JPH0153084B2 - - Google Patents
Info
- Publication number
- JPH0153084B2 JPH0153084B2 JP82883A JP82883A JPH0153084B2 JP H0153084 B2 JPH0153084 B2 JP H0153084B2 JP 82883 A JP82883 A JP 82883A JP 82883 A JP82883 A JP 82883A JP H0153084 B2 JPH0153084 B2 JP H0153084B2
- Authority
- JP
- Japan
- Prior art keywords
- dust
- gas
- gas flow
- flow path
- electrode
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/01—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust by means of electric or electrostatic separators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL-COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
- F01N3/027—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means
- F01N3/0275—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles using electric or magnetic heating means using electric discharge means
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Electrostatic Separation (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Description
本発明は、排ガス等に含まれるカーボン微細粒
子を集塵、焼却するダスト集塵焼却方法に関す
る。
デイーゼルエンジン排ガス等には、気相析出型
カーボン粒子が含まれ、この粒子のほとんどは、
1μ以下の微細である。このため排ガスの集塵装
置として微細な多孔を有するセラミツクスフイル
タが用いられている。このセラミツクスフイルタ
は、第1図及び第2図に示すように、多数の多孔
質薄壁1間にガス流路21,22を形成し、ガス流
路21の出口側をセラミツク目封じ材3で密封す
るとともにガス流路22の入口側をセラミツク目
封じ材4で密封する。この場合、出口側を密封し
たガス流路21は、入口側を密封せず、入口側を
密封したガス流路22は、出口側を密封しないよ
うにして、排ガスAがガス流路21から多孔質薄
壁1を通つてガス流路22に流入するようにして
いる。
このセラミツクスフイルタは、排ガスAが多孔
質薄壁1を通る際、集塵浄化しているが、機械的
な浄化方法なので、すぐ目詰まりが生じ、極めて
高い圧損を生じる。このため長時間の使用に耐え
られない問題がある。
本発明は、上記事情に鑑みてなされたもので、
その目的とするところは、電圧を印加して集塵率
を向上するとともに圧損の上昇速度を低減でき、
しかもダストが堆積した場合に放電を利用してカ
ーボン粒子を焼却、ガス化することにより、長時
間連続運転することができるダスト集塵焼却方法
を得んとするものである。
すなわち本発明は、ダスト含有ガスを通過させ
て集塵する絶縁多孔質フイルタを挾んでガス流入
側のガス流路に金属細線からなる電極を配置し、
ガス流出側のガス流路に電極を配置し、集塵時に
上記電極間に直流又は交流電圧を印加してダスト
を捕集するとともに、ダスト焼却時に上記電極間
に交流又は交流パルス電圧を印加して、捕集され
たダストを焼却することを特徴とする。
以下本発明を図示する実施例を参照して説明す
る。第3図は本発明方法で使用するダスト集塵焼
却装置の概略断面図である。この装置は、絶縁多
孔質フイルタ11と、電極12,13とを備えて
いる。このフイルタ11は、第1図及び第2図に
示すものと同様の構造で、多数の多孔質薄壁14
間にガス流路151,152を形成し、このガス流
路151,152の出口側及び入口側にセラミツク
目封じ材16,17を設けて、排ガスAがガス流
路151から多孔質薄壁14を通つてガス流路1
52に流入するようになつている。その構造の一
例として、下記第1表に示すものが挙げられる。
The present invention relates to a dust collection and incineration method for collecting and incinerating fine carbon particles contained in exhaust gas and the like. Diesel engine exhaust gas contains gas-phase deposited carbon particles, and most of these particles are
It is microscopic, less than 1μ. For this reason, a ceramic filter having fine pores is used as a dust collector for exhaust gas. As shown in FIGS. 1 and 2, this ceramic filter has gas channels 2 1 and 2 2 formed between a large number of porous thin walls 1, and the outlet side of the gas channels 2 1 is sealed with ceramic plugs. At the same time, the inlet side of the gas flow path 22 is sealed with a ceramic sealing material 4. In this case, the gas flow path 2 1 whose outlet side is sealed is not sealed at its inlet side, and the gas flow path 2 2 whose inlet side is sealed is not sealed at its outlet side, so that the exhaust gas A is 1 through the porous thin wall 1 and into the gas flow path 2 2 . This ceramic filter collects and purifies the exhaust gas A when it passes through the porous thin wall 1, but since it is a mechanical purification method, it quickly becomes clogged, resulting in extremely high pressure loss. For this reason, there is a problem that it cannot withstand long-term use. The present invention was made in view of the above circumstances, and
The purpose is to apply voltage to improve the dust collection rate and reduce the rate of increase in pressure drop.
Furthermore, the present invention aims to provide a dust collection and incineration method that can be operated continuously for a long period of time by incinerating and gasifying carbon particles using electric discharge when dust is accumulated. That is, in the present invention, an electrode made of a thin metal wire is arranged in a gas flow path on the gas inflow side, sandwiching an insulating porous filter that allows dust-containing gas to pass through and collect dust.
An electrode is placed in the gas flow path on the gas outlet side, and a DC or AC voltage is applied between the electrodes during dust collection to collect dust, and an AC or AC pulse voltage is applied between the electrodes during dust incineration. The method is characterized in that the collected dust is incinerated. The present invention will be described below with reference to illustrative embodiments. FIG. 3 is a schematic sectional view of a dust collection and incineration device used in the method of the present invention. This device includes an insulating porous filter 11 and electrodes 12 and 13. This filter 11 has a structure similar to that shown in FIGS. 1 and 2, and has a large number of porous thin walls 14.
Gas flow paths 15 1 and 15 2 are formed between the gas flow paths 15 1 and 15 2 , and ceramic plugging materials 16 and 17 are provided on the outlet and inlet sides of the gas flow paths 15 1 and 15 2 , so that exhaust gas A can flow from the gas flow path 15 1 . Gas flow path 1 through porous thin wall 14
5 It is starting to flow into 2 . Examples of the structures include those shown in Table 1 below.
【表】
なお上表中符号D,Lは、第2図に示すフイル
タの直径及び長さを示し、符号t,p,hについ
ては第4図に示す。
一方電極12は、W,Au,Pt等の材質からな
る線径50〜1000μの金属細線からなり、ガス流入
側のガス流路151内すなわちダスト集塵側に挿
入配置されている。また電極13は、電極12と
同材質、同寸法の金属細線からなり、ガス流出側
のガス流路152内に挿入配置されている。従つ
て電極151,152が多孔質薄壁14を介して相
対向している。この場合電極12,13は、ガス
流路151,152内にすべて配置する必要がな
く、1つ又は複数個おきに挿入配置してもよい。
またガス流出側のガス流路152内に配置された
電極13′は、金属細線に限らず、例えば第5図
に示すように多孔質導体を多孔質薄壁14に沿つ
て配置したものでもよい。
しかして本発明方法は、微細カーボン粒子を含
む排ガスAを流通して多孔質薄壁14により微細
カーボン粒子を機械的に捕集する。この捕集に際
し、電極12,13間に電圧を印加する。この場
合印加電圧は、直流、交流又はこれらのパルス電
圧で、カーボン粒子が加熱酸化しない程度の比較
的低い電圧とする。電圧印加により、主として交
流の作用で微細カーボン粒子が凝集粗大化し、又
主とて直流の作用で空隙率の大きい堆積ダスト層
が形成される。従つて空隙率が大きいため圧損上
昇が防止され、又粒子が凝集粗大化するため集塵
率が向上する。
次にダストがある程度堆積すると、電極12,
13間に交流又は交番パルス電圧を印加する。こ
の場合印加電圧を高い電圧として、ストリーマ放
電を発生させ、この放電によりカーボン粒子を酸
化焼却して、ガス化する。
なお、ダスト焼却のための高電圧印加は、ガス
温度が600〜700℃以上と高くなつた時にこれと同
期して行なうのが好ましい。
以上説明したように本発明方法によれば、粒子
を凝集、粗大化して集塵率の向上を図るととも
に、堆積粒子層の空隙率を上げて圧損が上昇する
のを防止し、更にダストが堆積し、圧損が上昇し
た場合に、放電を利用してカーボン粒子を焼却、
ガス化するため、目詰りを阻止し長時間連続運転
が可能になる顕著な効果を奏する。[Table] The symbols D and L in the above table indicate the diameter and length of the filter shown in FIG. 2, and the symbols t, p, and h are shown in FIG. 4. On the other hand, the electrode 12 is made of a thin metal wire made of a material such as W, Au, or Pt and has a wire diameter of 50 to 1000 μm, and is inserted into the gas flow path 15 1 on the gas inflow side, that is, on the dust collection side. The electrode 13 is made of a fine metal wire of the same material and size as the electrode 12, and is inserted into the gas flow path 152 on the gas outlet side. Therefore, the electrodes 15 1 and 15 2 face each other with the porous thin wall 14 in between. In this case, the electrodes 12 and 13 do not all need to be placed in the gas flow paths 15 1 and 15 2 , and may be inserted every other electrode or every other electrode.
Further, the electrode 13' disposed in the gas flow path 152 on the gas outlet side is not limited to a thin metal wire, but may also be one in which a porous conductor is disposed along the porous thin wall 14, as shown in FIG. good. Thus, in the method of the present invention, the exhaust gas A containing fine carbon particles is passed through and the fine carbon particles are mechanically collected by the porous thin wall 14. During this collection, a voltage is applied between the electrodes 12 and 13. In this case, the applied voltage is a direct current, an alternating current, or a pulsed voltage thereof, and is set to a relatively low voltage that does not heat and oxidize the carbon particles. By applying a voltage, fine carbon particles are aggregated and coarsened mainly due to the action of alternating current, and a deposited dust layer with a high porosity is formed mainly due to the action of direct current. Therefore, since the porosity is large, an increase in pressure drop is prevented, and the particles are aggregated and coarsened, so that the dust collection rate is improved. Next, when a certain amount of dust accumulates, the electrode 12,
An alternating current or alternating pulse voltage is applied between 13 and 13. In this case, the applied voltage is set to a high voltage to generate a streamer discharge, and the carbon particles are oxidized and burned by this discharge, and are gasified. Note that the application of high voltage for dust incineration is preferably performed in synchronization with the gas temperature rising to 600 to 700° C. or higher. As explained above, according to the method of the present invention, the particles are aggregated and coarsened to improve the dust collection rate, and the porosity of the deposited particle layer is increased to prevent pressure loss from increasing, and the dust is further deposited. However, when the pressure drop increases, the carbon particles are incinerated using electrical discharge.
Because it is gasified, it has the remarkable effect of preventing clogging and allowing continuous operation for long periods of time.
第1図は、従来使用されていたセラミツクスフ
イルタの構造モデルを示す正面図、第2図は同断
面図、第3図は本発明の一実施例を示すダスト集
塵焼却装置の構造モデル図、第4図は第1表の構
造特性における記号t,p,hを示す説明図、第
5図は本発明の他の実施例を示すダスト集塵焼却
装置の構造モデル図である。
11……絶縁多孔質フイルタ、12,13……
電極、14……多孔質薄壁、151,152……ガ
ス流路、16,17……セラミツク目封じ材。
FIG. 1 is a front view showing a structural model of a conventionally used ceramic filter, FIG. 2 is a cross-sectional view of the same, and FIG. 3 is a structural model diagram of a dust collection and incineration device showing an embodiment of the present invention. FIG. 4 is an explanatory diagram showing the symbols t, p, and h in the structural characteristics of Table 1, and FIG. 5 is a structural model diagram of a dust collection and incineration apparatus showing another embodiment of the present invention. 11... Insulating porous filter, 12, 13...
Electrode, 14... Porous thin wall, 15 1 , 15 2 ... Gas flow path, 16, 17... Ceramic sealing material.
Claims (1)
孔質フイルタを挾んでガス流入側のガス流路に金
属細線からなる電極を配置し、ガス流出側のガス
流路に電極を配置し、集塵時に上記電極間に直流
又は交流電圧を印加してダストを捕集するととも
に、ダスト焼却時に上記電極間に交流又は交流パ
ルス電圧を印加して、捕集されたダストを焼却す
ることを特徴とするダスト集塵焼却方法。1. Place an electrode made of thin metal wire in the gas flow path on the gas inflow side between the insulated porous filters that collect dust by passing the dust-containing gas, and place an electrode in the gas flow path on the gas outflow side to collect the dust. At times, a DC or AC voltage is applied between the electrodes to collect the dust, and at the time of dust incineration, an AC or AC pulse voltage is applied between the electrodes to incinerate the collected dust. Dust collection and incineration method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58000828A JPS59127621A (en) | 1983-01-07 | 1983-01-07 | Dust collecting and burning method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58000828A JPS59127621A (en) | 1983-01-07 | 1983-01-07 | Dust collecting and burning method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59127621A JPS59127621A (en) | 1984-07-23 |
| JPH0153084B2 true JPH0153084B2 (en) | 1989-11-13 |
Family
ID=11484494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58000828A Granted JPS59127621A (en) | 1983-01-07 | 1983-01-07 | Dust collecting and burning method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59127621A (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63123460A (en) * | 1986-11-10 | 1988-05-27 | Honda Motor Co Ltd | Method for washing painting apparatus |
| JPH0653240B2 (en) * | 1986-11-10 | 1994-07-20 | 本田技研工業株式会社 | Paint gun cleaning equipment |
| JPH0644969B2 (en) * | 1988-01-27 | 1994-06-15 | 工業技術院長 | Combustible particle removal device |
| FR2812685B1 (en) * | 2000-08-03 | 2003-04-04 | Ecia Equip Composants Ind Auto | CLEANING DEVICE FOR A HEAT ENGINE AND PROPULSION UNIT COMPRISING SAME |
| FR2864141B1 (en) * | 2003-12-19 | 2007-08-24 | Renault Sas | ELECTROSTATIC FILTRATION SYSTEM FOR EXHAUST GASES OF AN INTERNAL COMBUSTION ENGINE |
| FR2864143B1 (en) * | 2003-12-19 | 2006-04-07 | Renault Sas | ELECTROSTATIC FILTRATION SYSTEM FOR EXHAUST GASES OF AN INTERNAL COMBUSTION ENGINE |
| GB2429417B (en) | 2005-08-25 | 2010-08-11 | Perkins Engines Co Ltd | Autoselective regenerating particulate filter |
| US8679209B2 (en) | 2011-12-20 | 2014-03-25 | Caterpillar Inc. | Pulsed plasma regeneration of a particulate filter |
| WO2014174609A1 (en) * | 2013-04-24 | 2014-10-30 | 三井造船株式会社 | Exhaust gas treatment device and method for controlling same |
| JP6341043B2 (en) * | 2014-10-02 | 2018-06-13 | トヨタ自動車株式会社 | Oil removal equipment |
| JP6094555B2 (en) * | 2014-10-02 | 2017-03-15 | トヨタ自動車株式会社 | Oil removal equipment |
| CN105240090B (en) * | 2015-10-28 | 2018-04-24 | 重庆工商大学 | A kind of technical method for being used to remove Vehicle Exhaust Particulate |
-
1983
- 1983-01-07 JP JP58000828A patent/JPS59127621A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59127621A (en) | 1984-07-23 |
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