JP3779344B2 - Dust collector consisting of perforated screen - Google Patents

Dust collector consisting of perforated screen Download PDF

Info

Publication number
JP3779344B2
JP3779344B2 JP29807194A JP29807194A JP3779344B2 JP 3779344 B2 JP3779344 B2 JP 3779344B2 JP 29807194 A JP29807194 A JP 29807194A JP 29807194 A JP29807194 A JP 29807194A JP 3779344 B2 JP3779344 B2 JP 3779344B2
Authority
JP
Japan
Prior art keywords
perforated screen
perforated
oil
opening
screen
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 - Lifetime
Application number
JP29807194A
Other languages
Japanese (ja)
Other versions
JPH08131736A (en
Inventor
正博 今西
武久 木ノ山
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.)
Duskin Co Ltd
Original Assignee
Duskin 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 Duskin Co Ltd filed Critical Duskin Co Ltd
Priority to JP29807194A priority Critical patent/JP3779344B2/en
Publication of JPH08131736A publication Critical patent/JPH08131736A/en
Application granted granted Critical
Publication of JP3779344B2 publication Critical patent/JP3779344B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Separating Particles In Gases By Inertia (AREA)

Description

【0001】
【産業上の利用分野】
本発明は粉塵或いはガス流中のカーボン等の除去に利用可能な集塵部材に係り、特に微細な油粒子(油ミスト)や油蒸気を含むガス流からこれら油ミストおよび油蒸気を除去するのに効果的な集塵部材に関する。
【0002】
【従来の技術】
例えばホテルや飲食店の厨房においては調理過程で油が微細粒子(ミスト)状或いは蒸気となって大量に発生する。このような油ミスト或いは油蒸気を含有する気体(以下「油含有気体」と称する)をそのまま外部に排出することは大気汚染の一因となり、また排気ダクト内に付着した油が発火して火災を生じる危険性もある。このため油含有気体は外部に排出される前に含有する油分を除去する必要があり、油分除去用に各種の装置が提案されかつ現に用いられている。
【0003】
【発明が解決しようとする課題】
この種の従来型油除去装置のうち、例えば油蒸気を除去するものとしては活性炭等の吸着材が充填されたフィルタを用いたものが提供されている。この装置は比較的高い油蒸気除去効率を有するものの、油ミストの除去率はかなり低いため油ミストが共存する気体には不向きである。また除去した油を保持する傾向が高く、このため時間の経過とともに目詰まりを生じて圧力損失が大幅に増大し、かつ保持する油分による発火の危険性もまた大きくなるという問題がある。
【0004】
一方油ミストの除去は主として慣性衝突法が採用されている。この方法は特に油粒子が大きい場合には効果的であるが、粒子が微細な場合には捕集効率が低下する問題がある。慣性衝突を効果的に行う手段として油含有気体の通過方向に対して一定の角度(例えば30〜60度)の傾斜角をもった開口が多数形成された網目スクリーンが配置され、かつこの網目スクリーンの開口相互が90度ずつ面方向に向けて角度変位するよう複数の網目スクリーンが配置された構成が提案されている(特願昭58−27672号)。
【0005】
上記提案の構成によれば、開口相互が90度ずつ変位するため、各スクリーンの開口を通過する油含有気体は旋回流を形成し、慣性衝突方式による効果的な塵埃或いは油分の捕集が期待される。しかしながらこのような捕集効果を発揮するためには前記網目スクリーンを10枚程度、場合によっては20枚程度積層配置する必要があり、これら各網目スクリーンに付着した油分の洗浄除去もまた困難になる。
【0006】
さらにフィルタ方式の集塵では、流体の通過速度を高めても余り集塵効率は向上しないのに対し、慣性衝突方式による集塵では、低速域ではフィルタ方式に比較して効率が劣るものの、通過する流体の速度の増加に対応して集塵効率が大幅に向上する。このため流体の通過速度を高く設定すれば前記フィルタ方式に比較してより高い効率の集塵が可能となることが知られている。即ち、慣性衝突方式による集塵装置では集塵効率を高率にするためには通過流体速度を高めて運転する必要があるが、前述の如く多数の網目スクリーンを設置する構成では流体の圧力損失は多大なものとなる。このため高い流体通過速度を保持するために送風機の容量を大きくする等、従来装置に比較して装置のランニングコストがかなり上昇してうまうこになる。
【0007】
【課題を解決するための手段】
本発明は上述の問題点に鑑み構成されたものであって、油含有気体等、除去対象物を含有した流体の流れ方向に対して所定の角度の傾斜角を持った開口が多数形成されたスクリーン(以下「多孔スクリーン」と称する)が、複数枚配置され、かつ隣接する各多孔スクリーンはそれぞれ表裏が対向位置するよう180度反転させて、即ち相互に裏返しとなるように配置された構成の集塵部材において、多孔スクリーンの開口を各々区画する開口壁面には流体流れ方向に沿って1以上の溝を形成して除去対象物の捕集効率を高め、かつ油分等の捕集物を樋を用いて効率的に排除するよう構成している。
【0008】
【作用】
最初の多孔スクリーンに流入した流体は、各開口の傾斜角に対応した角度で例えば下降流となり、かつ表裏が逆に配置された次の多孔スクリーンにおいては前記下降流が反転して開口の傾斜角に沿った上昇流となる。このように各多孔スクリーンを通過する度に流体は下降・上昇を繰り返し、含有する捕集対象物、例えば油ミストの殆どが慣性衝突により捕集され、かつ油蒸気もこの過程で凝集して捕集される。捕集された捕集対象物は樋を介して集塵部材外に効率的に排除される。
【0009】
【実施例】
次に本発明の実施例を図面を参考に具体的に説明する。
【0010】
図1は本発明に使用される多孔スクリーンの一例を示す図であり、図2はこの多孔スクリーンを用いた集塵部材の構成例を示す。
【0011】
先ず図1を用いて多孔スクリーンの構成を説明する。矢印1は多孔スクリーン全体を示し、この多孔スクリーン1は例えばSUS304系のステンレス、アルミニウムまたはニッケル等の金属材料により形成されている。但し金属材料で形成されることは多孔スクリーン形成の必須の要件ではなく、これら金属材料以外に、例えばプラスッチクス或いはセラミックス等により形成することも可能であるが、以下金属材料により形成される場合を例に説明する。
【0012】
2は開口であり、多孔スクリーン1はこの開口2が多数連設されることにより形成される。例えばその形成方法としては金属板に多数の切り口(スリット)を予め形成し、かつこの金属板を所定の方向に引っ張ることにより切り口部分を開いて開口とする構成、即ちエキスパンドメタルと称される形成方法等が用いられる。各開口2は油含有気体Gの流れ方向に対して所定の角度αを以て斜めに開口している。この角度αは油含有気体Gが開口内に流入する際に含有する油分を慣性により分離し、かつその流れが乱流とならずほぼ層流を維持する程度の角度が効果的である。この様な点から発明者らが試験をした結果、前記角度αは25度乃至70度の間が適当であるとの結論に達した。
【0013】
図2は図1に示される多孔スクリーン1を3枚用いた集塵部材の構成例を示す。1aは図1に示す多孔スクリーン1を図1の配置状態と同じ状態、即ち各開口2が角度αを以て斜め上に開口している状態で配置されたものを、また1bはこの多孔スクリーンを180度反転させて、即ち裏返して配置されたものを示す。従って多孔スクリーン1bの開口2は角度αを以て下向きとなるので、多孔スクリーン1bの開口において、油含有気体Gに対する開口角度は以後−αで示す事とする。1cはこの多孔スクリーン1bを更に180度反転させて、つまり前記第1の多孔スクリーン1aの位置に戻す位置で配置されている。従って開口角度は多孔スクリーン1aと同様のαとなる。また多孔スクリーン1aの開口2は2a、同1bの開口2は2b、同1cの開口2は2cとして以下説明する。なお図示の構成では多孔スクリーン1は3枚配置されているが、4枚以上配置することももとより可能であるが、捕集効率と圧力損失とを比較考量すれば図示の3枚構成から多くても5枚構成程度とするのが好ましい。
【0014】
図3は図2に示す多孔スクリーン3枚の構成から成る集塵部材の全体を示し、各多孔スクリーン1a〜1cは枠体3により一体的な集塵部材4として構成され、この集塵部材が油含有気体流路(図示せず)に着脱可能に配置されることにより油分の捕集を行う。またこの集塵部材は使い捨てとすることももとよりより可能であるが、定期的に交換し、取り外された集塵部材を回収して洗浄工程に回し再生して再利用する方が環境衛生上或いは経済的にも望ましい。
【0015】
次に上記構成の作動状態を主として図2を用いて説明する。油含有気体Gは集塵部材4の下流側に配置された誘引型の送風機(IDF/図示せず)により吸引され第1の多孔スクリーン1aに向かう。この場合、第1の多孔スクリーン1aに於けるの油含有気体Gの流入速度は0.5〜2.0m/sec程度となるよう前記IDFが運転される。第1の多孔スクリーン1aに至った油含有気体Gは各開口2aが所定の角度αを以て斜めに開口しているため、開口壁面に衝突し含有する油ミストを開口壁面に付着させながら下降流G1を形成する。なお含有する油蒸気もこの衝突により一部凝結し前記ミストと共に付着し、付着した油は自重により多孔スクリーンに沿って流下し、図示しない油溜に捕集される。
【0016】
一方第1の多孔スクリーン1aを出た油含有気体Gは次に再度−αを以て開口する第2の多孔スクリーン1bの開口2bに流入し、前記下降流G1は一転して上昇流G2となる。この反転の際、前記第1の多孔スクリーン1bにおいて捕集されなかった油ミストの多くが慣性により振り分け除去される(図中の破線による矢印で示す)。更に上昇流G2に転じた油含有気体Gは前記第1の多孔スクリーン1aにおけると同様の慣性衝突方式により油ミストが除去されると共に油蒸気は開口壁面に凝集し除去される。
【0017】
第2の多孔スクリーン1bを出た上昇流G2は更に第3の多孔スクリーン1cにおいて再度下降流G3となり、前記第1の多孔スクリーン1aと同様の作用により残りの油分の殆どが除去される。このように上記構成においては、油含有気体Gは各多孔スクリーン1a〜1cが順次180度反転して配置されているため、上昇・下降を繰り返し、その間に衝突による油捕集、油蒸気の凝集及び流体反転時の慣性による油除去を繰り返す。この様に油含有気体Gは隣接する各多孔スクリーンの間で急激に流路を変更するため一つの多孔スクリーンに於ける油分の除去効率が高い。従って多孔スクリーンの配置枚数を例えば図示の如く3枚とし、従来の構成枚数に比較してその構成枚数が1/3〜1/10と大幅に少なくでき、しかも効率のよい油分の除去が可能となる。このため装置全体としての圧力損失を大幅に低減できる。
【0018】
図4は上記構成の多孔スクリーンの個々の開口部壁面の形状を示す。このような形状に構成することにより捕集した油分をより効率良く多孔スクリーンから除去することが可能となる。
【0019】
先ず(A)の構成では開口2を形成する壁面の一部(図示の構成では中央部)において壁面高さ方向、即ち油含有気体Gの流れ方向に沿って溝5が形成されている。この溝5の形成により開口2の壁面に衝突付着した油分は油含有気体Gの流れに助けられて溝5側に集まり、さらに当該油含有気体Gの流れ及び自然落下により順次多孔スクリーンの下部に流れ落ちる。
【0020】
同図(B)の構成はこの溝5が開口2の壁面に対して複数本形成された構成を示す。この構成では開口2の壁面に衝突付着した油分は各溝5に流入しかつこれらの溝5を伝って下降することになる。
【0021】
図5及び図6は第の実施例を示す。図中符号6は多孔スクリーンにおいて捕集した油を流す樋であって、第1の多孔スクリーン1aおよび第2の多孔スクリーン1bの間、第2の多孔スクリーン1bおよび第3の多孔スクリーン1cの間に介在配置され、かつ場合によっては第3の多孔スクリーン1cの背後にも配置される。またこの樋6はこれら各多孔スクリーン1a、1bおよび1cの間に介在配置されるスペーサとしての役目も果たす。因に油分を効率よく捕集するためには各多孔スクリーンの間は1〜3mm程度の間隔を持たせる必要があるが、前記樋6はこの間隔を保持するスペーサとしての機能も果たすことができて好都合である。
【0022】
図6(A)及び(B)は集塵部材4における樋6の配置状態を示し、(A)は集塵部材4の一方の側縁に向かって斜めに下降するよう樋6が配置されている構成を、また(B)は集塵部材4の中央部から両側縁に向かって斜めに下降するよう樋6が配置された構成を示す。何れの構成も一方若しくは両方の側縁に向かって樋6が下降するよう構成されることにより捕集した油がこの樋6に沿って流れ下るよう構成されている。また樋6の下降部側端部には集塵部材4の側縁に沿って配置された油捕集道(ヘッダ)7が設けられ、かつこの捕集道7の下端には油溜8が設けられている。なおこの油捕集道7の下端を開放させ、図示しない油含有気体流路中に設けられた共通の油溜に捕集油が集まるよう構成することももとより可能である。
【0023】
以上の構成において、第1の多孔スクリーン1aの各開口2aの壁面に沿って流れ下った油分、及び下降気流G1から上昇気流G2に変わる際に分離された油分は第1の樋6に集まる。これら各樋6は図6の如く斜めに配置されているため樋6に沿って流れ下り、集塵部材から分離除去される。なお、上昇流G2から下降流G3に転じる第2の多孔スクリーン1bと第3の多孔スクリーン1cの間に配置された部分では主として第2の開口2bの壁面に沿って吹き上げられた油を捕集除去することになる。また第3の多孔スクリーン1cの背後に配置された樋6は更に下降流G3から分離された油分を除去する。
【0024】
以上本発明の構成を、処理対象の流体が油含有気体である場合を例に説明したが、本集塵部材はもとより油分を含有する油含有気体に対してのみ有効なものではなく、固体または液体の如何を問わず種々の塵埃を含む流体に対して幅広く有効であることは当業者において容易に推測できるものである。
【0025】
【発明の効果】
本発明においては、複数枚配置されかつ隣接する各多孔スクリーンがそれぞれ表裏が対向位置するよう180度反転位置し、各多孔スクリーンを通過する流体が各多孔スクリーンの通過時に上下に波うつように流動することにより慣性・衝突集塵方式により高効率で対象物を捕集し、捕集した油分等の捕集物を多孔スクリーンの開口壁面に形成した溝に集中させ、かつ集中した捕集物を樋によって装置外部に排出するよう構成してあるため、高効率で捕集した捕集物を効果的に装置外に排除でき、従って集塵装置を長期間にわたって高効率で運転することが可能となる。
【図面の簡単な説明】
【図1】 本発明の実施例に使用される多孔スクリーンの斜視部分図である。
【図2】 多孔スクリーンを複数枚配置した集塵部材の断面部分図であって、各多孔スクリーンは図1のA−A線による断面図に相当する。
【図3】 集塵部材の一部を省略した断面図である。
【図4】 本発明の実施例であって、のB−B線における開口壁面の断面形状の構成例を各々示し、(A)は溝が一つの構成を、(B)は複数の溝が形成された構成を各々示す。
【図5】 本発明の第の実施例を示す集塵部材の断面部分図である。
【図6】 (A)及び(B)共に集塵部材における樋の配置状態を示す集塵部材の正面概略図である。
【符号の説明】
1 多孔スクリーン
1a 第1の多孔スクリーン
1b 第2の多孔スクリーン
1c 第3の多孔スクリーン
2 開口
2a 第1の多孔スクリーンの開口
2b 第2の多孔スクリーンの開口
2c 第3の多孔スクリーンの開口
3 枠体
4 (多孔スクリーンから成る)集塵部材
5 溝
6 樋
[0001]
[Industrial application fields]
The present invention relates to a dust collecting member that can be used to remove dust or carbon in a gas stream, and in particular, removes oil mist and oil vapor from a gas stream containing fine oil particles (oil mist) and oil vapor. The present invention relates to an effective dust collecting member.
[0002]
[Prior art]
For example, in a kitchen of a hotel or a restaurant, a large amount of oil is generated in the form of fine particles (mist) or steam during the cooking process. If such gas containing oil mist or oil vapor (hereinafter referred to as “oil-containing gas”) is discharged to the outside as it is, it will contribute to air pollution, and oil attached to the exhaust duct will ignite and cause a fire. There is also a risk of causing. For this reason, it is necessary to remove the oil content contained in the oil-containing gas before being discharged to the outside, and various apparatuses have been proposed and used for oil removal.
[0003]
[Problems to be solved by the invention]
Among this type of conventional oil removing device, for example, an oil removing device that uses a filter filled with an adsorbent such as activated carbon is provided. Although this apparatus has a relatively high oil vapor removal efficiency, the removal rate of oil mist is considerably low, so it is not suitable for a gas in which oil mist coexists. In addition, there is a high tendency to retain the removed oil. Therefore, there is a problem that clogging occurs with time, pressure loss is greatly increased, and the risk of ignition due to the retained oil is also increased.
[0004]
On the other hand, the inertial collision method is mainly used to remove oil mist. This method is effective particularly when the oil particles are large, but there is a problem that the collection efficiency is lowered when the particles are fine. As a means for effectively performing inertial collision, a mesh screen having a large number of openings having an inclination angle of a certain angle (for example, 30 to 60 degrees) with respect to the passage direction of the oil-containing gas is disposed, and this mesh screen There has been proposed a configuration in which a plurality of mesh screens are arranged so that the openings of each other are angularly displaced by 90 degrees in the plane direction (Japanese Patent Application No. 58-27672).
[0005]
According to the proposed configuration, since the openings are displaced by 90 degrees, the oil-containing gas passing through the openings of the screens forms a swirling flow, and effective dust or oil collection by the inertial collision method is expected. Is done. However, in order to exert such a trapping effect, it is necessary to arrange about 10 mesh screens, or in some cases about 20 mesh screens, and it is also difficult to clean and remove oil adhering to each mesh screen. .
[0006]
Furthermore, in the filter type dust collection, the dust collection efficiency is not improved much even if the fluid passage speed is increased. The dust collection efficiency is greatly improved corresponding to the increase in the speed of the fluid to be collected. For this reason, it is known that if the passage speed of the fluid is set high, dust collection with higher efficiency can be achieved as compared with the filter system. That is, in order to increase the dust collection efficiency in the dust collector using the inertial collision method, it is necessary to increase the speed of the passing fluid. However, as described above, the pressure loss of the fluid is increased in a configuration in which a large number of mesh screens are installed. Will be enormous. For this reason, the running cost of the apparatus is considerably increased as compared with the conventional apparatus, such as increasing the capacity of the blower in order to maintain a high fluid passage speed.
[0007]
[Means for Solving the Problems]
The present invention is configured in view of the above-described problems, and a large number of openings having an inclination angle of a predetermined angle with respect to a flow direction of a fluid containing an object to be removed such as oil-containing gas are formed. A plurality of screens (hereinafter referred to as “perforated screens”) are arranged, and the adjacent perforated screens are inverted 180 degrees so that the front and back faces each other, that is, arranged so as to be reversed with respect to each other. In the dust collecting member, one or more grooves are formed along the fluid flow direction in the opening wall surface that divides each opening of the perforated screen to improve the collection efficiency of the removal target, and trap the collected matter such as oil. It is configured to eliminate efficiently using
[0008]
[Action]
The fluid that has flowed into the first perforated screen becomes, for example, a downward flow at an angle corresponding to the inclination angle of each opening, and in the next perforated screen in which the front and back surfaces are reversed, the downflow is reversed and the inclination angle of the opening is reversed. Ascending current along. In this way, the fluid repeatedly descends and rises as it passes through each perforated screen, so that most of the collected object, for example, oil mist, is collected by inertial collision, and oil vapor also aggregates and is captured in this process. Be collected. The collected object to be collected is efficiently removed out of the dust collecting member through the basket.
[0009]
【Example】
Next, embodiments of the present invention will be specifically described with reference to the drawings.
[0010]
FIG. 1 is a view showing an example of a perforated screen used in the present invention, and FIG. 2 shows a configuration example of a dust collecting member using the perforated screen.
[0011]
First, the configuration of the perforated screen will be described with reference to FIG. An arrow 1 indicates the entire perforated screen, and this perforated screen 1 is formed of a metal material such as SUS304 stainless steel, aluminum, or nickel. However, forming with a metal material is not an essential requirement for the formation of a perforated screen, and other than these metal materials, for example, plastics or ceramics can be used. Explained as an example.
[0012]
Reference numeral 2 denotes an opening, and the perforated screen 1 is formed by connecting a large number of openings 2. For example, as a forming method thereof, a structure in which a large number of cuts (slits) are formed in a metal plate in advance and the cut part is opened by pulling the metal plate in a predetermined direction, that is, a formation called expanded metal. A method or the like is used. Each opening 2 opens obliquely with a predetermined angle α with respect to the flow direction of the oil-containing gas G. The angle α is effective so that the oil component contained when the oil-containing gas G flows into the opening is separated by inertia, and the flow does not become turbulent and maintains almost laminar flow. As a result of examinations by the inventors from such a point, it was concluded that the angle α is suitably between 25 and 70 degrees.
[0013]
FIG. 2 shows a configuration example of a dust collecting member using three perforated screens 1 shown in FIG. 1a shows the perforated screen 1 shown in FIG. 1 arranged in the same state as that shown in FIG. 1, that is, each opening 2 is opened obliquely upward at an angle α. Inverted, i.e., reversed. Therefore, since the opening 2 of the perforated screen 1b faces downward with an angle α, the opening angle with respect to the oil-containing gas G in the opening of the perforated screen 1b is hereinafter denoted by −α. 1c is disposed at a position where the perforated screen 1b is further inverted 180 degrees, that is, returned to the position of the first perforated screen 1a. Therefore, the opening angle is α which is the same as that of the perforated screen 1a. The aperture 2 of the perforated screen 1a is 2a, the aperture 2 of 1b is 2b, and the aperture 2 of 1c is 2c. In the configuration shown in the figure, three perforated screens 1 are arranged. However, it is possible to arrange four or more perforated screens. However, if the collection efficiency and the pressure loss are weighed, the number of the perforated screens 1 can be increased. Also, it is preferable that the number is about five.
[0014]
FIG. 3 shows the entire dust collecting member composed of three perforated screens shown in FIG. 2, and each perforated screen 1a to 1c is configured as an integrated dust collecting member 4 by a frame 3, and this dust collecting member is Oil is collected by being detachably disposed in an oil-containing gas channel (not shown). This dust collecting member can be made more disposable, but it is better to replace it periodically, collect the removed dust collecting member, put it in the cleaning process, recycle and reuse it. Economically desirable.
[0015]
Next, the operation state of the above configuration will be described mainly with reference to FIG. The oil-containing gas G is sucked by an attracting blower (IDF / not shown) disposed on the downstream side of the dust collecting member 4 and travels toward the first perforated screen 1a. In this case, the IDF is operated so that the inflow speed of the oil-containing gas G in the first perforated screen 1a is about 0.5 to 2.0 m / sec. The oil-containing gas G that has reached the first perforated screen 1a has a downward flow G1 while oil mist that collides with the opening wall surface and adheres to the opening wall surface because each opening 2a opens obliquely at a predetermined angle α. Form. The oil vapor contained therein is partially condensed by this collision and adheres together with the mist. The adhering oil flows down along the perforated screen by its own weight and is collected in an oil reservoir (not shown).
[0016]
On the other hand, the oil-containing gas G that has exited the first perforated screen 1a then flows again into the opening 2b of the second perforated screen 1b that opens with -α, and the downward flow G1 turns into an upward flow G2. During this reversal, much of the oil mist that has not been collected in the first perforated screen 1b is sorted and removed by inertia (indicated by the broken arrows in the figure). Further, oil mist is removed from the oil-containing gas G that has turned into the upward flow G2 by the same inertial collision method as that in the first perforated screen 1a, and oil vapor is condensed and removed on the opening wall surface.
[0017]
The upward flow G2 exiting the second perforated screen 1b becomes a downward flow G3 again in the third perforated screen 1c, and most of the remaining oil is removed by the same action as the first perforated screen 1a. As described above, in the above-described configuration, the oil-containing gas G is arranged so that each of the perforated screens 1a to 1c is sequentially inverted by 180 degrees. And oil removal due to inertia during fluid reversal is repeated. In this way, the oil-containing gas G has a high oil removal efficiency in one porous screen because the flow path is rapidly changed between adjacent porous screens. Thus the arrangement number of the porous screen and three as shown for example, as compared with the conventional configuration number that configuration number can be greatly reduced to 1 / 3-1 / 10, moreover enables efficient oil removal Become. For this reason, the pressure loss as the whole apparatus can be reduced significantly.
[0018]
FIG. 4 shows the shape of the wall surface of each opening of the perforated screen having the above configuration. By configuring in such a shape, it becomes possible to more efficiently remove the collected oil from the perforated screen.
[0019]
First, in the configuration of (A), the groove 5 is formed along the height direction of the wall surface, that is, the flow direction of the oil-containing gas G, in a part of the wall surface forming the opening 2 (the central portion in the illustrated configuration). The oil component that collides and adheres to the wall surface of the opening 2 due to the formation of the groove 5 is gathered on the groove 5 side with the help of the flow of the oil-containing gas G. run down.
[0020]
The configuration of FIG. 5B shows a configuration in which a plurality of the grooves 5 are formed on the wall surface of the opening 2 . In this configuration, the oil that collides and adheres to the wall surface of the opening 2 flows into the grooves 5 and descends along the grooves 5.
[0021]
5 and 6 show a second embodiment. Reference numeral 6 in the figure denotes a trough for flowing oil collected in the perforated screen, between the first perforated screen 1a and the second perforated screen 1b, and between the second perforated screen 1b and the third perforated screen 1c. And in some cases, it is also disposed behind the third perforated screen 1c. Further, the ridge 6 also serves as a spacer interposed between the perforated screens 1a, 1b and 1c. In order to efficiently collect the oil, it is necessary to provide a gap of about 1 to 3 mm between the perforated screens. However, the rod 6 can also function as a spacer for maintaining this gap. Is convenient.
[0022]
6 (A) and 6 (B) show the arrangement state of the eaves 6 in the dust collecting member 4, and FIG. 6 (A) shows the eaves 6 arranged so as to descend obliquely toward one side edge of the dust collection member 4. (B) shows a configuration in which the eaves 6 are arranged so as to descend obliquely from the central portion of the dust collecting member 4 toward both side edges. Any configuration is configured such that the oil collected by flowing down the scissors 6 flows by the scissors 6 being lowered toward one or both side edges. An oil collecting passage (header) 7 disposed along the side edge of the dust collecting member 4 is provided at the end of the descending portion of the rod 6, and an oil reservoir 8 is provided at the lower end of the collecting passage 7. Is provided. It is possible to open the bottom of the oil collecting passage 7 so that the collected oil is collected in a common oil reservoir provided in an oil-containing gas passage (not shown).
[0023]
In the above configuration, the oil component that has flowed down along the wall surface of each opening 2a of the first perforated screen 1a and the oil component that has been separated when changing from the descending airflow G1 to the ascending airflow G2 are collected in the first basket 6. Since each of these ridges 6 is disposed obliquely as shown in FIG. 6, it flows down along the ridge 6 and is separated and removed from the dust collecting member. In addition, in the part arrange | positioned between the 2nd perforated screen 1b and the 3rd perforated screen 1c which turns to the downflow G3 from the upward flow G2, the oil blown up mainly along the wall surface of the 2nd opening 2b is collected. Will be removed. Further, the eaves 6 disposed behind the third perforated screen 1c further removes the oil component separated from the descending flow G3.
[0024]
The configuration of the present invention has been described by taking the case where the fluid to be treated is an oil-containing gas as an example, but this dust collection member is not only effective for oil-containing gas containing oil as well as solid or It can be easily estimated by those skilled in the art that the present invention is widely effective for fluids containing various kinds of dust regardless of liquid.
[0025]
【The invention's effect】
In the present invention , a plurality of adjacent perforated screens are reversed 180 degrees so that the front and back are opposed to each other, and the fluid passing through each perforated screen flows so as to wave up and down when passing through each perforated screen. By collecting the collected object such as oil and the like in the groove formed in the opening wall of the perforated screen, and collecting the collected object Since it is configured to be discharged to the outside of the device by the soot, it is possible to effectively remove the collected matter outside the device, so that the dust collector can be operated with high efficiency over a long period of time. Become.
[Brief description of the drawings]
FIG. 1 is a perspective partial view of a perforated screen used in an embodiment of the present invention.
2 is a partial cross-sectional view of a dust collecting member in which a plurality of perforated screens are arranged , and each perforated screen corresponds to a cross-sectional view taken along line AA in FIG.
FIG. 3 is a cross-sectional view in which a part of the dust collecting member is omitted.
4 is an example of the present invention, and each shows a configuration example of the cross-sectional shape of the opening wall surface along the line BB in FIG. 2 , wherein (A) shows a configuration with one groove, and (B) shows a plurality of configurations. Each of the configurations in which grooves are formed is shown.
FIG. 5 is a partial cross-sectional view of a dust collecting member showing a second embodiment of the present invention.
FIGS. 6A and 6B are schematic front views of the dust collecting member showing the arrangement state of the soot in the dust collecting member.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Perforated screen 1a 1st perforated screen 1b 2nd perforated screen 1c 3rd perforated screen 2 opening 2a 1st perforated screen opening 2b 2nd perforated screen opening 2c 3rd perforated screen opening 3 Frame 4 Dust collecting member (consisting of a perforated screen) 5 Groove 6 樋

Claims (3)

多数の開口が形成された多孔スクリーンの複数枚を有する集塵用の部材であり、多孔スクリーンの各開口は流体の流れ方向に対して所定の角度で斜めに形成され、かつ隣接する各多孔スクリーンはその対向面が表裏を成すよう180度反転して配置されることにより、各多孔スクリーンを通過する流体は下降上昇を繰り返すよう構成した集塵部材において、多孔スクリーンの開口を各々区画する開口壁面に対し、流体流れ方向に沿って1以上の溝が形成されていることを特徴とする多孔スクリーンから成る集塵部材。A dust collecting member having a plurality of perforated screens in which a large number of openings are formed, each opening of the perforated screen being formed obliquely at a predetermined angle with respect to the fluid flow direction, and adjacent perforated screens Are arranged so as to be reversed 180 degrees so that the opposing surfaces are front and back, so that the fluid passing through each perforated screen repeatedly descends and rises, and the opening wall surface that divides each perforated screen opening. pair, and the dust collecting member comprising a porous screen, characterized in that one or more grooves along the fluid flow direction are formed. 多数の開口が形成された多孔スクリーンの複数枚を有する集塵用の部材であり、多孔スクリーンの各開口は流体の流れ方向に対して所定の角度で斜めに形成され、かつ隣接する各多孔スクリーンはその対向面が表裏を成すよう180度反転して配置されることにより、各多孔スクリーンを通過する流体は下降上昇を繰り返すよう構成した集塵部材において、各多孔スクリーンの間には樋が設けられ、かつ当該樋は少なくともその一端が多孔スクリーンの側縁に向かって下降するよう配置されていることを特徴とする多孔スクリーンから成る集塵部材。A dust collecting member having a plurality of perforated screens in which a large number of openings are formed, each opening of the perforated screen being formed obliquely at a predetermined angle with respect to the fluid flow direction, and adjacent perforated screens The dust collecting member is configured so that the fluid passing through each perforated screen repeatedly descends and rises by disposing 180 degrees so that the opposite surfaces are front and back, and a flaw is provided between each perforated screen. And a dust collecting member comprising a perforated screen , wherein at least one end of the soot is arranged to descend toward a side edge of the perforated screen. 多数の開口が形成された多孔スクリーンの複数枚を有する集塵用の部材であり、多孔スクリーンの各開口は流体の流れ方向に対して所定の角度で斜めに形成され、かつ隣接する各多孔スクリーンはその対向面が表裏を成すよう180度反転して配置されることにより、各多孔スクリーンを通過する流体は下降上昇を繰り返すよう構成した集塵部材において、多孔スクリーンの開口を各々区画する開口壁面に対し、流体流れ方向に沿って1以上の溝が形成され、これら多孔スクリーンの間には樋が設けられ、かつ当該樋は少なくともその一端が多孔スクリーンの側縁に向かって下降するよう配置されていることを特徴とする多孔スクリーンから成る集塵部材。A dust collecting member having a plurality of perforated screens in which a large number of openings are formed, each opening of the perforated screen being formed obliquely at a predetermined angle with respect to the fluid flow direction, and adjacent perforated screens Are arranged so as to be reversed 180 degrees so that the opposing surfaces are front and back, so that the fluid passing through each perforated screen repeatedly descends and rises, and the opening wall surface that divides each perforated screen opening. against the, one or more grooves along the fluid flow direction are formed, arranged these gutter between the perforated screen is provided, and the trough is at least such that one end is lowered toward the side edges of the perforated screen A dust collecting member comprising a perforated screen.
JP29807194A 1994-11-08 1994-11-08 Dust collector consisting of perforated screen Expired - Lifetime JP3779344B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29807194A JP3779344B2 (en) 1994-11-08 1994-11-08 Dust collector consisting of perforated screen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29807194A JP3779344B2 (en) 1994-11-08 1994-11-08 Dust collector consisting of perforated screen

Publications (2)

Publication Number Publication Date
JPH08131736A JPH08131736A (en) 1996-05-28
JP3779344B2 true JP3779344B2 (en) 2006-05-24

Family

ID=17854773

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29807194A Expired - Lifetime JP3779344B2 (en) 1994-11-08 1994-11-08 Dust collector consisting of perforated screen

Country Status (1)

Country Link
JP (1) JP3779344B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE497824T1 (en) * 2006-12-22 2011-02-15 Sulzer Chemtech Ag DEVICE FOR SEPARATING LIQUID FROM A FLUID STREAM LOADED WITH LIQUID DROPS
WO2014014159A1 (en) * 2012-07-17 2014-01-23 진우통상(주) Air purifier using ozone water generator
JP6167326B2 (en) * 2013-03-14 2017-07-26 パナソニックIpマネジメント株式会社 Paint mist processing equipment
CN103418192B (en) * 2013-08-09 2015-07-29 华南理工大学 A kind of liquefied natural gas aerosol removal device of application of paint silk screen and method
CN111547986A (en) * 2020-06-01 2020-08-18 郑庆国 Shipborne oil residue dehydration device and oil residue dehydration method

Also Published As

Publication number Publication date
JPH08131736A (en) 1996-05-28

Similar Documents

Publication Publication Date Title
US6797041B2 (en) Two stage air filter
US7314495B2 (en) Process and device for eliminating the particles contained in a stream of fluid
JP2010509564A (en) Collision filter with oil trap
US6238464B1 (en) Method and apparatus for separating droplets for particles from a gas stream
CA2168486C (en) Particle agglomeration and precipitation from a gaseous stream
JP3779344B2 (en) Dust collector consisting of perforated screen
US6068674A (en) Removal of suspended fine particles from gases by turbulent deposition
US6280491B1 (en) Cartridge filter
JPH0618604B2 (en) Device for separating droplets from a gas flow in a vertical flow-through tube
JP2003222016A (en) Dust removal apparatus
CN100509114C (en) Two-stage air filter
JP3605157B2 (en) Dust collection member
JP3070068U (en) Grease filter for kitchen
JPS5932917A (en) Method and apparatus for enhancing efficiency of internal collecting and filtering bag
JP4555233B2 (en) Device for removing particles contained in a fluid flow
JPH0842888A (en) Air filtering apparatus
JPH0740055A (en) Welding exhaust gas dust collecting device
JPH07289832A (en) Collision catching filter for oil mist collector
JPH075858Y2 (en) Mist collector
JP3098981B2 (en) Filter cleaning device
JP3503083B2 (en) Dust collection member with pressure drop gradient
JP3379795B2 (en) Filter unit
JP2726382B2 (en) Design method of suction device for local ventilation
JPH043617Y2 (en)
JPS59154119A (en) Dust collecting screen

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20051018

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20051128

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060214

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060302

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120310

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120310

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150310

Year of fee payment: 9

EXPY Cancellation because of completion of term