JPS6135271Y2 - - Google Patents

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Publication number
JPS6135271Y2
JPS6135271Y2 JP1981010853U JP1085381U JPS6135271Y2 JP S6135271 Y2 JPS6135271 Y2 JP S6135271Y2 JP 1981010853 U JP1981010853 U JP 1981010853U JP 1085381 U JP1085381 U JP 1085381U JP S6135271 Y2 JPS6135271 Y2 JP S6135271Y2
Authority
JP
Japan
Prior art keywords
dust
screen
particulate matter
granular
separated
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
JP1981010853U
Other languages
Japanese (ja)
Other versions
JPS57123679U (en
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 filed Critical
Priority to JP1981010853U priority Critical patent/JPS6135271Y2/ja
Publication of JPS57123679U publication Critical patent/JPS57123679U/ja
Application granted granted Critical
Publication of JPS6135271Y2 publication Critical patent/JPS6135271Y2/ja
Expired legal-status Critical Current

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  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Combined Means For Separation Of Solids (AREA)

Description

【考案の詳細な説明】 本考案はダストを含む粒状物からダストを分離
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 separating dust from particulate matter containing dust.

窒素酸化物を含む燃焼排ガスは触媒の存在下、
アンモニアと反応させ無害化して大気に放散され
るが、その際に用いられる竪型触媒移動層におけ
る粒状触媒は循環使用される間に燃焼排ガス中に
同伴するダストが表面に付着して活性が低下した
り或いはそれ自体が粉化して次第に触媒作用が減
衰する。
In the presence of a catalyst, combustion exhaust gas containing nitrogen oxides is
It reacts with ammonia to render it harmless and is dissipated into the atmosphere, but during the cyclic use of the granular catalyst in the vertical catalyst transfer bed, dust entrained in the combustion exhaust gas adheres to the surface and its activity decreases. Otherwise, the catalyst itself becomes powder and its catalytic action gradually decreases.

上記窒素酸化物を含む燃焼排ガス処理における
粒状触媒に限らず、ダストの混在する流動性の粒
状物からダストを分離除去するには該粒状物をそ
の粒径よりも小さな網目を持つたスクリーン
(篩)上に供給し、スクリーンを上下又は水平に
揺動させるなどの物理的手段により、スクリーン
の網目を通過する細かい粒径のダストとスクリー
ン上に残る粒状物とに分離する方法が一般に行わ
れる。しかし、このような分離操作を行う場合、
その粒状物が粉体をバインダーで固めて成型した
例えば前記窒素酸化物を含む燃焼排ガスの処理に
おける触媒のような造粒物の場合には、粒状触媒
の強度はそれほど大きくなく上記スクリーン上で
の揺動によつて破壊され、未だ使用に耐える粒状
触媒までもが粉化して減量するという欠点があつ
た。
In order to separate and remove dust not only from granular catalysts used in the treatment of combustion exhaust gases containing nitrogen oxides but also from fluid granules containing dust, the granules can be passed through a screen (sieve) with a mesh smaller than the particle size. ) and by physical means such as shaking the screen vertically or horizontally, the dust is separated into fine particle size dust that passes through the mesh of the screen and particulate matter that remains on the screen. However, when performing such a separation operation,
If the granular material is a granular material such as a catalyst used in the treatment of combustion exhaust gas containing nitrogen oxides, the strength of the granular catalyst is not so great that it can be molded by solidifying powder with a binder. There was a drawback that even the granular catalyst, which was destroyed by the shaking and could still be used, was powdered and lost in weight.

本考案は上記のような従来のダスト分離装置に
みられる欠点を解消した特定構造のダスト分離装
置に係わるもので、例えば窒素酸化物含有燃焼排
ガス処理設備の竪型触媒移動層における粒状触媒
のような比較的強度の小さな粒状物の表面に付着
するダストや粉化物を効率よく分離するものであ
る。
The present invention relates to a dust separator with a specific structure that eliminates the drawbacks of conventional dust separators as described above. This method efficiently separates dust and powdered materials that adhere to the surface of granular materials with relatively low strength.

即ち、本考案はダストを含む粒状物の流動を緩
和する螺旋羽根を内部に備え、傾斜貫通するシヤ
フトにより回転する円筒状の傾斜スクリーン及び
これを内蔵する傾斜ケーシングよりなり、更に、
該ケーシングには、一端部に前記傾斜スクリーン
内へダストを含む粒状物を装入する装入口、なら
びに、粒状物の装入衝撃を緩和する溜り部、中央
部に分離されたダストの排出口、及び他端部に前
記傾斜スクリーンからダストの分離された粒状物
を排出する排出口を備えてなることを特徴とする
ダストを含む粒状物からダストを分離する装置を
要旨とする。
That is, the present invention comprises a cylindrical inclined screen which is equipped with a spiral blade inside which moderates the flow of particulate matter including dust and is rotated by a shaft penetrating the screen at an inclined angle, and an inclined casing containing the same;
The casing includes a charging port for charging granular material containing dust into the inclined screen at one end, a reservoir portion for mitigating the impact of charging the granular material, and a dust outlet separated in the center. The gist of the invention is an apparatus for separating dust from particulate matter containing dust, characterized in that the other end is provided with an outlet for discharging the particulate matter from which the dust has been separated from the inclined screen.

以下、本考案のダストを含む粒状物からダスト
を分離する装置をその一実施例を示す図面に基づ
いて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An apparatus for separating dust from granular materials containing dust according to the present invention will be described below with reference to drawings showing one embodiment thereof.

第1図において4は後記する傾斜スクリーン3
を内蔵した傾斜ケーシングで、これには一端部に
ダストが表面に付着した粒状物の装入口5、粒状
物の溜め部6、底部中央に分離されたダストの排
出口7及び他端部にダストの分離された粒状物の
排出口8が設けられている。又、ケーシング4内
には螺旋羽根2のとりつけられているシヤフト1
の支持アーム1aにより支持されて回転する両端
開口部を有する円筒状の傾斜スクリーン3が内蔵
されている。更にシヤフト1は軸受9,9により
支持され、駆動装置の駆動を受けるスプロケツト
ホイル10により回転するようになつている。
尚、回転方向はスプロケツトホイル10側より見
て反時計廻りとする。傾斜スクリーン3の材料の
具体例としては金網、多孔性板、ウエツヂワイヤ
スクリーン等があげられ、これらは粒状物の粒径
よりも小さなメツシユ又はスリツトを有するもの
であることが必要である。
In Fig. 1, 4 is an inclined screen 3 which will be described later.
This is a slanted casing with a built-in particulate matter inlet 5 with dust attached to its surface at one end, a particulate matter reservoir part 6, a dust outlet part 7 separated in the center of the bottom, and a dust outlet part 7 at the other end. A discharge port 8 for the separated particulate matter is provided. Also, inside the casing 4 is a shaft 1 on which a spiral blade 2 is attached.
A cylindrical inclined screen 3 having openings at both ends is built in and rotates while being supported by a support arm 1a. Further, the shaft 1 is supported by bearings 9, 9, and rotated by a sprocket wheel 10 driven by a drive device.
Note that the direction of rotation is counterclockwise when viewed from the sprocket wheel 10 side. Specific examples of the material for the inclined screen 3 include wire mesh, porous plate, wedge wire screen, etc., and these must have meshes or slits smaller than the particle size of the granules.

尚、11は回転中の傾斜スクリーン3の表面を
払拭し、分離されたダストや粉化物による目づま
りを防止するためのブラシで、コイルバネ12に
傾斜スクリーン3の表面を押圧するようにして設
けられるものである。
Reference numeral 11 denotes a brush for wiping the surface of the rotating inclined screen 3 to prevent clogging caused by separated dust and powdered substances, and is provided so as to press the surface of the inclined screen 3 against the coil spring 12. It is.

本考案のダスト分離装置は、第1図に示すとお
り、粒状物が傾斜ケーシング4の一端部の装入口
5から排出口8の設けられる他端部へ自重により
移動するよう装入口5の方を高くしてある。即
ち、装入口5から投入されたダストを含む粒状物
は、先ず溜り部6へ堆積し緩衝域が形成される。
次に投入が続けられると粒状物は一旦緩衝域へ落
ち、次いで回転中の円筒状の傾斜スクリーン3内
へすべり落ち自重により排出口8へ移動する間
に、粒状物の表面に付着しているダストのみは網
目又はスリツトから落下して分離されダスト排出
口7へ排出され、又、粒状物は排出口8から落下
する。この場合、粒状物はシヤフト1に取付けら
れる螺旋羽根2により排出口8への流動が緩和さ
れ途中に於ける粒子同志の衝突が最大限に阻止さ
れ粒状物自体の粒化を回避するような構造となつ
ており、これが本考案のダスト分離装置の大きな
特徴である。
As shown in FIG. 1, the dust separator of the present invention opens the charging port 5 so that the granules move by their own weight from the charging port 5 at one end of the inclined casing 4 to the other end where the discharge port 8 is provided. It's expensive. That is, the particulate matter containing dust introduced from the charging port 5 first accumulates in the reservoir 6, forming a buffer zone.
Next, as the input continues, the granules fall into the buffer area, then slide into the rotating cylindrical inclined screen 3, and while moving to the discharge port 8 due to their own weight, they adhere to the surface of the granules. Only the dust falls from the mesh or slit, is separated and discharged to the dust outlet 7, and the particulate matter falls from the outlet 8. In this case, the flow of the granular material toward the discharge port 8 is relaxed by the spiral vane 2 attached to the shaft 1, and collisions between particles on the way are prevented to the maximum, thereby avoiding the granulation of the granular material itself. This is a major feature of the dust separation device of the present invention.

第3図は窒素酸化物を含む燃焼排ガスを処理す
る設備に本考案のダスト分離装置を適用して、同
設備において還元用粒状触媒の表面に付着した燃
焼排ガスに同伴するダストを分離する場合の例に
ついての概略図である。
Figure 3 shows the case where the dust separator of the present invention is applied to equipment that processes combustion exhaust gas containing nitrogen oxides to separate dust accompanying the combustion exhaust gas adhering to the surface of a granular catalyst for reduction. FIG. 2 is a schematic diagram for an example.

同図中、Aはアンモニア(還元剤)の混合され
た窒素酸化物含有燃焼排ガスで燃焼によつて生ず
るダスト(粉塵)を同伴して導入管13より矢印
方向に導入され、通気側壁によつて保持された粒
状触媒の竪型移動層14を通過し、還元無毒化及
び除塵され清浄なガスとなつて排出導管15,1
5へ導出される。
In the figure, A is nitrogen oxide-containing combustion exhaust gas mixed with ammonia (reducing agent), which is introduced from the inlet pipe 13 in the direction of the arrow along with dust generated by combustion, and is passed through the ventilation side wall. It passes through the vertical moving bed 14 of the retained granular catalyst, is reduced, detoxified and dust removed, and becomes clean gas, which is discharged into the discharge pipes 15 and 1.
5.

即ち、竪型移動層14は上部が粒状触媒供給ホ
ツパー16と連結し、下部はロータリーフイーダ
ー17と接しており、触媒供給ホツパー16から
の補給とロータリーフイーダー17の回転排出に
より粒状触媒は竪型移動層14中を下方へ向つて
移動し、その間に燃焼排ガスと接触し、該ガス中
のダストが粒状触媒の表面に付着する。表面にダ
ストの付着した粒状触媒は、処理設備の下部ホツ
パー形成部18と連結する本考案のダスト分離装
置の装入口5から同装置に入りシヤフト1によ
り、回転する第1図における円筒状の傾斜スクリ
ーン3を下流の排出口8へ移動する間にダスト排
出口7からダストが排出分離され清浄化された粒
状触媒は排出口8から取出されて移動コンベア1
9により前記触媒供給ホツパー16へ循環され、
竪型移動層14へ供給される。
That is, the upper part of the vertical moving bed 14 is connected to the granular catalyst supply hopper 16, and the lower part is in contact with the rotary leaf feeder 17, and the granular catalyst is fed vertically by replenishment from the catalyst supply hopper 16 and rotational discharge from the rotary leaf feeder 17. It moves downward in the mold movement layer 14, during which it comes into contact with combustion exhaust gas, and the dust in the gas adheres to the surface of the granular catalyst. The granular catalyst with dust attached to its surface enters the dust separator of the present invention through the charging port 5 of the dust separator of the present invention, which is connected to the lower hopper forming part 18 of the processing equipment, and is rotated by the shaft 1 into the cylindrical inclined shape shown in FIG. While moving through the screen 3 to the downstream discharge port 8, dust is discharged and separated from the dust discharge port 7, and the purified granular catalyst is taken out from the discharge port 8 and transferred to the moving conveyor 1.
9 to the catalyst supply hopper 16;
It is supplied to the vertical moving layer 14.

本考案の粒状物からダストを分離する装置は以
上述べたように、螺旋羽根を備え内部を貫通する
シヤフトにより回転する円筒状の傾斜スクリーン
及びこの円筒状傾斜スクリーンを内蔵し、併せて
ダスト含有粒状物の装入口、分離したダストの排
出口、及び浄化された粒状物の排出口を備えた傾
斜ケーシングとより構成し、粒状物の装入とダス
ト分離操作における粒子同志の衝突による破壊を
前記螺旋羽根の緩衝作用により阻止するような構
造としたので、比較的強度の弱い粒状物でもそれ
自体の破壊をほとんど招くことなく表面に付着し
たダストや粉化物を効率よく分離することがで
き、例えば窒素酸化物含有燃焼排ガス処理装置に
おける流動性の粒状触媒の清浄手段に適用して大
きな効果をもたらすものである。
As described above, the apparatus for separating dust from granular materials according to the present invention includes a cylindrical inclined screen equipped with spiral blades and rotated by a shaft penetrating the inside, and this cylindrical inclined screen built-in, which also separates dust-containing granular materials. It consists of an inclined casing having a charging port for particles, a discharge port for separated dust, and a discharge port for purified granular materials, and the spiral casing prevents destruction due to collisions between particles during charging of granular materials and dust separation operations. Since the structure uses the buffering effect of the blades to block dust and powdered substances from being attached to the surface, even relatively weak particles can be efficiently separated without causing any damage to the particles themselves. It brings about great effects when applied to a means for cleaning fluid granular catalysts in oxide-containing combustion exhaust gas treatment equipment.

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

第1図は本考案のダスト分離装置の一例を示す
部分破断側面図、第2図は第1図のX−X線にお
ける縦断面図、第3図は窒素酸化物含有燃焼排ガ
ス処理設備に本考案の一例のダスト分離装置を適
用した断面略図である。 1……シヤフト、2……螺旋羽根、3……円筒
状の傾斜スクリーン、4……傾斜ケーシング、5
……装入口、6……溜め部、7……ダスト排出
口、8……排出口、11……ブラシ、12……コ
イルバネ、13……導入管、14……竪型移動
層、15……導出管、16……触媒供給ホツパ
ー、17……ロータリーフイーダー、19……移
動コンベア、18……下部ホツパー形成部。
Fig. 1 is a partially cutaway side view showing an example of the dust separation device of the present invention, Fig. 2 is a longitudinal sectional view taken along the line X-X of Fig. It is a cross-sectional schematic diagram to which a dust separation device of an example of the invention is applied. 1... Shaft, 2... Spiral blade, 3... Cylindrical inclined screen, 4... Inclined casing, 5
...Charging port, 6...Reservoir, 7...Dust discharge port, 8...Discharge port, 11...Brush, 12...Coil spring, 13...Introduction pipe, 14...Vertical moving bed, 15... ... Outlet pipe, 16 ... Catalyst supply hopper, 17 ... Rotary feeder, 19 ... Moving conveyor, 18 ... Lower hopper forming section.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ダストを含む粒状物の流動を緩和する螺旋羽根
を内部に備え、傾斜貫通するシヤフトにより回転
する円筒状の傾斜スクリーン、及びこれを内蔵す
る傾斜ケーシングよりなり、更に、該ケーシング
には、一端部に前記傾斜スクリーン内へダストを
含む粒状物を装入する装入口、ならびに、粒状物
の装入衝撃を緩和する溜り部、中央部に分離され
たダストの排出口、及び他端部に前記傾斜スクリ
ーンからダストの分離された粒状物を排出する排
出口を備えてなることを特徴とするダストを含む
粒状物からダストを分離する装置。
It consists of a cylindrical inclined screen that is internally equipped with a spiral vane to moderate the flow of particulate matter including dust and is rotated by a shaft penetrating the screen, and an inclined casing that houses the screen. A charging port for charging granular material containing dust into the inclined screen, a reservoir portion for mitigating the charging impact of the granular material, a dust outlet separated in the center, and the slanted screen at the other end. 1. A device for separating dust from particulate matter containing dust, comprising an outlet for discharging the particulate matter from which dust has been separated.
JP1981010853U 1981-01-28 1981-01-28 Expired JPS6135271Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1981010853U JPS6135271Y2 (en) 1981-01-28 1981-01-28

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1981010853U JPS6135271Y2 (en) 1981-01-28 1981-01-28

Publications (2)

Publication Number Publication Date
JPS57123679U JPS57123679U (en) 1982-08-02
JPS6135271Y2 true JPS6135271Y2 (en) 1986-10-14

Family

ID=29809003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1981010853U Expired JPS6135271Y2 (en) 1981-01-28 1981-01-28

Country Status (1)

Country Link
JP (1) JPS6135271Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS479016U (en) * 1971-02-19 1972-10-03

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS479016U (en) * 1971-02-19 1972-10-03

Also Published As

Publication number Publication date
JPS57123679U (en) 1982-08-02

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