JPS64999Y2 - - Google Patents
Info
- Publication number
- JPS64999Y2 JPS64999Y2 JP14542783U JP14542783U JPS64999Y2 JP S64999 Y2 JPS64999 Y2 JP S64999Y2 JP 14542783 U JP14542783 U JP 14542783U JP 14542783 U JP14542783 U JP 14542783U JP S64999 Y2 JPS64999 Y2 JP S64999Y2
- Authority
- JP
- Japan
- Prior art keywords
- wire
- moving
- particles
- louver
- wire mesh
- 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
Links
- 239000002245 particle Substances 0.000 claims description 16
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 229910000639 Spring steel Inorganic materials 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229940043430 calcium compound Drugs 0.000 description 1
- 150000001674 calcium compounds Chemical class 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
【考案の詳細な説明】
本考案は、固気分離または固気接触反応に使用
する移動層の移動粒子保持構造に関するものであ
る。[Detailed Description of the Invention] The present invention relates to a structure for holding moving particles in a moving bed used in solid-gas separation or solid-gas catalytic reaction.
従来、直交型移動層での粒子保持には、ルーバ
ー、金網、多孔板が使用されている。しかしとく
に、移動層のガス流れ後面に金網または多孔板を
使用する場合、移動粒子が直接金網または多孔板
に接触している上に、ガス流れによるガス圧のた
め、目詰りは避けがたい。またルーバーを使用す
る場合、目詰りは起こらないが、ガス流れにより
後面に粒子がこぼれる現象が生じ、かつガス流れ
が移動層の1箇所に集中した場合には、粒子を吹
き飛ばす現象が観察される。これらの現象を考慮
して、移動層のガス流れ後面にはルーバーを使用
し、ルーバーに直接金網を取り付け、金網には移
動粒子が直接接触しない構造とすることによつ
て、金網の目詰りと粒子の吹き抜けは一応同時に
解決できる。 Conventionally, louvers, wire mesh, and perforated plates have been used to retain particles in orthogonal moving beds. However, especially when a wire mesh or perforated plate is used on the rear side of the moving bed where the gas flows, clogging is unavoidable because the moving particles are in direct contact with the wire mesh or perforated plate and also because of the gas pressure caused by the gas flow. Furthermore, when using a louver, clogging does not occur, but if the gas flow causes particles to spill onto the rear surface, and if the gas flow is concentrated at one point in the moving bed, a phenomenon in which the particles are blown away is observed. . In consideration of these phenomena, a louver is used at the rear of the gas flow in the moving bed, a wire mesh is attached directly to the louver, and the structure is such that the moving particles do not come into direct contact with the wire mesh, thereby preventing clogging of the wire mesh. Particle blow-through can be solved at the same time.
しかしルーバーに直接取り付ける金網として平
織金網を使用すると、カルシウム化合物のように
付着性の強い微粉の場合には、金網の開口部が
徐々に閉塞する現象が生じるという問題がある。 However, when a plain weave wire mesh is used as the wire mesh directly attached to the louver, there is a problem in that the openings of the wire mesh gradually become clogged in the case of highly adhesive fine particles such as calcium compounds.
本考案は上記の諸点に鑑みなされたもので、ル
ーバー間に移動粒子を保持させ、ガスをルーバー
に対して直交して流すようにした移動層におい
て、ガス流れ後面のルーバーの後面に硬鋼丸線と
金属製平線または金属製丸線とですだれ織された
長いスロツト状の網目を有する金網をルーバーに
接するように固定することにより、金網の閉塞を
少なくするようにした移動層の移動粒子保持構造
を提供せんとするものである。 The present invention was developed in view of the above points, and in a moving layer in which moving particles are held between the louvers and gas is allowed to flow perpendicularly to the louvers, a hard steel circle is attached to the rear surface of the louvers at the rear of the gas flow. A wire mesh having a long slot-like mesh weaved with a wire and a metal flat wire or a metal round wire is fixed in contact with a louver, thereby reducing clogging of the wire mesh by moving particles in a moving layer. It is intended to provide a holding structure.
以下、本考案の構成を図面に基づいて説明す
る。第1図は本考案の一実施態様として、焼却炉
排ガスの乾式移動層反応装置における移動層まわ
りを示している。ルーバー1,1間に生石灰粒子
からなる移動粒子2を保持させ、HCl,SOxを含
む焼却炉排ガスをルーバー1に対して直交または
ほぼ直交して流すようにして移動層を形成する。
ガス流れ後面のルーバー1の後面に、第2図およ
び第3図に示すように、スプリング鋼線またはピ
アノ線のような硬鋼丸線3と金属製平線4とです
だれ織された長いスロツト状の網目5を有する金
網6(いわゆるタイロツド金網)をルーバー1に
接するように固定する。硬鋼丸線3としては、た
とえば直径1mmのステンレススチール線を用い、
金属製平線4としては、たとえば厚さ0.3mm、幅
3mmのステンレススチール線を用いる。またスロ
ツト状の網目の長さは50mm程度とする。なお金属
製平線4の代りに硬鋼丸線3より径の小さい金属
製丸線を使用しても差し支えない。 Hereinafter, the configuration of the present invention will be explained based on the drawings. FIG. 1 shows the area around the moving bed in a dry moving bed reactor for incinerator exhaust gas, as one embodiment of the present invention. Moving particles 2 made of quicklime particles are held between the louvers 1, 1, and incinerator exhaust gas containing HCl and SOx is caused to flow perpendicularly or almost perpendicularly to the louvers 1, thereby forming a moving layer.
On the rear surface of the louver 1 on the rear surface of the gas flow, as shown in FIGS. 2 and 3, there is a long slot weaved with a hard steel round wire 3 such as a spring steel wire or piano wire and a metal flat wire 4. A wire mesh 6 (so-called tie-rod wire mesh) having a shaped mesh 5 is fixed so as to be in contact with the louver 1. As the hard steel round wire 3, for example, a stainless steel wire with a diameter of 1 mm is used,
As the metal flat wire 4, for example, a stainless steel wire with a thickness of 0.3 mm and a width of 3 mm is used. Also, the length of the slot-like mesh should be approximately 50 mm. Note that a metal round wire having a smaller diameter than the hard steel round wire 3 may be used instead of the metal flat wire 4.
以上説明したように、本考案によればガス流れ
により粒子が移動層の後面にこぼれたり、吹き抜
けたりすることがきわめて少なく、しかも微粉が
生じても金網の目詰りを少なくすることができる
という効果を奏する。 As explained above, according to the present invention, it is extremely unlikely that particles will spill onto the rear surface of the moving bed or blow through due to the gas flow, and even if fine powder is generated, clogging of the wire mesh can be reduced. play.
第1図は本考案の移動層の移動粒子保持構造の
一実施態様を示す説明図、第2図は第1図におい
て用いる金網の一例を示す平面図、第3図は同側
面図である。
1…ルーバー、2…移動粒子、3…硬鋼丸線、
4…金属製平線、5…スロツト状の網目、6…金
網。
FIG. 1 is an explanatory diagram showing one embodiment of the moving particle holding structure of the moving layer of the present invention, FIG. 2 is a plan view showing an example of the wire mesh used in FIG. 1, and FIG. 3 is a side view of the same. 1... Louver, 2... Moving particles, 3... Hard steel round wire,
4...Metal flat wire, 5...Slot-like mesh, 6...Wire mesh.
Claims (1)
バーに対して直交して流すようにした移動層にお
いて、ガス流れ後面のルーバーの後面に硬鋼丸線
と金属製平線または金属製丸線とですだれ織され
た長いスロツト状の網目を有する金網をルーバー
に接するように固定したことを特徴とする移動層
の移動粒子保持構造。 In a moving layer where moving particles are held between the louvers and gas is allowed to flow perpendicular to the louvers, a hard steel round wire and a metal flat wire or a metal round wire are placed on the rear surface of the louver at the rear of the gas flow. A structure for retaining moving particles in a moving layer, characterized in that a wire mesh having long slot-like meshes is fixed in contact with a louver.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14542783U JPS6053336U (en) | 1983-09-20 | 1983-09-20 | Moving particle retention structure of moving layer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14542783U JPS6053336U (en) | 1983-09-20 | 1983-09-20 | Moving particle retention structure of moving layer |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6053336U JPS6053336U (en) | 1985-04-15 |
JPS64999Y2 true JPS64999Y2 (en) | 1989-01-11 |
Family
ID=30324012
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14542783U Granted JPS6053336U (en) | 1983-09-20 | 1983-09-20 | Moving particle retention structure of moving layer |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6053336U (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0525704Y2 (en) * | 1986-07-31 | 1993-06-29 | ||
KR20000067776A (en) * | 1999-09-10 | 2000-11-25 | 주식회사세일플란트 | Apparatus for purifing waste gas |
-
1983
- 1983-09-20 JP JP14542783U patent/JPS6053336U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS6053336U (en) | 1985-04-15 |
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