JP3899563B2 - FRP waste disposal method - Google Patents

FRP waste disposal method Download PDF

Info

Publication number
JP3899563B2
JP3899563B2 JP26115796A JP26115796A JP3899563B2 JP 3899563 B2 JP3899563 B2 JP 3899563B2 JP 26115796 A JP26115796 A JP 26115796A JP 26115796 A JP26115796 A JP 26115796A JP 3899563 B2 JP3899563 B2 JP 3899563B2
Authority
JP
Japan
Prior art keywords
frp
raw material
waste
frp waste
melting furnace
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
Application number
JP26115796A
Other languages
Japanese (ja)
Other versions
JPH1085704A (en
Inventor
新 河西
淳 山沢
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.)
Nitto Boseki Co Ltd
Original Assignee
Nitto Boseki Co 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 Nitto Boseki Co Ltd filed Critical Nitto Boseki Co Ltd
Priority to JP26115796A priority Critical patent/JP3899563B2/en
Publication of JPH1085704A publication Critical patent/JPH1085704A/en
Application granted granted Critical
Publication of JP3899563B2 publication Critical patent/JP3899563B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C25/00Surface treatment of fibres or filaments made from glass, minerals or slags
    • C03C25/002Thermal treatment
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B3/00Charging the melting furnaces
    • C03B3/02Charging the melting furnaces combined with preheating, premelting or pretreating the glass-making ingredients, pellets or cullet
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C25/00Surface treatment of fibres or filaments made from glass, minerals or slags
    • C03C25/70Cleaning, e.g. for reuse
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)

Description

【0001】
【発明の属する技術分野】
本発明はFRP廃棄物の処理方法に関するものである。
【0002】
【従来の技術】
ガラス繊維を使用したFRP製品が不要になったとき、焼却してもガラス繊維が残り、焼却するとかえって焼却前より体積が増加したり、繊維が脆くなり作業中に周囲に飛散しかえって扱い難いものとなる。またガラス繊維は不燃性で腐らないので埋め立て処分してもなんら問題はないのであるが、繊維が長く強いのでコンパクトに圧縮しにくいため嵩高で処理費用がかさむという問題がある。
そのため、FRP廃棄物を細かく砕き、粉末状にしたものをコンクリ−トに入れたり、FRPに使用する充填剤として再利用するなどの試みがされている。しかし技術的、経済的に種々の問題があるためなかなか十分な量を処理し有効利用するまでには至っていない。
これらの問題を解決するため、FRPの廃棄物を適当な大きさに粉砕したものを直接、断熱材、吸音材などに使用されるガラス短繊維の原料ガラス溶融炉中に投入し、FRP製品中の樹脂成分を加熱用燃料に利用しながらガラス繊維部分を原料の一部として溶融し、ガラス短繊維を製造する方法が特開平6−40735号公報に開示されている。
【0003】
しかしながら、FRPの製品の樹脂含有率は成形方法により違い、例えばハンドレイアップ方法では樹脂の含有量は約70重量%、フィラメントワインディング法では約30重量%など、その屑が、どの成型方法によって製造されたかによって樹脂の含有量に大きな差がある。また難燃剤を使用したものも混じり樹脂の燃焼速度が違う。このような差があるので最適の燃焼条件が違い、これら種々の原料を同じ炉で使用するには炉内の酸化条件のコントロ−ルが難しく、屑ガラス繊維の表面に炭素成分が残る危険があった。炭素成分が溶融原料中に巻き込まれると気泡が発生したり、繊維が切れやすくなるなどの問題が起きるため、樹脂の燃焼をより高めるため炉内の状況に応じて酸素あるいは空気の炉内導入をするなどの高度の操炉技術を必要としていた。
しかも、溶融炉の内部は高温で赤熱状態であり溶融原料中の炭素成分がどのような状況であるか把握することは非常に困難であった。
【0004】
【発明が解決しようとする課題】
この様にFRP廃棄物は、大量に発生するにもかかわらず、その処理には決め手がない。本発明はFRP廃棄物を直接、溶融炉に投入する時、炭素成分が溶融物中に入るのを防ぎ、大量に製造されるガラス短繊維あるいはロックウ−ルの原料の一部をFRP廃棄物中のガラス繊維や充填剤により代替しようとするものである。
【0005】
【課題を解決するための手段】
本発明は、FRP廃棄物中のガラス繊維をガラス短繊維あるいはロックウ−ルの原料として溶融炉に投入するに当たり、FRP廃棄物とガラス短繊維原料あるいはロックウール原料を混合し、有機物を予め燃焼酸化して除去する。そして除去する過程で加熱された材料の熱が屑から逃げないうちに溶融炉に投入し、予熱の効果を最大限に利用しFRP廃棄物を有効利用するものである。
【0006】
【発明の実施の形態】
本発明でFRP廃棄物とは、ガラス繊維を使用したFRP製品、射出成型製品あるいはこれらの製造工程で発生する屑、切れ端、不良品あるいはFRPのバスタブ、レジャ−用ボ−ト、漁船、構造物などの耐用年数が経過し不要になったものの破砕品など、樹脂を使用した製品で焼却してもガラス繊維が残るものを意味する。
FRP廃棄物の使用形態としては、原料保管ホッパ−から公知の取り出し方法、輸送方法を使用し焼却炉に供給するので、公知のFRP製品の破砕、粉砕方法によりホッパ−中でブリッジ現象を起こすことなく容易に取り出せる形態にしたものが好ましい。使用原料により設備設計者がホッパ−形状を考えて、例えば、FRPなら1辺の長さが5cm以下好ましくは1cm以下と設定することが出来るし、もし必要であれば、1mm以下の粉体とすることも出来る。
これらのFRP廃棄物はFRP廃棄物単独で焼却することも、ガラス短繊維あるいはロックウ−ル原料と混合して焼却することもできる。
【0007】
FRP廃棄物の燃焼熱を原料の予熱に有効に利用することができるので、ガラス短繊維、またはロックウ−ル原料とFRP廃棄物とを混合して焼却することが望ましいが、FRP廃棄物のみを焼成することもできる。その場合、焼成したものをガラス短繊維、ロックウ−ルの原料と別々に溶融炉に投入したり、それらの原料と混合してから投入することも出来る。
これらのFRP廃棄物を加熱し有機物を除去する焼却手段には、通常使用される各種の公知の産業用廃棄物焼却炉が使用できる。たとえば、大型のものでは移動床型、ロ−タリ−キルン型、小型のものでは、直火型、あるいは乾留型などの焼却炉が例示出来る。これらの炉には補助加熱用の装置、例えばガスバ−ナ−を備えたものが望ましい。
この焼却手段は有機物を含む材料を効率良く燃焼させ、加熱された材料を冷却することなく、容易に取り出せる機能を備えたものであればよく特に構造を限定する必要はない。しかしFRP廃棄物を含む原料を連続的に大量に焼却処理する手段としては連続焼成タイプの加熱炉が好ましく、投入した原料の有機物を焼却後、溶融したものを溶融炉に供給することも可能である。
【0008】
焼却炉でFRP廃棄物を加熱し有機物を酸化除去する過程で、炭素の含有量は0.5重量%以下に短時間でなることが望ましく、ガラス短繊維用の原料は更に少ない量にすることが望ましい。
酸化温度は高いほど有機物の除去には望ましいが、加熱温度が高くなるとFRP廃棄物同志が融着し、固形炭素を閉じ込め、溶融原料中で発泡し、製造した繊維の強度が低下したり、白金ノズルと化合物を作りノズルを破壊する原因となりやすい。このようなことがないよう、有機物の燃焼が進み残存炭素の量が少なくなるまでの焼成炉の部分の温度をガラス繊維の溶融温度以下に押さえる、あるいはガラス短繊維、またはロックウ−ル原料とFRP廃棄物と混合したり、炉の壁に付着し堆積しないよう炭酸カルシュウム、ドロマイトの粉末を1−5重量%FRP廃棄物原料に混合して加熱処理することが有効である。
使用するFRP廃棄物の発熱量が不十分なときは、粉粒状の石炭、コ−クスなどを配合し原料の予熱温度を高くすることも出来る。
【0009】
加熱温度は酸化が急速に行われる約450℃好ましくは600℃以上が望ましく、高温の方はロックウ−ルの原料と混合加熱する場合、約1200℃ぐらいまでの温度で処理することが可能である。その加熱温度はFRP廃棄物物の量、含まれる有機物の量、FRP廃棄物に配合される他の原料などの割合を考慮して適宜決定される。
その条件を決める大きな要素は、出来るだけ酸化を完全に行うことの出来る加熱温度であり、原料供給量であり、これらは実験により条件を確認し設定する条件である。
【0010】
この焼成した高温の材料は冷却されないうちに直ちに、ロックウ−ルあるいはガラス短繊維用原料溶融炉に投入される。焼成条件によっては、原料が溶融し大きな塊になることもあるので、焼成後はそのような塊を公知のロ−ルクラッシャ−などの破砕手段により細かく砕くことが必要である。
本発明で言う、焼却炉で有機物を酸化除去した後、直ちにガラス短繊維あるいはロックウ−ル原料溶融炉に投入する、とは、溶融炉の液面の変化を出来るだけ少なくすることを考慮した上で、FRP廃棄物の加熱炉出口から溶融炉の上部に設けた開口部から直接、投入するか、焼却から出てくる焼成された原料の量の変動を調整するため周囲を断熱した小型のホッパ−を設けFRP廃棄物を一時滞留させ冷却しないうちに、スクリュ−フィ−ダ−など公知の原料輸送方法により溶融炉に投入するように、焼成した材料のもつ熱を利用できる間に溶融炉に投入することを意味する。
【0011】
【実施例】
以下実施例により本発明を説明するが、発明の思想の具体的な例示であり、この用途、この方法に限られるものではない。
【0012】
原料には、ハンドレイアップ法で製造されたレジャ−用ボ−トを切断、破砕した1辺の平均長さが1cmのFRP屑20重量%とロックウ−ルショット屑(ロックウ−ル製造において発生する非繊維物)及び小石状のロックウ−ル原料80重量%を混合したものを用いた。
その混合物を移動床式焼却炉1に1時間1tonの割合で供給し、補助加熱装置としてガスバ−ナ−を使用し炉内最高温度を800℃にして運転し有機物を除去した。
【0013】
有機物の含有量を0.3重量%以下にした原料は、焼却炉出口に設置された耐熱金属製の輸送手段2によりロックウ−ル原料を溶解する3本の黒鉛電極を備えた電気炉3に供給された。供給量はフィ−ダ−の一部に設けられた計量器(図示せず。)により制御されている。
電気炉3中で溶融された加熱原料は、1450℃の温度の溶融された状態でフィ−ダ−により高速回転する耐熱金属製のスピンナ−を有するロックウ−ル用繊維化装置4に供給され遠心力によりロックウ−ル繊維とした。
【0014】
【発明の効果】
本発明によれば、従来廃棄していたFRP廃棄物をガラス短繊維あるいはロックウ−ルの原料として使用することができ産業廃棄物が減少するだけでなく、
今後大量に発生するFRP廃棄物の持つエネルギ−をガラス短繊維あるいはロックウ−ル原料の予熱に使用することができるという省エネによる経済的な効果も合せ持つ有効な資源再利用方法である。
また、FRP廃棄物を直接溶融炉に投入しないで、有機物を燃焼させる焼却炉と繊維化する原料を溶融する溶融炉が別れているので、FRP廃棄物の樹脂含有量、配合量などが変動しても、それに応じた適正な条件で焼却炉を運転することにより廃棄物中に残存する炭素の量をコントロ−ルすることが容易である。溶融炉の温度条件とは無関係に、焼成の温度などの条件を変更できるので、溶融炉の溶解状況に影響をおよぼさないという利点がある。
また、焼却炉と溶融炉の間に断熱された予熱原料供給ホッパ−を設けると予熱した原料を冷ますことなく、焼却炉、溶融炉の状況に応じて原料供給の調整をすることができる。
【図面の簡単な説明】
【図1】本発明の一実施例を示す。
【符号の説明】
1、移動床式焼却炉
2、FRP廃棄物焼成物を炉に供給する輸送手段
3、ロックウ−ル製造用の黒鉛電極を使用する電気溶融炉
4、繊維化装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for treating FRP waste.
[0002]
[Prior art]
When FRP products that use glass fiber are no longer needed, glass fiber remains even after incineration, and instead of incineration, the volume increases or the fiber becomes brittle and scatters to the surroundings during work, making it difficult to handle It becomes. Glass fiber is non-flammable and does not rot, so there is no problem even if it is disposed of in landfills. However, since the fiber is long and strong, it is difficult to compress compactly, and there is a problem that it is bulky and processing costs are high.
For this reason, attempts have been made to finely pulverize FRP waste and put the powder into a concrete or reuse it as a filler used in FRP. However, due to various technical and economic problems, a sufficient amount cannot be processed and effectively used.
In order to solve these problems, FRP waste pulverized to an appropriate size is directly put into a glass short glass fiber melting furnace used for heat insulating materials, sound absorbing materials, etc. Japanese Patent Application Laid-Open No. 6-40735 discloses a method for producing a short glass fiber by melting a glass fiber part as a part of a raw material while using the above resin component as a heating fuel.
[0003]
However, the resin content of FRP products varies depending on the molding method. For example, the resin content is about 70% by weight in the hand lay-up method and about 30% by weight in the filament winding method. There is a big difference in the resin content depending on whether it is done. Also, those using flame retardants are mixed and the burning speed of the resin is different. Because of these differences, optimal combustion conditions are different, and in order to use these various raw materials in the same furnace, it is difficult to control the oxidation conditions in the furnace, and there is a risk that carbon components remain on the surface of the waste glass fiber. there were. When carbon components are entrained in the molten material, problems such as bubbles are generated and fibers are likely to break, so oxygen or air can be introduced into the furnace depending on the conditions in the furnace in order to further enhance resin combustion. It requires advanced furnace operation technology.
Moreover, since the inside of the melting furnace is in a red hot state at a high temperature, it is very difficult to grasp the state of the carbon component in the molten raw material.
[0004]
[Problems to be solved by the invention]
As described above, although the FRP waste is generated in a large amount, there is no decisive factor in its processing. The present invention prevents the carbon component from entering the melt when the FRP waste is directly put into the melting furnace, and a part of the raw material of the short glass fiber or rock wool produced in a large amount is contained in the FRP waste. The glass fiber and filler are to be replaced.
[0005]
[Means for Solving the Problems]
In the present invention, when glass fiber in FRP waste is introduced into a melting furnace as a raw material for short glass fiber or rock wool, FRP waste and short glass fiber raw material or rock wool raw material are mixed, and organic matter is pre-combusted and oxidized. And remove. Then, the heat of the material heated in the removal process is put into the melting furnace before it escapes from the waste, and the FRP waste is effectively used by making the best use of the effect of preheating.
[0006]
DETAILED DESCRIPTION OF THE INVENTION
In the present invention, FRP waste refers to FRP products using glass fibers, injection molded products or scraps, shards, defective products or FRP bathtubs, leisure boats, fishing boats, structures produced in these manufacturing processes. It means that glass fiber remains even if it is incinerated with a product using resin, such as a crushed product that is no longer needed after its useful life has elapsed.
As FRP waste is used from a raw material storage hopper, it is supplied to the incinerator using a known removal method and transportation method, so that a bridging phenomenon occurs in the hopper by a known FRP product crushing and pulverization method. It is preferable to use a form that can be easily removed. The equipment designer considers the hopper shape depending on the raw materials used. For example, if it is FRP, the length of one side can be set to 5 cm or less, preferably 1 cm or less. You can also
These FRP wastes can be incinerated with FRP wastes alone or mixed with short glass fibers or rock wool raw materials for incineration.
[0007]
Since the combustion heat of FRP waste can be used effectively for preheating the raw material, it is desirable to mix and incinerate short glass fiber or rock wool raw material and FRP waste, but only FRP waste It can also be fired. In that case, the fired product can be put into a melting furnace separately from the short glass fiber or rock wool material, or can be added after mixing with the raw material.
Various well-known industrial waste incinerators that are usually used can be used as incineration means for heating these FRP wastes to remove organic substances. For example, an incinerator such as a moving floor type or a rotary kiln type can be used for a large type, and a direct fire type or a dry distillation type can be used for a small type. These furnaces are preferably equipped with an auxiliary heating device such as a gas burner.
The incineration means is not particularly limited as long as it has a function of efficiently burning a material containing an organic substance and easily taking out the heated material without cooling. However, as a means for continuously incinerating a large amount of raw materials containing FRP waste, a continuous firing type heating furnace is preferable, and after injecting the organic material of the input raw materials, it is possible to supply the molten material to the melting furnace. is there.
[0008]
During the process of oxidizing and removing organic matter by heating FRP waste in an incinerator, it is desirable that the carbon content be 0.5% by weight or less in a short time, and the raw material for short glass fibers should be further reduced. Is desirable.
The higher the oxidation temperature, the better for the removal of organic matter, but when the heating temperature increases, the FRP wastes fuse together, confine solid carbon, foam in the molten raw material, and the strength of the manufactured fiber decreases, platinum It tends to cause nozzles and compounds to break down the nozzles. In order to prevent such a situation, the temperature of the portion of the baking furnace until the combustion of organic matter proceeds and the amount of residual carbon decreases is kept below the melting temperature of the glass fiber, or the glass short fiber, or the rock wool raw material and the FRP It is effective to mix calcium carbonate and dolomite powder with 1-5 wt% FRP waste raw material and heat-treat so that it does not mix with waste or adhere to the wall of the furnace.
When the heat generation amount of the FRP waste to be used is insufficient, it is possible to increase the preheating temperature of the raw material by blending granular coal, coke and the like.
[0009]
The heating temperature is about 450.degree. C., preferably 600.degree. C. or higher, at which oxidation takes place rapidly. The higher temperature can be processed at a temperature up to about 1200.degree. C. when mixed and heated with the rock wool raw material. . The heating temperature is appropriately determined in consideration of the amount of FRP waste, the amount of organic matter contained, and the ratio of other raw materials blended into the FRP waste.
The major factors that determine the conditions are the heating temperature at which the oxidation can be carried out completely as much as possible, and the amount of raw material supplied.
[0010]
The fired high-temperature material is immediately put into a rock wall or a short glass fiber raw material melting furnace before being cooled. Depending on the firing conditions, the raw material may melt into large lumps, and after calcination, such lumps need to be finely crushed by a crushing means such as a known roll crusher.
In the present invention, after oxidizing and removing organic substances in an incinerator, immediately putting it into a short glass fiber or rock wool raw material melting furnace means that the change in the liquid level of the melting furnace is minimized. A small hopper that is directly insulated from the opening of the FRP waste heating furnace through the opening provided in the upper part of the melting furnace or insulates the surroundings in order to adjust fluctuations in the amount of the baked raw material that comes out of the incineration. In the melting furnace, the heat of the calcined material can be used so that the FRP waste is temporarily retained and cooled before being put into the melting furnace by a known raw material transportation method such as a screw feeder. It means to throw in.
[0011]
【Example】
EXAMPLES The present invention will be described below with reference to examples, but it is a specific illustration of the idea of the invention and is not limited to this application and this method.
[0012]
As raw materials, 20% by weight of FRP scraps having an average length of 1 cm on one side cut and crushed by a boat for lager manufactured by the hand lay-up method and rock wool shot scraps (generated in the production of rock wool) Non-fiber) and 80% by weight of pebble-like rock wool material were used.
The mixture was supplied to the moving bed incinerator 1 at a rate of 1 ton for 1 hour, and a gas burner was used as an auxiliary heating device and the furnace was operated at a maximum temperature of 800 ° C. to remove organic substances.
[0013]
The raw material having an organic content of 0.3% by weight or less is supplied to an electric furnace 3 equipped with three graphite electrodes for dissolving a rock wool raw material by means of a heat-resistant metal transportation means 2 installed at the incinerator outlet. Supplied. The supply amount is controlled by a measuring instrument (not shown) provided in a part of the feeder.
The heated raw material melted in the electric furnace 3 is supplied to a rock wool fiberizer 4 having a heat-resistant metal spinner which is rotated at high speed by a feeder in a molten state at a temperature of 1450 ° C. Rock wool fiber was formed by force.
[0014]
【The invention's effect】
According to the present invention, conventionally discarded FRP waste can be used as a raw material for short glass fiber or rock wool, and not only industrial waste is reduced,
This is an effective resource recycling method that combines the economic effect of energy saving that the energy of FRP waste generated in large quantities in the future can be used to preheat short glass fiber or rock wool raw material.
In addition, since the incinerator that burns organic matter and the melting furnace that melts the raw material to be fiberized are separated without directly putting the FRP waste into the melting furnace, the resin content and blending amount of the FRP waste fluctuate. However, it is easy to control the amount of carbon remaining in the waste by operating the incinerator under appropriate conditions according to the conditions. Regardless of the temperature conditions of the melting furnace, conditions such as the firing temperature can be changed, so there is an advantage that the melting state of the melting furnace is not affected.
If a preheated raw material supply hopper insulated between the incinerator and the melting furnace is provided, the raw material supply can be adjusted according to the conditions of the incinerator and the melting furnace without cooling the preheated raw material.
[Brief description of the drawings]
FIG. 1 shows an embodiment of the present invention.
[Explanation of symbols]
1, moving bed incinerator 2, transportation means 3 for supplying FRP waste fired material to the furnace, electric melting furnace 4 using a graphite electrode for producing rock wool, fiberizing apparatus

Claims (1)

FRP廃棄物とガラス短維繊原料あるいはロックウール原料を混合し焼却炉で加熱し有機物を酸化除去した後、直ちにガラス短繊維原料溶融炉あるいはロックウール原料溶融炉に投入するFRP廃棄物の処理方法。And the FRP waste, mixed with glass short維繊material or rock wool material, after heating to remove oxidized organics incinerator, the FRP waste immediately charged into the glass wool material melting furnace or a rock wool material melting furnace Processing method.
JP26115796A 1996-09-11 1996-09-11 FRP waste disposal method Expired - Fee Related JP3899563B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26115796A JP3899563B2 (en) 1996-09-11 1996-09-11 FRP waste disposal method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26115796A JP3899563B2 (en) 1996-09-11 1996-09-11 FRP waste disposal method

Publications (2)

Publication Number Publication Date
JPH1085704A JPH1085704A (en) 1998-04-07
JP3899563B2 true JP3899563B2 (en) 2007-03-28

Family

ID=17357910

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26115796A Expired - Fee Related JP3899563B2 (en) 1996-09-11 1996-09-11 FRP waste disposal method

Country Status (1)

Country Link
JP (1) JP3899563B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019207259A1 (en) 2018-04-27 2019-10-31 Arkema France Method for recycling composite materials with an improved energy balance
WO2021004601A1 (en) 2019-07-05 2021-01-14 Sumitomo SHI FW Energia Oy An arrangement for and a method of recycling mineral wool waste

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2023276617A1 (en) * 2021-06-29 2023-01-05 日東紡績株式会社 Method for producing long glass fibers

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019207259A1 (en) 2018-04-27 2019-10-31 Arkema France Method for recycling composite materials with an improved energy balance
FR3080624A1 (en) * 2018-04-27 2019-11-01 Arkema France ENHANCED ENERGY BALANCE COMPOSITE RECYCLING PROCESS
JP2021522085A (en) * 2018-04-27 2021-08-30 アルケマ フランス Composite material recycling method with improved energy balance
JP7449871B2 (en) 2018-04-27 2024-03-14 アルケマ フランス Composite recycling method with improved energy balance
WO2021004601A1 (en) 2019-07-05 2021-01-14 Sumitomo SHI FW Energia Oy An arrangement for and a method of recycling mineral wool waste

Also Published As

Publication number Publication date
JPH1085704A (en) 1998-04-07

Similar Documents

Publication Publication Date Title
JP2804370B2 (en) Method and apparatus for recycling mineral fiber scrap
US6857999B2 (en) Method for destroying and/or inerting waste
US5711018A (en) Rotary kiln treatment of potliner
CA1180952A (en) Method for melting and treating waste
JP4005770B2 (en) Waste incineration method
CN112460603A (en) Hazardous waste incineration system and hazardous waste incineration method
JP3967539B2 (en) Cement manufacturing method
JP3899563B2 (en) FRP waste disposal method
JPH02261589A (en) Method for melting material and device for executing said method
JP2945311B2 (en) Waste incineration method
JP3779095B2 (en) Glass fiber waste material recycling equipment
JP3683699B2 (en) Method for treating fibrous glass covered with organic matter
JP2001280614A (en) Waste processing apparatus
JPH07247143A (en) Production of cement clinker
JPH10158023A (en) Utilization of erp waste
JP3783146B2 (en) Self-burning fuel rods using ash body
CA2008488A1 (en) Process and a device for transferring leachable substances in waste material into gas of leach stable compounds
JPS6099921A (en) Process for melting and treating burned ash
JP2003129138A (en) Recycling method for end-of-life vehicle or waste electrical household appliance
JPH0465289B2 (en)
JP2004232024A (en) Steelmaking method
JPH0522808B2 (en)
JPH08178239A (en) Melting furnace
JP3670848B2 (en) Method for producing crystallized slag
JP3962178B2 (en) Hazardous material processing method and apparatus

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20050310

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050405

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050603

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20061205

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20061218

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110112

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110112

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110112

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120112

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120112

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130112

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130112

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140112

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees