JP2001201033A - Exhaust gas processor having honeycomb-type molded item and its clogging preventive method - Google Patents

Exhaust gas processor having honeycomb-type molded item and its clogging preventive method

Info

Publication number
JP2001201033A
JP2001201033A JP2000008488A JP2000008488A JP2001201033A JP 2001201033 A JP2001201033 A JP 2001201033A JP 2000008488 A JP2000008488 A JP 2000008488A JP 2000008488 A JP2000008488 A JP 2000008488A JP 2001201033 A JP2001201033 A JP 2001201033A
Authority
JP
Japan
Prior art keywords
honeycomb
exhaust gas
sphere
heat storage
gas treatment
Prior art date
Legal status (The legal status 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 status listed.)
Granted
Application number
JP2000008488A
Other languages
Japanese (ja)
Other versions
JP4155542B2 (en
Inventor
Satoshi Sekihara
智 関原
Yasuyuki Aiura
恭幸 相浦
Akira Beppu
暁 別府
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Soda Co Ltd
Original Assignee
Nippon Soda Co Ltd
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 Nippon Soda Co Ltd filed Critical Nippon Soda Co Ltd
Priority to JP2000008488A priority Critical patent/JP4155542B2/en
Publication of JP2001201033A publication Critical patent/JP2001201033A/en
Application granted granted Critical
Publication of JP4155542B2 publication Critical patent/JP4155542B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Air Supply (AREA)
  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method of efficiently preventing the clogging caused by dust, without degrading catalyst efficiency or heat efficiency, in a honeycomb type of molded catalyst for processing the exhaust gas including fine particles such as dust, or in the honeycomb type of molded heat accumulator of a heating deodorizing furnace used for processing of the similar exhaust gas. SOLUTION: Spheres are arranged on one side or both sides of a honeycomb type of molded item, and the spheres shift properly up and down and right and left on the honeycomb molded item by the balance between the force of gas flowing in and/or flowing out and the dead weight of the spheres, and deposits are wiped off or scattered by the shock or friction at that time.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ハニカム型成形体
を有する粉塵を含む排ガス処理装置に関し、更に詳しく
は排ガス中に含まれる可燃性有害成分や可燃性悪臭成分
を触媒燃焼又は直接燃焼させて無害無臭な物質に変化さ
せると共にその際に生ずる熱を回収して排ガス処理に再
利用するハニカム型成形体を有する蓄熱型排ガス処理装
置に関し、更には、前記のハニカム型成形体の目詰防止
方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment device containing dust having a honeycomb-shaped formed body, and more particularly, to catalytic combustion or direct combustion of combustible harmful components and combustible malodorous components contained in exhaust gas. The present invention relates to a heat storage type exhaust gas treatment apparatus having a honeycomb type molded body for converting into a harmless and odorless substance and recovering heat generated at that time and reusing it for exhaust gas treatment, and further relates to a method for preventing clogging of the honeycomb molded body. About.

【0002】[0002]

【従来の技術】排ガス中に含まれる可燃性有害成分や可
燃性悪臭成分を触媒燃焼又は直接燃焼させて無害無臭な
物質に変化させる装置として、熱交換器付き直接燃焼
式、触媒式の装置等が知られているが、中でもその熱効
率の点から蓄熱式の装置が最近注目されている。
2. Description of the Related Art As a device for converting flammable harmful components and flammable odor components contained in exhaust gas into harmless and odorless substances by catalytic combustion or direct combustion, such as a direct combustion type with a heat exchanger, a catalytic type device, etc. Among them, a heat storage type device has recently been receiving attention from the viewpoint of its thermal efficiency.

【0003】蓄熱式装置に用いられる蓄熱体の構造とし
ては、種々の形が提案されているが、熱効率が優れてい
るという点でハニカム構造を有する蓄熱体が多く用いら
れている。また、触媒式装置においても、触媒効率が優
れていることから、同様にハニカム型の成形触媒が多く
用いられている。
[0003] Various structures have been proposed for the structure of the heat storage element used in the heat storage type apparatus, but a heat storage element having a honeycomb structure is often used because of its excellent thermal efficiency. Also, in a catalytic device, a honeycomb-type formed catalyst is similarly used in many cases because of excellent catalytic efficiency.

【0004】しかし、発電ボイラー、内燃機関、コーク
ス炉、焼却炉等の種々の工場プロセス排ガス中には、可
燃性有害成分や可燃性悪臭成分以外にもダスト等の微細
粒が置く含まれており、ダストによるハニカム成形体開
口部の閉塞に伴う圧損の増大、それに伴うエネルギー消
費量の増大等の問題を引き起こしていた。
[0004] However, various factory process exhaust gases from power boilers, internal combustion engines, coke ovens, incinerators, and the like contain fine particles such as dust in addition to combustible harmful components and combustible malodorous components. This has caused problems such as an increase in pressure loss due to the blockage of the honeycomb formed body opening due to dust and an increase in energy consumption.

【0005】上記閉塞を防止するために、(イ)ハニカ
ム成形体の開口部を大きくする、(ロ)ハニカム成形体
の壁厚を薄くする、(ハ)スートブローを頻繁に行う等
の方法が考えられるが、上記(イ)の方法では、熱効
率、触媒効率を下げる結果、全容量を大きくする必要が
あり、(ロ)の方法ではハニカム成形体の機械的強度が
低下し、更に(ハ)の方法では、経済的理由と共に、ハ
ニカム成形体の強度をやはり弱めることなる。
In order to prevent the above-mentioned blockage, there are conceivable methods such as (a) increasing the opening of the honeycomb formed body, (b) reducing the wall thickness of the honeycomb formed body, and (c) frequent soot blowing. However, in the above method (a), the thermal efficiency and the catalyst efficiency are lowered, and as a result, the total capacity needs to be increased. In the method (b), the mechanical strength of the honeycomb formed body is reduced, and further, in the method (c). The method also reduces the strength of the honeycomb formed body, together with economic reasons.

【0006】特開昭57−50532号公報には、ハニ
カム型成形触媒のガス流入口の前面に、このハニカム型
成形触媒の横断面と同一又は相似のハニカム断面形状を
有し、その壁厚がハニカム型成形触媒の壁厚よりも厚く
なく、かつハニカム型成形触媒と接する側の壁の厚さが
ハニカム型成形触媒の壁厚より薄くない耐熱性基材から
なるハニカム形状の保護具を、上記ハニカム型成形触媒
の流入口又は流出口に、緊密に接触した状態、10mm
以内に離れた状態又ははかまのように被せた状態で、か
つ上記ハニカム型触媒と上記保護具とのハニカム形状が
実質的に重なるように取り付けることによりダストが堆
積するのを防止できることが記載されている。
Japanese Patent Application Laid-Open No. 57-50532 discloses a honeycomb shaped catalyst having a honeycomb cross-sectional shape which is the same as or similar to the cross-sectional shape of the honeycomb shaped catalyst at the front surface of the gas inlet. A honeycomb-shaped protector made of a heat-resistant base material that is not thicker than the wall thickness of the honeycomb-shaped catalyst, and the thickness of the wall in contact with the honeycomb-shaped catalyst is not thinner than the wall thickness of the honeycomb-shaped catalyst, 10 mm in close contact with the inlet or outlet of the honeycomb shaped catalyst
It is described that dust can be prevented from being deposited by attaching the honeycomb type catalyst and the protector so that the honeycomb shapes are substantially overlapped with each other in a state where they are separated from each other or as a hook. I have.

【0007】しかし、上記保護具を実質的にハニカム型
成形触媒に密着させることは技術に難しく、又同一又は
相似のハニカム断面形状を有する保護具はその形状によ
っては困難な場合がある。また、ハニカム型の成形体
は、その機械的強度の関係及び焼結生成時の熱による歪
みの問題から構造上縦方向の長さに制限があり、熱効
率、触媒効率を考えた場合、ハニカム型成形体を複数段
に積層して用いる場合がある。この場合、各層の中間を
完全に密着させることが困難であり、その結果、各層に
ダストが堆積する問題が生じる。このような場合には、
上記の方法ではこの問題を解決することは困難であっ
た。
However, it is technically difficult to make the above-mentioned protector substantially adhere to the honeycomb molded catalyst, and a protector having the same or similar honeycomb sectional shape may be difficult depending on the shape. In addition, the honeycomb molded body has a structurally limited longitudinal length due to its mechanical strength and the problem of distortion due to heat generated during sintering. In some cases, the compacts may be used in a plurality of layers. In this case, it is difficult to completely adhere the middle of each layer, and as a result, there is a problem that dust is deposited on each layer. In such a case,
It has been difficult to solve this problem by the above method.

【0008】本発明は、ダスト等の微細粒の含む排ガス
を処理するハニカム型成形触媒又は同様の排ガスの処理
に用いられる加熱脱臭炉のハニカム型成形蓄熱体におい
て、触媒効率又は熱効率を損なうことなく効率的にダス
トによる目詰を防止する方法を提供するものである。
The present invention relates to a honeycomb-type molded catalyst for treating exhaust gas containing fine particles such as dust or a honeycomb-type molded heat storage element of a heating deodorizing furnace used for treating similar exhaust gas without impairing the catalyst efficiency or thermal efficiency. An object of the present invention is to provide a method for efficiently preventing clogging due to dust.

【0009】[0009]

【課題を解決するための手段】本発明者等は上記課題を
解決すべく鋭意検討した結果、ハニカム型成形体の片面
又は両面に球体を配し、ガスの流入及び/又は流出する
力と球体の自重とのバランスによりハニカム成形体上で
球体が上下左右に適度に移動し、その際の衝撃又は摩擦
で堆積物を拭き取る若しくは飛散させることができるこ
とを見出し本発明を完成するに至った。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and as a result, arranged a sphere on one side or both sides of a honeycomb molded body, the force for inflow and / or outflow of gas and the sphere. It has been found that the sphere moves appropriately up, down, left, and right on the honeycomb formed body due to the balance with its own weight, and that the deposit can be wiped or scattered by the impact or friction at that time, and the present invention has been completed.

【0010】即ち、本発明は、ハニカム型成形体を有す
る排ガス処理装置であって、ハニカム型成形体の片面及
又は両面に球体を配したことを特徴とする排ガス処理装
置(請求項1)に関し、更に詳しくはハニカム型成形体
を有する排ガス処理装置であって、ハニカム型成形体が
複数段に積層されて用いられ、その複数段全体の片面又
は両面、並びに各段の中間に球体を配することを特徴と
する排ガス処理装置(請求項2)に関する。
That is, the present invention relates to an exhaust gas treating apparatus having a honeycomb molded body, wherein a spherical body is arranged on one side or both sides of the honeycomb molded body (claim 1). More specifically, an exhaust gas treatment apparatus having a honeycomb-shaped formed body, wherein the honeycomb-shaped formed body is used by being stacked in a plurality of stages, and a sphere is disposed on one or both surfaces of the entire plurality of stages, and in the middle of each stage. The present invention relates to an exhaust gas treatment device (claim 2).

【0011】また、球体の周囲を囲む壁を設けたことを
特徴とする請求項1又は2に記載の排ガス処理装置(請
求項3)に関し、単一又は複数段に積層されたハニカム
型成形体が上下方向に配置されたおり、かつハニカム型
成形体の最下面に球体を支持する網目状構造体を設けた
ことを特徴とする請求項1〜3のいずれかに記載の排ガ
ス処理装置(請求項4)に関する。
The exhaust gas treatment apparatus according to claim 1 or 2, wherein a wall surrounding the periphery of the sphere is provided, and the honeycomb molded body is stacked in a single or multiple stages. The exhaust gas treatment device according to any one of claims 1 to 3, wherein a mesh-like structure supporting the sphere is provided on the lowermost surface of the honeycomb molded body. Regarding item 4).

【0012】更に、燃焼室に連通した複数の部屋に単一
又は複数段に積層されたハニカム型成形体が蓄熱体とし
て配置されており、各部屋に対して被処理ガスの供給、
パージガスの供給、及び燃焼室内で酸化分解した処理ガ
スの排気を順次切り換えながら排ガスを処理することを
特徴とする請求項1〜4に記載の排ガス処理装置(請求
項5)に関する。
[0012] Further, a honeycomb-shaped formed body stacked in a single or a plurality of stages is arranged as a heat storage in a plurality of chambers communicating with the combustion chamber, and supply of a gas to be processed to each chamber is performed.
The exhaust gas processing apparatus according to any one of claims 1 to 4, wherein the exhaust gas is processed while sequentially switching the supply of the purge gas and the exhaust of the processing gas oxidized and decomposed in the combustion chamber.

【0013】また、球体の最大幅がハニカム型成形体の
各開口部の最大幅よりも大きいことを特徴とする請求項
1〜5のいずれかに記載の排ガス処理装置(請求項
6)、球体がセラミックス製であることを特徴とする請
求項1〜6のいずれかに記載の排ガス処理装置(請求項
7)、また球体をハニカム型成形体単体開口部に対して
0.2〜0.7個用いることを特徴とする請求項1〜7
のいずれかに記載の排ガス装置(請求項8)に関する。
The exhaust gas treatment apparatus according to any one of claims 1 to 5, wherein the maximum width of the sphere is larger than the maximum width of each opening of the honeycomb molded body. The exhaust gas treatment apparatus according to any one of claims 1 to 6, wherein the sphere is made of ceramics. 8. The method according to claim 1, wherein the number is used.
The present invention relates to an exhaust gas device according to any one of claims 1 to 7.

【0014】また、排ガスが粉塵を含む排ガスであるこ
とを特徴とする請求項1〜8のいずれかに記載の排ガス
処理装置(請求項9)に関する。更に、ハニカム型成形
体を有する排ガス処理装置において、ハニカム型成形体
の片面又は両面に球体を配し、ガスの流入及び/又は流
出に伴って前記球体が上下及び/又は左右に移動するこ
とによりハニカム成形体の各開口部の堆積物を除去する
ことを特徴とするハニカム型成形体の目詰防止方法(請
求項10)に関する。
Further, the present invention relates to an exhaust gas treating apparatus according to any one of claims 1 to 8, wherein the exhaust gas is an exhaust gas containing dust. Furthermore, in an exhaust gas treatment device having a honeycomb-shaped formed body, a sphere is arranged on one or both sides of the honeycomb-shaped formed body, and the sphere moves up and down and / or left and right with the inflow and / or outflow of gas. The present invention relates to a method for preventing clogging of a honeycomb molded body, which comprises removing deposits at openings of the honeycomb molded body.

【0015】[0015]

【発明の実施の形態】本発明に用いられるハニカム型成
形体は、排ガス処理装置においては、蓄熱体として用い
られ、更に成形体各セルの内壁に触媒をコーティングす
ることにより又は材質中に触媒を混合して成形すること
により触媒として機能する。ハニカム型成形体は、例え
ば、コージライト磁器などで形成される単体を平面状に
並列させて形成される。ハニカム単体は、通常、高さが
5〜30cmで、成形体全体の開口密度は、熱効率又は
触媒効率を考慮して、50〜400セル/inch2
比較的細かいものが用いられる。また、セルの開口部の
形状は、三角形、四角形、六角形、八角形等の多角形、
その他円形、サインウエーブ等どのような形状であって
もよいが、四角形が製作上好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The honeycomb molded body used in the present invention is used as a heat storage body in an exhaust gas treatment device, and the catalyst is coated on the inner wall of each cell of the molded body or the catalyst is contained in the material. It functions as a catalyst by mixing and molding. The honeycomb molded body is formed by, for example, arranging single bodies made of cordierite porcelain or the like in parallel in a plane. The honeycomb single body usually has a height of 5 to 30 cm and a relatively fine opening density of the whole formed body of 50 to 400 cells / inch 2 in consideration of thermal efficiency or catalytic efficiency. In addition, the shape of the opening of the cell is a polygon such as a triangle, a square, a hexagon, and an octagon,
Other shapes such as a circle and a sign wave may be used, but a quadrangle is preferable in terms of manufacturing.

【0016】ハニカム型成形体は、単一で用いることも
できるが、熱効率、触媒活性等を考慮して複数段に積層
して使用することもできる。積層する場合、各段の間を
密着して用いることもできるが、完全に密着させること
が技術的に困難であることから適度な空間を設けること
もできる。その際、図3に示すように各段の中間に空間
を確保するためにスペーサー31を配置することができ
る。スペーサーの形状、大きさ、高さ、材質、数量は、
各段を一定の位置に支持することができれば特に制限さ
れない。具体的には、ハニカム成形体が150mm四方
の場合、直径10mmの丸棒で外枠130mm、内枠1
10mmの正方形の枠を例示することができる。ハニカ
ム成形体を確実に積層させるため、成形体の外周よりも
若干小さ目の大きさに設定するのが好ましい。また、ス
ペーサーは球体の飛散を防止する壁の役割をすることに
なる。
The honeycomb molded body may be used alone, but may be used in a plurality of layers in consideration of thermal efficiency, catalytic activity and the like. When laminating, it is possible to use the layers in close contact with each other, but since it is technically difficult to achieve complete close contact, an appropriate space can be provided. At that time, as shown in FIG. 3, a spacer 31 can be arranged in the middle of each step to secure a space. The shape, size, height, material and quantity of the spacer
There is no particular limitation as long as each step can be supported at a fixed position. Specifically, when the honeycomb formed body is 150 mm square, an outer frame 130 mm and an inner frame 1
An example is a 10 mm square frame. In order to reliably stack the honeycomb formed body, it is preferable to set the size to be slightly smaller than the outer periphery of the formed body. The spacer also functions as a wall for preventing the sphere from scattering.

【0017】ハニカム型成形体を縦型に配置し下部に球
体を設けた場合、例えば図2に示すように球体を保持す
る網目状構造体23を設置することができる。網目状構
造体23は、球体を保持できるだけの目の粗さがあれば
特に制限されず、材質はセラミック、金属等の耐熱性の
ある材質であればどんなものでも用いることができる。
When the honeycomb molded body is arranged vertically and a sphere is provided at the lower part, a mesh structure 23 for holding the sphere can be provided as shown in FIG. 2, for example. The mesh structure 23 is not particularly limited as long as the mesh has enough roughness to hold a sphere, and any material can be used as long as it is a heat-resistant material such as ceramic or metal.

【0018】網目構造体は、開口面に対して、球体の最
大幅よりも長い距離で、しかも球体が排ガスの流入出に
伴って上下左右運動し開口部に接触できるような位置に
配するのが好ましい。また、前記網目構造体とハニカム
成形体の間に、先に述べたと同様の働きをするスペーサ
ーを設けることができる。
The mesh structure is disposed at a distance longer than the maximum width of the sphere with respect to the opening surface, and at a position where the sphere moves up and down, left and right with the inflow and outflow of exhaust gas, and can contact the opening. Is preferred. In addition, a spacer having the same function as described above can be provided between the network structure and the honeycomb formed body.

【0019】ハニカム型成形体を有する排ガス処理装置
は、例えば、図1に示すように、燃焼室に連通した複数
の部屋に単一又は複数段に積層したハニカム型成形体を
有し、各部屋に対して被処理ガスの供給、パージガスの
供給、及び燃焼室内で酸化分解した処理ガスの排気を順
次切り換えながら排ガスを処理する装置を例示すること
ができる。
As shown in FIG. 1, for example, an exhaust gas treatment apparatus having a honeycomb-shaped formed body has a honeycomb-shaped formed body stacked in a single or a plurality of stages in a plurality of chambers communicating with a combustion chamber. In contrast, an apparatus that treats exhaust gas while sequentially switching the supply of the gas to be treated, the supply of the purge gas, and the exhaust of the oxidatively decomposed processing gas in the combustion chamber can be exemplified.

【0020】上記3つの動作は、ある一定間隔をおいて
切り替えることにより行うこともできるが、後述するよ
うに特殊なロータリー分配弁等を用いて連続的に行うこ
ともできる。連続的に切り替えた場合の方が、球体の運
動を促進し除去効果を向上させることができる。
The above three operations can be performed by switching at certain intervals, but can be performed continuously using a special rotary distribution valve or the like as described later. In the case of continuous switching, the movement of the sphere can be promoted and the removal effect can be improved.

【0021】図1を用いて、更に詳しく説明する。図1
において便宜上蓄熱型排ガス処理装置として説明を行う
が、ハニカム型成形体を蓄熱体としてではなく触媒とし
て用いることもできる。図1においては、内部にハニカ
ム型蓄熱体(3a、3b)を上下2段に配した蓄熱室
(2A、2B、2C)とこれら蓄熱室の頂部と連通した
燃焼室5とを備え、各蓄熱室2A、2B、2Cの底部に
は、被処理ガス供給管7、処理ガス排出管8及びパージ
ガス供給管9の各分枝管をそれぞれ接続してあり、前記
燃焼室5にはバーナ6を設けてある。上部蓄熱体3bの
表面、上部蓄熱体3bと下部蓄熱体3aの中間4、下部
蓄熱体の下面にはセラミック製の小球が設けられてお
り、下部蓄熱体の下部に設けられた小球を支持するため
に、網目状セラミック板16が設けられている。また、
4及び3aと16の間にスペーサーが設置されている。
This will be described in more detail with reference to FIG. FIG.
For convenience, a description will be given as a heat storage type exhaust gas treatment apparatus, but a honeycomb formed body may be used as a catalyst instead of a heat storage body. In FIG. 1, heat storage chambers (2A, 2B, 2C) in which honeycomb-type heat storage bodies (3a, 3b) are arranged in two stages above and below, and a combustion chamber 5 communicating with the top of these heat storage chambers are provided. At the bottoms of the chambers 2A, 2B and 2C, respective branch pipes of a gas supply pipe 7, a processing gas discharge pipe 8 and a purge gas supply pipe 9 are connected, respectively, and a burner 6 is provided in the combustion chamber 5. It is. Ceramic small balls are provided on the surface of the upper heat storage element 3b, the middle 4 between the upper heat storage element 3b and the lower heat storage element 3a, and the lower surface of the lower heat storage element. A reticulated ceramic plate 16 is provided for support. Also,
Spacers are installed between 4 and 3a and 16.

【0022】被処理ガスは、まず蓄熱室2Aに入れられ
熱を加えられた蓄熱体部を上昇通過することで予熱され
その後、高温雰囲気下の燃焼室で酸化分解されクリーン
なガスとなり、蓄熱室2Bの蓄熱体部を下降通過しなが
ら蓄熱体に熱を与えて排気される。
The gas to be treated is first preheated by ascending and passing through the heat storage section heated and heated in the heat storage chamber 2A, and then oxidized and decomposed in a combustion chamber under a high-temperature atmosphere to become a clean gas. Heat is given to the heat storage body while passing down through the heat storage part of 2B, and exhausted.

【0023】その間蓄熱2Cではクリーンなガスを導入
し、1サイクル前の処理で配管や蓄熱室に滞留している
未処理ガスを上方へパージし燃焼室で酸化分解され、蓄
熱室2Bを経由して排気される。第1サイクルで一定時
間経過後、処理ガスとパージガスのバルブを切り換える
ことにより、第1サイクルでは処理ガス入側であった蓄
熱室2Aがパージとなり、蓄熱体は降温→除冷状態に、
クリーンガス出側であった蓄熱室2Bが処理ガス入側に
なり蓄熱体は昇温→降温状態に、パージであった蓄熱室
2Cがクリーンガス出側になり蓄熱体は除冷→昇温状態
になる。尚、第1図における各切換弁12a、12b、
12c、13a、13b、13c及び14a、14b、
14cにおいて□は開状態、■は閉状態を示し、第1図
は上記した第1サイクルの状態を示す図である。
In the meantime, in the heat storage 2C, a clean gas is introduced, and the unprocessed gas remaining in the pipe or the heat storage chamber is purged upward in the processing one cycle before, oxidized and decomposed in the combustion chamber, and passed through the heat storage chamber 2B. Exhausted. After a certain period of time has passed in the first cycle, the valves for the processing gas and the purge gas are switched, so that the heat storage chamber 2A, which was on the processing gas inlet side in the first cycle, is purged, and the heat storage body is cooled down to a de-cooled state.
The heat storage chamber 2B, which was on the clean gas outlet side, is on the processing gas inlet side, and the heat storage body has been heated to a temperature-lowering state, and the heat storage chamber 2C, which has been purged, has been on the clean gas outlet side, and the heat storage body has been de-cooled → the temperature has been raised. become. In addition, each switching valve 12a, 12b in FIG.
12c, 13a, 13b, 13c and 14a, 14b,
In FIG. 14c, □ indicates an open state, Δ indicates a closed state, and FIG. 1 is a view illustrating the state of the first cycle described above.

【0024】第2サイクルで一定時間経過後、再び処理
ガスとパージガスバルブを切り換え、第2サークルでは
パージであった蓄熱室2Aがクリーンガス出側となり、
蓄熱体は除冷→昇温状態に、処理ガス入側であった蓄熱
室2Bがパージとなり、蓄熱体は降温→除冷状態に、ク
リーンガス出側であった蓄熱室2Cが処理ガス入側とな
り蓄熱体は昇温→降温状態になる。この状態が一定時間
経過後、再びバルブを切り換えることにより、元の第1
サイクルに戻り、順次このシーケンスを繰り返すこと
で、被処理ガスを効率よく加熱酸化分解できる。
After a lapse of a predetermined time in the second cycle, the processing gas and the purge gas valve are switched again, and in the second circle, the heat storage chamber 2A, which has been purged, becomes the clean gas outlet side,
The heat storage body is de-cooled → increased temperature, the heat storage chamber 2B on the processing gas inlet side is purged, and the heat storage body is cooled → de-cooled state, and the heat storage chamber 2C on the clean gas output side is processed gas inlet side. The temperature of the heat storage body changes from a temperature rise to a temperature fall. After this state has passed for a certain period of time, by switching the valve again, the original first
By returning to the cycle and sequentially repeating this sequence, the gas to be treated can be efficiently heated and oxidized and decomposed.

【0025】本発明の方法は、例えば図2に示すように
各蓄熱室への被処理ガスの供給、パージガスの供給、処
理ガスの排出を回転式の切り換え弁(分配弁)により順
次切り換える構成とした処理装置にも容易に採用するこ
とができる。また、ハニカム型成形体が蓄熱体のみなら
ず、ハニカム型触媒においても適用することができる。
The method of the present invention has a structure in which the supply of the gas to be processed, the supply of the purge gas, and the discharge of the processing gas to each heat storage chamber are sequentially switched by a rotary switching valve (distribution valve) as shown in FIG. It can be easily adopted in the processing apparatus which has been used. Further, the present invention can be applied not only to a heat storage body of a honeycomb molded body but also to a honeycomb catalyst.

【0026】図2において、各蓄熱室17に連通する開
口28aを有する固定弁28と、該固定弁28と対向配
置され、それぞれ図示しない被処理ガス供給用開口、パ
ージガス供給用開口、及び処理ガス排出用開口を、周方
向に所定間隔をあけて設けた回転弁32からなる切換弁
33を取り付けている。また、被処理ガス供給管18を
接続する一方、回転弁32を回転可能に支持する支持体
19には処理ガス排出管34、及びパージガス管20を
接続している。このようにすれば、各蓄熱室17に対し
て回転弁32の回転により、被処理ガスの供給、パージ
ガスの供給、及び処理ガスの排出を順次切り換えること
ができる。
In FIG. 2, a fixed valve 28 having an opening 28a communicating with each of the heat storage chambers 17, and a processing gas supply opening, a purge gas supply opening (not shown), and a processing gas A switching valve 33 composed of a rotary valve 32 having a discharge opening provided at a predetermined interval in a circumferential direction is attached. The processing gas discharge pipe 34 and the purge gas pipe 20 are connected to the support 19 that rotatably supports the rotary valve 32, while the processing gas supply pipe 18 is connected. In this way, the supply of the gas to be processed, the supply of the purge gas, and the discharge of the processing gas can be sequentially switched by rotating the rotary valve 32 with respect to each heat storage chamber 17.

【0027】なお、固定弁28の各開口28aと各蓄熱
室17とは、図2(B)に示すように、各蓄熱室17の
下部にダクト25を設け、固定弁28の各開口28aを
塞ぐように設けたフランジ27とダクト25を配管26
で連通し、開口28aと蓄熱室17が1対1で対応する
ように接続すればよい。
As shown in FIG. 2B, each opening 28a of the fixed valve 28 and each heat storage chamber 17 are provided with a duct 25 at a lower portion of each heat storage chamber 17, and each opening 28a of the fixed valve 28 is connected to each other. A pipe 26 connects the flange 27 and the duct 25 provided so as to close the pipe.
And the heat storage chamber 17 may be connected so as to correspond one-to-one.

【0028】用いる球体の大きさは、その最大幅がハニ
カム型成形体の各単位開口部の最大幅よりも大きければ
特に制限されないが、排ガスの流入又は流出速度と球体
の自重を考慮してして球体が、適度の運動を行える大き
さに調節する。例えば、ハニカム型成形体の各単位開口
部最大幅の1.1倍〜4倍くらいの最大幅を有する球体
が好ましい。
The size of the sphere used is not particularly limited as long as its maximum width is larger than the maximum width of each unit opening of the honeycomb molded body. However, the size of the sphere is taken into consideration in consideration of the inflow or outflow speed of exhaust gas and the weight of the sphere. Adjust the size of the sphere so that it can exercise moderately. For example, a sphere having a maximum width of about 1.1 to 4 times the maximum width of each unit opening of the honeycomb molded body is preferable.

【0029】球体の形状は真球である必要はなく、多少
楕円状に変形しているものでも使用することができる。
また、球体の重量を考慮して中空状の球体を使用するこ
ともできる。また、排ガスの流れを拡散させて球体の運
動を促進するために表面に凹凸を設けたり、中空状の球
体の表面に貫通する小孔を1つ以上設けることもでき
る。
The shape of the sphere does not need to be a true sphere, and any shape which is slightly elliptical can be used.
Alternatively, a hollow sphere can be used in consideration of the weight of the sphere. Further, in order to diffuse the flow of the exhaust gas to promote the movement of the sphere, irregularities may be provided on the surface, or one or more small holes penetrating the surface of the hollow sphere may be provided.

【0030】材質は、耐熱性があれば特に制限されず、
セラミック、金属等いずれも使用することができるが、
耐摩耗性等を考慮した場合、セラミックが好ましい。用
いる球体の数は、特に制限されないが、ハニカム型成形
体単体開口部に対して0.2〜0.7個用いるのが好ま
しい。
The material is not particularly limited as long as it has heat resistance.
Any of ceramic, metal, etc. can be used,
Ceramics are preferred in consideration of wear resistance and the like. Although the number of spheres to be used is not particularly limited, it is preferable to use 0.2 to 0.7 spheres for the opening of the single honeycomb molded body.

【0031】本発明の方法は、あらゆる排ガスを処理す
る装置に適用が可能であるが、特に微粒子の粉塵を多く
含む排ガスの処理において顕著な効果を有する。粉塵と
しては、煤煙、塩、等が挙げられる。
The method of the present invention can be applied to any equipment for treating exhaust gas, but has a remarkable effect particularly in the treatment of exhaust gas containing a large amount of fine particles. Examples of the dust include soot, salt, and the like.

【0032】粉塵を多く含む排ガスがハニカム型成形体
を通過し排出される際、急激に拡散することから気流の
乱れが生じ、粉塵の多くはガスの排出口付近に堆積す
る。各セルの流路は通常1〜2mm前後であり、多量の
粉塵が連続的に排出された場合、すぐに各流路は堆積し
た粉塵で塞がれ、大きな圧損を生じることとなる。この
場合、本発明の球体を開口面に配することで、例えば、
排ガスの流出に伴って球体が緩やかに吹き上げられ、自
重もしくは球体の回転による気流の乱れにより、球体は
開口面上を上下左右に移動し、その際の衝撃、摩擦等に
より、堆積した粉塵を巻き上げることで、目詰りを防ぐ
ことができる。
When the exhaust gas containing a large amount of dust passes through the honeycomb molded body and is discharged, it rapidly diffuses, causing turbulence in the air flow, and most of the dust is deposited near the gas outlet. The flow path of each cell is usually about 1 to 2 mm, and when a large amount of dust is continuously discharged, each flow path is immediately blocked by the accumulated dust, causing a large pressure loss. In this case, by arranging the sphere of the present invention on the opening surface, for example,
The sphere is gently blown up due to the outflow of exhaust gas, and the sphere moves up, down, left, and right on the opening surface due to its own weight or turbulence of the air flow due to rotation of the sphere, and the accumulated dust is taken up by impact, friction, etc. This can prevent clogging.

【0033】ハニカム型成形体を数段積層し中間にスペ
ーサーを設けた場合、そのスペーサー内に球体を配置す
ることにより、球体の偏りや飛散を防ぐことができ目詰
防止効果を上げることができる。
When a plurality of honeycomb molded bodies are stacked and a spacer is provided in the middle, by disposing the spheres in the spacers, the spheres can be prevented from being biased or scattered, and the effect of preventing clogging can be improved. .

【0034】[0034]

【実施例】以下実施例により詳細に説明するが、本発明
の技術的範囲はかかる実施例により限定されるものでは
ない。
EXAMPLES The present invention will be described in detail below with reference to examples, but the technical scope of the present invention is not limited to these examples.

【0035】実施例 100セル/inch2のハニカム状で大きさが150
mm×150mm×150mm蓄熱体と100セル/i
nch2のハニカム状で大きさが150mm×150m
m×300mm蓄熱体を上下2段に重ね、下段の蓄熱体
の下には高さ10mmの間隔でセラミック製の網を配置
した。上下蓄熱体の中間及び下部蓄熱体とその下に設け
られた網との中間に太さ10mmの丸棒を角の部分のみ
が互いに接触するように敷き並べ、真四角状のスペーサ
ーとして、そのような蓄熱室を8室有する処理装置を用
いた。各部屋を順番に1〜8とした場合、ガス供給→ガ
ス排出→ガスパージの工程を1、2、3→4、5、6→
7、8の組み合わせで順次サイクルして行う。各ハニカ
ム蓄熱体の上部、中間、及び下部に直径4〜6ミリのセ
ラミックボールを3.1kgづつ配した。炭酸カルシウ
ムを凡そ15mg/m 3含む排ガスを蓄熱体に入る手前
で130℃まで加熱し、更に蓄熱体上段上面部での断面
風速が4m/秒になるように調節してガス導入し、燃焼
室の温度が800℃に維持されているハニカム型蓄熱体
中を通し、上部燃焼室で酸化分解した場合に、連続運転
2ヶ月でも圧損は上昇せずに運転可能であった。また、
セラミックの小球を設けたことによる熱効率の低下は見
られなかった。排ガスと一緒に排出された粉塵は別の集
塵装置により捕集した。
Embodiment 100 cells / inchTwoHoneycomb shape and size 150
mm × 150mm × 150mm heat storage unit and 100 cells / i
nchTwoThe size is 150mm x 150m with honeycomb shape of
mx300mm heat storage body is stacked on the upper and lower two layers, the lower one
Ceramic nets are placed at 10mm height intervals below
did. Middle and lower thermal storage of upper and lower thermal storage and below
A round bar with a thickness of 10 mm in the middle of the net
Are arranged so that they are in contact with each other, and a square spacer
Used a processing apparatus having eight such heat storage chambers.
Was. When each room is set to 1 to 8 in order, gas supply → gas
Discharge → gas purge process 1, 2, 3 → 4, 5, 6 →
Cycles are sequentially performed with a combination of 7 and 8. Each Hanika
In the upper, middle and lower part of the heat storage
3.1 kg of lamic balls were placed. Calcium carbonate
About 15mg / m ThreeBefore exhaust gas containing heat enters heat storage
And heat up to 130 ° C.
Introduce gas by adjusting the wind speed to 4m / sec and burn
Honeycomb regenerator with room temperature maintained at 800 ° C
Continuous operation when oxidized and decomposed in the upper combustion chamber through the inside
The operation was possible without increasing the pressure loss even in two months. Also,
The decrease in thermal efficiency due to the provision of ceramic globules is not
I couldn't. The dust discharged with the exhaust gas is collected separately.
Collected with a dust device.

【0036】比較例 セラミックの小球を設けない以外は実施例と同様にして
排ガスを処理したところ、連続運転2週間で圧損が増大
し、目詰を起こし、掃除する必要があった。
COMPARATIVE EXAMPLE Exhaust gas was treated in the same manner as in the Example except that no ceramic globules were provided. As a result, pressure loss increased in two weeks of continuous operation, clogging occurred, and cleaning was required.

【0037】[0037]

【発明の効果】以上述べたように、本発明は、ハニカム
型成形体の性能(触媒能、熱効率)を損なうことなく、
しかも、粉塵の多いガスの処理において効果的にハニカ
ム成形体の目詰を防止できることから、従来のような頻
繁に運転を休止して清掃する必要がなく長期安定して操
業することが可能となった。
As described above, according to the present invention, the performance (catalytic ability, thermal efficiency) of the honeycomb molded body is not impaired.
In addition, since the clogging of the honeycomb formed body can be effectively prevented in the processing of a gas having a large amount of dust, it is possible to stably operate for a long period of time without having to frequently stop and clean the conventional operation. Was.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明のハニカム型成形体を有する排ガス処理
装置による被処理ガスの処理工程を示す概略図である。
FIG. 1 is a schematic view showing a process of treating a gas to be treated by an exhaust gas treating apparatus having a honeycomb molded body of the present invention.

【図2】本発明の具体的構成を示した蓄熱式排ガス処理
装置であり、(A)は斜視図であり、(B)は(A)の
要部斜視図である。
FIG. 2 is a heat storage type exhaust gas treatment apparatus showing a specific configuration of the present invention, wherein (A) is a perspective view and (B) is a perspective view of a main part of (A).

【図3】本発明の要部の具体的構成を示した斜視図であ
る。
FIG. 3 is a perspective view showing a specific configuration of a main part of the present invention.

【符号の説明】[Explanation of symbols]

1…ハニカム型蓄熱体(触媒)を有する排ガス処理装
置、2A、2B、2C…蓄熱室(触媒室)、3…蓄熱体
(触媒)、3a…上流側蓄熱体(触媒)、3b…下流側
蓄熱体(触媒)、4…酸化分解室(空間)、5…燃焼
室、6…バーナー、7…被処理ガス供給管、8…処理ガ
ス排出管、9…パージガス供給管、10…排気ファン、
11…煙突、12a、12b、12c、13a、13
b、13c、14a、14b、14c…切換弁、15…
球体、16…球体支持構造体、17…ハニカム型蓄熱
体、18…被処理ガス供給管、19…支持体、20…パ
ージガス供給管、21…排突、22…球体、23…球体
支持体、24…蓄熱体、25…ダクト、26…配管、2
7…フランジ、28…固定弁、29…ハニカム型成形
体、30…球体、31…スペーサー、32…回転弁、3
3…切換弁、34…処理ガス排出管
DESCRIPTION OF SYMBOLS 1 ... Exhaust gas processing apparatus which has a honeycomb type heat storage material (catalyst), 2A, 2B, 2C ... heat storage room (catalyst chamber), 3 ... heat storage material (catalyst), 3a ... upstream heat storage material (catalyst), 3b ... downstream side Heat storage unit (catalyst), 4: Oxidation decomposition chamber (space), 5: Combustion chamber, 6: Burner, 7: Gas supply pipe to be processed, 8: Processing gas discharge pipe, 9: Purge gas supply pipe, 10: Exhaust fan,
11 ... chimney, 12a, 12b, 12c, 13a, 13
b, 13c, 14a, 14b, 14c ... switching valve, 15 ...
Spherical body, 16: spherical support structure, 17: honeycomb-type regenerator, 18: gas supply pipe to be processed, 19: support body, 20: purge gas supply pipe, 21: discharge, 22: spherical body, 23: spherical support body, 24: heat storage element, 25: duct, 26: pipe, 2
7 ... Flange, 28 ... Fixed valve, 29 ... Honeycomb molded body, 30 ... Spherical body, 31 ... Spacer, 32 ... Rotary valve, 3
3 switching valve, 34 processing gas discharge pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 別府 暁 新潟県中頸城郡中郷村大字藤沢950日本曹 達株式会社二本木工場生産技術研究所内 Fターム(参考) 3K078 AA01 BA03 BA07 BA10 BA15 BA21 EA01 EA04 EA07 EA08 ────────────────────────────────────────────────── ─── Continuing from the front page (72) Inventor Akira Beppu F-term in Nihon Soda Co., Ltd. Nihongi Plant Production Engineering Laboratory, Fukusawa 950, Nakago-mura, Nakakubijo-gun, Niigata Prefecture EA08

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】ハニカム型成形体を有する排ガス処理装置
であって、ハニカム型成形体の片面及又は両面に球体を
配したことを特徴とする排ガス処理装置。
An exhaust gas treating apparatus having a honeycomb-shaped formed body, wherein a spherical body is arranged on one side or both sides of the honeycomb formed body.
【請求項2】ハニカム型成形体を有する排ガス処理装置
であって、ハニカム型成形体が複数段に積層されて用い
られ、その複数段全体の片面又は両面、並びに各段の中
間に球体を配することを特徴とする排ガス処理装置。
2. An exhaust gas treatment apparatus having a honeycomb-shaped formed body, wherein the honeycomb-shaped formed body is used by being laminated in a plurality of stages, and a sphere is disposed on one or both surfaces of the entire plurality of stages and in the middle of each stage. An exhaust gas treatment device characterized by:
【請求項3】球体の周囲を囲む壁を設けたことを特徴と
する請求項1又は2に記載の排ガス処理装置。
3. The exhaust gas treatment device according to claim 1, wherein a wall surrounding the periphery of the sphere is provided.
【請求項4】単一又は複数段に積層されたハニカム型成
形体が上下方向に配置されたおり、かつハニカム型成形
体の最下面に球体を支持する網目状構造体を設けたこと
を特徴とする請求項1〜3のいずれかに記載の排ガス処
理装置。
4. A honeycomb-shaped formed body laminated in a single or plural stages is vertically arranged, and a mesh-like structure for supporting a sphere is provided on the lowermost surface of the honeycomb-shaped formed body. The exhaust gas treatment device according to claim 1.
【請求項5】燃焼室に連通した複数の部屋に単一又は複
数段に積層されたハニカム型成形体が蓄熱体として配置
されており、各部屋に対して被処理ガスの供給、パージ
ガスの供給、及び燃焼室内で酸化分解した処理ガスの排
気を順次切り換えながら排ガスを処理することを特徴と
する請求項1〜4に記載の排ガス処理装置。
5. A honeycomb-shaped formed body laminated in a single or plural stages in a plurality of chambers communicating with a combustion chamber is disposed as a heat storage body, and supply of a gas to be treated and supply of a purge gas to each chamber are provided. The exhaust gas treatment apparatus according to any one of claims 1 to 4, wherein the exhaust gas is treated while sequentially switching the exhaust of the processing gas oxidized and decomposed in the combustion chamber.
【請求項6】球体の最大幅がハニカム型成形体の各開口
部の最大幅よりも大きいことを特徴とする請求項1〜5
のいずれかに記載の排ガス処理装置。
6. The honeycomb body according to claim 1, wherein the maximum width of the sphere is larger than the maximum width of each opening of the honeycomb molded body.
An exhaust gas treatment device according to any one of the above.
【請求項7】球体がセラミックス製であることを特徴と
する請求項1〜6のいずれかに記載の排ガス処理装置。
7. The exhaust gas treatment apparatus according to claim 1, wherein the sphere is made of ceramics.
【請求項8】球体をハニカム型成形体単体開口部に対し
て0.2〜0.7個用いることを特徴とする請求項1〜
7のいずれかに記載の排ガス装置。
8. The method according to claim 1, wherein 0.2 to 0.7 spheres are used for the single opening of the honeycomb molded body.
8. The exhaust gas device according to any one of 7 above.
【請求項9】排ガスが粉塵を含む排ガスであることを特
徴とする請求項1〜8のいずれかに記載の排ガス処理装
置。
9. The exhaust gas treatment apparatus according to claim 1, wherein the exhaust gas is an exhaust gas containing dust.
【請求項10】ハニカム型成形体を有する排ガス処理装
置において、ハニカム型成形体の片面又は両面に球体を
配し、ガスの流入及び/又は流出に伴って前記球体が上
下及び/又は左右に移動することによりハニカム成形体
の各開口部の堆積物を除去することを特徴とするハニカ
ム型成形体の目詰防止方法。
10. An exhaust gas treatment apparatus having a honeycomb molded body, wherein a sphere is arranged on one or both sides of the honeycomb molded body, and the sphere moves up and down and / or left and right with the inflow and / or outflow of gas. A method for preventing clogging of a honeycomb molded body, comprising removing deposits at each opening of the honeycomb molded body.
JP2000008488A 2000-01-18 2000-01-18 Exhaust gas treatment apparatus having a honeycomb molded body and method for preventing clogging thereof Expired - Lifetime JP4155542B2 (en)

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Application Number Priority Date Filing Date Title
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100444602B1 (en) * 2002-02-08 2004-08-16 권순목 Hori. distribution type regenerative thermal oxidizer
JP2009229043A (en) * 2008-03-25 2009-10-08 Ngk Insulators Ltd Spacer for heat exchanger
CN108709192A (en) * 2018-06-20 2018-10-26 山西文龙中美环能科技股份有限公司 Ultralow concentration gas dual oxide device
JP2021105466A (en) * 2019-12-26 2021-07-26 東京窯業株式会社 Heat storage part structure of exhaust gas combustion treatment device and exhaust gas combustion treatment method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100444602B1 (en) * 2002-02-08 2004-08-16 권순목 Hori. distribution type regenerative thermal oxidizer
JP2009229043A (en) * 2008-03-25 2009-10-08 Ngk Insulators Ltd Spacer for heat exchanger
CN108709192A (en) * 2018-06-20 2018-10-26 山西文龙中美环能科技股份有限公司 Ultralow concentration gas dual oxide device
CN108709192B (en) * 2018-06-20 2023-09-08 山西文龙中美环能科技股份有限公司 Ultra-low concentration gas double oxidation device
JP2021105466A (en) * 2019-12-26 2021-07-26 東京窯業株式会社 Heat storage part structure of exhaust gas combustion treatment device and exhaust gas combustion treatment method
JP7344790B2 (en) 2019-12-26 2023-09-14 東京窯業株式会社 Heat storage part structure of exhaust gas combustion treatment device and exhaust gas combustion treatment method

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