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JPH0119928B2 - - Google Patents
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JPH0119928B2 - - Google Patents

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Publication number
JPH0119928B2
JPH0119928B2 JP54122908A JP12290879A JPH0119928B2 JP H0119928 B2 JPH0119928 B2 JP H0119928B2 JP 54122908 A JP54122908 A JP 54122908A JP 12290879 A JP12290879 A JP 12290879A JP H0119928 B2 JPH0119928 B2 JP H0119928B2
Authority
JP
Japan
Prior art keywords
gas
filling
packed bed
partition wall
cylindrical body
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
JP54122908A
Other languages
Japanese (ja)
Other versions
JPS5645722A (en
Inventor
Takahiro Yasuda
Kenzaburo Kodama
Katsumi Suehiro
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP12290879A priority Critical patent/JPS5645722A/en
Publication of JPS5645722A publication Critical patent/JPS5645722A/en
Publication of JPH0119928B2 publication Critical patent/JPH0119928B2/ja
Granted legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ガス処理装置に係り、特に集塵器や
反応器として小型化と集塵効率や反応効率の向上
することのできるガス処理装置の構造に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a gas treatment device, and particularly to a gas treatment device that can be used as a dust collector or reactor to reduce its size and improve dust collection efficiency and reaction efficiency. Regarding the structure of

〔従来の技術〕[Conventional technology]

従来、集塵器、反応器として充填層を備えたガ
ス処理装置が広範が使用されている。充填層は、
ガス処理装置が集塵器として使用される場合は砂
或は鋼球等が充填され、又ガス処理装置が反応器
として使用される場合、例えば石炭の乾留として
使用される場合は石炭が充填される。このように
充填された充填物は、上部から充填層内に連続供
給され、供給された分だけ下部から排出し、これ
を再生し、連続入れ換えできるようになつてい
る。
Conventionally, gas treatment apparatuses equipped with packed beds as dust collectors and reactors have been widely used. The packed bed is
When the gas treatment equipment is used as a dust collector, it is filled with sand or steel balls, and when the gas treatment equipment is used as a reactor, for example, when it is used for carbonization of coal, it is filled with coal. Ru. The packed material thus filled is continuously supplied into the packed bed from the upper part, and the supplied amount is discharged from the lower part to be regenerated and replaced continuously.

以下、集塵器として使用された場合を例に説明
する。従来の充填層を備えた集塵器は、第5図に
示す如く充填層5が円筒体2と同心状に、その内
部に配設され、ガス入口部1から入つたガスは充
填層5の外側から内側に向つて通過した後、円筒
体2の中心部に集められ出口6から出るようにな
つていた。
Hereinafter, the case where it is used as a dust collector will be explained as an example. In a conventional precipitator equipped with a packed bed, a packed bed 5 is disposed concentrically with the cylindrical body 2 as shown in FIG. After passing from the outside to the inside, it was collected at the center of the cylinder 2 and exited from the outlet 6.

このような構造の集塵器において、充填物とガ
スの接触時間を長くして集塵効率を向上させるた
めには、充填層5の厚さを厚くするか、ガスの流
速を遅くするために円筒体2の径を大きくしてい
た。
In a dust collector with such a structure, in order to increase the contact time between the filling material and the gas and improve the dust collection efficiency, it is necessary to increase the thickness of the filling layer 5 or to slow down the gas flow rate. The diameter of the cylindrical body 2 was increased.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、充填層5の層の厚さを厚くする
か、円筒体2の径を大きくするかのいずれかによ
つて集塵器の集塵効率を上げたり、反応器の反応
効率を上げる上述の従来の手段においては、集塵
器や反応器が大型化し、高圧、高真空で使用され
るものでは強度上問題があり、円筒体2の肉厚が
厚くなつて不経済であるのみならず、円筒体2の
径を大きくしてガス流速を遅くし、集塵効率や反
応効率を向上させるには自ら限界があるという問
題点があつた。
However, by either increasing the thickness of the packed bed 5 or increasing the diameter of the cylindrical body 2, the dust collection efficiency of the dust collector can be increased, or the reaction efficiency of the reactor can be increased. In conventional means, the dust collector and reactor become large, and those used under high pressure and high vacuum have problems in terms of strength, and the wall thickness of the cylindrical body 2 becomes thick, which is not only uneconomical. There is a problem in that there is a limit to increasing the diameter of the cylindrical body 2 to slow down the gas flow rate and improve dust collection efficiency and reaction efficiency.

又充填物の充填量の増大と相対的に円筒体2を
大型化することが難しく、流速もあまり遅くない
ことにより、ガスと充填物の接触時間も相対的に
短かく集塵効率や反応効率を向上させることが困
難であるという問題点があつた。
In addition, it is difficult to increase the size of the cylindrical body 2 relative to the increase in the amount of filling material, and the flow rate is not very slow, so the contact time between the gas and the filling material is relatively short, which improves dust collection efficiency and reaction efficiency. The problem was that it was difficult to improve.

〔発明の目的〕[Purpose of the invention]

本発明は上記のような課題を解決するためにな
されたもので、小型化できるとともに高圧、高真
空中での強度上の問題を解決し、集塵器や反応器
として集塵効率や反応効率を向上させる限界を拡
大できるガス処理装置を提供することを目的とす
るものである。
The present invention was made to solve the above-mentioned problems, and it is possible to reduce the size, solve the problem of strength under high pressure and high vacuum, and improve dust collection efficiency and reaction efficiency as a dust collector or reactor. It is an object of the present invention to provide a gas treatment device that can expand the limits of improvement.

〔課題を解決するための手段〕[Means to solve the problem]

上記課題を解決するための本発明のガス処理装
置は、円筒体の中心部に、筒状の仕切壁を同心に
配設し、円筒体と仕切壁との間の環状空間に複数
の充填層を放射状に配設して該充填層により区切
られた部分を交互にガス入口部、ガス出口部とな
し、前記仕切壁内を前記充填層内の充填物の搬送
路又はガス流路となして、前記充填層又はガス出
口座に連通したことを特徴とするものである。
In order to solve the above problems, the gas treatment device of the present invention includes a cylindrical partition wall arranged concentrically in the center of a cylindrical body, and a plurality of packed layers in an annular space between the cylindrical body and the partition wall. are arranged in a radial manner, and the portions separated by the packed bed are alternately used as a gas inlet part and a gas outlet part, and the inside of the partition wall is used as a transport path for the filling in the packed bed or a gas flow path. , which is characterized in that it communicates with the packed bed or the gas outlet.

〔作 用〕[Effect]

上記の如く構成された本発明のガス処理装置
は、充填層を円筒体内の環状空間で放射状に配設
しているので、高圧、高温ガスを取扱うに於いて
設置条件が厳しく、コンパクトな集塵器や反応器
を要求される場合でも、充填層体積を大きくとる
ことができ、且つガスを円筒体内に充満させ乍ら
流すことができ、従つてガスの流速が遅く、ガス
と充填層内の充填物との接触時間が長くなり、集
塵或いは反応効率を向上できる集塵器や反応器を
実現できる。
In the gas treatment device of the present invention configured as described above, the packed beds are arranged radially in the annular space inside the cylindrical body, so installation conditions are strict when handling high-pressure and high-temperature gas, and compact dust collection is possible. Even if a vessel or reactor is required, the volume of the packed bed can be large, and the gas can flow while filling the cylinder, so the flow rate of the gas is low, and the gas and the inside of the packed bed are It is possible to realize a dust collector or reactor in which the contact time with the filler is extended, and dust collection or reaction efficiency can be improved.

また本発明のガス処理装置は、円筒体中心部に
同心に配設した筒状の仕切壁内を充填層内の充填
物の搬送路又はガス流路となして充填層又はガス
出口座に連通しているので、充填物の搬送機構を
コンパクトにしたり、又はガス流路をコンパクト
にしたりすることができて、一層集塵器や反応器
のコンパクト化に対応できると共に高圧、高真空
での強度上の問題も解決でき、集塵或いは反応効
率を向上させる限界を大幅に拡大できることとな
る。
Further, in the gas treatment device of the present invention, the inside of the cylindrical partition wall arranged concentrically at the center of the cylindrical body serves as a transport path for the filling in the packed bed or a gas flow path, and communicates with the packed bed or the gas outlet port. Because of this, it is possible to make the packing transport mechanism more compact or the gas flow path more compact, making it possible to make dust collectors and reactors even more compact, as well as providing strength under high pressure and high vacuum conditions. The above problem can also be solved, and the limits for improving dust collection or reaction efficiency can be greatly expanded.

〔実施例〕 本発明のガス処理装置の実施例を集塵器の場合
について説明する。
[Example] An example of the gas treatment apparatus of the present invention will be described in the case of a dust collector.

第1図及び第2図は、充填層を備えた集塵器の
横断面図で、図において円筒体2の中心部に、同
心状に筒状の仕切壁3が設けられ、この円筒体2
と仕切壁3との間の環状の空間に複数、本例では
16個の充填層5を放射状に配設して、該充填層5
により区切られた部分を交互にガス入口部12、
ガス出口部13となしている。
1 and 2 are cross-sectional views of a dust collector equipped with a packed bed. In the figures, a cylindrical partition wall 3 is provided concentrically at the center of a cylindrical body 2.
In the annular space between the partition wall 3 and the partition wall 3, there are a plurality of
16 filling layers 5 are arranged radially, and the filling layers 5
Gas inlet portions 12,
It serves as a gas outlet section 13.

充填層5は、通気性のある部材13、例えば鋼
球等の隙間部に砂粒或は鋼球等が充填されてい
る。
The filling layer 5 is formed by filling gaps between air-permeable members 13, such as steel balls, with sand grains, steel balls, or the like.

第1図は、仕切壁3の内部を充填層5の充填物
の搬送路として利用するようにしたもので、10
は搬送機、例えばエレベータ等である。第2図
は、仕切壁3の内部をガス流路4として利用した
もので、仕切壁3はガス出口部11部分のみ通気
口14をもたせている。
In FIG. 1, the inside of the partition wall 3 is used as a conveyance path for the filling material of the filling layer 5.
is a conveyor, such as an elevator. In FIG. 2, the inside of the partition wall 3 is used as a gas flow path 4, and the partition wall 3 has a vent hole 14 only at the gas outlet portion 11. As shown in FIG.

第3図は、第1図の縦断面図で、図において1
はガス入口用座で、第1図に示したガス入口部1
2に連通している。又このガス入口用座1から入
つたガスは、第1図に示すガス出口部11に入ら
ないようになつている。上記ガス入口部12の上
部はプレート22によつて閉塞されている。
Figure 3 is a longitudinal sectional view of Figure 1, with 1
is the gas inlet seat, which is located at the gas inlet section 1 shown in Fig. 1.
It is connected to 2. Further, gas entering from this gas inlet seat 1 is prevented from entering the gas outlet portion 11 shown in FIG. The upper part of the gas inlet section 12 is closed by a plate 22.

一方第1図におけるガス出口部11は、その上
部がプレート18で空間部19が形成されてお
り、この空間部19にガス出口座6が接続され、
ガスはここから排出されるようになつている。
On the other hand, the gas outlet section 11 in FIG. 1 has a plate 18 at its upper part and a space 19 formed therein, and the gas outlet port 6 is connected to this space 19.
Gas is supposed to be exhausted from here.

なお、第3図中10は充填物搬送機、例えばエ
レベータ等である。分離装置23は一種のふるい
部分で、充填物に付着した塵埃はここでふるい落
され、きれいになつた充填物は、エレベータで再
び上方へ運搬される。塵埃を含んだ充填物は排出
口20から塵埃・充填物分離装置に流れる。又ガ
ス入口部で落下した塵埃は排出口21からそれぞ
れ排出される。なお17は充填物の量を調節する
ためのダンパ装置である。
In addition, 10 in FIG. 3 is a filling conveying machine, for example, an elevator. The separator 23 is a kind of sieve part, in which dust adhering to the filling is screened out, and the cleaned filling is transported upward again by an elevator. The dust-laden filling flows from the outlet 20 to the dust/fill separation device. Further, dust that has fallen at the gas inlet is discharged from the discharge port 21, respectively. Note that 17 is a damper device for adjusting the amount of filling material.

第4図は、第2図の縦断面図で、1はガス入口
座で第2図に示すガス入口部12に連通してい
る。又このガス入口座1から入つたガスは、第2
図に示すガス出口部11には入らないようになつ
ている。
FIG. 4 is a longitudinal sectional view of FIG. 2, and numeral 1 denotes a gas inlet port which communicates with the gas inlet section 12 shown in FIG. Also, the gas that entered from this gas entry account 1 is transferred to the 2nd gas account.
It is designed so that it does not enter the gas outlet section 11 shown in the figure.

上記ガス入口部の上部は、プレート22によつ
て閉塞されている。一方第2図に示すガス出口部
11は、その上部がプレート22で閉塞されてお
り、仕切壁3に設けた通気口14によつて、仕切
壁3の内部のガス通路4を連通しており、このガ
ス通路4は、ガス出口座6に接続されている。な
お7は充填物搬送機、8は充填層5に充填物を分
配するための分配路、9は充填物の充填量を調節
するための抜取機である。排出口20,21につ
いては、第3図のところで説明したのと同じであ
るのでここでは省略する。
The upper part of the gas inlet section is closed by a plate 22. On the other hand, the gas outlet section 11 shown in FIG. , this gas passage 4 is connected to a gas outlet 6. Note that 7 is a filling conveyor, 8 is a distribution path for distributing the filling to the packed bed 5, and 9 is a extractor for adjusting the filling amount of the filling. Since the discharge ports 20 and 21 are the same as those described in FIG. 3, their description will be omitted here.

以上のように構成した本発明の集塵器としての
ガス処理装置の実施例において、ガス入口座1か
ら入つたガスは、ガス入口部12内に入つて充満
し、通気性のある部材13を通つて充填層5内に
入り、ここで除塵された後、別の通気性のある部
材13を通つてガス出口部11に入る。このよう
にしてガス出口部11に入つたガスは、第1図及
び第3図に示す実施例では、空間部19に集ま
り、ガス出口座6から排出される。又第2図及び
第4図に示す実施例では、仕切壁3に設けた通気
口14を通つて、ガス通路4に集まり、ここから
ガス出口座6に導かれて排出される。一方充填物
は、連続的に充填層5内に供給され、分離装置に
よつて塵埃を除去しながら排出され、充填層5内
の充填物は連続的に入れ換えられる。この充填物
の入れ換えに際して第3図の実施例を、充填物を
介して高温ガスの熱を回収する装置として使用し
た場合、充填物の搬送路が、この装置の中心部を
通るので熱損失がない。
In the embodiment of the gas treatment device as a dust collector of the present invention configured as described above, the gas entering from the gas inlet port 1 enters the gas inlet portion 12 and fills the gas inlet portion 12, and the gas permeable member 13 is The gas passes through the packed bed 5 and, after being dedusted there, enters the gas outlet 11 through another air permeable member 13. In the embodiment shown in FIGS. 1 and 3, the gas that has entered the gas outlet portion 11 in this manner collects in the space 19 and is discharged from the gas outlet port 6. In the embodiments shown in FIGS. 2 and 4, the gas passes through the vent hole 14 provided in the partition wall 3, collects in the gas passage 4, and is led to the gas outlet port 6 and discharged from there. On the other hand, the filling material is continuously supplied into the filling bed 5, and is discharged while removing dust by a separator, and the filling material in the filling bed 5 is continuously replaced. When replacing the filling, if the embodiment shown in Fig. 3 is used as a device for recovering heat from high-temperature gas through the filling, the feeding path for the filling passes through the center of the device, reducing heat loss. do not have.

〔発明の効果〕〔Effect of the invention〕

上記詳述した通り本発明のガス処理装置は、円
筒体の中心部に、筒状の仕切壁を同心に設け、円
筒体と仕切壁との間の環状空間に複数の充填層を
放射状に配置して該充填層により区切られた部分
を交互にガス入口部、ガス出口部となし、前記仕
切壁内を前記充填層内の充填物の搬送路又はガス
流路となして、前記充填層又はガス出口座に連通
したものであるから、充填物の充填量を多くする
ことができて実質上充填層の層を厚くして充填層
体積を大きくすることができ、且つガスを円筒体
内に充満させ乍ら流すことができ、従つてガスの
流速が遅く、ガスと充填層内の充填物との接触時
間が長くなり、集塵或は反応効率を向上できる集
塵器や反応器を実現できる。また本発明のガス処
理装置は、筒状の仕切壁内を充填層内の充填物の
搬送路又はガス流路となして充填層又はガス出口
座に連通しているので、充填物の搬送機構をコン
パクトにしたり、又はガス流路をコンパクトにし
たりすることができて一層集塵器や反応器のコン
パクト化に対応できると共に高圧、高真空での強
度上の問題も解決でき集塵或は反応効率を向上さ
せる限界を大巾に拡大できることとなり、その効
果多大なるものがある。
As detailed above, in the gas treatment device of the present invention, a cylindrical partition wall is provided concentrically at the center of the cylindrical body, and a plurality of packed layers are arranged radially in the annular space between the cylindrical body and the partition wall. The parts separated by the packed bed are alternately used as a gas inlet part and a gas outlet part, and the inside of the partition wall is used as a conveyance path or a gas flow path for the filling in the packed bed. Since it communicates with the gas outlet port, it is possible to increase the amount of filling material, substantially thicken the layer of the packed bed and increase the volume of the packed bed, and fill the cylinder with gas. It is possible to realize dust collectors and reactors that can flow while allowing the gas to flow, thereby slowing down the gas flow rate and increasing the contact time between the gas and the packing in the packed bed, thereby improving dust collection or reaction efficiency. . Further, in the gas treatment device of the present invention, the inside of the cylindrical partition wall serves as a transport path for the filling in the packed bed or a gas flow path and communicates with the packed bed or the gas outlet, so that the filling transport mechanism It is possible to make the dust collector and reactor more compact by making the gas flow path more compact, and it also solves the problem of strength under high pressure and high vacuum. This means that the limits for improving efficiency can be greatly expanded, and the effects are significant.

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

第1図は集塵器としての本発明のガス処理装置
の一実施例を示す横断面図、第2図は他の実施例
の横断面図、第3図は第1図の集塵器としてのガ
ス処理装置の縦断面図、第4図は第2図の集塵器
としてのガス処理装置の縦断面図、第5図は従来
の充填層を備えた集塵器の横断面図である。 2……円筒体、3……仕切壁、4……ガス通
路、5……充填層、6……ガス出口座、10……
搬送機、11……ガス出口部、12……ガス出口
部、13……通気性のある部材、14……通気
口。
Fig. 1 is a cross-sectional view showing one embodiment of the gas treatment device of the present invention as a dust collector, Fig. 2 is a cross-sectional view of another embodiment, and Fig. 3 is a cross-sectional view showing an embodiment of the gas processing device of the present invention as a dust collector. FIG. 4 is a vertical cross-sectional view of the gas treatment device as a dust collector in FIG. 2, and FIG. 5 is a cross-sectional view of a conventional dust collector equipped with a packed bed. . 2... Cylindrical body, 3... Partition wall, 4... Gas passage, 5... Filled layer, 6... Gas outlet port, 10...
Conveyor, 11...Gas outlet section, 12...Gas outlet section, 13...Breathable member, 14...Vent hole.

Claims (1)

【特許請求の範囲】[Claims] 1 円筒体の中心部に、筒状の仕切壁を同心に配
設し、円筒体と仕切壁との間の環状空間に複数の
充填層を放射状に配設して該充填層により区切ら
れた部分を交互にガス入口部、ガス出口部とな
し、前記仕切壁内を前記充填層内の充填物の搬送
路又はガス流路となして、前記充填層又はガス出
口座に連通したことを特徴とするガス処理装置。
1 A cylindrical partition wall is arranged concentrically at the center of the cylindrical body, and a plurality of filling layers are arranged radially in the annular space between the cylindrical body and the partition wall, and the space is separated by the filling layers. The parts are alternately designated as a gas inlet part and a gas outlet part, and the inside of the partition wall is used as a conveyance path for the filling in the packed bed or a gas flow path, which communicates with the packed bed or the gas outlet port. gas treatment equipment.
JP12290879A 1979-09-25 1979-09-25 Structure of packing layer type dust collector and the like Granted JPS5645722A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12290879A JPS5645722A (en) 1979-09-25 1979-09-25 Structure of packing layer type dust collector and the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12290879A JPS5645722A (en) 1979-09-25 1979-09-25 Structure of packing layer type dust collector and the like

Publications (2)

Publication Number Publication Date
JPS5645722A JPS5645722A (en) 1981-04-25
JPH0119928B2 true JPH0119928B2 (en) 1989-04-13

Family

ID=14847581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12290879A Granted JPS5645722A (en) 1979-09-25 1979-09-25 Structure of packing layer type dust collector and the like

Country Status (1)

Country Link
JP (1) JPS5645722A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008081798A1 (en) * 2006-12-28 2008-07-10 Shin-Etsu Polymer Co., Ltd. Selectively permeable material, method for producing selectively permeable membrane structure, selectively permeable membrane structure, and air conditioning system

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3311108A1 (en) * 1983-03-26 1984-09-27 Klöckner-Humboldt-Deutz AG, 5000 Köln GAS CLEANING FILTER
JPS62140926U (en) * 1986-02-25 1987-09-05
CN103230723B (en) * 2013-04-22 2015-01-07 西安西热锅炉环保工程有限公司 Annular sectional cross-flow fume cleaning adsorption tower

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52120282A (en) * 1976-04-02 1977-10-08 Taiyo Chuki Kk Gas purification apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008081798A1 (en) * 2006-12-28 2008-07-10 Shin-Etsu Polymer Co., Ltd. Selectively permeable material, method for producing selectively permeable membrane structure, selectively permeable membrane structure, and air conditioning system

Also Published As

Publication number Publication date
JPS5645722A (en) 1981-04-25

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