JPS6025175B2 - Fine mist separation device - Google Patents

Fine mist separation device

Info

Publication number
JPS6025175B2
JPS6025175B2 JP7501476A JP7501476A JPS6025175B2 JP S6025175 B2 JPS6025175 B2 JP S6025175B2 JP 7501476 A JP7501476 A JP 7501476A JP 7501476 A JP7501476 A JP 7501476A JP S6025175 B2 JPS6025175 B2 JP S6025175B2
Authority
JP
Japan
Prior art keywords
exhaust gas
fibrous filter
mist
separation device
introduction chamber
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
JP7501476A
Other languages
Japanese (ja)
Other versions
JPS531372A (en
Inventor
繁治 鬼頭
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP7501476A priority Critical patent/JPS6025175B2/en
Publication of JPS531372A publication Critical patent/JPS531372A/en
Publication of JPS6025175B2 publication Critical patent/JPS6025175B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はガスまたは蒸気等のガス流から微細ミスト分離
する微細ミスト分離装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fine mist separation device for separating fine mist from a gas stream such as gas or steam.

従来、可溶性ダストあるいはミスト等を含有するガス又
は蒸気等のガス流から微細ミストを分離する分離装置と
しては、適当な間隔に保持された多数の波形衝突板を有
する衝突板ミスト分離器が広く知られている。
Conventionally, as a separation device for separating fine mist from a gas flow such as gas or steam containing soluble dust or mist, an impingement plate mist separator having a large number of corrugated impingement plates held at appropriate intervals has been widely known. It is being

この衝突板ミスト分離器は比較的高ガス流速で圧力損失
も少なく、微細ミストを分離除去することができるもの
であるが、しかしながら効率よく分離除去できるミスト
粒径はせいぜし、10ム程度までであり、それ以下の細
かい粒径の微細ミストの分離には効率が非常に低下する
という欠点があった。まず金網分離器を2段以上設け、
ガス類が第1段金網分離器を通過する流速を、その金網
が微細ミストに対して最高分離効率を発揮する限界流速
より高速とし、大きい粒径になったミストを第2段以下
の金網分離器で除去するミスト分離装置も知られている
が、このものは第2段以下の金網分離器の通過ガス流速
を、第1段金網分離器のガス流速よりもかなり4・さく
する必要があり、そのため第2段以下の金網分離器のガ
ス通過面積を大きくする必要があり、分離装置全体が大
型かつ複数となり、設置面積が増大し、価格的にも高価
となり、さらに圧力損失が非常に大きい等、多くの欠点
があった。
This collision plate mist separator has a relatively high gas flow rate and low pressure loss, and can separate and remove fine mist. However, the mist particle size that can be efficiently separated and removed is at most about 10 mm. However, separation of fine mist having a particle size smaller than this has the disadvantage that the efficiency is extremely reduced. First, install two or more wire mesh separators,
The flow rate at which the gases pass through the first stage wire mesh separator is set higher than the critical flow velocity at which the wire mesh exhibits the highest separation efficiency for fine mist, and the mist with large particle size is separated by the wire mesh in the second stage and below. There is also a known mist separator that removes mist using a device, but with this device, the flow rate of gas passing through the wire mesh separators in the second and lower stages must be considerably lower than the gas flow rate in the first stage wire mesh separators. Therefore, it is necessary to increase the gas passage area of the wire mesh separator in the second stage and below, making the entire separation device large and multiple, increasing the installation area, making it expensive, and furthermore, the pressure loss is extremely large. There were many drawbacks.

本発明の微細ミスト分離装置は従来のこのような欠点を
解決した微細分離装置であり、堅型の分離塔内の下方部
に支持枠内に設けられた複数個の繊維状フィルターを並
立して設置し、その上方部に排ガス中間室を隔てて折板
型衝突板よりなるミスト分離器を配談し、各繊維状フィ
ルターの頂部と頂部および底部と底部とをそれぞれ交互
に遮蔽板で連結して繊維状フィルターの下方部に排ガス
導入口を有する排ガス導入室を形成し、底部と底部とを
連結した漏斗状の遮蔽板に液貯留槽中に関口する液滴排
出口を設け、さらにその繊維状フィルターを通して前記
排ガス導入室と連結した排ガス中間室の上部に、折板型
衝突板よりなるミスト分離器を配設するとともに、繊維
状フィルターのガス流入側の排ガス導入室内に頃霧ノズ
ルを繊維状フィルター側に開口して設置した微細ミスト
分離装置である。
The fine mist separator of the present invention is a fine mist separator that solves these conventional drawbacks, and includes a plurality of fibrous filters installed in a support frame in parallel at the lower part of a rigid separation column. A mist separator consisting of a folded plate type collision plate is arranged above the exhaust gas intermediate chamber, and the top and bottom of each fibrous filter are alternately connected with shielding plates. An exhaust gas introduction chamber having an exhaust gas inlet is formed in the lower part of the fibrous filter, a funnel-shaped shielding plate connecting the bottoms is provided with a droplet outlet that enters the liquid storage tank, and the fiber A mist separator made of a folded plate-type collision plate is installed in the upper part of the exhaust gas intermediate chamber which is connected to the exhaust gas introduction chamber through the fibrous filter, and a mist nozzle is installed in the exhaust gas introduction chamber on the gas inflow side of the fibrous filter. This is a fine mist separation device installed with an opening on the side of the filter.

さらに詳しい本発明の構成を一具体例を示す第1図に基
ずし、て説明すれば分離塔1の下部の排ガス導入室2に
開口して排ガス導入室口3を設ける。
A more detailed explanation of the structure of the present invention will be given with reference to FIG. 1 showing a specific example. An exhaust gas introduction chamber opening 3 is provided in an exhaust gas introduction chamber 2 at the bottom of the separation column 1.

そして分離塔1内の排ガス導入室2の上方に、アングル
等の支持腕4によって支持枠5内に保持された天然繊維
、合成繊維あるいはガラス繊維等よりなる複数の繊維状
フィルター6を設置する。
A plurality of fibrous filters 6 made of natural fibers, synthetic fibers, glass fibers, etc. are installed above the exhaust gas introduction chamber 2 in the separation tower 1 and held in a support frame 5 by support arms 4 such as angles.

なお繊維状フィルター6の表面はその飛散を防止するた
め金網7等で包囲することが好ましい。そして複数の繊
維状フィルター6をそれぞれ保持する支持枠5のうち最
外周の支持枠5と分離塔1とを排ガスか吹抜けしないよ
う遮蔽板8で密封するとともに、各支持枠5相互間を、
図示するように排ガス吹抜防止兼、橘集液滴排出用の遮
蔽板8で頂部と頂部および底部と底部とを交互に密封し
排ガス導入室2よりの排ガスが繊維状フィルター6の部
分のみを通過するよう密封保持する。そして複数の綾織
状フィルター6を通して排ガス導入室2と連結した排ガ
ス中間室9の上部に、適当な間隔に保持された多数の折
板型衝突板10よりなるミスト分離器11を配設する。
さらに、各繊維状フィルター6の排ガス流入側の排ガス
流入側の排ガス導入室2内に頃霧ノズル12を繊維フィ
ルター6側に向けて設置した横造よりなる微細ミスト分
離装置である。
Note that the surface of the fibrous filter 6 is preferably surrounded by a wire mesh 7 or the like to prevent it from scattering. The outermost support frame 5 of the support frames 5 holding the plurality of fibrous filters 6 and the separation tower 1 are sealed with a shielding plate 8 to prevent exhaust gas from blowing through, and the spaces between each support frame 5 are
As shown in the figure, the top part and the bottom part are alternately sealed with shielding plates 8 for preventing exhaust gas blowing and for discharging Tachibana liquid droplets, so that the exhaust gas from the exhaust gas introduction chamber 2 passes only through the fibrous filter 6. Keep it tightly sealed. A mist separator 11 consisting of a large number of folded plate type collision plates 10 held at appropriate intervals is disposed above the exhaust gas intermediate chamber 9 which is connected to the exhaust gas introduction chamber 2 through a plurality of twill filters 6.
Furthermore, it is a fine mist separation device made of a horizontal structure in which a mist nozzle 12 is installed in the exhaust gas introduction chamber 2 on the exhaust gas inflow side of each fibrous filter 6 so as to face the fiber filter 6 side.

なお繊維状フィルター6は90〜聡%、好ましくは92
〜95%程度の気孔率を有するものを5〜35柳程度の
厚さで使用するとよい。また、ミスト分離器11を形成
する折板型衝突板10‘こ、各種形状の衝突片および捕
集橘を設けることはより好ましいものである。
The fibrous filter 6 has a content of 90% to 92%, preferably 92%.
It is preferable to use a material having a porosity of about 95% and a thickness of about 5 to 35 willows. Further, it is more preferable that the folded plate type collision plate 10' forming the mist separator 11 is provided with collision pieces and collection particles of various shapes.

さらに、折板型衝突板101こ瓶集液滴排出用の溝等を
設けることも好ましい。
Furthermore, it is also preferable that the folded plate type collision plate 101 be provided with a groove for collecting and discharging droplets from the bottle.

本発明の微細ミスト分離器装置は以上のような構成より
成るものであるので、可溶性ダストあるいはミストを含
有するガス、または蒸気等の排ガス流が、分離塔1の下
部の排ガス導入口3より排ガス導入室2に導入されると
、排ガス流は分離塔1内に上昇し、贋霧ノズル12より
の噴霧によって、液体連続相を形成している繊維状フィ
ルター6に衝突し、その繊維状フィルター6中を通過し
て排ガス中間室9に入る。
Since the fine mist separator device of the present invention has the above-described configuration, the exhaust gas flow such as gas or steam containing soluble dust or mist is passed through the exhaust gas inlet 3 at the bottom of the separation column 1. Once introduced into the introduction chamber 2, the exhaust gas stream rises into the separation column 1 and, by atomization from the atomizing nozzle 12, collides with the fibrous filter 6 forming a liquid continuous phase. The exhaust gas passes through the interior and enters the exhaust gas intermediate chamber 9.

この時排ガス中に含まれる微細なダストおよびミストの
大部分は、繊維状フィルター6中の液体連続相に合体さ
れ、大粒となってその一部は下方の捕集液瓶排出用の遮
蔽板8に落下し、液封構造よりなる液滴貯留槽13をへ
て分離塔1下部の液溜14に落下する。
At this time, most of the fine dust and mist contained in the exhaust gas are combined with the liquid continuous phase in the fibrous filter 6, and become large particles, some of which are disposed of on the shielding plate 8 for discharging the collected liquid bottle below. The liquid drops to a liquid reservoir 14 at the bottom of the separation tower 1 through a liquid droplet storage tank 13 having a liquid seal structure.

一方排ガス中間室9に流入した大粒液滴を含むガス流は
、上昇して折板型衝突板10よりなるミスト分離器11
中に入り、残留大粒液滴は折板型衝突板10に衝突して
楠集除去され、より大粒となって排ガス中間室9中を落
下して捕集液滴排出用の遮蔽板8上に落ち、前述のごと
く液溜14に貯留されるとともに、ミストをほとんど含
まないガス流は分離塔1の最上部のガス排出室15より
排出されるものである。
On the other hand, the gas flow containing large droplets that has flowed into the exhaust gas intermediate chamber 9 rises to a mist separator 11 consisting of a folded plate type collision plate 10.
The remaining large droplets collide with the folded plate-type collision plate 10 to be collected and removed, become even larger droplets, fall through the exhaust gas intermediate chamber 9, and land on the shielding plate 8 for discharging the collected droplets. The gas stream that falls and is stored in the liquid reservoir 14 as described above, and that contains almost no mist, is discharged from the gas discharge chamber 15 at the top of the separation column 1.

本発明の微細ミスト分離装置は以上述べたように、1塔
の分離塔内のガス導入側に、液体連続相を形成する繊維
状フィルターを複数設け、その排出側にさらに折板型衝
突板よりなるミスト分離器を設けた2段階補集帯よりな
る微細ミスト分離装置であるので、10一以下の細かい
微細ミストおよびダストをも完全に橘集除去できるもの
であり、さらに装置の小型化が可能である。
As described above, the fine mist separator of the present invention is provided with a plurality of fibrous filters that form a continuous liquid phase on the gas introduction side of one separation column, and a folded plate type collision plate on the discharge side. This is a fine mist separation device consisting of a two-stage collection zone equipped with a mist separator of It is.

また本発明は、前記の構成を有することにより、下記の
如き作用効果がある。
Moreover, the present invention has the following effects by having the above-mentioned configuration.

(ィ)繊維状フィルターによるミストの橘集面積が大き
い。
(b) The fibrous filter has a large mist accumulation area.

{口)繊維状フィルターと折板型衝突板よりなるミスト
分離器との2重フィル夕により俺集効率がよい。
{Exposure) The double filter system consisting of a fibrous filter and a mist separator made of a folded plate type collision plate provides good collection efficiency.

し一 折板型衝突板よりなるミスト分離器により楠集さ
れた液滴が遮蔽板により集められて漏斗状の液滴排出口
より液滴貯槽中に排出されるので繊維状フィルターによ
る櫨過の障害とならない。
The droplets collected by the mist separator made of a folded plate-type collision plate are collected by the shielding plate and discharged from the funnel-shaped droplet outlet into the droplet storage tank, so that the filtration by the fibrous filter is prevented. Not a hindrance.

従って各種の排ガス流から微細ミストを分離除去できる
ものであって、大気汚染による公害防止の鶴見点よりも
極めて有用な装置である。
Therefore, it is a device that can separate and remove fine mist from various exhaust gas flows, and is a much more useful device than the Tsurumi point for preventing air pollution.

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

第1図は本発明の微細ミスト分離装置の漠式的断面図を
示す説明図である。 1・・・分離塔、2・・・排ガス導入室、3・・・排ガ
ス導入口、4…支持枠、6・・・繊維状フィルター、7
・・・金網、8・・・遮蔽板、9・・・排ガス中間室、
10・・・折板型衝突板、11・・・ミスト分離器、1
2・・・階霧ノズル、13・・・液滴貯留槽、14・・
・液溜。
FIG. 1 is an explanatory diagram showing a vague cross-sectional view of the fine mist separating device of the present invention. DESCRIPTION OF SYMBOLS 1... Separation tower, 2... Exhaust gas introduction chamber, 3... Exhaust gas inlet, 4... Support frame, 6... Fibrous filter, 7
...wire mesh, 8...shielding plate, 9...exhaust gas intermediate chamber,
10... Folded plate type collision plate, 11... Mist separator, 1
2... Floor fog nozzle, 13... Droplet storage tank, 14...
・Liquid pool.

Claims (1)

【特許請求の範囲】[Claims] 1 竪型の分離塔内の下方部に支持枠内に設けられた複
数個の繊維状フイルターを並列して設置し、その上方部
に排ガス中間室を隔てて折板型衝突板よりなるミスト分
離器を配設し、各繊維状フイルターの頂部と頂部および
底部と底部とをそれぞれ交互に遮蔽板で連結して繊維状
フイルターの下方部に排ガス導入室口を有する排ガス導
入室を形成し、底部と底部とを連結した漏斗状の遮蔽板
に液滴貯留槽中に開口する液滴排出口を設け、さらに繊
維状フイルターのガス流入側の排ガス導入室内に噴霧ノ
ズルを繊維状フイルター側に開口して設置したことを特
徴とする微細ミスト分離装置。
1. A plurality of fibrous filters installed in a support frame are installed in parallel in the lower part of a vertical separation tower, and a mist separation device consisting of a folded plate type collision plate is installed in the upper part with an intermediate chamber for exhaust gas separated. The top of each fibrous filter and the bottom of each fibrous filter are connected alternately with shielding plates to form an exhaust gas introduction chamber having an exhaust gas introduction chamber opening in the lower part of the fibrous filter. A droplet outlet opening into the droplet storage tank is provided in the funnel-shaped shielding plate connected to the bottom part, and a spray nozzle is provided in the exhaust gas introduction chamber on the gas inflow side of the fibrous filter, and a spray nozzle is opened toward the fibrous filter side. A fine mist separation device characterized by being installed at
JP7501476A 1976-06-26 1976-06-26 Fine mist separation device Expired JPS6025175B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7501476A JPS6025175B2 (en) 1976-06-26 1976-06-26 Fine mist separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7501476A JPS6025175B2 (en) 1976-06-26 1976-06-26 Fine mist separation device

Publications (2)

Publication Number Publication Date
JPS531372A JPS531372A (en) 1978-01-09
JPS6025175B2 true JPS6025175B2 (en) 1985-06-17

Family

ID=13563893

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7501476A Expired JPS6025175B2 (en) 1976-06-26 1976-06-26 Fine mist separation device

Country Status (1)

Country Link
JP (1) JPS6025175B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6326897U (en) * 1986-08-07 1988-02-22

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5915513A (en) * 1982-07-13 1984-01-26 Toray Ind Inc Production of polyester fiber
JPS63136722U (en) * 1987-02-27 1988-09-08
JP4817420B2 (en) * 2005-12-19 2011-11-16 独立行政法人産業技術総合研究所 Hydrogen production apparatus and method
KR101000723B1 (en) 2008-07-21 2010-12-14 (주)현보산업 A wet scrubber for removing substances in the phase of gas by surface contact

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6326897U (en) * 1986-08-07 1988-02-22

Also Published As

Publication number Publication date
JPS531372A (en) 1978-01-09

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