JPS606682B2 - Exhaust gas purification device - Google Patents

Exhaust gas purification device

Info

Publication number
JPS606682B2
JPS606682B2 JP52008346A JP834677A JPS606682B2 JP S606682 B2 JPS606682 B2 JP S606682B2 JP 52008346 A JP52008346 A JP 52008346A JP 834677 A JP834677 A JP 834677A JP S606682 B2 JPS606682 B2 JP S606682B2
Authority
JP
Japan
Prior art keywords
exhaust gas
particulate matter
angle
repose
packed bed
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.)
Expired
Application number
JP52008346A
Other languages
Japanese (ja)
Other versions
JPS5395177A (en
Inventor
智成 垣下
宏明 井田
定雄 関田
克美 宮田
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP52008346A priority Critical patent/JPS606682B2/en
Publication of JPS5395177A publication Critical patent/JPS5395177A/en
Publication of JPS606682B2 publication Critical patent/JPS606682B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/12Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)
  • Gas Separation By Absorption (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

【発明の詳細な説明】 本発明は煤塵を含有する排ガスの浄化装置に関するもの
で、さらに詳しくは排ガスを処理すべき粒状物質を充填
した層を斜めに傾斜させ、かつ適切な間隔で安息角保持
板を設けて粒状物質を排出させる機構を有し、充填層の
上部面を粒状物質の安息角により形成した面とし下部面
は排ガスを通過するが粒状物質は落下させない多孔材料
に支えられる面として排ガスを上部面より下部面に流が
して処理する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for purifying exhaust gas containing soot and dust, and more specifically, the present invention relates to a device for purifying exhaust gas containing soot and dust, and more specifically, a layer filled with particulate matter to be treated for exhaust gas is inclined obliquely and is spaced at appropriate intervals to maintain an angle of repose. It has a mechanism for discharging particulate matter by providing a plate, with the upper surface of the packed bed being a surface formed by the angle of repose of the particulate matter, and the lower surface being supported by a porous material that allows exhaust gas to pass through but does not allow particulate matter to fall. This relates to a device that processes exhaust gas by flowing it from an upper surface to a lower surface.

従来より触媒や吸着剤等の粒状物質に排ガスを接触させ
た処理する装置は数多く提案され実施されてきた。
BACKGROUND OF THE INVENTION Many devices have been proposed and implemented in the past for treating exhaust gas by bringing it into contact with particulate materials such as catalysts and adsorbents.

しかしその多くは煤塵を含まないいわゆるクリーンな排
ガス用のものであった。近年、公害防止の観点から煤塵
を含有する排ガスの処理が要望され、実施されるように
なった。例えばボイラー排ガス中の硫黄酸化物、窒素酸
化物、化学製造工程からの各種悪臭物質の処理である。
これ0らはほとんどの場合その排ガス中に微細な固体す
なわち煤塵を含んでいるため従来の装置ではその目づま
りにより除去処理を長期間安定させることが困難であっ
た。このためやむなく、装置全体を停止させ目づまりの
洗浄を行なう必要があった。タ生産工程の装置であれば
停止によって、製品が出なくなるのみであるが公害防止
装置であれば停止中はやむなく有害物質が大気中に排出
されることになり社会的にも不都合である。これらの要
望をかなえるため研究の結果、本発明に致つたのであ0
る。従来の装置の多くは粒状物質の支持のため上下又は
前後とも多孔材料を使用するのが普通であったがこれら
の装置で煤塵を含有する排ガスを処理すると排ガス導入
部の多孔材料又は多孔材料と粒状物質の間にいまいま目
づまりを生ずる欠点があった。本発明の装置によれば排
ガス導入部に多孔材料を使用しないため目づまりはない
。またたとえ排ガス導入部の粒状物質間に煤塵が目づま
りしても粒状物質を容易に移動させ新しい粒状物質によ
り新しい安息角面を形成させるのでただちに目づまりを
解消しうる。充填層の排ガス排出部に使用した多孔材料
は本発明においては斜めに傾斜しており、粒状物質の移
動により常にその面がセルフクリーニングされる。これ
によりたとえ軽度の目づまりによる充填層の圧力損失の
上昇があっても、もとのベースまで回復できる。充填層
下部の多孔材料としては基本的には排ガスを通過させる
が、粒状物質を落下させない材料であれば任意に使用し
うるが、その好ましい形態は丸孔、角孔、ヘリンボン型
、スリット孔型等のパンチングプレート、スリット「金
網、ラスターメル、ベネシャンスクリーン等である。
However, most of them were for so-called clean exhaust gas that does not contain soot and dust. In recent years, treatment of exhaust gas containing soot and dust has been requested and implemented from the viewpoint of pollution prevention. For example, treatment of sulfur oxides and nitrogen oxides in boiler exhaust gas, and various malodorous substances from chemical manufacturing processes.
In most cases, these 0 contain fine solids, that is, soot dust, in the exhaust gas, so it has been difficult to stabilize the removal process for a long period of time in conventional equipment due to the clogging. For this reason, it was necessary to stop the entire apparatus and clean the clogged area. If the equipment is used in a data production process, stopping the equipment will only result in no product being produced, but if it is a pollution control equipment, harmful substances will inevitably be emitted into the atmosphere during the shutdown, which is socially inconvenient. As a result of research, we have come up with this invention to meet these demands.
Ru. Most conventional devices usually use porous materials at the top and bottom or front and back to support particulate matter, but when these devices treat exhaust gas containing soot and dust, the porous material in the exhaust gas introduction section or There was a drawback that clogging occurred between the particulate materials. According to the device of the present invention, no porous material is used in the exhaust gas introduction section, so there is no clogging. Furthermore, even if particulate matter in the exhaust gas introduction section becomes clogged with soot and dust, the particulate matter is easily moved and a new angle of repose plane is formed by new particulate matter, so that the clogging can be immediately cleared. In the present invention, the porous material used for the exhaust gas discharge part of the packed bed is obliquely inclined, and its surface is constantly self-cleaned by the movement of particulate matter. As a result, even if there is an increase in pressure loss in the packed bed due to slight clogging, it can be restored to the original base. As the porous material at the bottom of the packed bed, any material can be used as long as it basically allows exhaust gas to pass through but does not allow particulate matter to fall, but the preferred forms are round holes, square holes, herringbone holes, and slit hole types. Punching plates, slits, wire mesh, lastemel, venetian screens, etc.

本発明においては粒状物質の充填層は常に傾斜して使用
するが、その傾斜角は粒状物質の安息角によって若干の
中をもって変更すべきである。
In the present invention, the packed bed of granular material is always used with an inclination, but the angle of inclination should be slightly changed depending on the angle of repose of the granular material.

また粒状物質の移動に関与する「流れ角」によっても変
わるが、通常20o〜80o好ましくは40o〜700
付近が良い。またト充填層上部に設ける安息角保持板は
、この傾斜角が粒状物質の安息角と異なる場合、その程
度が大きくなるにつれ間隔をせばめて数多く挿入した方
が充填層を一定の厚みに保たしめる意味で好ましい。加
えてこの安息角保持板は装置の振動などによる安息角の
くずれを防止する役目を有し特に有効である。本発明に
いう安息角保持板とは「粒状物質を支える多孔材料の上
部に「水平面に対して垂直方向をなし、かつ「多孔材料
と該安息角保持板の間を粒状物質が移動できるような位
置に、缶体に支持されて設けられており、粒状物質の落
下及び安息角のくずれを防止し、かつ、排ガス浄化装置
の底部に付設した排出部より粒状物質を排出させたとき
、多孔材料と該安息角保持板の間を通って粒状物質が容
易に移動可能なように構成した板をいつ。
Although it also varies depending on the "flow angle" involved in the movement of particulate matter, it is usually 20° to 80°, preferably 40° to 700°.
Good nearby. In addition, if the angle of repose of the angle of repose maintenance plates installed above the packed bed differs from the angle of repose of the granular material, it is better to insert more plates at smaller intervals as the degree of inclination increases to keep the packed layer at a constant thickness. It is preferable in the sense of tightening. In addition, this angle of repose holding plate is particularly effective because it serves to prevent the angle of repose from being distorted due to vibrations of the device. The angle of repose retention plate referred to in the present invention is defined as "a plate placed on the top of a porous material that supports particulate matter, perpendicular to the horizontal plane, and at a position that allows the particulate matter to move between the porous material and the angle of repose retention plate." , which is supported by the can body, prevents particulate matter from falling and the angle of repose from collapsing, and when particulate matter is discharged from the discharge part attached to the bottom of the exhaust gas purification device, the porous material and the When the plates are configured to allow easy movement of particulate matter between the angle-of-repose holding plates.

本発明の装置は充填層面を安息角を利用すること、移動
を容易にすることにより前述のごとく傾斜させるが該充
填層上、下部面はもっとも単純な場合は平面である。
In the apparatus of the present invention, the surface of the packed bed is tilted as described above by utilizing the angle of repose and facilitating movement, but the upper and lower surfaces of the packed bed are flat in the simplest case.

この場合であっても充填層は1つである必要はなく「組
合せによって充填層が屋根型や粒状物質の供給部、排出
部を直線上に集めた形、すなわち上を屋根型、下を逆屋
根型に組合せた形、あるいはそれのくりかえし何段か積
みかさねた形も取りうる。又、充填層上、下部面は平面
でなく、円錐面、多角錐面でもよくそれらの組合せでも
よい。円錐の組合せとしては「そろばん玉」状のものが
ある。但し粗合せた場合常に排ガスが安息角形成の充填
層上部面より導入する必要から、それに応じ上下の支切
り板を設け各々に入口を設ける工夫がいる。本発明は上
記のごとき構造によりなるので排ガス処理に際して触媒
や吸着剤等の粒状物質充填層に、煤塵が目づまりするこ
となく連続的に浄化処理が可能なものであり、著しく優
れた排ガス浄化装置である。
Even in this case, the number of packed beds does not need to be one; depending on the combination, the packed bed has a shape in which the roof type, granular material supply part, and discharge part are gathered in a straight line, that is, the upper part is the roof type, and the lower part is reversed. It can be combined into a roof shape, or it can be repeated and stacked in several tiers. Also, the upper and lower surfaces of the packed layer are not flat, but may be conical surfaces, polygonal pyramidal surfaces, or a combination thereof. Conical There is a combination of ``Abacus beads''. However, in the case of rough matching, it is necessary to always introduce the exhaust gas from the upper surface of the packed bed forming the angle of repose, so it is necessary to provide upper and lower partition plates and provide inlets for each. Since the present invention has the above-described structure, it is possible to continuously purify the bed of particulate matter such as catalysts and adsorbents during exhaust gas treatment without clogging with soot and dust, and it is an extremely superior exhaust gas purification device. It is.

以下本発明の実施例を図面に基づいて説明するが本発明
は実施例に限定されるものではない。
Examples of the present invention will be described below based on the drawings, but the present invention is not limited to the examples.

各図中1は排ガスの流入口、2は粒状物質充填層の支持
用多孔材料で粒状物質層の安息角より急なる角度に固定
されており、その上に粒状物質層3を形成している。多
孔材料の角度と粒状物質の安息角度との差による粒状物
質層の厚みの斜面上下間の変化を防ぐため、安息角保持
板4を設けている。流入口1より導びかれた排ガスは安
息角保持板4の間より粒状材料層3に導びかれ浄化され
た後、多孔材料2の間隔を通過し排出口7より排出され
「健道より大気中に放出される。
In each figure, 1 is an inlet for exhaust gas, and 2 is a porous material for supporting the granular material packed layer, which is fixed at an angle steeper than the angle of repose of the granular material layer, on which the granular material layer 3 is formed. . An angle of repose holding plate 4 is provided to prevent the thickness of the granular material layer from changing between the upper and lower slopes due to the difference between the angle of the porous material and the angle of repose of the granular material. Exhaust gas led from the inlet 1 is guided to the granular material layer 3 between the angle of repose holding plates 4 and purified, then passes through the gap between the porous materials 2 and is discharged from the outlet 7. released inside.

第3〜第6図は他の実施例で粒状物質層が上下2組より
形成される場合であって、この場合は仕切板6により排
ガス入口と浄化後の排ガスを分離される。一方粒状物質
は排ガスの処理により煤塵により汚れた場合、多孔材料
2と安息角保持板4の間を斜め下方へと流れ粒状物質抜
き出し口9より間欠的あるいは定常的に抜き出され、ふ
るい分け機101こ導びかれ煤塵と粒状物質に分離され
る。煤塵は煤塵排出ロー2より外部に排出され、粒状物
質は搬送機liにより粒状物質投入口8より再び充填層
3に導びかれ浄化に利用される。多孔材料2と安息角保
持板4は、缶体51こより支持されており、同時に缶体
5は排ガスと大気を隔離している。
3 to 6 show another embodiment in which the granular material layer is formed in two sets, upper and lower, and in this case, the exhaust gas inlet and the purified exhaust gas are separated by a partition plate 6. On the other hand, when particulate matter becomes contaminated with soot and dust due to exhaust gas treatment, it flows obliquely downward between the porous material 2 and the angle of repose holding plate 4, and is intermittently or constantly extracted from the particulate matter extraction port 9. This is separated into soot and particulate matter. The soot and dust are discharged to the outside from the soot and dust discharge row 2, and the particulate matter is led back to the packed bed 3 through the particulate matter inlet 8 by the conveyor li and is used for purification. The porous material 2 and the angle of repose holding plate 4 are supported by the can body 51, and at the same time, the can body 5 isolates the exhaust gas from the atmosphere.

【図面の簡単な説明】[Brief explanation of the drawing]

図面は本発明の実施例を示し第1図は充填層が1つで平
面をなすものの縦断面図、第2図は第1図のフカン図、
第3図は充填層が4つの平面よりなる屋根型と逆屋根型
の組合されたものの縦断面図、第4図は第3図のフカン
図、第5図は充填層が円錐面の組合せたものいわゆるそ
ろばん玉型の縦断面図、第6図は第5図のフカン図であ
る。 1・・・・・・排ガス流入口、2・・・・・・多孔材料
、3・…・・粒状物質充填層、4・・・・・・安息角保
持板、5・・・・・・缶体、6…・・・仕切板、7・・
・・・・排ガス排出口、8・・・…粒状物投入口、9…
・・・粒状物質抜取口、10・・・・・・ふるいわけ機
、11・・・・・・搬送機、12・・・・・・煤塵排出
口。 オー図 ガス‘a オジ図 オ乳2 大S釘 オ5‘幻
The drawings show an embodiment of the present invention, and FIG. 1 is a vertical cross-sectional view of a plane with one filling layer, and FIG. 2 is a diagram of the hook of FIG.
Figure 3 is a vertical cross-sectional view of a combination of a roof type and an inverted roof type in which the packed bed has four planes, Figure 4 is a hook diagram of Figure 3, and Figure 5 is a combination of a packed bed with a conical surface. A vertical cross-sectional view of the so-called abacus bead shape, FIG. 6 is a hook diagram of FIG. 5. 1... Exhaust gas inlet, 2... Porous material, 3... Particulate matter packed layer, 4... Angle of repose holding plate, 5... Can body, 6... Partition plate, 7...
...Exhaust gas outlet, 8...Particle inlet, 9...
... Particulate matter extraction port, 10 ... Sieving machine, 11 ... Conveyor, 12 ... Dust discharge port. O figure gas'a O figure O breasts 2 Big S nail O 5' illusion

Claims (1)

【特許請求の範囲】[Claims] 1 煤塵を含有する排ガスを触媒または吸着剤等の粒状
物質と接触させて浄化する装置において、粒状物質を充
填した装置の頂部に供給部を底部に排出部を付設させ粒
状物質を容易に排出させる機構を有し、かつ粒状物質を
充填した層を傾斜させ、充填層の上部面は基本的には粒
状物質の安息角により形成された面となし、かつ適切な
間隔で安息角保持板を設け、充填層下部面は排ガスを通
過するが粒状物質は落下させない多孔材料により支えら
れた面とし、処理すべき排ガスの流れを充填層上部面よ
り導入し、下部面より排出し処理させるごとき構造を有
することを特徴とする排ガス浄化装置。
1. In a device that purifies exhaust gas containing soot and dust by bringing it into contact with particulate matter such as a catalyst or adsorbent, the particulate matter is easily discharged by attaching a supply section to the top of the device filled with particulate matter and a discharge section to the bottom. The layer filled with particulate matter is tilted, the upper surface of the packed bed is basically a surface formed by the angle of repose of the particulate material, and angle of repose retaining plates are provided at appropriate intervals. The lower surface of the packed bed is supported by a porous material that allows exhaust gas to pass through but does not allow particulate matter to fall, and the structure is such that the flow of exhaust gas to be treated is introduced from the upper surface of the packed bed and discharged from the lower surface for treatment. An exhaust gas purification device comprising:
JP52008346A 1977-01-27 1977-01-27 Exhaust gas purification device Expired JPS606682B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52008346A JPS606682B2 (en) 1977-01-27 1977-01-27 Exhaust gas purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52008346A JPS606682B2 (en) 1977-01-27 1977-01-27 Exhaust gas purification device

Publications (2)

Publication Number Publication Date
JPS5395177A JPS5395177A (en) 1978-08-19
JPS606682B2 true JPS606682B2 (en) 1985-02-20

Family

ID=11690647

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52008346A Expired JPS606682B2 (en) 1977-01-27 1977-01-27 Exhaust gas purification device

Country Status (1)

Country Link
JP (1) JPS606682B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS592417U (en) * 1982-06-28 1984-01-09 荏原インフイルコ株式会社 Deodorizing device
EP0692295A1 (en) * 1994-07-11 1996-01-17 Shell Internationale Researchmaatschappij B.V. Device for contacting gas with granular material
JP3820027B2 (en) * 1998-03-27 2006-09-13 三菱重工業株式会社 Removal equipment for hydrogen chloride and sulfur dioxide

Also Published As

Publication number Publication date
JPS5395177A (en) 1978-08-19

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