JP3408223B2 - Exhaust gas detoxification equipment - Google Patents
Exhaust gas detoxification equipmentInfo
- Publication number
- JP3408223B2 JP3408223B2 JP2000051343A JP2000051343A JP3408223B2 JP 3408223 B2 JP3408223 B2 JP 3408223B2 JP 2000051343 A JP2000051343 A JP 2000051343A JP 2000051343 A JP2000051343 A JP 2000051343A JP 3408223 B2 JP3408223 B2 JP 3408223B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- slit
- molten glass
- shaped
- air supply
- 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 - Fee Related
Links
- 238000001784 detoxification Methods 0.000 title description 4
- 239000006060 molten glass Substances 0.000 claims description 35
- 238000002844 melting Methods 0.000 claims description 16
- 230000008018 melting Effects 0.000 claims description 16
- 239000011521 glass Substances 0.000 claims description 13
- 239000000919 ceramic Substances 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 description 45
- 239000000126 substance Substances 0.000 description 16
- 102100027340 Slit homolog 2 protein Human genes 0.000 description 9
- 101710133576 Slit homolog 2 protein Proteins 0.000 description 9
- 239000010881 fly ash Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 150000002013 dioxins Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 229910003439 heavy metal oxide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
Landscapes
- Chimneys And Flues (AREA)
- Treating Waste Gases (AREA)
Description
【0001】[0001]
【発明の属する技術分野】この発明は、排ガス中の有害
物質を溶融ガラスで除去する排ガスの無害化処理装置に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas detoxifying apparatus for removing harmful substances in exhaust gas with molten glass.
【0002】[0002]
【従来の技術および発明が解決しようとする課題】焼却
炉等から排出される排ガス中には、ダイオキシンや重金
属等の有毒物質や、炭酸ガス等の地球環境を破壊する物
質が含まれており、これらの有害物質を排ガスから除去
して無害化する技術の開発が望まれている。このうち、
溶融ガラスを用いて有害物質を除去する技術は、有毒な
ダイオキシンやポリ塩化ビフェニールの分解除去のみな
らず、炭酸ガスや窒素酸化物、硫黄酸化物、鉛や砒素等
の重金属酸化物、ハロゲン系物質等のガスもガラスに溶
け込ませて除去することができ、注目されている。2. Description of the Related Art Exhaust gas discharged from incinerators, etc. contains toxic substances such as dioxins and heavy metals, and substances that destroy the global environment such as carbon dioxide gas. It is desired to develop a technology for removing these harmful substances from exhaust gas to render them harmless. this house,
The technology for removing harmful substances using molten glass is not limited to the decomposition and removal of toxic dioxins and polychlorinated biphenyls, but also carbon dioxide, nitrogen oxides, sulfur oxides, heavy metal oxides such as lead and arsenic, and halogen-based substances. Such gases can be dissolved in the glass and removed, and are attracting attention.
【0003】この溶融ガラスで排ガス中の有害物質を除
去する技術では、排ガスを溶融ガラスに接触させる方法
を工夫して有害物質の除去効率を高めることが課題であ
り、例えば、本出願人による特開2000−2407号
公報に開示されたものでは、焼却炉から排出される排ガ
スをガラス溶融炉に導いて、排ガスを溶融ガラス中にバ
ブリングさせ、ガラス溶融炉の中に多孔板やメッシュ板
を配置することにより、バブリングされる排ガスの気泡
を細かく分断し、排ガスと溶融ガラスとの接触面積を大
きくして、有害物質の除去効率を高める装置を採用して
いる。In the technique of removing harmful substances in exhaust gas with this molten glass, it is a problem to improve the removal efficiency of harmful substances by devising a method of contacting the exhaust gas with the molten glass. In the one disclosed in Kai 2000-2407, the exhaust gas discharged from the incinerator is guided to a glass melting furnace, the exhaust gas is bubbled into the molten glass, and a porous plate or a mesh plate is arranged in the glass melting furnace. By so doing, the bubble of the exhaust gas to be bubbled is finely divided, the contact area between the exhaust gas and the molten glass is increased, and a device for increasing the efficiency of removing harmful substances is adopted.
【0004】そこで、この発明の課題は、排ガス中の有
害物質を溶融ガラスで効率よく除去して無害化する排ガ
スの無害化処理装置を提供することである。SUMMARY OF THE INVENTION An object of the present invention is to provide an exhaust gas detoxification treatment apparatus which efficiently removes harmful substances in exhaust gas with molten glass to render them harmless.
【0005】[0005]
【課題を解決するための手段】上記の課題を解決するた
めに、この発明の排ガスの無害化処理装置は、横長形状
のガラスの溶融槽の底に、長手方向に連なるスリットを
設け、このスリットを形成する一方のスリット壁また
は、このスリット壁の下方に延長した垂れ壁に、排ガス
が供給される給気室と連通する多数の微小孔を設け、前
記スリットの下方に、スリットから落下する溶融ガラス
を受ける溜まり槽を設け、前記微小孔を設けたスリット
壁または垂れ壁に沿ってカーテン状に落下する溶融ガラ
スの中に、前記給気室に供給される排ガスを前記微小孔
から混入させる構成を採用した。In order to solve the above-mentioned problems, the exhaust gas detoxifying apparatus of the present invention is provided with a slit continuous in the longitudinal direction at the bottom of a horizontally elongated glass melting tank, One of the slit walls forming the, or the hanging wall extending below this slit wall, provided with a large number of micropores communicating with the air supply chamber to which the exhaust gas is supplied, below the slit, the melt falling from the slit A configuration is provided in which a reservoir for receiving glass is provided, and the exhaust gas supplied to the air supply chamber is mixed into the molten glass that falls in a curtain shape along the slit wall or the hanging wall provided with the minute holes, from the minute holes. It was adopted.
【0006】すなわち、横長形状のガラスの溶融槽の底
に、長手方向に連なるスリットを設け、このスリットか
らカーテン状に落下する溶融ガラスの中に、排ガスを微
小孔から満遍なく混入させて、多数の細かい排ガスの気
泡を溶融ガラスと接触させながら溜まり槽に落下させ、
さらに、これらの気泡を落下の勢いで溜まり槽に沈み込
ませて浮上させることにより、排ガスを広い接触面積
で、かつ長時間均一に溶融ガラスと接触させて、排ガス
中の有害物質を効率よく除去できるようにした。That is, a slit extending in the longitudinal direction is provided at the bottom of a horizontally long glass melting tank, and exhaust gas is evenly mixed through fine holes into the molten glass that drops like a curtain from the slits, and a large number of slits are formed. While letting fine exhaust gas bubbles contact molten glass, drop them into a collecting tank,
Furthermore, by letting these bubbles sink into the reservoir with the force of falling and floating, the exhaust gas is contacted uniformly with the molten glass over a wide contact area for a long time, and the harmful substances in the exhaust gas are efficiently removed. I made it possible.
【0007】前記空気室の入側に、セラミックまたは耐
熱金属から成る多孔状、メッシュ状、ハニカム状、ファ
イバ状もしくはウィスカ状のフィルタを設けることによ
り、排ガスの顕熱や未燃焼成分の燃焼熱によりこれらの
フィルタを赤熱させて、排ガス中の飛灰等に含まれる未
燃焼成分を燃焼させ、固形の有害物質をガス化して溶融
ガラス中にバブリングさせることができる。また、飛灰
等による微小孔の目詰まりも防止することができる。By providing a porous, mesh, honeycomb, fiber or whisker filter made of ceramic or heat-resistant metal on the inlet side of the air chamber, sensible heat of exhaust gas and combustion heat of unburned components are generated. These filters can be red-heated to burn unburned components contained in the fly ash and the like in the exhaust gas to gasify solid harmful substances and bubble them in the molten glass. Further, it is possible to prevent the clogging of the micropores due to fly ash or the like.
【0008】[0008]
【発明の実施の形態】以下、図面に基づき、この発明の
実施形態を説明する。この排ガスの無害化処理装置は、
図1および図2に示すように、ガラス原料が溶解される
横長形状の溶融槽1の底に、長手方向に連なるスリット
2が設けられ、スリット2を形成するスリット壁3の一
方の下方に垂れ壁4が延長され、この垂れ壁4の裏側
に、フィルタ室5を介して排ガス6が供給される給気室
7が並設され、スリット2の下方にスリット2から落下
する溶融ガラス8を受ける溜まり槽9が設けられ、垂れ
壁4に設けられた多数の微小孔10から、給気室7に供
給された排ガス6が、垂れ壁4に沿ってカーテン状に落
下する溶融ガラス8の中に満遍なく混入されるようにな
っている。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. This exhaust gas detoxification treatment device is
As shown in FIGS. 1 and 2, a slit 2 continuous in the longitudinal direction is provided at the bottom of a horizontally long melting tank 1 in which a glass raw material is melted, and the slit 2 hangs down one of the slit walls 3 forming the slit 2. The wall 4 is extended, and on the back side of the hanging wall 4, an air supply chamber 7 to which the exhaust gas 6 is supplied via a filter chamber 5 is arranged in parallel, and receives a molten glass 8 falling from the slit 2 below the slit 2. An exhaust gas 6 supplied to an air supply chamber 7 from a large number of minute holes 10 provided in a drooping wall 4 is provided with a reservoir tank 9 into a molten glass 8 that drops in a curtain shape along the drooping wall 4. It is mixed evenly.
【0009】前記溶融槽1の一方の長手方向側壁11は
垂直に、他方の長手方向側壁12は傾斜して形成され、
スリット2は垂直な側壁11に沿って設けられている。
各側壁11、12の外側には、ガラス原料を溶解するヒ
ータ13が配置され、各スリット壁3の外側には、スリ
ット2内を落下する溶融ガラス8を加熱するヒータ14
が配置され、各側壁11、12と各スリット壁3の外側
は、それぞれキャスタブル耐火物15で覆われている。One longitudinal side wall 11 of the melting tank 1 is formed vertically and the other longitudinal side wall 12 is inclined.
The slit 2 is provided along the vertical side wall 11.
A heater 13 for melting the glass raw material is arranged outside each of the side walls 11 and 12, and a heater 14 for heating the molten glass 8 falling inside the slit 2 is arranged outside each slit wall 3.
The side walls 11 and 12 and the outside of each slit wall 3 are covered with castable refractory material 15.
【0010】前記スリット2は、図2に示すように、長
手方向で下方に幅狭まりに形成され、スリット2から落
下する溶融ガラス8を安定してカーテン状とするように
している。このカーテン状の溶融ガラス8は、その落下
速度により負圧となるので、給気室7内の排ガス6は特
別な加圧手段を設けなくても微小孔10から溶融ガラス
8の中に混入され、細かい気泡16となって溶融ガラス
8とともに、溜まり槽9に落下する。As shown in FIG. 2, the slit 2 is formed so as to be narrowed downward in the longitudinal direction so that the molten glass 8 falling from the slit 2 can be stably shaped like a curtain. Since the curtain-shaped molten glass 8 has a negative pressure due to its falling speed, the exhaust gas 6 in the air supply chamber 7 is mixed into the molten glass 8 through the fine holes 10 without providing a special pressurizing means. Then, the fine bubbles 16 are dropped into the pool tank 9 together with the molten glass 8.
【0011】前記溶融ガラス8とともに落下する細かい
気泡16は、落下の勢いで溜まり槽9内の溶融ガラス8
に沈み込んだのち、浮力で溶融ガラス8の液面に浮上
し、広い接触面積で、かつ長時間均一に高温の溶融ガラ
ス8と接触する。したがって、排ガス6中の有害物質は
熱で分解されたり、溶融ガラス8中に溶け込んだりして
除去され、無害化されたクリーンな排ガス6が、溜まり
槽9の上部に形成された排気室17に回収される。The fine bubbles 16 falling together with the molten glass 8 are accumulated in the pool 9 by the force of the falling.
Then, it floats on the liquid surface of the molten glass 8 due to buoyancy, and comes into contact with the high temperature molten glass 8 uniformly over a wide contact area for a long time. Therefore, the harmful substances in the exhaust gas 6 are decomposed by heat or melted in the molten glass 8 to be removed, and the clean exhaust gas 6 detoxified into the exhaust chamber 17 formed in the upper part of the collecting tank 9. Be recovered.
【0012】前記排気室17に回収されたクリーンな排
ガス6は、溶融ガラス8のオーバフロー口18に連通す
る排気口19から外部に放出される。この排ガス6の放
出とともに、排気室17にはオーバフロー口18から大
気が流れ込み、前記垂れ壁4に沿ってカーテン状に落下
する溶融ガラス8の排気口19側の表面には、大気中の
酸素と溶融ガラス8の反応により、二酸化珪素の皮膜が
形成される。この皮膜は、カーテン状の溶融ガラス8の
中から排ガス6の気泡16が排気室17側に抜け出るの
を防止する役目をする。したがって、有害物質を含む排
ガス6が排気室17側に漏れることはない。The clean exhaust gas 6 collected in the exhaust chamber 17 is discharged to the outside from an exhaust port 19 communicating with an overflow port 18 of the molten glass 8. At the same time as the discharge of the exhaust gas 6, the atmosphere flows into the exhaust chamber 17 through the overflow port 18, and the surface of the molten glass 8 on the exhaust port 19 side, which drops along the hanging wall 4 in a curtain shape, is exposed to oxygen in the atmosphere. The reaction of the molten glass 8 forms a film of silicon dioxide. This film functions to prevent the bubbles 16 of the exhaust gas 6 from coming out of the curtain-shaped molten glass 8 toward the exhaust chamber 17 side. Therefore, the exhaust gas 6 containing harmful substances does not leak to the exhaust chamber 17 side.
【0013】前記フィルタ室5には、アルミナの焼結板
で形成された多孔状のフィルタ20が取り付けられてい
る。このフィルタ20は、フィルタ室5の入口21から
供給される排ガス6中の飛灰等に含まれる未燃焼成分を
燃焼させ、固形の有害物質をガス化して、排ガス6を給
気室7に供給する。なお、フィルタ20は排ガス6の顕
熱や未燃焼成分の燃焼熱により赤熱し、未燃焼成分を燃
焼させ、飛灰等による微小孔7の目詰まりも防止する。A porous filter 20 made of a sintered plate of alumina is mounted in the filter chamber 5. The filter 20 burns unburned components contained in fly ash and the like in the exhaust gas 6 supplied from the inlet 21 of the filter chamber 5, gasifies solid harmful substances, and supplies the exhaust gas 6 to the air supply chamber 7. To do. The filter 20 is red-heated by the sensible heat of the exhaust gas 6 and the combustion heat of the unburned component, burns the unburned component, and prevents the fine holes 7 from being clogged by fly ash or the like.
【0014】上述した実施形態では、給気室7と連通す
る微小孔10を垂れ壁4に設けたが、スリット壁3に設
けることもできる。また、ガラス原料の溶解を直接溶融
槽1の中で行うようにしたが、ガラス原料を溶解する溶
融槽または溶解窯を別に設け、これらで溶解した溶融ガ
ラスを溶融槽1に投入するようにしてもよい。In the above-described embodiment, the minute holes 10 communicating with the air supply chamber 7 are provided in the hanging wall 4, but they may be provided in the slit wall 3. Further, the glass raw material is melted directly in the melting tank 1, but a melting tank or a melting kiln for melting the glass raw material is separately provided, and the molten glass melted by these is put into the melting tank 1. Good.
【0015】[0015]
【発明の効果】以上のように、この発明の排ガスの無害
化処理装置は、横長形状のガラスの溶融槽の底に、長手
方向に連なるスリットを設け、このスリットからカーテ
ン状に落下する溶融ガラスの中に、排ガスを微小孔から
満遍なく混入させて、多数の細かい排ガスの気泡を溶融
ガラスと接触させながら溜まり槽に落下させ、さらに、
これらの気泡を落下の勢いで溜まり槽に沈み込ませて浮
上させるようにしたので、排ガスを広い接触面積で、か
つ長時間均一に溶融ガラスと接触させて、排ガス中の有
害物質を確実に効率よく除去することができる。As described above, according to the apparatus for detoxifying exhaust gas of the present invention, a slit extending in the longitudinal direction is provided at the bottom of a horizontally long glass melting tank, and a molten glass dropping from this slit in a curtain shape. Inside, the exhaust gas was evenly mixed through the micropores, and a large number of fine exhaust gas bubbles were dropped into the reservoir while contacting with the molten glass.
Since these bubbles are made to sink by the force of falling and float in the collecting tank, the exhaust gas is contacted with the molten glass uniformly over a wide contact area for a long time, and the harmful substances in the exhaust gas are reliably and efficiently discharged. Can be removed well.
【0016】前記空気室の入側に、セラミックまたは耐
熱金属から成る多孔状、メッシュ状、ハニカム状、ファ
イバ状もしくはウィスカ状のフィルタを設けることによ
り、排ガスの顕熱や未燃焼成分の燃焼熱によりこれらの
フィルタを赤熱させて、排ガス中の飛灰等に含まれる未
燃焼成分を燃焼させ、全ての有害物質をガス化して溶融
ガラス中にバブリングさせることができる。A porous, mesh-shaped, honeycomb-shaped, fiber-shaped or whisker-shaped filter made of ceramic or heat-resistant metal is provided on the inlet side of the air chamber so that sensible heat of exhaust gas and combustion heat of unburned components are generated. These filters can be red-heated to burn unburned components contained in fly ash and the like in the exhaust gas, gasify all harmful substances, and bubble in the molten glass.
【図1】排ガスの無害化処理装置の実施形態を示す縦断
面図FIG. 1 is a vertical cross-sectional view showing an embodiment of an exhaust gas detoxification treatment apparatus.
【図2】図1のII−II線に沿った断面図FIG. 2 is a sectional view taken along line II-II in FIG.
1 溶融槽 2 スリット 3 スリット壁 4 垂れ壁 5 フィルタ室 6 排ガス 7 給気室 8 溶融ガラス 9 溜まり槽 10 微小孔 11、12 側壁 13、14 ヒータ 15 キャスタブル耐火物 16 気泡 17 排気室 18 オーバフロー口 19 排気口 20 フィルタ 21 入口 1 melting tank 2 slits 3 slit walls 4 hanging wall 5 filter room 6 exhaust gas 7 air supply room 8 molten glass 9 reservoir 10 micropores 11, 12 Side wall 13, 14 heater 15 Castable refractories 16 bubbles 17 Exhaust chamber 18 Overflow port 19 exhaust port 20 filters 21 entrance
Claims (2)
方向に連なるスリットを設け、このスリットを形成する
一方のスリット壁または、このスリット壁の下方に延長
した垂れ壁に、排ガスが供給される給気室と連通する多
数の微小孔を設け、前記スリットの下方に、スリットか
ら落下する溶融ガラスを受ける溜まり槽を設け、前記微
小孔を設けたスリット壁または垂れ壁に沿ってカーテン
状に落下する溶融ガラスの中に、前記給気室に供給され
る排ガスを前記微小孔から混入させるようにした排ガス
の無害化処理装置。1. Exhaust gas is supplied to a slit wall extending in the longitudinal direction at the bottom of a horizontally long glass melting tank, and one slit wall forming this slit or a hanging wall extending below the slit wall. A large number of minute holes communicating with the air supply chamber are provided, a reservoir for receiving molten glass falling from the slits is provided below the slit, and a curtain shape is provided along the slit wall or the hanging wall provided with the minute holes. An apparatus for detoxifying an exhaust gas, wherein the exhaust gas supplied to the air supply chamber is mixed into the molten glass that falls through the fine holes.
耐熱金属から成る多孔状、メッシュ状、ハニカム状、フ
ァイバ状もしくはウィスカ状のフィルタを設けた請求項
1に記載のガラス溶融炉。2. The glass melting furnace according to claim 1, wherein a porous, mesh-shaped, honeycomb-shaped, fiber-shaped or whisker-shaped filter made of ceramic or heat-resistant metal is provided on the inlet side of the air supply chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000051343A JP3408223B2 (en) | 2000-02-28 | 2000-02-28 | Exhaust gas detoxification equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000051343A JP3408223B2 (en) | 2000-02-28 | 2000-02-28 | Exhaust gas detoxification equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2001232141A JP2001232141A (en) | 2001-08-28 |
| JP3408223B2 true JP3408223B2 (en) | 2003-05-19 |
Family
ID=18573005
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000051343A Expired - Fee Related JP3408223B2 (en) | 2000-02-28 | 2000-02-28 | Exhaust gas detoxification equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3408223B2 (en) |
-
2000
- 2000-02-28 JP JP2000051343A patent/JP3408223B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP2001232141A (en) | 2001-08-28 |
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