JP3507157B2 - Incineration ash solidification equipment - Google Patents
Incineration ash solidification equipmentInfo
- Publication number
- JP3507157B2 JP3507157B2 JP30716294A JP30716294A JP3507157B2 JP 3507157 B2 JP3507157 B2 JP 3507157B2 JP 30716294 A JP30716294 A JP 30716294A JP 30716294 A JP30716294 A JP 30716294A JP 3507157 B2 JP3507157 B2 JP 3507157B2
- Authority
- JP
- Japan
- Prior art keywords
- cement
- incinerated ash
- incineration
- stabilizing agent
- sio
- 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
Landscapes
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は、一般ゴミ、下水汚泥、
産業廃棄物等を焼却した後に残る有害な重金属等を含む
焼却灰をセメント化する、焼却灰のセメントによる固化
方法に関する。
【0002】
【従来の技術】従来ゴミ処理工場では、再利用できない
ゴミは焼却によりゴミの体積を減容させ、後に残る焼却
灰をそのまま管理型の処分場に捨てるか、あるいは、セ
メントを混ぜて固化するなどして処理している。焼却灰
をセメントに混ぜて固化させることで環境への有害物質
の溶出を防止する方法は一応の効果はあるが、セメント
に過剰の水分を使用するため、その水分の蒸発によって
固化後に毛細管ができ、固化物に水の浸透性が出て、有
害物が溶出する可能性があり、長い期間にわたっては、
溶出が無視できないほどになる場合がある。
【0003】
【発明が解決しようとする課題】焼却後の灰についての
問題点は、灰の中に有害な成分や重金属類や有機質分が
多く含まれている場合である。これらのものは、焼却に
ともなう高熱で分解されなかったものであり、化学的な
処理が困難なことが多い。脱塩素処理で石灰による強ア
ルカリ性を示すため、酸化物として存在している金属や
重金属は水に溶け出すと水酸化物の不溶性塩となるが、
溶出試験を行うと少量であっても溶出して来るので、微
量でも永続的に重金属類の溶出が続くことになる。この
ような有害成分を含む焼却灰をそのまま埋立てなどに用
いると、有害成分が溶出し、環境に悪影響を与えること
から、有害物の重金属を溶出しないような処理を施した
うえで廃棄しなければならない。
【0004】従って本発明は、焼却灰をポルトランドセ
メントによる固化のみならず、焼却灰をセメントで安定
した状態で固化させ、それによって得られる固化成形物
の多角的利用をはかるためのものである。
【0005】
【課題を解決するための手段】本発明は有害重金属、若
しくは有機塩を含む、焼却灰を無水炭酸ナトリウム等の
ガラス形成成分を主成分とする有機物安定処理剤を加え
て、コンクリート容器中で固化させることにより、環境
への有害物質の溶出を防ぐものである。
【0006】本発明で使用する有害物質安定処理剤は二
酸化炭素とケイ酸ナトリウムの反応を基礎としたもので
あり、これは炭酸ソーダ等から発生する二酸化炭素がケ
イ酸ソーダの分解を助けて系内にコロイド状シリカを生
成させ、このコロイドシリカが炭素−ケイ素結合を形成
するためと考えられる。本発明の安定処理剤はSi
O2、Na2SiO3、NaCO3、CaCO3のよう
なガラスの固化成分の他に炭酸ガス供給成分を含み、炭
酸ガス供給成分としてはポリイソシアネート及びポリオ
ールのようなウレタン生成反応も便利に利用することが
できる。さらに無水ホウ酸H3BO3を加えれば硬質ガ
ラス系のものとなるものであり、またCaCO3、Si
O2、SO2Al2O3、Fe2O3、MgO等セメン
ト成分も混合するものである。このセメントの成分は1
00gに対して20gほど加えることにより一層の造岩
作業の働きを強め、岩石の主成分であるH2SiO3+
SiO2を長い年月をかけてつくりあげるものである。
【0007】焼却灰に含まれている有害物の薬品処理方
法では、どのような処理方法であっても焼却灰と薬品の
混合、攪拌効率が一番の問題となるため、処理対象物に
見合った混合方法、処理時間のテストを繰り返し、その
結果、焼却灰粒子の無機質成分は固化に必要な石灰分
(CaO)、ケイ酸分(SiO2)、アルミナ分(Al
2O3)、鉄分(Fe2O3)、硫酸根(−SO4)等
の化合物を水と反応させて水和物を生成し、液性イオン
濃度の変化に応じてイオン荷電が修正され、沈積が始ま
る。
【0008】焼却灰内の液層、気層、さらに有機質の硬
化に対する最大の阻害要因は、セメントの水硬性鉱物が
加水分解によって生ずるカルシウムイオンといち早く反
応して、不溶性、又は可溶性の化合物を形成する点にあ
る。例えば不溶性塩を形成する場合はその生成分が、セ
メント粒子の表面を被覆して以後の反応を進まなくする
作用、又可溶性塩の場合は次々に反応して溶液として水
和反応の系外に持ち去ってしまう作用である。いずれに
しても、このように水和反応の主体であるべき、カルシ
ウムイオンが他の反応系に持ち去られたのでは水和反応
の化学バランスが崩れる。依って本発明の安定カルシウ
ム処理剤を混合することにより、液相が石灰含有量を増
大し、アルカリ性の組成となることを、さらには急速な
水和反応によって水和阻止効果の及ぶ前に固化を達成す
る組成とすることで、アルミン酸石灰水和物の水和反応
を促進し、エトリンガイト(3CaO・Al2O3・3
CaSO4・32H2O)の生成をより多くするもの
で、これら複塩は重金属を含む、有害物を固定し、溶出
させない状態にするものである。
【0009】
【実施例】以下に本発明の実施例を示すが、これらの実
施例は単に本発明の理解を助けるための手段に過ぎず、
これらの実施例によって本発明が何等限定されるもので
ないことは当然理解されなければならないところであ
る。なお、以下の実施例は大阪市、東京都、字都宮市、
栃木広域行政区、富里町等20ケ町村で実施し、厚生省
認定検査機関での試験データによるものである。なお、
実施例では「東京都のごみ焼却場より出された焼却灰」
などと表現するが、該焼却灰にセメントを添加してロー
タリーキルンで加熱処理した焼却灰を意味する。
【0010】実施例1
安定処理剤の主原料として二酸化ケイ素SiO2 10
g、酸化カルシウムCaO 3g、無水炭酸ナトリウム
Na2CO3 10g、酸化アルミニウムAl2O3
2g、無水ホウ酸B2O3 10g、無水炭酸カリウム
K2CO3 3g、酢酸ナトリウムCH3COONa・
3H2O 5g、ケイ酸カリウムSiO2・K2O 5
g、水H2O 5000ml、副原料として有機アンモ
ニウム塩50ml、食塩NaCl 2g、酸化コバルト
CoO 2g、触媒としてメチルエチルケトンC2H5
COCH3 5g、エチレンジアミンNH2CH2CH
2NH2 5gを使用した。水H2Oの温度を60℃と
し触媒を入れる前に30分薬品の攪拌を行い、さらに触
媒を入れて30分攪拌を続けた。大阪市ゴミ焼却場より
出された焼却灰1000gに、ポルトランドセメント2
00g、本発明の安定処理剤4lを混練し、スランプ8
cmの水分量で固化して、1ケ月間養生期間を置き、溶
出試験を行った。溶出試験は、カドミウム、シアン、有
機リン、鉛、六価クロム、ひ素、アルキル水銀、PCB
について行った。この試験の結果、シアン、有機りん、
六価クロム、アルキル水銀、PCBについては検出され
ず、鉛は0.5mg/l未満、カドミウム及びひ素は
0.05mg/l未満、全水銀は0.0005mg/l
未満といずれも有害物の判定基準に達しない値であっ
た。
【0011】実施例2
東京都のごみ焼却場より出された焼却灰1000gにポ
ルトランドセメント200g、本発明の安定処理剤4l
を混練し、同じく固化後1ケ月して溶出試験を行った。
水銀、カドミウム、鉛、ひ素、シアン、クロムの中、鉛
が0.34mg/l未満、クロムが0.06mg/l未
満で水銀、カドミウム、ひ素、シアンについては不検出
であった。
【0012】実施例3
宇都宮市焼却場の焼却灰1000gに、ポルトランドセ
メント200g、本発明の処理剤4lを混練したものに
ついて同じく固化後1ケ月して溶出試験を行った。溶出
試験は鉛、カドミウム、ひ素、六価クロム、全水銀、有
機リン、全シアンについて行った。この溶出試験の結果
は、鉛0.17mg/l未満、カドミウム0.005m
g/l未満、ひ素0.02mg/l、六価クロム0.1
4mg/l未満、全水銀0.0005mg/l未満、有
機リンと全シアンは不検出といずれも有害物の判定基準
に達しない価であった。
【0013】実施例4
栃木地区広域行政事務組合焼却場の焼却灰1000gに
ポルトランドセメント200g、本発明の処理剤4lを
混練したものを固化し、同じく1ケ月後に溶出試験を行
った。鉛、カドミウム、ひ素、六価クロム、全水銀、有
機リン、全シアンの溶出試験結果は鉛1.00、カドミ
ウム0.0005、ひ素0.02、六価クロム0.0
6、全水銀0.0005、有機リンと全シアンは不検出
で、すべて判定基準に達しない価であった。
【0014】実施例5
焼却灰1000Kgをコンクリート混練機に入れて回転
させながらセメント200Kgを入れて10分間攪拌
し、その後本発明の安定処理剤18lを10倍の水で希
釈して投入、更に5分間混練した後、スランプ15cm
にて圧送ポンプにて内部を中空ブロック状に形成された
コンクリート製廃棄場所に流し込んで密閉した。
【0015】
【発明の効果】本発明の安定処理剤を用いて焼却灰をブ
ロック状に固化成形させることによって、移送が簡便と
なるばかりでなく、これまで困難とされてきた焼却灰に
含まれている有害物質が漏出することのない固化成形物
を得ることができるため、固化成形物はそのままで土
木、建設資材としてコンクリートブロック等に利用する
ことができる。また本発明による生成物のセメント材料
としての圧縮強度はポルトランドセメント及び安定処理
剤の比率を調整することにより任意に変えることもでき
る。これにより焼却灰は廃棄物ではなく、セメント材料
として充分使用できる副産物となる。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to general waste, sewage sludge,
Cementation of incineration ash containing cement, which contains harmful heavy metals etc. remaining after incineration of industrial waste
About the method . 2. Description of the Related Art In a conventional refuse treatment plant, the volume of refuse that cannot be reused is reduced by incineration, and the remaining incinerated ash is discarded as it is in a controlled disposal site or mixed with cement. It is processed by solidification. A method of preventing the release of harmful substances into the environment by mixing incinerated ash with cement and solidifying it has a prima facie effect, but since excess water is used in the cement, a capillary is formed after solidification due to the evaporation of the water. , The solidified material has water permeability, and harmful substances may elute, and over a long period of time,
Elution may not be negligible. The problem with the ash after incineration is that the ash contains a lot of harmful components, heavy metals and organic matter. These substances were not decomposed due to the high heat of incineration, and were often difficult to chemically treat. Dechlorination shows strong alkalinity due to lime, so metals and heavy metals present as oxides become insoluble salts of hydroxides when dissolved in water,
When the dissolution test is carried out, even a small amount of the metal is eluted, so that the elution of heavy metals continues even in a very small amount. If incinerated ash containing such harmful components is used as such in landfills, the harmful components elute and adversely affect the environment. Must. Accordingly, the present invention is intended not only to solidify incinerated ash with Portland cement but also to solidify the incinerated ash in a stable state with cement, and to use the solidified molded product thus obtained in various ways. SUMMARY OF THE INVENTION The present invention relates to a concrete container comprising a hazardous heavy metal or an organic salt, and an incineration ash added with an organic substance stabilizing agent mainly containing a glass-forming component such as anhydrous sodium carbonate. The solidification in the medium prevents harmful substances from being eluted into the environment. The harmful substance stabilizing agent used in the present invention is based on the reaction between carbon dioxide and sodium silicate. Carbon dioxide generated from sodium carbonate or the like assists the decomposition of sodium silicate to reduce the system. It is believed that colloidal silica is formed within the colloidal silica, which forms a carbon-silicon bond. The stabilizer of the present invention is Si
It contains a carbon dioxide gas supply component in addition to glass solidification components such as O 2 , Na 2 SiO 3 , NaCO 3 , and CaCO 3. As the carbon dioxide gas supply component, urethane formation reactions such as polyisocyanates and polyols are also conveniently used. can do. Further, by adding boric anhydride H 3 BO 3 , a hard glass-based material can be obtained, and CaCO 3 , Si
Cement components such as O 2 , SO 2 Al 2 O 3 , Fe 2 O 3 , and MgO are also mixed. The component of this cement is 1
By adding about 20 g to 00 g, the work of the rock formation work is further strengthened, and H 2 SiO 3 + which is a main component of the rock is added.
It is intended to develop a SiO 2 over the years. In the chemical treatment method for harmful substances contained in the incinerated ash, the efficiency of mixing and stirring the incinerated ash and the chemical is the most important issue in any treatment method. The test of the mixing method and the treatment time was repeated, and as a result, the inorganic components of the incinerated ash particles required for solidification were lime (CaO), silicic acid (SiO 2 ), and alumina (Al
Compounds such as 2 O 3 ), iron (Fe 2 O 3 ), and sulfate (—SO 4 ) are reacted with water to form hydrates, and the ionic charge is corrected according to the change in the liquid ion concentration. , Deposition begins. [0008] The greatest impediment to the hardening of liquid layers, gas layers and organic matter in incinerated ash is that the hydraulic mineral of cement reacts quickly with calcium ions generated by hydrolysis to form insoluble or soluble compounds. Is to do. For example, when an insoluble salt is formed, the formed product covers the surface of the cement particles so that the subsequent reaction does not proceed.In the case of a soluble salt, it reacts one after another to form a solution outside the hydration reaction system. This is the effect of taking away. In any case, the chemical balance of the hydration reaction is disrupted if calcium ions, which should be the main component of the hydration reaction, are carried away to another reaction system. Therefore, by mixing the stable calcium treating agent of the present invention, the liquid phase increases the lime content and becomes an alkaline composition, and further solidifies before the hydration inhibiting effect is exerted by the rapid hydration reaction. Hydration reaction of lime aluminate hydrate is promoted, and ettringite (3CaO.Al 2 O 3 .3
CaSO 4 .32H 2 O) is produced more, and these double salts fix harmful substances including heavy metals and keep them from being eluted. Examples of the present invention will be described below, but these examples are merely means for assisting the understanding of the present invention.
It should be understood that these examples do not limit the invention in any way. In the following examples, Osaka City, Tokyo, Tsunomiya City,
The test was conducted in 20 towns and villages such as Tochigi regional administrative district and Tomisato town, and was based on test data from a Ministry of Health and Welfare-certified inspection organization. In addition,
In the example, "Incineration ash from a waste incineration plant in Tokyo"
Etc., but cement is added to the incinerated ash
It means incinerated ash that has been heat-treated in a tally kiln. Example 1 Silicon dioxide SiO 2 10 as a main raw material of a stabilizing agent
g, calcium oxide CaO 3 g, anhydrous sodium carbonate Na 2 CO 3 10 g, aluminum oxide Al 2 O 3
2 g, boric anhydride B 2 O 3 10 g, anhydrous potassium carbonate K 2 CO 3 3 g, sodium acetate CH 3 COONa ·
5 g of 3H 2 O, potassium silicate SiO 2 · K 2 O 5
g, water H 2 O 5000 ml, organic ammonium salt 50 ml as auxiliary material, salt NaCl 2 g, cobalt oxide CoO 2 g, methyl ethyl ketone C 2 H 5 as catalyst
COCH 3 5 g, ethylenediamine NH 2 CH 2 CH
5 g of 2 NH 2 were used. The temperature of water H 2 O was set to 60 ° C., and the chemicals were stirred for 30 minutes before the catalyst was added, and the catalyst was further added and stirring was continued for 30 minutes. Portland cement 2 is added to 1000 g of incinerated ash from Osaka city garbage incineration plant.
00 g and 4 l of the stabilizing agent of the present invention are kneaded, and slump 8
The solidification was carried out with a water content of 1 cm, and a curing period of one month was allowed, followed by a dissolution test. The dissolution test is cadmium, cyanide, organic phosphorus, lead, hexavalent chromium, arsenic, alkylmercury, PCB
I went about. As a result of this test, cyanide, organic phosphorus,
Hexavalent chromium, alkylmercury, PCB not detected, lead less than 0.5 mg / l, cadmium and arsenic less than 0.05 mg / l, total mercury 0.0005 mg / l.
Both values were less than the harmful substance criteria. EXAMPLE 2 200 g of Portland cement and 4 l of the stabilizing agent of the present invention were added to 1000 g of incineration ash discharged from a waste incineration plant in Tokyo.
Was kneaded, and one month after solidification, a dissolution test was conducted.
Among mercury, cadmium, lead, arsenic, cyan and chromium, lead was less than 0.34 mg / l and chromium was less than 0.06 mg / l, and no mercury, cadmium, arsenic and cyan were detected. Example 3 A mixture of 1000 g of incineration ash from a Utsunomiya incineration plant, 200 g of Portland cement and 4 l of the treating agent of the present invention was kneaded and subjected to a dissolution test one month after solidification. The dissolution test was performed on lead, cadmium, arsenic, hexavalent chromium, total mercury, organic phosphorus, and total cyan. The results of this dissolution test were as follows: lead less than 0.17 mg / l, cadmium 0.005 m
g / l, arsenic 0.02 mg / l, hexavalent chromium 0.1
Less than 4 mg / l, less than 0.0005 mg / l of total mercury, non-detection of organophosphorus and total cyan were all values that did not reach the criteria for harmful substances. Example 4 200 g of Portland cement and 4 liters of the treating agent of the present invention were kneaded with 1000 g of incineration ash from the incineration plant of the Tochigi district wide area administrative office, and the dissolution test was carried out one month later. The dissolution test results of lead, cadmium, arsenic, hexavalent chromium, total mercury, organic phosphorus, and total cyan were 1.00 for lead, 0.0005 for cadmium, 0.02 for arsenic, 0.0 for hexavalent chromium.
6. Total 0.0005 of mercury, organic phosphorus and total cyan were not detected, and all had a value not meeting the criteria. Example 5 1000 kg of incinerated ash was put into a concrete kneader, and 200 kg of cement was put therein while rotating, followed by stirring for 10 minutes. Then, 18 l of the stabilizing agent of the present invention was diluted with 10 times water and added. After kneading for 15 minutes, slump 15cm
The inside was poured into a concrete disposal place formed into a hollow block by a pressure pump and sealed. [0015] By solidifying and shaping the incinerated ash into a block using the stabilizing agent of the present invention, not only the transportation is simplified, but also the incinerated ash included in the incinerated ash, which has been considered difficult so far, is included. Since a solidified molded product from which no harmful substance leaks out can be obtained, the solidified molded product can be used as it is as a civil engineering or construction material for concrete blocks and the like. The compressive strength of the product of the present invention as a cement material can be arbitrarily changed by adjusting the ratio of Portland cement and stabilizing agent. As a result, the incinerated ash is not waste but a by-product that can be sufficiently used as a cement material.
【図面の簡単な説明】
【図1】本発明の焼却灰固化装置の一例を示すための模
式的平面図。
【符号の説明】
1.セメント原料受入れホッパー
2.ベルトフィーダー
3.6.7.ベルトコンベヤー
4.バツグンフィード
5.振動篩
8.磁選機1.8KW1.5KW
9.ロータリーキルン
10.11.12.13.17.21.22.25.2
8.33.38.スクリューコンベア
14.バケットエレベーター
15.原料タンク
16.差込みスライドゲート
18.ローラーミル
19.サイクロン
20.集塵機
23.トレー
24.バケットエレベーター
26.原料タンク
27.ローラーバルブ
29.計量ホッパー
30.混錬ミキサー
31.チャージホッパー
32.ロータリーバルブ
35.ホイスト
36.セメントサイロ
39.集塵機
40.安定剤投入装置BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic plan view showing an example of an incineration ash solidification device of the present invention. [Explanation of reference numerals] 1. Chopper receiving hopper Belt feeder 3.6.7. Belt conveyor4. Excellent feed5. Vibrating screen 8. Magnetic separator 1. 8KW 5KW 9. Rotary kiln 10.11.12.13.17.21.22.25.2
8.33.38. Screw conveyor 14. Bucket elevator 15. Raw material tank 16. Insert slide gate 18. Roller mill 19. Cyclone 20. Dust collector 23. Tray 24. Bucket elevator 26. Raw material tank 27. Roller valve 29. Weighing hopper 30. Kneading mixer 31. Charge hopper 32. Rotary valve 35. Hoist 36. Cement silo 39. Dust collector 40. Stabilizer dosing device
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−15248(JP,A) 特開 平5−317830(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-6-15248 (JP, A) JP-A-5-317830 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B09B 3/00
Claims (1)
残る有害な重金属や有機質分を含む焼却灰にセメントを
添加してロータリーキルンで加熱処理し、その後の工程
で有害物質安定処理剤を添加してから、ポルトランドセ
メントを加えて固化させることを特徴とするセメントを
主成分とする焼却灰の固化方法であって、上記有害物質
安定処理剤が、主原料としてSiO 2 、CaO、Na 2 C
O 3 、Al 2 O 3 、B 2 O 3 、K 2 CO 3 、CH 3 COONa・
3H 2 O 、SiO 2 ・K 2 O、水、副原料として有機アン
モニウム塩、NaCl、CoO、触媒としてC 2 H 5 CO
CH 3 、NH 2 CH 2 CH 2 NH 2 を使用したものであるこ
とを特徴とする方法。 (57) [Claims] [Claim 1] After incineration of sewage sludge, industrial waste, etc.
Cement is added to the remaining incinerated ash containing harmful heavy metals and organic matter , heat-treated in a rotary kiln, and the subsequent processes
A method for solidifying incinerated ash comprising cement as a main component, characterized by adding a harmful substance stabilizing agent in the above, and then adding Portland cement to solidify the harmful substance.
The stabilizing agent is SiO 2 , CaO, Na 2 C as a main raw material.
O 3 , Al 2 O 3 , B 2 O 3 , K 2 CO 3 , CH 3 COONa
3H 2 O , SiO 2 · K 2 O, water, and organic
Monium salt, NaCl, CoO, C 2 H 5 CO as catalyst
This is obtained by using a CH 3, NH 2 CH 2 CH 2 NH 2
And a method characterized by the following.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP30716294A JP3507157B2 (en) | 1994-11-05 | 1994-11-05 | Incineration ash solidification equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30716294A JP3507157B2 (en) | 1994-11-05 | 1994-11-05 | Incineration ash solidification equipment |
Publications (2)
Publication Number | Publication Date |
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JPH08131990A JPH08131990A (en) | 1996-05-28 |
JP3507157B2 true JP3507157B2 (en) | 2004-03-15 |
Family
ID=17965782
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JP30716294A Expired - Fee Related JP3507157B2 (en) | 1994-11-05 | 1994-11-05 | Incineration ash solidification equipment |
Country Status (1)
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JP (1) | JP3507157B2 (en) |
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1994
- 1994-11-05 JP JP30716294A patent/JP3507157B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
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JPH08131990A (en) | 1996-05-28 |
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