smaller than the upper section and communicating with the through hole; It is preferable that the lower section is formed.

상기 베이스부의 관통홀은 상기 촉매블럭의 외경에 비해 상대적으로 작은 직경으로 형성되며, 상기 지지부는 상기 베이스부의 상면에 안착되되 상기 관통홀과 대응하는 위치에 상기 촉매블럭의 외경에 대응하는 직경을 갖는 지지홀이 형성된 판재 형상으로 형성될 수도 있다.The through hole of the base part is formed to have a diameter relatively smaller than the outer diameter of the catalyst block, and the support part is seated on an upper surface of the base part and has a diameter corresponding to the outer diameter of the catalyst block at a position corresponding to the through hole. The support hole may be formed in a plate shape.

본 발명에 따른 허니컴 촉매장치는 촉매블럭의 절단이 필요없기 때문에 촉매블럭의 낭비를 최소화할 수 있고, 촉매블럭의 분리 및 교체가 매우 용이한 이점이 있다.The honeycomb catalyst device according to the present invention can minimize the waste of the catalyst block because it does not need to cut the catalyst block, there is an advantage that the separation and replacement of the catalyst block is very easy.

도 1은 본 발명의 허니컴 촉매장치가 적용된 휘발성 유기화합물 처리장치를 도시한 단면도,
도 2는 본 발명의 허니컴 촉매장치의 일 실시예를 도시한 사시도,
도 3은 도 2의 허니컴 촉매장치의 부분발췌 사시도,
도 4는 도 2의 허니컴 촉매장치의 단면도,
도 5는 허니컴 촉매장치의 다른 실시예를 도시한 부분절단 사시도,
도 6은 도 5의 허니컴 촉매장치의 단면도이다. 1 is a cross-sectional view showing a volatile organic compound processing apparatus to which the honeycomb catalyst device of the present invention is applied;
Figure 2 is a perspective view showing one embodiment of the honeycomb catalyst device of the present invention,
3 is a partial excerpt perspective view of the honeycomb catalyst device of FIG.
4 is a cross-sectional view of the honeycomb catalytic device of FIG.
5 is a partially cutaway perspective view showing another embodiment of the honeycomb catalytic apparatus,
6 is a cross-sectional view of the honeycomb catalyst device of FIG.

이하, 첨부된 도면을 참조하여 본 발명에 따른 허니컴 촉매장치를 더욱 상세하게 설명한다.Hereinafter, a honeycomb catalyst device according to the present invention will be described in more detail with reference to the accompanying drawings.

도 1에는 본 발명에 따른 허니컴 촉매장치가 설치된 휘발성 유기화합물 처리장치가 도시되어 있다.1 shows a volatile organic compound processing apparatus in which a honeycomb catalytic apparatus according to the present invention is installed.

휘발성 유기화합물 처리장치(100)는 본체(110)와, 본체(110)에 설치되는 버너(120), 보조히터(130), 축열부(140), 허니컴 촉매장치(150) 및 열교환부(160)를 포함한다.The volatile organic compound processing apparatus 100 includes a main body 110, a burner 120 installed in the main body 110, an auxiliary heater 130, a heat storage unit 140, a honeycomb catalytic device 150, and a heat exchanger 160. ).

상기 본체(110)는 연소실(111)과 가스배출부(112)를 갖는데, 연소실(111)은 처리 대상이 되는 휘발성 유기화합물이 유입될 수 있도록 공급관(10)과 연결되어 있으며, 일측에 상기 버너(120)가 설치되어 내부로 유입된 휘발성 유기화합물을 연소시키도록 가열한다. 휘발성 유기화합물은 버너(120)에 의해 산화되면서 1차 처리가 이루어진다.The main body 110 has a combustion chamber 111 and a gas discharge unit 112, the combustion chamber 111 is connected to the supply pipe 10 so that the volatile organic compounds to be processed can be introduced, the burner on one side 120 is installed and heated to burn the volatile organic compounds introduced into the interior. The volatile organic compound is oxidized by the burner 120 and the first treatment is performed.

상기 가스배출부(112)는 연소실(111)과 연통되며 상하방향으로 연장되게 형성되어 있어서, 연소실(111)에서 산화처리된 처리가스가 상방으로 이동하면서 배출될 수 있도록 소정의 이동통로(113)를 갖는다.The gas discharge part 112 is in communication with the combustion chamber 111 and is formed to extend in the vertical direction, so that a predetermined movement passage 113 can be discharged while the processing gas oxidized in the combustion chamber 111 moves upward. Has

상기 보조히터(130)는 상기 연소실(111)의 일측에 설치되어 연소된 처리가스가 가스배출부(112)로 배출되기 전 가열될 수 있도록 작동하는데, 상기 보조히터(130)는 처리가스의 온도가 충분히 높지 않을 때 가열을 통해 후술하는 열교환부(160)에서 연소실(111)로 유입되는 휘발성 유기화합물이 처리가스에 의해 충분히 예열될 수 있도록 하기 위한 것이다.The auxiliary heater 130 is installed at one side of the combustion chamber 111 so that the burnt process gas is heated before being discharged to the gas discharge unit 112, the auxiliary heater 130 is the temperature of the process gas Is not sufficiently high to allow the volatile organic compounds introduced into the combustion chamber 111 from the heat exchanger 160 to be described later through heating to be sufficiently preheated by the processing gas.

상기 축열부(140)는 가스배출부(112)에 설치되어 있는데, 축열부재들로 이루어져 있어서, 처리가스가 축열부(140)를 통과하는 과정에서 축열부(140)에서 축열을 하게 되며, 뒤이어 이동하는 처리가스의 온도가 일정수준 이상이 되지 않을 때에는 축열부(140)에서 처리가스를 가온한다.The heat storage unit 140 is installed in the gas discharge unit 112, and consists of heat storage members, the heat accumulating in the heat storage unit 140 during the process gas passes through the heat storage unit 140, and then When the temperature of the moving process gas does not exceed a predetermined level, the heat treatment unit 140 heats the process gas.

축열부(140)를 통과한 처리가스는 허니컴 촉매장치(150)를 통과하게 된다.The processing gas passing through the heat storage unit 140 passes through the honeycomb catalytic device 150.

허니컴 촉매장치(150)는 가스배출부(112)에 탈착 가능하게 결합되어 배출되는 배기가스를 정화한다. The honeycomb catalyst device 150 is detachably coupled to the gas discharge unit 112 to purify the exhaust gas discharged.

허니컴 촉매장치(150)의 상부에는 열교환부(160)가 마련되어 있다.The heat exchange part 160 is provided in the upper part of the honeycomb catalyst device 150.

열교환부(160)는 처리가스가 상방으로 이동할 수 있도록 형성된 제1 이송부(161)와, 상기 공급관(10)과 연통되어 연소실(111)로 공급되는 휘발성 유기화합물이 이동할 수있는 이동통로(113)를 제공하는 제2 이송부(162)를 포함하는데, 상기 제1 이송부(161)가 제2 이송부(162)를 관통하여 상방으로 이동하도록 형성되어 있기 때문에 고온의 처리가스가 제1 이송부(161)를 통과하는 과정에서 휘발성 유기화합물과 열교환되어 휘발성 유기화합물을 예열시키게 된다.The heat exchange part 160 may include a first transfer part 161 formed to move the processing gas upwardly, and a moving path 113 through which the volatile organic compound supplied to the combustion chamber 111 may be communicated with the supply pipe 10. And a second transfer part 162 for providing a high temperature treatment gas to the first transfer part 161 because the first transfer part 161 is formed to move upward through the second transfer part 162. During the passage, heat is exchanged with the volatile organic compounds to preheat the volatile organic compounds.

상기 열교환부(160)는 가스배출부(112) 상에서 상하방향으로 이격되게 두 개가 형성되어 있으며, 공급관(10)은 두 개의 열교환부(160)를 차례로 통과하도록 연결되어 있기 때문에 휘발성 유기화합물은 연소실(111)로 공급되기 전에 두 번에 걸쳐 처리가스와 열교환을 통해 예열이 이루어지며, 예열된 휘발성 유기화합물은 연소실(111)에서 더욱 쉽게 산화처리가 이루어질 수 있으므로 휘발성 유기화합물의 처리 효율을 증대시킬 수 있다.Two heat exchangers 160 are formed on the gas discharge unit 112 so as to be spaced apart in the vertical direction. Since the supply pipe 10 is connected to pass through the two heat exchangers 160 in sequence, the volatile organic compounds are burned in the combustion chamber. Before being supplied to the (111) is preheated by heat exchange with the process gas twice, the preheated volatile organic compounds can be more easily oxidized in the combustion chamber 111, thereby increasing the treatment efficiency of the volatile organic compounds. Can be.

상기 허니컴 촉매장치(150)는 가스배출부(112)의 내부에 마련된 걸림턱에 지지되는 하우징(151)과, 하우징(151)에 설치되는 촉매블럭(157)을 구비한다.The honeycomb catalyst device 150 includes a housing 151 supported by a locking step provided in the gas discharge unit 112 and a catalyst block 157 installed in the housing 151.

상기 하우징(151)은 베이스부(152)와, 상기 베이스부(152)의 가장자리에서 상방으로 연장되는 측벽부(154)와, 상기 베이스부(152)에 설치되어 촉매블럭(157)을 지지하는 지지부(155)를 포함한다.The housing 151 has a base portion 152, a side wall portion 154 extending upward from an edge of the base portion 152, and installed on the base portion 152 to support the catalyst block 157. And a support 155.

상기 베이스부(152)는 상하면을 관통하는 복수개의 관통홀(153)들이 형성되어 있다.The base portion 152 is formed with a plurality of through holes 153 penetrating the upper and lower surfaces.

상기 측벽부(154)는 베이스부(152)의 가장자리에서 상방으로 연장되며 상기 가스배출부(112)의 내벽에 밀착되어 처리가스가 상기 베이스부(152)의 관통홀(153)을 통해서만 상방으로 이동할 수 있게 한다. 본 실시예에서는 도시되지 않았으나 상기 측벽부(154)의 외주면에는 가스배출부(112)의 내벽과의 밀착률을 높이기 위한 실링수단을 더 구비할 수 있다.The side wall part 154 extends upward from the edge of the base part 152 and is in close contact with the inner wall of the gas discharge part 112 so that the processing gas is directed upward only through the through hole 153 of the base part 152. Make it moveable. Although not shown in the present embodiment, the outer peripheral surface of the side wall portion 154 may further include a sealing means for increasing the adhesion rate with the inner wall of the gas discharge portion 112.

본 실시예에서는 판재형상의 베이스부(152)와 측벽부(154)를 개별적으로 생산한 다음 이를 용접을 통해 상호 결합하여 하우징(151)을 형성하였으나, 베이스부(152)와 측벽부(154)를 일체로 형성하는 것도 가능하다.In this embodiment, the base portion 152 and the side wall portion 154 of the plate shape are separately produced and then coupled to each other by welding to form the housing 151, but the base portion 152 and the side wall portion 154 It is also possible to form integrally.

상기 지지부(155)는 베이스부(152)의 상부에 장착되는 것으로 상하로 관통된 중공(156) 원통형으로 형성된다. 지지부(155)의 중공(156)은 상기 촉매블럭(157)의 외경에 대응하는 직경을 갖는 상부구간(156a)과, 상부구간(156a)의 하부에 형성되며 촉매블럭(157)의 외경에 비해 상대적으로 작은 직경을 갖는 하부구간(156b)으로 나뉘는데, 상부구간(156a)과 하부구간(156b)의 직경차이에 의해 그 경계부에는 단턱이 형성되며 촉매블럭(157)이 지지부(155)의 중공(156)으로 삽입되면 이 단턱에 지지된다. The support part 155 is mounted on the upper part of the base part 152 and is formed in a hollow 156 cylindrical shape that is vertically penetrated. The hollow 156 of the support portion 155 is formed in the upper section 156a having a diameter corresponding to the outer diameter of the catalyst block 157 and the lower portion of the upper section 156a and compared with the outer diameter of the catalyst block 157. It is divided into a lower section 156b having a relatively small diameter. A stepped portion is formed at the boundary due to the difference in diameter between the upper section 156a and the lower section 156b, and the catalyst block 157 is formed in the hollow of the support part 155. 156 is supported on this step.

도 5 및 도 6에는 허니컴 촉매장치(170)의 다른 실시예가 도시되어 있다.5 and 6 show another embodiment of the honeycomb catalytic apparatus 170.

본 실시예의 허니컴 촉매장치(170)는 베이스부(171)에 다수개의 관통홀(172)들이 형성되어 있는데, 상기 관통홀(172)의 직경이 촉매블럭(175)의 외경에 비해 상대적으로 작은 직경을 갖도록 되어 있다.In the honeycomb catalyst device 170 of the present embodiment, a plurality of through holes 172 are formed in the base portion 171, and the diameter of the through holes 172 is relatively smaller than the outer diameter of the catalyst block 175. It is supposed to have

촉매블럭(175)을 지지하기 위한 지지부(173)는 상기 베이스부(171)의 상면에 안착되는 판재형상으로 형성되며 상기 관통홀(172)들에 대응하는 위치에 다수의 지지홀(174)들이 형성되어 있다. 상기 지지홀(174)들은 촉매블럭(175)의 외경에 대응하는 직경을 갖도록 형성되어 있어서 이 지지홀(174)에 촉매블럭(175)을 끼우면 촉매블럭(175)의 하단 가장자리가 베이스부(171)의 상면에 지지되는 형태가 된다. The support 173 for supporting the catalyst block 175 is formed in the shape of a plate seated on the upper surface of the base portion 171 and a plurality of support holes 174 are formed at positions corresponding to the through holes 172. Formed. The support holes 174 are formed to have a diameter corresponding to the outer diameter of the catalyst block 175. When the catalyst block 175 is inserted into the support holes 174, the bottom edge of the catalyst block 175 is the base portion 171. ) Is supported on the upper surface.

도 2 내지 도 4에 도시된 실시예와 도 5 및 도 6에 도시된 실시예의 허니컴 촉매장치(150,170)는 모두 베이스부(152,171)의 관통홀(153,172)을 통해서만 처리가스가 상방으로 이동할 수 있으며 각각의 관통홀(153,172)들에 원통형의 촉매블럭(157,175)을 지지할 수 있는 지지부(155,173)가 형성되어 있어서 촉매블럭(157,175)을 원통형의 촉매블럭을 사각 또는 팔각기둥과 같은 각기둥 형태로 절단하지 않고도 사용할 수 있으며, 상기 촉매블럭을 지지하는 지지구조가 단순하여 촉매블럭의 설치 및 해체가 매우 용이하다. In the honeycomb catalyst devices 150 and 170 of the embodiment illustrated in FIGS. 2 to 4 and the embodiments illustrated in FIGS. 5 and 6, the processing gas may move upward only through the through holes 153 and 172 of the base parts 152 and 171. Support portions 155 and 173 capable of supporting cylindrical catalyst blocks 157 and 175 are formed in the respective through holes 153 and 172 to cut the catalyst blocks 157 and 175 into cylindrical columns such as square or octagonal columns. It can be used without, and the support structure for supporting the catalyst block is simple, it is very easy to install and dismantle the catalyst block.

그리고 상기 실시예들의 경우 촉매블럭이 원통형으로 형성된 것으로만 기재하고 도면에 도시했으나, 촉매블럭은 이 외에도 타원기둥 또는 다각기둥 형태로 초기 제작될 수도 있으며, 이 경우 지지부가 상기 촉매블럭의 단면형상에 대응하여 촉매블럭이 끼워질 수 있도록 형성되어 동일한 방법으로 사용될 수 있다. In the above embodiments, only the catalyst block is described as being formed in a cylindrical shape and is illustrated in the drawings, but the catalyst block may be initially manufactured in the form of an elliptic cylinder or a polygonal pillar, and in this case, the support part may have a cross-sectional shape of the catalyst block. Correspondingly, the catalyst blocks may be formed so that they can be fitted and used in the same manner.

100; 폐촉매를 이용한 휘발성 유기화합물 처리장치
110; 본체 120; 버너
130; 보조히터 140; 축열부
150; 허니컴 촉매장치
151; 하우징
152; 베이스부 154; 측벽부
155; 지지부
157; 촉매블럭
160; 열교환부100; Volatile Organic Compound Treatment System Using Waste Catalyst
110; A body 120; burner
130; Auxiliary heater 140; Heat storage unit
150; Honeycomb Catalyst
151; housing
152; Base portion 154; Side wall
155; Support
157; Catalyst Block
160; Heat exchanger

Claims (3)

처리대상 가스가 이동하는 이송부의 내부를 상기 처리가스가 이동하는 방향을 따라 상하로 구획하며, 구획된 상부와 하부를 상호 연통시키는 관통홀이 형성된 베이스부와;
상기 관통홀을 통해 통과하는 처리대상 가스를 정화하도록 상기 베이스부에 설치되는 촉매블럭과;
상기 촉매블럭이 상기 베이스부에 착탈 가능하게 결합되도록 상기 베이스부에 촉매블럭을 지지시키는 지지부;를 구비하는 것을 특징으로 하는 허니컴 촉매장치.A base part which partitions the inside of the conveying part through which the processing target gas moves up and down along the direction in which the processing gas moves, and has a through hole communicating the partitioned upper and lower parts with each other;
A catalyst block installed in the base unit to purify the gas to be processed passing through the through hole;
And a support part supporting the catalyst block on the base part such that the catalyst block is detachably coupled to the base part. 제 1항에 있어서,
상기 촉매블럭은 원통형, 타원기둥 또는 다각기둥 중 선택된 어느 하나의 형상으로 형성되고,
상기 지지부는 상하로 관통되며 상기 촉매블럭의 단면 형상에 대응하는 중공을 가지는 원통 또는 각기둥 형태로 형성되어 하단 외주면이 상기 관통홀에 끼워지거나 상기 관통홀의 상부에 위치하도록 상기 베이스부의 상면에 결합되며,
상기 중공은 상기 촉매블럭이 끼워질 수 있게 상기 촉매블럭의 외경에 대응하는 내경으로 상기 지지부의 상단으로부터 하방으로 소정길이 연장되는 상부구간과, 상기 상부구간의 하단으로부터 하방으로 연장되되 상기 상부구간에 비해 상대적으로 직경이 작은 하부구간으로 된 것을 특징으로 하는 허니컴 촉매장치.The method of claim 1,
The catalyst block is formed in the shape of any one selected from cylindrical, elliptic cylinder or polygonal pillar,
The support portion penetrates up and down and is formed in a cylindrical or prismatic shape having a hollow corresponding to the cross-sectional shape of the catalyst block, and is coupled to an upper surface of the base portion so that a lower outer peripheral surface is fitted into the through hole or positioned above the through hole.
The hollow has an upper section extending a predetermined length downward from the upper end of the support portion with an inner diameter corresponding to the outer diameter of the catalyst block so that the catalyst block can be fitted, and extending downward from the lower end of the upper section, Honeycomb catalytic device characterized in that the lower section compared to the relatively small diameter. 제 1항에 있어서,
상기 촉매블럭은 원통형, 타원기둥 또는 다각기둥 중 선택된 어느 하나의 형상으로 형성되고,
상기 베이스부의 관통홀은 상기 촉매블럭의 외경에 비해 상대적으로 작은 직경으로 형성되며,
상기 지지부는 상기 베이스부의 상면에 안착되되 상기 관통홀과 대응하는 위치에 상기 촉매블럭이 끼워질 수 있게 상기 촉매블럭의 단면형상에 대응하고 촉매블럭과 동일 직경으로 형성된 지지홀을 갖는 판재 형상으로 형성된 것을 특징으로 하는 허니컴 촉매장치.The method of claim 1,
The catalyst block is formed in the shape of any one selected from cylindrical, elliptic cylinder or polygonal pillar,
The through-hole of the base portion is formed with a relatively small diameter compared to the outer diameter of the catalyst block,
The support part may be seated on an upper surface of the base part and formed in a plate shape having a support hole corresponding to a cross-sectional shape of the catalyst block and having the same diameter as the catalyst block so that the catalyst block can be fitted at a position corresponding to the through hole. Honeycomb catalytic device, characterized in that.
KR1020110016910A 2011-02-25 2011-02-25 Honeycomb catalyst device KR20120097605A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180135367A (en) * 2017-06-12 2018-12-20 (주)대양이엔아이 Small city hazardous gas process unit
KR20200021013A (en) * 2018-08-16 2020-02-27 (주)대양이엔아이 Hazardous gas process unit for cofeee roasting

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180135367A (en) * 2017-06-12 2018-12-20 (주)대양이엔아이 Small city hazardous gas process unit
KR20200021013A (en) * 2018-08-16 2020-02-27 (주)대양이엔아이 Hazardous gas process unit for cofeee roasting

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