JPH0823414B2 - Dust removal method of sludge incinerator - Google Patents

Dust removal method of sludge incinerator

Info

Publication number
JPH0823414B2
JPH0823414B2 JP3255714A JP25571491A JPH0823414B2 JP H0823414 B2 JPH0823414 B2 JP H0823414B2 JP 3255714 A JP3255714 A JP 3255714A JP 25571491 A JP25571491 A JP 25571491A JP H0823414 B2 JPH0823414 B2 JP H0823414B2
Authority
JP
Japan
Prior art keywords
exhaust gas
sludge incinerator
bag filter
dust
dust removal
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
JP3255714A
Other languages
Japanese (ja)
Other versions
JPH0566011A (en
Inventor
丈太郎 宮田
治彦 山本
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 JP3255714A priority Critical patent/JPH0823414B2/en
Publication of JPH0566011A publication Critical patent/JPH0566011A/en
Publication of JPH0823414B2 publication Critical patent/JPH0823414B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Gasification And Melting Of Waste (AREA)
  • Chimneys And Flues (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は下水汚泥の焼却炉からの
排ガス中に含まれているダストを捕集し、清浄化して大
気中に排出する汚泥焼却炉の除塵方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust removal method for a sludge incinerator, which collects dust contained in exhaust gas from an incinerator for sewage sludge, cleans it, and discharges it into the atmosphere.

【0002】[0002]

【従来の技術】従来、汚泥焼却炉の除塵装置としては
に示すように、サイクロン11、乾式電気集塵機12、ス
クラバ13、湿式電気集塵機14を直列に接続したものが使
用されていた。しかし最近では環境上の観点から排ガス
中のダスト濃度を更に低下させることが望まれている。
Conventionally, the figure as filtration apparatus of sludge incinerator
As shown in FIG. 2 , a cyclone 11, a dry electrostatic precipitator 12, a scrubber 13, and a wet electrostatic precipitator 14 connected in series were used. However, recently, from the environmental point of view, it has been desired to further reduce the dust concentration in the exhaust gas.

【0003】ところが、電気集塵機の除塵性能を上げる
には機器自体を大型にしなけばならず、例えば、除塵性
能が90%の電気集塵機の機器寸法を100とすれば、
99%のものは200、99、9%のものは300とい
うように指数関数的に大型のものが必要になり、電気集
塵機の除塵性能のアップ率に比べ大型化が著しいという
問題がある。そこで、これを解決するために本発明者等
は小型で除塵性能の高いバグフィルタを汚泥焼却炉の除
塵装置に使用することを検討している。しかし汚泥の焼
却炉の排ガスは水分を30〜50%も含むためにダスト
の付着力が強く、払い落とし時に濾布表面からダストが
均一に落ちずにアバタ状となり、濾過再開時にこのアバ
タ部に急激にダストが付着し、圧損上昇が短時間に起き
るので安定した運転ができないという問題があった。
However, in order to improve the dust removing performance of the electrostatic precipitator, the size of the device itself must be increased. For example, if the device size of the electrostatic precipitator having a dust removing performance of 90% is 100,
99% requires 200, 99, and 9% requires 300, which is exponentially large, and there is a problem that the size of the electrostatic precipitator is significantly larger than the dust removal performance. Therefore, in order to solve this, the present inventors are studying the use of a small bag filter with high dust removal performance in a dust removal device of a sludge incinerator. However, since the exhaust gas from the sludge incinerator contains 30 to 50% of water, the dust has a strong adhesive force, and the dust does not uniformly drop from the surface of the filter cloth at the time of removing it and becomes an avatar shape. There was a problem that stable operation could not be performed because dust suddenly adhered and pressure loss increased in a short time.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解消し、汚泥焼却炉の排ガス中のダストを経
済的に、かつ安定して除去することができる汚泥焼却炉
の除塵方法を提供するために完成されたものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems, and can remove dust in the exhaust gas of a sludge incinerator economically and stably, and a dust removing method for a sludge incinerator. Has been completed in order to provide.

【0005】[0005]

【課題を解決するための手段】記の課題を解決するため
になされた本発明は、汚泥焼却炉の除塵ライン中にサイ
クロンとバグフィルタとを設けておき、汚泥焼却炉の排
ガスをサイクロンに通して粗粒ダストを除いたうえバグ
フィルタに送るとともに、一部の排ガスをサイクロンを
通すことなく直接バグフィルタに送ることによって、こ
のバグフィルタに供給される排ガス中に含まれる10μm
以上の粗粒子の割合を10%以上に調整することを特徴と
するものである。
[Means for Solving the Problems ] To solve the above problems
The present invention, which has been made possible, can be installed in a dust removal line of a sludge incinerator.
A cron and a bag filter are installed to remove sludge incinerator
The gas is passed through a cyclone to remove coarse particles and bugs.
While sending it to the filter, a part of the exhaust gas is cyclone
By sending it directly to the bug filter without passing it,
10 μm contained in the exhaust gas supplied to the bag filter of
It is characterized by adjusting the ratio of the above coarse particles to 10% or more.
Is what you do.

【0006】[0006]

【実施例】次に、本発明を図示の実施例に基づいて詳細
に説明する。図1は本発明の実施例を示すもので、1は
流動式の汚泥焼却炉、2は熱交換器、3は排ガス中のダ
ストを捕集するバグフィルタであり、バグフィルタ3と
前記汚泥焼却炉1との間には粗粒ダストを分離捕集する
ためのサイクロン4を配設してある。本実施例ではサイ
クロン4と並列にバイパス5を設けることにより、粗粒
ダストを含有する排ガスの一部をそのままバグフィルタ
3に導くことにより、バグフィルタ3に供給される排ガ
ス中の10μm 以上の粗粒子の割合を10%以上、より好ま
しくは20%以上に調整している。
EXAMPLES will be described in detail based on the illustrated embodiment of the present invention. FIG. 1 shows an embodiment of the present invention , 1 is a fluidized sludge incinerator, 2 is a heat exchanger, 3 is a bag filter for collecting dust in exhaust gas, and the bag filter 3 and the sludge incinerator are shown. A cyclone 4 for separating and collecting coarse particles is provided between the furnace 1 and the furnace 1. In this embodiment, a bypass 5 is provided in parallel with the cyclone 4 so that a part of the exhaust gas containing coarse particles is guided to the bag filter 3 as it is, so that the exhaust gas supplied to the bag filter 3 has a roughness of 10 μm or more. The proportion of particles is adjusted to 10% or more, more preferably 20% or more.

【0007】ここで10μm 以上の粗粒子の割合を10%以
上としたのは、バグフィルタ3の濾布に付着するダスト
中に粗粒子を混在させることによって払い落としを容易
にするためであって、その割合が10%未満では従来と同
様に払い落とし性が悪いためである。この粗粒子の割合
の調整はバイパス5の排ガス流量を調整することにより
行うことができる。なお、6は排ガス中のHCl 、SOX
の酸性ガスの除去、及び残留したダストを洗い流すため
のスクラバ、7は排ガスファン、8 は煙突である。
The reason for setting the ratio of coarse particles of 10 μm or more to 10% or more is to facilitate the removal by mixing coarse particles in the dust adhering to the filter cloth of the bag filter 3. The reason is that if the ratio is less than 10%, the pay-off property is poor as in the conventional case. The ratio of the coarse particles can be adjusted by adjusting the exhaust gas flow rate of the bypass 5. In addition, 6 is a scrubber for removing acidic gas such as HCl and SO X in the exhaust gas and washing away residual dust, 7 is an exhaust gas fan, and 8 is a chimney.

【0008】この除塵ラインは、汚泥焼却炉1から排出
された排ガスをサイクロン4に通して粗粒ダストを除い
たうえでバグフィルタ3に送るとともに、一部の排ガス
をバイパスダクト5を介して直接バグフィルタ3に送る
ことによりバグフィルタ3に供給される排ガス中の10μ
m 以上の粗粒子の割合を10%以上としたもので、バグフ
ィルタ3の濾布表面に付着するダスト層には粗粒ダスト
が混在することとなるので、目詰まりすることなく圧力
損失を低く保つことができるとともに、ダスト層の払い
落としの際にはダストが均一に払い落とされることとな
る。
This dedusting line passes exhaust gas discharged from the sludge incinerator 1 through a cyclone 4 to remove coarse particle dust, and then sends it to the bag filter 3, and also part of the exhaust gas directly through the bypass duct 5. 10μ in the exhaust gas supplied to the bag filter 3 by sending it to the bag filter 3
When the proportion of coarse particles of m or more is set to 10% or more, coarse particles are mixed in the dust layer adhering to the filter cloth surface of the bag filter 3, so the pressure loss is low without clogging. In addition to being able to keep it, the dust is evenly removed when the dust layer is removed.

【0009】なお、汚泥焼却炉1から排出された排ガス
中の粗粒子量が不足する場合には、粗粒子注入装置から
バグフィルタ3に粗粒子を注入することもできる。この
場合に注入される粗粒子として、サイクロンにより分離
されたものを使用できることはいうまでもないことであ
る。
Exhaust gas discharged from the sludge incinerator 1
If the amount of coarse particles inside is insufficient, use the coarse particle injection device.
It is also possible to inject coarse particles into the bag filter 3. this
Separation by cyclone as coarse particles if injected
It goes without saying that you can use the
It

【0010】[0010]

【発明の効果】本発明は以上の説明から明らかなよう
に、汚泥焼却炉の除塵ライン中にサイクロンとバグフィ
ルタを設けたので装置を大型化することなく排ガス中の
ダスト濃度を低下させることができるうえ、バイパスダ
クトによりバグフィルタに流入させる排ガス中に粒子径
10μm 以上の粗粒ダストを10%以上混入させるようにし
たので、圧力損失を低く保つことができるともに、払い
落とし性能も向上させることができ、安定した運転を行
うことができる。
As is apparent from the above description, the present invention provides a cyclone and a bag filter in the dust removal line of a sludge incinerator, so that the dust concentration in exhaust gas can be reduced without increasing the size of the device. You can do it
Particle size in the exhaust gas flowing into the bag filter due to
Since 10% or more of coarse particles of 10 μm or more are mixed, the pressure loss can be kept low, the discharging performance can be improved, and stable operation can be performed.

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

【図1】本発明の実施例を示すフローシートである。FIG. 1 is a flow sheet showing an embodiment of the present invention.

【図2】従来例を示すフローシートである。 FIG. 2 is a flow sheet showing a conventional example.

【符号の説明】[Explanation of symbols]

1 汚泥焼却炉 3 バグフィルタ 4 サイクロン 5 バイパス 1 Sludge incinerator 3 Bag filter 4 Cyclone 5 Bypass

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 汚泥焼却炉の除塵ライン中にサイクロン
バグフィルタ設けておき、汚泥焼却炉の排ガスを
サイクロンに通して粗粒ダストを除いたうえバグフィル
タに送るとともに、一部の排ガスをサイクロンを通すこ
となく直接バグフィルタに送ることによって、このバグ
フィルタに供給される排ガス中に含まれる10μm 以上の
粗粒子の割合を10%以上に調整することを特徴とする汚
泥焼却炉の除塵方法。
1. A cyclone in a dust removal line of a sludge incinerator.
And may be provided and a bag filter, the exhaust gas of sludge incinerator
After passing through a cyclone to remove coarse particles, bag fill
Not only send it to the computer but also pass some exhaust gas through a cyclone.
A dust removal method for a sludge incinerator, characterized in that the proportion of coarse particles of 10 μm or more contained in the exhaust gas supplied to the bag filter is adjusted to 10% or more by directly sending it to the bag filter.
JP3255714A 1991-09-06 1991-09-06 Dust removal method of sludge incinerator Expired - Lifetime JPH0823414B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3255714A JPH0823414B2 (en) 1991-09-06 1991-09-06 Dust removal method of sludge incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3255714A JPH0823414B2 (en) 1991-09-06 1991-09-06 Dust removal method of sludge incinerator

Publications (2)

Publication Number Publication Date
JPH0566011A JPH0566011A (en) 1993-03-19
JPH0823414B2 true JPH0823414B2 (en) 1996-03-06

Family

ID=17282628

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3255714A Expired - Lifetime JPH0823414B2 (en) 1991-09-06 1991-09-06 Dust removal method of sludge incinerator

Country Status (1)

Country Link
JP (1) JPH0823414B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5367471B2 (en) * 2009-06-11 2013-12-11 大陽日酸株式会社 Burner for producing inorganic spheroidized particles, inorganic spheroidized particle producing apparatus, and method for producing inorganic spheroidized particles
CN118320557B (en) * 2024-06-13 2024-08-23 成都伊斯顿过滤器有限公司 Shale gas filtering method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06169B2 (en) * 1989-01-13 1994-01-05 荏原インフイルコ株式会社 Exhaust gas treatment apparatus and method thereof

Also Published As

Publication number Publication date
JPH0566011A (en) 1993-03-19

Similar Documents

Publication Publication Date Title
US4220478A (en) Method for removing particulate matter from a gas stream and a method for producing a product using the removed particulate matter
US3892543A (en) Method of the removal of chemically active components from dust-laden gas streams
JPH0823414B2 (en) Dust removal method of sludge incinerator
JPS6080008A (en) Fluidized-bed combustion apparatus
JP3173999B2 (en) Waste gas treatment facility exhaust gas treatment equipment
CN207694535U (en) A kind of titanium dioxide processing exhaust dust device with bag
JP2003336080A (en) Particle recovering method and system therefor
CN114763909B (en) Boiler system of circulating fluidized bed coupling ion waterfall
JP3572148B2 (en) Dust removal device
CN206880029U (en) A kind of feed manufacturing dust arrester
CN207667308U (en) A kind of exhaust gas particle object filter device
JPH04274260A (en) Evacuation and cleaning device for electrophotography applying equipment
CN206965405U (en) A kind of flue gas ash removal machine
CN103495314A (en) Environment-friendly dust collection device
CN107185336A (en) A kind of flue gas ash removal machine
CN203764025U (en) Bag type dust collector capable of preventing bonding and blocking
JPH067892B2 (en) Backwashing method for dry dust collector
CN213527952U (en) Be used for panel raw materials dust filtration processing apparatus
Scholtens Air pollution control: a comprehensive look
KR920001254B1 (en) High performance air filter with backwash
USRE26337E (en) Vosseller method and means for conditioning gases
JPH07213837A (en) Treatment device for waste combustion gas and treatment of waste combustion gas
AU735231B2 (en) Method for cleaning dust-laden process off-gases
CN201719943U (en) A ventilation and dust isolation device
First Stack gas cleaning

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 19960906