JPS6113845B2 - - Google Patents
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- Publication number
- JPS6113845B2 JPS6113845B2 JP4486579A JP4486579A JPS6113845B2 JP S6113845 B2 JPS6113845 B2 JP S6113845B2 JP 4486579 A JP4486579 A JP 4486579A JP 4486579 A JP4486579 A JP 4486579A JP S6113845 B2 JPS6113845 B2 JP S6113845B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- cylindrical body
- dust
- combustion
- bottomed cylindrical
- 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
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- Filtering Materials (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Description
【発明の詳細な説明】
本発明は、高温燃焼排ガス中の煤塵を除去し
て、排ガスを浄化する高温排ガス浄化用のセラミ
ツクフイルターに関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a ceramic filter for purifying high-temperature exhaust gas that removes soot and dust from high-temperature combustion exhaust gas and purifies the exhaust gas.
火力発電所や各種工場等のボイラー、燃焼炉あ
るいは焼却炉等から排出される燃焼排ガス中に
は、可燃性物質としての未燃カーボンやタールあ
るいは熱分解生成ガス、不燃性物質としてのフラ
イアツシユ等の塵埃が多量に含まれている。これ
らの物質はいずれも大気汚染防止上除去する必要
があり、この排ガス浄化処理としては、可燃性物
質の再燃焼処理とその後工程における除塵処理が
一般的である。 Combustion exhaust gas discharged from boilers, combustion furnaces, incinerators, etc. of thermal power plants and various factories contains combustible substances such as unburned carbon and tar, gases produced by thermal decomposition, and non-flammable substances such as fly ash. Contains a large amount of dust. All of these substances need to be removed to prevent air pollution, and the exhaust gas purification process generally includes a re-burning process for combustible substances and a dust removal process in the subsequent process.
すなわち、従来これら燃焼排ガスの浄化処理と
しては、燃焼排ガスを一旦燃焼炉内に設置した2
次燃焼室か、あるいは燃焼炉とは別に設けた再燃
焼炉に導き、燃焼排ガス中に含まれる未燃の可燃
性物質を再燃焼させ、その後その燃焼排ガスを除
塵装置に導いて除塵するものである。そして、こ
の排ガスの除塵法としては、湿式法と乾式法とが
知られているが、乾式法は、乾式集塵機のほかに
水処理装置やミスト分離器を附設しなければなら
ない等、除塵設備が大型かつ複雑化し、さらに運
転保守が面倒である等の欠点があるものであり、
また乾式法は、サイクロン集塵機を除き、一般的
な電気集塵機やバツグフイルター等を使用する装
置においては、500℃〜900℃程度の高温の燃焼排
ガスをそのまま使用することは勿論できないもの
であるので、大量に排出される高温燃焼排ガス
を、例えば電気集塵機使用の場合は300℃〜350℃
程度まで、またバツグフイルター使用の場合は
100℃程度までに冷却することが必要であり、そ
のために大型の冷却装置を必要とするため、除塵
設備が複雑かつ大型となり高価となる等の欠点が
あつた。 In other words, in the past, the purification treatment of these combustion exhaust gases was carried out once the combustion exhaust gases were placed in a combustion furnace.
The combustion exhaust gas is guided to the next combustion chamber or to a re-combustion furnace installed separately from the combustion furnace, where unburned combustible substances contained in the combustion exhaust gas are re-burned, and then the combustion exhaust gas is guided to a dust removal device to remove dust. be. There are two known methods for removing dust from exhaust gas: a wet method and a dry method. However, the dry method requires a water treatment device and a mist separator in addition to a dry dust collector. They have drawbacks such as being large and complex, and also requiring troublesome operation and maintenance.
In addition, with the dry method, except for cyclone dust collectors, it is of course impossible to use combustion exhaust gas at a high temperature of about 500°C to 900°C with equipment that uses general electrostatic precipitators or bag filters. For example, when using an electrostatic precipitator, the temperature of high-temperature combustion exhaust gas that is emitted in large quantities is 300℃ to 350℃.
degree, and when using a negative filter
It is necessary to cool down to about 100°C, which requires a large cooling device, which has disadvantages such as making the dust removal equipment complex, large and expensive.
本発明の高温用セラミツクフイルターは、従来
のこれらの欠点を解決するためになされたもので
あり、高温燃焼排ガスを冷却することなく直接使
用して、燃焼排ガス中に含まれる煤塵類を効率的
に捕集除去するとともに、排ガス中に含まれる可
燃性物質の燃焼を促進するものであり、耐火性粒
子の集合体よりなる通気性を有する多孔質の有底
筒状体であつて、その有底筒状体の開口端近傍の
隔壁が他の部分の隔壁より厚い環状肉厚部を有す
る形状であり、その有底筒状体を形成する耐火性
粒子が平均粒子径60〜250μの粒子よりなるもの
であるとともに有底筒状体の気孔率が25%〜45%
である燃焼排ガス中の煤塵を除去する高温用セラ
ミツクフイルターである。 The high-temperature ceramic filter of the present invention has been developed to solve these conventional drawbacks, and can efficiently remove soot and dust contained in the combustion exhaust gas by directly using the high-temperature combustion exhaust gas without cooling it. It collects and removes combustible substances contained in exhaust gas and promotes the combustion of combustible substances contained in exhaust gas. The partition wall near the open end of the cylindrical body has an annular thick part that is thicker than the partition walls in other parts, and the refractory particles forming the bottomed cylindrical body are composed of particles with an average particle size of 60 to 250μ. The porosity of the bottomed cylindrical body is 25% to 45%.
This is a high-temperature ceramic filter that removes soot and dust from combustion exhaust gas.
本発明のさらに詳しい構成を一具体例を示す第
1図に基づいて説明すれば、珪砂、陶磁器紛砕
物、Al2O3、TiO2、ZrO2等の金属酸化物、炭化珪
素、窒化物、硼化物あるいはその他の耐火性材料
等によりなる所定粒度に整粒された耐火性粒子2
が、水ガラス、フリツト、釉薬等の耐火性結合材
で通気性を有する多孔質の有底筒状体1に形成さ
れ、内外面に連通した多数の細孔を有するもので
あつて、その有底筒状体1の開口端3近傍の隔壁
4aが他の部分の隔壁4bよりも肉厚の厚い環状
肉厚部5を形成する形状であつて、その有底筒状
体を形成する前記耐火性粒子2か、平均粒子径60
μ〜250μ、より好ましくは120μ〜160μに整粒
されたものよりなるとともに、有底筒状体1の気
孔率が25%〜45%より好ましくは30%〜40%の範
囲内であるセラミツクフイルターである。 A more detailed configuration of the present invention will be described based on FIG. 1 showing a specific example. Silica sand, crushed ceramics, metal oxides such as Al 2 O 3 , TiO 2 , ZrO 2 , silicon carbide, nitride, Refractory particles 2 made of boride or other refractory materials and sized to a predetermined particle size
is made of a fire-resistant binder such as water glass, frit, glaze, etc., into a porous bottomed cylindrical body 1 having air permeability, and has a large number of pores communicating with the inner and outer surfaces. The partition wall 4a near the open end 3 of the bottom cylindrical body 1 has a shape that forms an annular thick portion 5 that is thicker than the partition wall 4b in other parts, and the refractory forming the bottomed cylindrical body particle size 2 or average particle size 60
Ceramic filter made of sized particles of μ to 250 μ, more preferably 120 μ to 160 μ, and the porosity of the bottomed cylindrical body 1 is within the range of 25% to 45%, more preferably 30% to 40%. It is.
すなわち本発明は、フイルターが特定の形状を
有するとともに、そのフイルターを形成する粒子
およびフイルターの気孔率が所定の範囲内にある
ことにより、排ガス中の煤塵類の捕集除去に極め
て優れた形状および細孔構造を有する高温用フイ
ルターを究明したものである。 That is, in the present invention, the filter has a specific shape, and the particles forming the filter and the porosity of the filter are within a predetermined range. This study revealed a high-temperature filter with a pore structure.
すなわち、有底筒状体の気孔率が25%〜45%の
範囲内であることが最も大切であり25%未満で
は、機械的強度は増すが通気抵抗が著しく増大
し、排ガスフイルターとしては、実用上使用困難
となりまた45%を越えると捕集効率が低下すると
ともに、機械的強度の減少から、安定した長期間
の連続使用が困難となる。 In other words, it is most important that the porosity of the bottomed cylindrical body be within the range of 25% to 45%; if it is less than 25%, the mechanical strength will increase, but the ventilation resistance will increase significantly, making it difficult to use as an exhaust gas filter. It becomes difficult to use it in practice, and if it exceeds 45%, the collection efficiency decreases and mechanical strength decreases, making it difficult to use stably and continuously for a long period of time.
また、耐火性粒子の平均粒子径を60μ〜250μ
としたのは、セラミツクフイルターにおいては上
記の気孔率とともに気孔径が非常に重要な要因と
なるものであり、耐火性粒子の平均粒子径が極め
て小さくなるとたとえ気孔率が大きくても目詰ま
り現象を起こしやすいものであり、また反対に粒
子径が大き過ぎるとたとえ気孔率が小さくても吹
抜け現象が生じやすい。 In addition, the average particle size of the refractory particles is 60μ to 250μ.
This is because, in addition to the above-mentioned porosity, pore size is a very important factor in ceramic filters, and if the average particle size of the refractory particles is extremely small, clogging will occur even if the porosity is large. On the other hand, if the particle size is too large, the blow-through phenomenon is likely to occur even if the porosity is small.
したがつて、煤塵類の捕集に最適な気孔径を得
るためには、耐火性粒子の平均粒子径を60μ〜
250μに整粒することが大切であつて、平均粒子
径60μ未満では、短期的に捕集効率は高くなるも
のの、通気抵抗が増大し、短時間の使用で目詰ま
りを生ずるものであり、また250μを越えると排
ガスの吹抜けに伴う補集効率の低下が著しく、い
ずれも実用的なフイルターが得られないため好ま
しくない。なお、耐火性粒子の粒子径は均一なも
のほどよいが、好ましは所定の平均粒子径の粒度
±50μの範囲内に80%以上の耐火性粒子が含まれ
るものがよい。 Therefore, in order to obtain the optimum pore size for collecting soot and dust, the average particle size of the refractory particles should be set to 60 μm or more.
It is important to size the particles to 250μ; if the average particle size is less than 60μ, the collection efficiency will be high in the short term, but ventilation resistance will increase and clogging will occur after short time use. If it exceeds 250μ, the collection efficiency decreases significantly due to exhaust gas blow-through, and in either case, a practical filter cannot be obtained, which is not preferable. Incidentally, the more uniform the particle diameter of the refractory particles is, the better; however, it is preferable that 80% or more of the refractory particles be contained within a particle size range of ±50 μ of a predetermined average particle diameter.
さらに、セラミツクフイルターの筒状部の隔壁
の肉厚は5mm以上であればよいが、好ましくは10
mm〜20mm程度がよい。 Further, the wall thickness of the partition wall of the cylindrical part of the ceramic filter may be 5 mm or more, but preferably 10 mm or more.
Approximately 20 mm to 20 mm is best.
さらに、耐火性粒子としては、前述のような耐
火性材料よりなる粒子であれば十分であるが、排
ガス温度が高くなるほど、あるいは排ガス中の有
害ガス成分が多くなるほど熱的、化学的に安定し
たものを使用する必要があり、そのような場合に
は、アルミナ、炭化珪素、窒化物、硼化物等の粒
子が特によいものであり、また当然のことながら
結合材も熱的、化学的により安定したものを使用
した方がよいものである。 Furthermore, as refractory particles, particles made of the above-mentioned refractory material are sufficient, but the higher the exhaust gas temperature or the more harmful gas components in the exhaust gas, the more thermally and chemically stable the particles become. In such cases, particles of alumina, silicon carbide, nitrides, borides, etc. are particularly good, and of course the binder is also more thermally and chemically stable. It is better to use the one that has been prepared.
本発明の高温用セラミツクフイルターは、以上
のような構成よりなるものであり、使用に際して
は環状肉厚部5を保持して、排ガス中に懸架し、
各種燃焼装置より排出される高温の燃焼排ガスを
セラミツクフイルターの外部より内筒部方向に、
隔壁4bの細孔中を通過させると、燃焼排ガス中
に含まれる煤塵等はセラミツクフイルターの外表
面上で捕集除去され、微細な紛塵は細孔内を通過
する過程で捕集除去される。そして、未燃炭素や
タール等の可燃性物質が煤塵中に含まれる場合
は、その可燃性物質は、高温状態のセラミツクフ
イルター表面上で燃焼されるものであり、本発明
のセラミツクフイルターは、除塵と燃焼床とを兼
ね備える効果のあるものである。 The high-temperature ceramic filter of the present invention has the above-described structure, and when in use, the thick annular portion 5 is held and suspended in exhaust gas.
Directs high-temperature combustion exhaust gas discharged from various combustion devices from the outside of the ceramic filter toward the inner cylinder.
When the combustion exhaust gas passes through the pores of the partition wall 4b, the soot and dust contained in the combustion exhaust gas are collected and removed on the outer surface of the ceramic filter, and fine dust is collected and removed during the process of passing through the pores. . When combustible substances such as unburned carbon and tar are included in the soot and dust, the combustible substances are burned on the surface of the ceramic filter in a high temperature state. This has the effect of having both a combustion bed and a combustion bed.
以上述べたとおり本発明の高温用セラミツクフ
イルターは、耐火性粒子の集合体よりなる通気性
を有する多孔質の有底筒状体で、その有底筒状体
の開口端近傍の隔壁が他の部分の隔壁より厚い環
状肉厚部を有する燃焼排ガス中の煤塵を除去する
高温用セラミツクフイルターであつて、有底筒状
体を形成する耐火性粒子が平均粒子径が60μ〜
250μでかつ平均粒子径の粒度の±50μの範囲内
に80%以上の耐火性粒子を含む粒子よりなるこ
と、筒状体の気孔率が25%〜45%で筒状部の隔壁
の肉厚が5〜20mmであることにより、燃焼排ガス
中の煤塵の捕集除去効率の向上が顕著に期待でき
るのである。また本発明のセラミツクフイルター
は500℃〜900℃という高温の燃焼排ガスに直接使
用することができるので、未燃分を完全に燃焼さ
せる効果がある。従つて本発明のフイルターを用
いた除塵装置は従来のように冷却装置を全く必要
としないため除塵設備が簡単かつ小型ですむもの
であり、さらに後処理等を必要としない。しかも
所定数値限定範囲内の平均細孔部および細孔容積
を有することにより燃焼排ガス中の煤塵の捕集除
去に最も適した細孔構造を有するものであつて、
捕集効率に極めて優れたフイルターである。ま
た、炭素やタール等の可燃性物質が煤塵中に含ま
れる場合、その可燃性物質は高温状態のセラミツ
クフイルター表面上で燃焼されることによつてそ
の除塵効果の向上が期待されるものであり、本発
明のセラミツクフイルターは除塵と燃焼床とを兼
ね備える効果のある等数多くの利点を有するもの
であるので、大気汚染の防止に役立つものであつ
て公害防止上極めて有用なフイルターである。 As described above, the high-temperature ceramic filter of the present invention is a porous bottomed cylindrical body made of an aggregate of refractory particles and has an air permeability, and the partition wall near the open end of the bottomed cylindrical body is A high-temperature ceramic filter for removing soot and dust from combustion exhaust gas, which has an annular wall thicker than the partition wall of the section, and the refractory particles forming the bottomed cylindrical body have an average particle diameter of 60 μm or more.
The diameter of the cylindrical body must be 250μ and the particles must contain 80% or more of fire-resistant particles within ±50μ of the average particle size, the porosity of the cylindrical body must be between 25% and 45%, and the thickness of the partition wall of the cylindrical part. When the diameter is 5 to 20 mm, it can be expected that the efficiency of collecting and removing soot and dust in the combustion exhaust gas will be significantly improved. Furthermore, since the ceramic filter of the present invention can be used directly for combustion exhaust gas at a high temperature of 500°C to 900°C, it has the effect of completely burning unburned components. Therefore, the dust removal device using the filter of the present invention does not require any cooling device unlike the conventional ones, so the dust removal equipment can be simple and compact, and furthermore, it does not require post-treatment. Moreover, it has a pore structure most suitable for collecting and removing soot and dust in combustion exhaust gas by having an average pore part and pore volume within a predetermined numerically limited range,
This filter has extremely high collection efficiency. In addition, when flammable substances such as carbon and tar are included in the soot and dust, it is expected that the dust removal effect will be improved by burning the flammable substances on the surface of the ceramic filter in a high temperature state. The ceramic filter of the present invention has many advantages such as being effective in both dust removal and a combustion bed, and is therefore an extremely useful filter that is useful for preventing air pollution.
第1図は、本発明の高温用セラミツクフイルタ
ーの一具体例を示す縦断面説明図である。
1……有底筒状体、2……耐火性粒子、3……
開口端、4a……開口端近傍の隔壁、4b……隔
壁、5……環状肉厚部。
FIG. 1 is an explanatory longitudinal cross-sectional view showing a specific example of the high temperature ceramic filter of the present invention. 1... Bottomed cylindrical body, 2... Fire-resistant particles, 3...
Opening end, 4a... partition wall near the opening end, 4b... partition wall, 5... annular thick part.
Claims (1)
多孔質の有底筒状体で、その有底筒状体の開口端
近傍の隔壁が他の部分の隔壁より厚い環状肉厚部
を有する燃焼排ガス中の煤塵を除去する高温用セ
ラミツクフイルターにおいて、その有底筒状体を
形成する耐火性粒子が平均粒子径が60μ〜250μ
で、かつ平均粒子径の粒度の±50μの範囲内に80
%以上の耐火性粒子を含む粒子よりなるものであ
るとともに、筒状体の気孔率が25%〜45%で筒状
部の隔壁の肉厚が5〜20mmであることを特徴とす
る燃焼排ガス中の煤塵を除去する高温用セラミツ
クフイルター。1 Combustion in which a porous bottomed cylindrical body made of an aggregate of refractory particles has an air permeability, and the partition wall near the open end of the bottomed cylindrical body has an annular thick part that is thicker than the partition walls in other parts. In high-temperature ceramic filters that remove soot and dust from exhaust gas, the refractory particles forming the bottomed cylindrical body have an average particle diameter of 60μ to 250μ.
and within the range of ±50 μ of the particle size of the average particle size 80
% or more of refractory particles, the porosity of the cylindrical body is 25% to 45%, and the wall thickness of the partition wall of the cylindrical part is 5 to 20 mm. A high-temperature ceramic filter that removes soot and dust inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4486579A JPS55137021A (en) | 1979-04-14 | 1979-04-14 | High temperature-use ceramic filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4486579A JPS55137021A (en) | 1979-04-14 | 1979-04-14 | High temperature-use ceramic filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55137021A JPS55137021A (en) | 1980-10-25 |
| JPS6113845B2 true JPS6113845B2 (en) | 1986-04-16 |
Family
ID=12703381
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4486579A Granted JPS55137021A (en) | 1979-04-14 | 1979-04-14 | High temperature-use ceramic filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS55137021A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2002062726A1 (en) | 2001-02-02 | 2002-08-15 | Ngk Insulators,Ltd. | Honeycomb structure and method for preparation thereof |
| US7011803B2 (en) | 2000-04-14 | 2006-03-14 | Ngk Insulators, Ltd. | Honeycomb structure and method for its manufacture |
| WO2009069731A1 (en) | 2007-11-30 | 2009-06-04 | Ngk Insulators, Ltd. | Silicon carbide porous body |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6067115U (en) * | 1983-10-17 | 1985-05-13 | 四季ロール株式会社 | filter |
| JPH0655251B2 (en) * | 1985-05-20 | 1994-07-27 | 旭硝子株式会社 | Dust removal purifier |
| US4735635A (en) * | 1986-01-10 | 1988-04-05 | Westinghouse Electric Corp. | Apparatus and process for filtering high temperature gas streams |
| JPH0797158B2 (en) * | 1986-02-27 | 1995-10-18 | 三機工業株式会社 | Radioactive waste transfer device |
| US4735638A (en) * | 1986-11-18 | 1988-04-05 | The United States Of America As Represented By The United States Department Of Energy | Filter unit for use at high temperatures |
-
1979
- 1979-04-14 JP JP4486579A patent/JPS55137021A/en active Granted
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7011803B2 (en) | 2000-04-14 | 2006-03-14 | Ngk Insulators, Ltd. | Honeycomb structure and method for its manufacture |
| WO2002062726A1 (en) | 2001-02-02 | 2002-08-15 | Ngk Insulators,Ltd. | Honeycomb structure and method for preparation thereof |
| US6764742B2 (en) | 2001-02-02 | 2004-07-20 | Ngk Insulators, Ltd. | Honeycomb structure body and production method thereof |
| WO2009069731A1 (en) | 2007-11-30 | 2009-06-04 | Ngk Insulators, Ltd. | Silicon carbide porous body |
| US8449644B2 (en) | 2007-11-30 | 2013-05-28 | Ngk Insulators, Ltd. | Silicon carbide porous body |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55137021A (en) | 1980-10-25 |
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