JP4430423B2 - Treatment method for wood-based industrial waste - Google Patents

Treatment method for wood-based industrial waste Download PDF

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JP4430423B2
JP4430423B2 JP2004032095A JP2004032095A JP4430423B2 JP 4430423 B2 JP4430423 B2 JP 4430423B2 JP 2004032095 A JP2004032095 A JP 2004032095A JP 2004032095 A JP2004032095 A JP 2004032095A JP 4430423 B2 JP4430423 B2 JP 4430423B2
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phenol resin
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弘道 黒田
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Misawa Homes Co Ltd
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本発明は、木質系産業廃棄物を破砕し、その木片原料にフェノール樹脂を含浸させて、フェノール樹脂を含浸させた木片原料を圧縮成形して樹脂成形品として木質系産業廃棄物を処理する方法に関する。   The present invention is a method for treating wood-based industrial waste as a resin molded product by crushing wood-based industrial waste, impregnating the wood-chip raw material with a phenol resin, and compression-molding the wood-chip raw material impregnated with the phenol resin. About.

現在、日本では年間約1千万トンの廃棄物が排出されており、これら廃棄物には、一般家庭で排出される使用済みのペットボトル、樹脂製のラッピングフィルム、レジ袋や紙袋、カップ麺の容器、お菓子や玩具等の箱類、アルミ缶、スチール缶、ガラスびん等の容器包装廃棄物(一般廃棄物)と、工場で排出される食品コンテナ等の包装部材を形成した際に出る端材や解体業者が解体した家屋の解体材、製材業者から排出される樹皮等の産業廃棄物とがある。
そして、このような廃棄物は、これまで焼却したり埋め立てたりすることで処理されてきたが、焼却によるダイオキシンの排出の問題や、埋め立て地のスペースが激減しており、その許容量に限界が生じてきている。また、焼却炉や鉄鋼所等から排出される汚泥、焼却スラグ、火山灰スラグ等も、最終処分場でしか廃棄することができず増加する一方であった。
また、建築廃材、土木廃材等から多くの廃材が排出され、それを焼却するだけでは、資源保護の観点から問題のあるものと指摘されている。
そのため、このような廃棄物を資源として有効に活用するマテリアルリサイクル化の推進が望まれている。
Currently, approximately 10 million tons of waste is discharged annually in Japan. These wastes include used plastic bottles, plastic wrapping films, plastic bags, paper bags, and cup noodles that are discharged at home. It comes out when forming packaging materials such as food containers, etc., and containers and packaging waste (general waste) such as containers, candy and toys, aluminum cans, steel cans, glass bottles, etc. There are scraps, demolition materials for houses demolished by demolition contractors, and industrial waste such as bark discharged from lumber contractors.
Such waste has been treated by incineration or landfill, but the problem of dioxin emissions due to incineration and the landfill space has been drastically reduced. It is happening. In addition, sludge, incineration slag, volcanic ash slag, etc. discharged from incinerators and steelworks can only be disposed of at the final disposal site and are increasing.
In addition, it is pointed out that there is a problem from the viewpoint of resource protection if many waste materials are discharged from building waste materials, civil engineering waste materials, etc., and only incinerating them.
Therefore, promotion of material recycling that effectively uses such waste as a resource is desired.

ところで、一般家庭で排出される容器包装廃棄物は、通常、ゴミを出す際に、容器包装の素材ごとに、例えば、ペットボトル、アルミ缶、紙類等に分別して排出し、市町村等の自治体が回収して、さらに、分別されるが、これらの容器包装廃棄物は様々な樹脂や紙類、アルミ箔、金属類等の不純物が混入しており、成分が不明であり、また、汚れ等が付着しているので、この廃棄物を再利用することが困難であった。
また、工場等で排出される産業廃棄物においては、ある程度はその成分が判断できるが、この場合においても依然として用途開発が進んでおらず、焼却や埋め立て処分による処理に頼らざるを得ないのが現状であり、マテリアルリサイクル化が進んでいない。
そこで昨今、様々な廃棄物を利用することによって成形品を製造し、廃棄物量を低減してマテリアルリサイクル化を推進する技術が試みられてきた。
By the way, waste containers and packaging discharged from ordinary households are usually separated into containers, packaging materials, for example, plastic bottles, aluminum cans, paper, etc. These containers and packaging waste are contaminated with impurities such as various resins, papers, aluminum foil, metals, etc., the ingredients are unknown, and dirt, etc. It was difficult to recycle this waste.
In addition, industrial waste discharged from factories, etc., can be judged to some extent, but in this case as well, application development is still not progressing, and there is no choice but to rely on treatment by incineration or landfill disposal. Currently, material recycling is not progressing.
Therefore, in recent years, a technique for manufacturing a molded product by using various wastes, reducing the amount of wastes, and promoting material recycling has been tried.

その一つに、本出願人が提案した廃棄物処理システムがある。(特許文献1参照)
これは、商品が消費された場合に不要になる容器または包装等の不純物を含む樹脂製容器包装廃棄物と、不純物を含む樹脂製産業廃棄物とのうち少なくとも一方の樹脂製廃棄物を回収する樹脂製廃棄物回収工程と、
この樹脂製廃棄物回収工程で回収された不純物を含む樹脂製廃棄物を、粗粉砕する樹脂製廃棄物粗粉砕工程と、
この樹脂製廃棄物粗粉砕工程で得られた樹脂粉砕物および不純物粉砕物を、それらの比重差によって分別する分別工程と、
この分別工程で得られた特定種類の樹脂粉砕物を、樹脂成形プラントに搬送する樹脂粉砕物搬送工程とを含むことを特徴とするものである。
One of them is a waste treatment system proposed by the present applicant. (See Patent Document 1)
This is to collect at least one resinous waste of resinous containers and packaging waste containing impurities such as containers or packaging that are not required when the product is consumed, and resinous industrial waste containing impurities. Resin waste collection process,
A resin waste coarse pulverization step for roughly pulverizing the resin waste containing impurities recovered in the resin waste recovery step;
A separation step of separating the resin pulverized product and the impurity pulverized product obtained in this resin waste coarse pulverization step according to their specific gravity difference;
And a resin pulverized material transporting step for transporting a specific type of resin pulverized material obtained in this separation step to a resin molding plant.

この技術は、樹脂製廃棄物回収工程と、樹脂製廃棄物粗粉砕工程と、分別工程と、樹脂粉砕物搬送工程とを含むもので、回収された樹脂製廃棄物は、前記樹脂製廃棄物粗粉砕工程で粗粉砕されて、分別工程で、ある程度、特定種類に分別されて前処理され、さらに、樹脂粉砕物搬送工程で処理されて成形品を得ることができるものである。
しかし、この技術の場合、成形品を作るために、比重の違いによる分別工程からなる前処理が必要で、廃棄物の処理システムとしてはコスト高になる等の不満がある。
This technology includes a resin waste recovery step, a resin waste coarse pulverization step, a separation step, and a resin pulverized material transfer step. The recovered resin waste is the resin waste It is coarsely pulverized in the coarse pulverization step, separated into a certain type to some extent in the separation step, pretreated, and further processed in the resin pulverized product conveying step to obtain a molded product.
However, in the case of this technique, in order to produce a molded product, pretreatment consisting of a separation process due to a difference in specific gravity is necessary, and there is a complaint that the cost of the waste treatment system is high.

特に建築廃材等の廃棄物を処理する上では、よりコストの低い廃棄物の処理方法の開発が望まれている。従来、コストにおいて、より安価に済む技術として、木質系廃材をチップ状に砕いて、それをフェノール樹脂で結合させて、ボードとして再利用しようとする技術がある。(特許文献2参照)   In particular, when processing waste such as building waste, it is desired to develop a waste processing method with lower cost. Conventionally, as a technology that can be made cheaper in cost, there is a technology in which a wood-based waste material is crushed into chips and bonded with a phenol resin to be reused as a board. (See Patent Document 2)

これは、フェノール樹脂を20〜40wt%に含浸させた木片原料の表裏面の双方又はいずれか一方に、フェノール樹脂の浸透性に優れた素材で形成した表面材を被設して、該表面材に加圧加熱過程で軟化したフェノール樹脂を浸透させると共に上記木片原料を圧縮した後の冷却固化により密組織に一体化させて成るものである。   This is achieved by placing a surface material made of a material excellent in phenol resin permeability on both or either of the front and back surfaces of a wood chip material impregnated with 20 to 40 wt% of a phenol resin. It is formed by impregnating with a phenol resin softened in the course of pressure and heating and integrating it into a dense structure by cooling and solidifying after compressing the wood chip material.

この技術は、建築廃材等を直径約6mm程度のチップ状に粉砕し、粉砕した木材チップ(木片原料)をレゾール型のフェノール樹脂槽に含浸させ、これを適当時間含浸状態に保ち、含浸した木材チップを取り出して、メタノールを蒸散させるもので、フェノール樹脂分の木材に対する残存量の調整が難しいという問題がある。   This technology pulverizes building waste materials, etc. into chips of about 6 mm in diameter, impregnates the crushed wood chips (raw wood raw material) into a resol-type phenolic resin tank, maintains this in an impregnated state for an appropriate time, and impregnates the wood The chip is taken out to evaporate methanol, and there is a problem that it is difficult to adjust the residual amount of phenol resin for wood.

さらに、フェノール樹脂は所定の量分、木片原料に含浸させる技術が難しく、また熱が加わることによって硬化したり、可塑性流れを起こしたりするので、フェノール樹脂の取り扱いも十分な管理が必要とされている。
フェノール樹脂を含浸させた木片原料の、余剰な成分を取り除くには、時間をおいて蒸散するのを待たなければならず、この場合、蒸散にムラがあったり、気候や環境によっては蒸散するまでの時間長かったりなど、品質管理の面においても課題があり、木質系産業廃棄物のリサイクル方法を簡便にするまでには至らなかった。
特開2003−080520号公報 実用新案登録第3080504号公報
In addition, it is difficult to impregnate the wood material with a predetermined amount of phenol resin, and it is hardened by heating and causes plastic flow, so the phenol resin must be handled well. Yes.
In order to remove the surplus components of the wood chip material impregnated with phenolic resin, it is necessary to wait for transpiration after a while. In this case, until the transpiration is uneven or depending on the climate and environment However, there was a problem in terms of quality control, such as the length of time, and the recycling method for wood-based industrial waste could not be simplified.
JP 2003-080520 A Utility Model Registration No. 3080504

そこで本発明は、木片原料とフェノール樹脂とを含浸させて樹脂成形品に成形する木質系産業廃棄物の処理方法を提案するにあたって、マテリアルリサイクルを前提とし、より安価に済み、品質管理を徹底した樹脂成形品を製造する工程を含む、木質系産業廃棄物の処理方法を提供することを目的とした。   Therefore, the present invention proposes a method for treating wood-based industrial waste that is impregnated with wood chip material and phenolic resin and molded into a resin molded product. An object of the present invention is to provide a method for treating wood-based industrial waste, including a step of producing a resin molded product.

請求項1の発明は、木質系産業廃棄物を回収し、回収された不純物を含む木質系産業廃棄物を破砕し、不純物を除去して、木片原料2のみを取り出し、当該木片原料2にフェノール樹脂3を含浸させて、フェノール樹脂3を含浸させた木片原料2を圧縮成形して樹脂成形品として木質系産業廃棄物を処理する方法であって、
木片原料2にフェノール樹脂3を含浸させる際に、
不純物を除去した木片原料2を計量して所定量含浸かご4に投入し、
当該含浸かご4をかご毎フェノール樹脂槽10に入れて木片原料2にフェノール樹脂3を含浸させ、その後、含浸かご4を回転させて余剰なフェノール樹脂3を分離し、
その後、余剰なフェノール樹脂3を取り除いた木片原料2を型枠14に投入して圧縮成形することを前記課題の解決手段とした。
The invention of claim 1 collects wood-based industrial waste, crushes the wood-based industrial waste containing the recovered impurities, removes impurities, takes out only the wood piece raw material 2, and adds phenol to the wood piece raw material 2 A method of treating wood-based industrial waste as a resin molded article by impregnating resin 3 and compression-molding wood chip material 2 impregnated with phenolic resin 3;
When impregnating the wood chip material 2 with the phenol resin 3,
Weigh the wooden piece raw material 2 from which impurities have been removed and put it into a predetermined amount of impregnated car 4,
The impregnated basket 4 is put into a phenolic resin tank 10 for each car, and the wood raw material 2 is impregnated with the phenolic resin 3, and then the impregnated car 4 is rotated to separate the excess phenolic resin 3 ,
Thereafter, the wood chip raw material 2 from which the excess phenolic resin 3 was removed was put into the mold 14 and compression-molded .

請求項1の発明によれば、木質系産業廃棄物を処理する方法は、木質系産業廃棄物を回収し、回収された不純物を含む木質系産業廃棄物を破砕し、不純物を除去して、木片原料2のみを取り出し、当該木片原料2にフェノール樹脂3を含浸させて、フェノール樹脂3を含浸させた木片原料2を圧縮成形する、これらの工程によって樹脂成形品を製造する方法である。
そして、木片原料2にフェノール樹脂3を含浸させる際に、不純物を除去した木片原料2を計量して所定量含浸かご4に投入し、含浸かご4をかご毎フェノール樹脂槽10に入れて木片原料2にフェノール樹脂3を含浸させることによって、定量化された木片原料2に効率良く、必要十分な量のフェノール樹脂3を含浸させることができる。
また、含浸かご4を回転させて余剰なフェノール樹脂3を分離することで、木片原料2に対してフェノール樹脂3をムラなく均等に含浸させて、品質の管理をすることができ、かつ余剰なフェノール樹脂を分離することによって、後工程でフェノール樹脂を硬化させる際にも時間を短縮することができる。
さらに、分離した余剰なフェノール樹脂3は、排出口13から元のフェノール樹脂槽10に返して再利用するので、無駄が無く、コストの削減にもつながる。
According to invention of Claim 1, the method of processing a wooden industrial waste collect | recovers wooden industrial waste, crushes the wooden industrial waste containing the collect | recovered impurity, removes an impurity, This is a method of manufacturing a resin molded article by these steps, in which only the wood chip material 2 is taken out, the wood material 2 is impregnated with the phenol resin 3, and the wood material 2 impregnated with the phenol resin 3 is compression-molded.
Then, when impregnating the phenolic resin 3 into the wood piece raw material 2, the wood piece raw material 2 from which impurities are removed is weighed and put into a predetermined amount of the impregnated car 4, and the impregnated car 4 is put into the phenol resin tank 10 for each car and the wood piece raw material By impregnating 2 with the phenol resin 3, the quantified wood chip material 2 can be efficiently impregnated with the necessary and sufficient amount of the phenol resin 3.
Further, by rotating the impregnated basket 4 to separate the excess phenolic resin 3, the wood chip material 2 can be uniformly impregnated with the phenolic resin 3 and the quality can be controlled, and the surplus phenolic resin 3 can be managed. By separating the phenol resin, the time can be shortened even when the phenol resin is cured in a later step.
Furthermore, since the separated excess phenol resin 3 is returned to the original phenol resin tank 10 from the discharge port 13 and reused, there is no waste and the cost is reduced.

樹脂成形品として木質系産業廃棄物を処理する方法を実施する工程は、木片原料破砕工程と、計量工程と、含浸工程と、回転工程と、加圧乾燥工程とからなり、木片原料破砕工程で木質系産業廃棄物を破砕して、不純物を取り除き、次に計量工程で、木片原料2を所定の量に計量して、含浸工程で計量した木片原料2をフェノール樹脂槽10に含浸して、次に回転工程で、余剰なフェノール樹脂3を排出して、最後に加圧乾燥工程で、フェノール樹脂に含浸させた木片原料2を型枠に投入して加圧し、熱風によって乾燥させ、樹脂成形品を製造する。 The process of treating wood-based industrial waste as a resin molded product consists of a wood chip material crushing process, a metering process, an impregnation process, a rotation process, and a pressure drying process. The wooden industrial waste is crushed, impurities are removed, and then the wood chip raw material 2 is weighed to a predetermined amount in the weighing process, and the phenol resin tank 10 is impregnated with the wood chip raw material 2 weighed in the impregnation process. Next, in the rotation process, excess phenol resin 3 is discharged. Finally, in the pressure drying process, the wood chip material 2 impregnated with the phenol resin is put into a mold and pressed, dried by hot air, and resin molded. Manufacturing goods.

前記木片原料破砕工程は、はじめに住宅等の建物を解体した際に排出される廃木材や家具を解体した際に排出される廃木材、建物建築中に排出される木材の端材、おが屑等の木質系産業廃棄物を、破砕機5によって破砕し、一定の大きさの木片原料2に形成する。次に、この木片原料2を風力選別機6に送り、風力によって、木片原料2よりも比重の重いものを選別する。比重の重いものは破砕機5から排出して、木片原料2は木片原料タンク7に送り貯蔵する。貯蔵した木片原料2を簡易除鉄装置8に通してネジや釘などの金属を取り除きつつ、計量機9により計量した所定の分ずつ排出する。
この際、廃材の含水率を調整して、3〜10wt%以下に乾燥させるようにし、木片原料2にフェノール樹脂3が含浸しやすくすることが好ましい。上記範囲に木片原料2の含水率を調整した場合、木片原料2の有する孔隙がスポンジ様の吸収効果を発揮し、また、外から一定の圧力がかかった場合に液を吐き出す弾辱性を保つので好ましい。
The wood chip material crushing process includes waste wood discharged when demolishing a building such as a house, waste wood discharged when demolishing furniture, wood scraps discharged during building construction, sawdust, etc. The wood-based industrial waste is crushed by a crusher 5 and formed into a piece of wood raw material 2 having a certain size. Next, this wood chip raw material 2 is sent to the wind power sorter 6, and a material having a higher specific gravity than the wood chip raw material 2 is sorted by the wind force. A material having a high specific gravity is discharged from the crusher 5, and the wood piece raw material 2 is sent to the wood piece raw material tank 7 for storage. The stored wood chip material 2 is passed through a simple iron removal device 8 and is removed by a predetermined amount measured by a measuring machine 9 while removing metal such as screws and nails.
At this time, it is preferable to adjust the moisture content of the waste material so as to be dried to 3 to 10 wt% or less so that the wood resin 2 is easily impregnated with the phenol resin 3. When the moisture content of the wood chip raw material 2 is adjusted to the above range, the pores of the wood chip raw material 2 exhibit a sponge-like absorption effect, and also keep the humiliating ability to spout liquid when a certain pressure is applied from the outside. Therefore, it is preferable.

前記計量工程は、前記木片原料破砕工程から送られた木片原料2を所定の量に計量する。この時木片原料2は含浸かご4に入れる。   In the measuring step, the wood piece raw material 2 sent from the wood piece raw material crushing step is weighed to a predetermined amount. At this time, the wood chip raw material 2 is put into the impregnated basket 4.

前記含浸工程は、含浸かご4に入れた木片原料2を、含浸かご4のままフェノール樹脂槽10に含浸して、木片原料2にフェノール樹脂3を十分に含浸させる。この時フェノール樹脂槽10は、温調機11によって粘度がコントロールされており、フェノール樹脂3が木片原料2に十分含浸するのに好適な粘度となるようにしている。   In the impregnation step, the wood chip raw material 2 put in the impregnated car 4 is impregnated in the phenol resin tank 10 as the impregnated car 4 and the wood raw material 2 is sufficiently impregnated with the phenol resin 3. At this time, the viscosity of the phenol resin tank 10 is controlled by the temperature controller 11 so that the phenol resin 3 has a viscosity suitable for sufficiently impregnating the wood chip material 2.

フェノール樹脂3には、フェノールとホルムアルデヒドを塩基性触媒の下で加熱反応させて得たレゾール型のものを用いる。
フェノール樹脂は粘度が高いので、例えばメタノール溶剤で希釈して含浸の可能な粘度とし、例えば、樹脂:メタノールを7:3程度の割合で混合するのが好ましい。
As the phenol resin 3, a resol type obtained by heating and reacting phenol and formaldehyde under a basic catalyst is used.
Since the phenol resin has a high viscosity, for example, it is preferable to dilute with a methanol solvent to obtain a viscosity capable of impregnation, and for example, it is preferable to mix resin: methanol at a ratio of about 7: 3.

フェノール樹脂3の含浸としては、後工程の回転工程を経たときに、フェノール樹脂分が木片原料2に対して、例えば、15〜50wt%残存する量とするのが好ましく、含浸割合を15〜50wt%としたのは、50wt%を超えると、フェノール樹脂としての強度は増すが、経済的に高価となり、一方、15wt%以下となると、一応固まっても、成形品としての物理的強度が不足するからである。 The impregnation of the phenol resin 3, when subjected to the rotation process of the post-process, to the phenolic resin component is wood raw material 2, for example, preferably in the amount of residual 1 5-50 wt%, the impregnation ratio 1 5 was set to 50 wt%, when more than 5 0 wt%, the strength of the phenol resin increases, but economically be expensive, whereas, when it comes to 1 5 wt% or less, even once solidified, physical as moldings This is because the strength is insufficient.

前記回転工程は、フェノール樹脂槽10にて含浸させていた木片原料2を含浸かご4のまま回転機12に入れて、回転による遠心力で木片原料2の余剰なフェノール樹脂3を分離する。この時分離された余剰なフェノール樹脂3は排出口から元のフェノール樹脂槽10に戻して再利用する。 In the rotation step, the wood piece raw material 2 impregnated in the phenol resin tank 10 is put into the rotating machine 12 as the impregnated basket 4 and the excess phenol resin 3 of the wood piece raw material 2 is separated by centrifugal force by rotation. The excess phenol resin 3 separated at this time is returned to the original phenol resin tank 10 from the discharge port and reused.

前記加圧乾燥工程は、余剰なフェノール樹脂3を取り除いた木片原料2を型枠14に投入して、熱プレス機で加圧する。次に熱風による加温と通気によって、型枠14に投入した木片原料2を乾燥させる。ここで、型枠に投入した木片原料2とフェノール樹脂3が結合して樹脂成形品を形成していたら、脱型して製品となる。   In the pressure drying step, the wood chip raw material 2 from which the excess phenol resin 3 is removed is put into the mold 14 and pressed by a hot press. Next, the wood chip material 2 put into the mold 14 is dried by heating with hot air and ventilation. Here, if the wood chip raw material 2 and the phenol resin 3 put into the mold form are combined to form a resin molded product, the product is removed from the mold.

本発明に係る木質系産業廃棄物の処理方法によれば、マテリアルリサイクルを前提に、木質系産業廃棄物を破砕して、その木片原料2をフェノール樹脂槽10に含浸させることによって、フェノール樹脂3を木片原料2に十分な量、含浸させることができるとともに、また回転機12によって、余剰なフェノール樹脂3を取り除くことで、フェノール樹脂3を均等に含浸させて、木片原料2を好適なフェノール樹脂残存量にすることができ、フェノール樹脂3が木片原料2にムラ無く含浸した樹脂成形品を製造でき、また安価で高品質な製品を提供できる木質系産業廃棄物のリサイクル方法を提案することができる。 According to the method for treating wood-based industrial waste according to the present invention, on the premise of material recycling, the wood-based industrial waste is crushed and the wood chip raw material 2 is impregnated in the phenol resin tank 10 to thereby obtain the phenol resin 3. Can be impregnated in a sufficient amount in the wood chip raw material 2, and the phenol resin 3 is uniformly impregnated by removing the excess phenol resin 3 by the rotating machine 12, so that the wood chip raw material 2 is suitable for the phenol resin. Proposing a recycling method for wood-based industrial waste that can be made into a residual amount, can produce a resin molded product in which the wood resin 2 is uniformly impregnated with the phenol resin 3 and can provide a low-cost and high-quality product. it can.

以下、この発明の好適な実施の形態について、添付の図1〜図3を参照して説明する。これらの図に示す実施の形態は、樹脂成形品製造装置1で使用するフェノール樹脂3に、フェノール樹脂58−62%、メタノール29−33%、フェノール7−8%、水分0−2%の混合物を用いた例を示すものである。   DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, preferred embodiments of the present invention will be described with reference to FIGS. In the embodiment shown in these figures, the phenol resin 3 used in the resin molded product manufacturing apparatus 1 is a mixture of phenol resin 58-62%, methanol 29-33%, phenol 7-8%, and moisture 0-2%. The example which used is shown.

樹脂成形品製造装置1は、図1に示すように、木片原料2をフェノール樹脂3で結合させるもので、フェノール樹脂槽10に木片原料2を浸漬して、フェノール樹脂3を前記木片原料2に含浸させるのに適当な粘度となるようにコントロールする温調機11を備えることによって、木片原料2に対してフェノール樹脂3を十分に含浸させることができる。そして、この時、温調機11で粘度を適当な状態にして温度管理を行うことで、熱の上昇によるフェノール樹脂3の硬化を防ぐことができる。
このような樹脂成形品製造装置1を使って、図2に示す工程のとおりに 樹脂成形品を製造していくことによって、より品質の良い樹脂成形品としての木質系産業廃棄物の処理方法を実施することができる。
As shown in FIG. 1, the resin molded product manufacturing apparatus 1 combines a wood chip raw material 2 with a phenol resin 3, immerses the wood chip raw material 2 in a phenol resin tank 10, and puts the phenol resin 3 into the wood chip raw material 2. By providing the temperature controller 11 that controls the viscosity to be appropriate for impregnation, the wood resin 2 can be sufficiently impregnated with the phenol resin 3. At this time, the temperature control is performed with the temperature controller 11 in a proper viscosity, whereby the phenol resin 3 can be prevented from being cured due to an increase in heat.
By using such a resin molded product manufacturing apparatus 1 to manufacture a resin molded product according to the process shown in FIG. 2, a method for treating wood-based industrial waste as a higher quality resin molded product is provided. Can be implemented.

ここで、本実施の形態に用いられる熱硬化性樹脂であるフェノール樹脂3は、加熱すると一度は軟化するが、次第に硬くなり、ついには硬化してしまう特性を持っている。図3に示すように、大小のフェノール樹脂の分子が互いに反応して高分子化する。これにより硬化という現象が起きるものである。   Here, the phenol resin 3 which is a thermosetting resin used in the present embodiment softens once when heated, but gradually becomes harder and finally hardens. As shown in FIG. 3, the large and small phenol resin molecules react with each other to be polymerized. This causes a phenomenon of curing.

このような、図1に示す樹脂成形品製造装置1を使用して、図2の工程どおりに樹脂成形品を製造していく。
まず、木質系産業廃棄物を破砕する。木質系産業廃棄物としては、住宅等の建物を解体した際に排出される木質系産業廃棄物や家具を解体した際に排出される木質系産業廃棄物、建物建築中に排出される木材の端材、おが屑等が用いられる。
Using such a resin molded product manufacturing apparatus 1 shown in FIG. 1, a resin molded product is manufactured according to the process of FIG.
First, the wooden industrial waste is crushed. Wood-based industrial waste includes wooden industrial waste discharged when demolishing buildings such as houses, wooden industrial waste discharged when dismantling furniture, and wood discharged during building construction. Mill materials, sawdust, etc. are used.

この木質系産業廃棄物は、木片原料破砕工程で、まず破砕機5に投入する。投入した木質系産業廃棄物を所定の大きさに破砕して、木片原料2とする。そして、木質系産業廃棄物は粉砕にあたって、含水率を3〜10wt%以下に乾燥させるが、これは、3〜10wt%以下とした場合木片原料1の有する孔隙がスポンジ様の吸収効果を発揮すると共に、外から一定の圧力が掛かった場合に液を吐き出す弾辱性を保つからである   This woody industrial waste is first put into the crusher 5 in the wood chip material crushing step. The wood-based industrial waste that has been input is crushed into a predetermined size to obtain a wood chip raw material 2. In the pulverization of the wood-based industrial waste, the moisture content is dried to 3 to 10 wt% or less, and when this is 3 to 10 wt% or less, the pores of the wood chip raw material 1 exhibit a sponge-like absorption effect. At the same time, it keeps the insulting property to spout liquid when a certain pressure is applied from the outside.

次に、木片原料2を風力選別機6へ送り、風力によって、木片原料2よりも比重の重いものを選別する。例えばコンクリート片やガラス片などの比重の重いものは破砕機5から排出し、木片原料2は木片原料タンク7へと送って貯蔵する。   Next, the wood piece raw material 2 is sent to the wind power sorter 6 and a material having a higher specific gravity than the wood piece raw material 2 is sorted by the wind force. For example, heavy concrete such as concrete pieces and glass pieces are discharged from the crusher 5, and the wood piece raw material 2 is sent to the wood piece raw material tank 7 for storage.

いったん貯蔵した木片原料2は簡易除鉄装置8を通ってネジや釘などの金属を取り除く。これにより、雑金属類なども取り除き、前記風力選別器6とともに、木片原料2以外の異物を取り除いていく。   Once stored, the wood chip material 2 passes through a simple iron removing device 8 to remove metal such as screws and nails. Thereby, miscellaneous metals and the like are also removed, and foreign substances other than the wood chip material 2 are removed together with the wind power sorter 6.

次に、木片原料2を計量機9で計量する。この際、計量機9には、木片原料2を受け入れるための含浸かご4を設置する。この含浸かご4は、金属製の直方体となっており、底枠の四隅に四本の柱を取り付けて、それぞれの面には金網を設け、同じく金属製の枠を設けた金網付きの蓋を設けている。この含浸かご4の中に木片原料2を計量機9で所定の量に計量して、所定の量に達すれば、含浸かご4の蓋をしてフェノール樹脂槽10に含浸する。   Next, the wood chip material 2 is weighed by the weighing machine 9. At this time, the weighing machine 9 is provided with an impregnated basket 4 for receiving the wood piece raw material 2. This impregnated basket 4 is a rectangular parallelepiped made of metal. Four pillars are attached to the four corners of the bottom frame, and a metal mesh is provided on each surface, and a lid with a metal mesh provided with a metal frame is also provided. Provided. The wood chip raw material 2 is weighed into a predetermined amount in the impregnated basket 4 by a measuring machine 9 and when the predetermined amount is reached, the impregnated basket 4 is covered and impregnated in the phenol resin tank 10.

次に、含浸かご4に入れた木片原料2を、含浸かご4のままフェノール樹脂槽10に含浸して、木片原料2にフェノール樹脂3を所定時間含浸させる。この時フェノール樹脂槽10は、フェノール樹脂3をメタノール等の溶剤で溶かした溶液であり、このフェノール樹脂3には、フェノールをホルムアルデヒドを塩基性触媒の下で加熱反応させて得たレゾール型のものを用いる。フェノール樹脂3は、粘度が高いので、メタノール溶剤で希釈して含浸の可能な粘度とする為であり、例えば、樹脂:メタノールを7:3程度の割合で混合する。また、温調機11によってフェノール樹脂槽10内の温度を安定させ、粘度をコントロールしており、フェノール樹脂3が木片原料2に十分含浸するのに好適な粘度となるようにしている。   Next, the wooden piece raw material 2 put in the impregnated basket 4 is impregnated in the phenol resin tank 10 as the impregnated basket 4, and the wooden piece raw material 2 is impregnated with the phenol resin 3 for a predetermined time. At this time, the phenol resin tank 10 is a solution obtained by dissolving the phenol resin 3 with a solvent such as methanol, and the phenol resin 3 is a resol type obtained by heating and reacting phenol with formaldehyde under a basic catalyst. Is used. Since the phenol resin 3 has a high viscosity, the phenol resin 3 is diluted with a methanol solvent to obtain a viscosity capable of impregnation. For example, resin: methanol is mixed at a ratio of about 7: 3. Moreover, the temperature inside the phenol resin tank 10 is stabilized by the temperature controller 11 to control the viscosity so that the phenol resin 3 has a viscosity suitable for sufficiently impregnating the wood chip material 2.

ここで、所定時間とは、必要量のフェノール樹脂3が含浸されるに適当な時間をいい、その必要量とは後の回転工程で(メタノール)を蒸散させるとともに、余分なフェノール樹脂3を取り除いた際のフェノール樹脂分が木片原料2に対して15〜50wt%残存する量をいう。含浸割合を15〜50wt%としたのは、50wt%を越えると、フェノール樹脂としての強度は増すが、経済的に高価となり、一方、15wt%以下となると、一応固まっても、製品としての物理的強度が不足するからである。 Here, the predetermined time means an appropriate time for impregnating the required amount of the phenolic resin 3, and the required amount is for evaporating (methanol) and removing the excess phenolic resin 3 in a later rotation process. This refers to the amount of 15-50 wt% of the phenolic resin remaining with respect to the wood chip raw material 2. The impregnation ratio was 1 5-50 wt% may exceeds 5 0 wt%, the strength of the phenol resin increases, but economically be expensive, whereas, if equal to or less than 15 wt%, even once solidified, as a product This is because the physical strength of is insufficient.

このようなフェノール樹脂3は、温度管理をすることで、加熱によるフェノール樹脂の硬化を防いだり、好適な温度に保つことで、木片原料2に対するフェノール樹脂3の含浸量を高めたりすることもできる。   By controlling the temperature of such a phenolic resin 3, curing of the phenolic resin due to heating can be prevented, or by maintaining the temperature at a suitable temperature, the amount of impregnation of the phenolic resin 3 into the wood chip material 2 can be increased. .

次に、所定時間含浸させた木片原料2を、含浸かご4のまま回転機12へ入れて、所定時間回転させ、余剰なフェノール樹脂3を取り除く。この時含浸かご4が金網状の面を有しているので、木片原料2から出る余剰なフェノール樹脂3は金網の隙間から、含浸かご4の外部へ流出する。この流出した余剰なフェノール樹脂3は、回転12内に設けた排出口13から、元のフェノール樹脂槽10へと戻る。これにより、余剰なフェノール樹脂3を再利用することができ、コストの削減にもつながる。 Next, the wood chip raw material 2 impregnated for a predetermined time is put into the rotating machine 12 as the impregnated car 4 and rotated for a predetermined time to remove excess phenolic resin 3. At this time, since the impregnated basket 4 has a wire net-like surface, excess phenol resin 3 coming out of the wood piece raw material 2 flows out of the impregnated car 4 through the gap of the wire net. The excess phenol resin 3 that has flowed out returns to the original phenol resin tank 10 from a discharge port 13 provided in the rotating machine 12 . Thereby, the excess phenol resin 3 can be reused, leading to cost reduction.

また、回転機12によって、余剰なフェノール樹脂3を取り除くことで、フェノール樹脂3を均等に含浸して、かつ木片原料2を好適なフェノール樹脂含浸量にすることができ、フェノール樹脂3が木片原料2にムラ無く結合した高品質な製品を提供することができる。 Moreover, by removing the excess phenol resin 3 by the rotating machine 12, the phenol resin 3 can be uniformly impregnated and the wood chip raw material 2 can be made into a suitable phenol resin impregnation amount. It is possible to provide a high-quality product that is uniformly bonded to 2.

さらに、この回転工程で、余剰なフェノール樹脂3を取り除くとともに、木片原料2に絡みつくフェノール樹脂3の絶対量が少なくなるので、フェノール樹脂3の混合物であるメタノールの蒸散を促すことができる。すると、モノマー(単量体)又はオリゴマー(重合体)状態にあるフェノール樹脂3は、表面が固化し、ベトベト感のないサラサラした状態となるので取扱いが容易となる。 Furthermore, in this rotating step, excess phenol resin 3 is removed, and the absolute amount of phenol resin 3 entangled with the wood chip material 2 is reduced, so that evaporation of methanol, which is a mixture of phenol resin 3, can be promoted. Then, the phenol resin 3 in a monomer (monomer) or oligomer (polymer) state is solidified and becomes a smooth state without a sticky feeling, so that the handling becomes easy.

次に、余剰なフェノール樹脂3を取り除き、またサラサラ状態となった木片原料2を含浸かご4から型枠14へと移して、敷き詰め、型内に充填する。そして熱プレス機15により、以下の工程により加圧する。   Next, the excess phenol resin 3 is removed, and the wooden piece raw material 2 in a smooth state is transferred from the impregnated basket 4 to the mold 14 and spread and filled in the mold. And it pressurizes with the following processes with the hot press machine 15. FIG.

まず、60分程度の間は、加圧下で熱を徐々に上昇させる。すると、フェノールとホルマリンとの間で架橋反応が開始されるが、比較的低温のこの間は、わずかの反応にとどまる。   First, heat is gradually increased under pressure for about 60 minutes. Then, a crosslinking reaction is initiated between phenol and formalin, but only a slight reaction during this period at a relatively low temperature.

次いで、温度が100℃付近に至った時点で、温度上昇を停止させ、約30分の間温度を100℃付近に保つ。すると、先ず、反応中間体としてのフェノール樹脂3に一種の軟化が惹起され、木片原料2に含浸していたフェノール樹脂3が液状化し、加えられた圧力に押されて木片原料2全体に浸透していく。   Next, when the temperature reaches around 100 ° C., the temperature rise is stopped and the temperature is kept around 100 ° C. for about 30 minutes. Then, first, a kind of softening is induced in the phenol resin 3 as a reaction intermediate, and the phenol resin 3 impregnated in the wood chip raw material 2 is liquefied and is pressed by the applied pressure to penetrate the whole wood chip raw material 2. To go.

さらに、100℃付近に温度を維持すると、木片原料2内部に浸透していたフェノール樹脂3にも液状化が及び、圧力で外へと浸みだしが起こり、このとき急激に木片原料2の嵩容積が減少し、あたかもスポンジが縮むかのように全体が圧縮される現象が起こる。即ち、樹脂の軟化が最高に達すると、木片原料2の相互を固定させていた固化樹脂の抗力が失われ、外部圧力によって絡み合いが潰され、木片原料2の組成全体が弾辱体のように縮む現象が惹起される。その結果、木片原料2相互の噛み合いが密となり、緻密な組成構造に変化する。   Furthermore, if the temperature is maintained at around 100 ° C., the phenol resin 3 that has penetrated into the wood chip raw material 2 is also liquefied and oozes out due to pressure. At this time, the bulk volume of the wood chip raw material 2 suddenly increases. The phenomenon that the whole is compressed as if the sponge shrinks occurs. That is, when the softening of the resin reaches the maximum, the drag of the solidified resin that fixes the wood chip raw materials 2 to each other is lost, the entanglement is crushed by the external pressure, and the entire composition of the wood chip raw material 2 is like an insulting body. A shrinking phenomenon is triggered. As a result, the wood chip materials 2 are closely meshed with each other, and change into a dense composition structure.

このとき、100℃付近に約30分程度保つことが重要で、もし、この工程を経ることなく、直線状に温度上昇を続けると、即座に硬化反応が開始され、木片原料2側への樹脂の浸透や、圧縮を伴う組織変化は困難となる。   At this time, it is important to keep the temperature around 100 ° C. for about 30 minutes. If the temperature rises linearly without going through this step, the curing reaction starts immediately, and the resin toward the wood chip raw material 2 side It is difficult to penetrate and to change the structure with compression.

上記、木片原料2の組成の変化がなされた後、加圧力を強めつつ再度加熱を始める。また、この時加熱とともに熱風乾燥機16によって熱風を送り込む。すると、加熱を促進するとともに、乾燥時間を促進させることができる。   After the composition of the wood chip material 2 is changed, heating is started again while increasing the pressure. At this time, hot air is fed by the hot air dryer 16 together with heating. Then, heating can be promoted and drying time can be promoted.

そして、120〜140℃付近でフェノール樹脂3の硬化反応が開始され、分子間に架橋反応が進行し、上記軟化した樹脂間に急速に硬化反応が進む。同時に加圧による押圧力で木片原料2どうしが食い込み、固い組織が形成される。即ち、浸透したフェノール樹脂3が硬化して結合力が生まれると共に、一定強度を備えた木片原料2が互いに交絡し合って食い込み効果を生み、二重の意味で強い結合力が得られる。   And hardening reaction of the phenol resin 3 is started at 120-140 degreeC vicinity, a crosslinking reaction advances between molecules, and hardening reaction advances rapidly between the said softened resin. At the same time, the wood chip raw material 2 bites in by the pressing force by pressurization, and a hard structure is formed. That is, the penetrated phenolic resin 3 is cured to produce a binding force, and the wood chip raw materials 2 having a certain strength are entangled with each other to produce a biting effect, thereby obtaining a strong binding force in a double sense.

その結果、木片原料2の組成が緻密な構造に変換された形態で固化される。従って、一連の工程で木片原料1とフェノール樹脂3とが簡潔な工程で一体成形されると共に、全体が緻密で、物理的強度に優れた樹脂成形品が得られる。   As a result, the composition of the wood chip raw material 2 is solidified in a form converted into a dense structure. Therefore, the wood chip raw material 1 and the phenol resin 3 are integrally formed by a simple process through a series of processes, and a resin molded product having a fine overall structure and excellent physical strength is obtained.

本発明の樹脂成形品製造装置1を示す概略図である。It is the schematic which shows the resin molded product manufacturing apparatus 1 of this invention. 本発明の樹脂成形品の製造工程を示す概略図である。It is the schematic which shows the manufacturing process of the resin molded product of this invention. フェノール樹脂3を加熱して硬化させたことを示す概念図である。It is a conceptual diagram which shows that the phenol resin 3 was heated and hardened.

符号の説明Explanation of symbols

1 樹脂成形品製造装置
2 木片原料
3 フェノール樹脂
4 含浸かご
5 破砕機
6 風力選別機
7 木片原料タンク
8 簡易除鉄機
9 計量機
10 フェノール樹脂槽
11 温調機
12 ディップスピン機
13 排出口
14 型枠
15 熱プレス機
16 熱風乾燥機
DESCRIPTION OF SYMBOLS 1 Resin molded product manufacturing apparatus 2 Wood piece raw material 3 Phenolic resin 4 Impregnation basket 5 Crusher 6 Wind sorter 7 Wood piece raw material tank 8 Simple iron removal machine 9 Weighing machine 10 Phenol resin tank 11 Temperature controller 12 Dip spin machine 13 Outlet 14 Form 15 Hot press 16 Hot air dryer

Claims (5)

木質系産業廃棄物を回収し、回収された不純物を含む木質系産業廃棄物を破砕し、不純物を除去して、木片原料のみを取り出し、当該木片原料にフェノール樹脂を含浸させて、フェノール樹脂を含浸させた木片原料を圧縮成形して樹脂成形品として木質系産業廃棄物を処理する方法であって、
木片原料にフェノール樹脂を含浸させる際に、
不純物を除去した木片原料を計量して所定量含浸かごに投入し、
当該含浸かごをかご毎フェノール樹脂槽に入れて木片原料にフェノール樹脂を含浸させ、その後、含浸かごを回転させて余剰なフェノール樹脂を分離し、
その後、余剰なフェノール樹脂を取り除いた木片原料を型枠に投入して圧縮成形することを特徴とする木質系産業廃棄物の処理方法。
Collecting wood-based industrial waste, crushing wood-based industrial waste containing the recovered impurities, removing impurities, taking out only the wood chip material, impregnating the wood material with the phenol resin, A method of treating wood-based industrial waste as a resin molded product by compression molding the impregnated wood piece raw material,
When impregnating phenolic resin into wood chip material,
Weigh out the wood chip material from which impurities have been removed, and put it into the impregnated basket.
Put the impregnated basket in a phenolic resin tank for each basket and impregnate the wood raw material with phenolic resin, then rotate the impregnated basket to separate excess phenolic resin ,
Thereafter, a wood-based industrial waste treatment method, wherein a wood chip material from which excess phenol resin is removed is put into a mold and compression-molded .
請求項1記載の木質系産業廃棄物の処理方法において、
木片原料の含水率を調整して、3〜10wt%以下に乾燥させることを特徴とする木質系産業廃棄物の処理方法。
In the processing method of the wooden industrial waste of Claim 1,
A method for treating wood-based industrial waste, comprising adjusting a moisture content of a wood chip material and drying to 3 to 10 wt% or less.
請求項1記載の木質系産業廃棄物の処理方法において、
フェノール樹脂槽に温調機を設け、この温調機によってフェノール樹脂の粘度をコントロールすることを特徴とする木質系産業廃棄物の処理方法。
In the processing method of the wooden type industrial waste of Claim 1,
A method for treating wood-based industrial waste, characterized in that a temperature controller is provided in a phenol resin tank, and the viscosity of the phenol resin is controlled by the temperature controller.
請求項1ないし3に記載の木質系産業廃棄物の処理方法において、
フェノール樹脂は、レゾール型フェノール樹脂であることを特徴とする木質系産業廃棄物の処理方法。
In the processing method of the wooden type industrial waste of Claim 1 thru | or 3,
The method for treating wood based industrial waste, wherein the phenolic resin is a resol type phenolic resin.
請求項1記載の木質系産業廃棄物の処理方法において、
前記含浸かごを回転させることによりフェノール樹脂分を木片原料に対して15〜50wt%残存する量としたことを特徴とする木質系産業廃棄物の処理方法。
In the processing method of the wooden type industrial waste of Claim 1,
Method of processing wood industrial waste, characterized in that the phenolic resin component by rotating the impregnated car was the amount remaining 1 5-50 wt% with respect to wood raw material.
JP2004032095A 2004-02-09 2004-02-09 Treatment method for wood-based industrial waste Expired - Fee Related JP4430423B2 (en)

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Cited By (1)

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Publication number Priority date Publication date Assignee Title
KR101315896B1 (en) * 2011-09-09 2013-10-08 경남과학기술대학교 산학협력단 Containing resin for pellet, and its manufacturing method

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GB2436083B (en) * 2006-03-15 2011-04-27 Fergal Martin Conroy A process for recycling timber products
JP5458275B2 (en) * 2009-03-10 2014-04-02 Dic株式会社 Manufacturing method of high-strength particle board
CN113171859A (en) * 2021-05-21 2021-07-27 南京林业大学 Online crushing treatment system and method for waste artificial board continuous hot-pressing line

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101315896B1 (en) * 2011-09-09 2013-10-08 경남과학기술대학교 산학협력단 Containing resin for pellet, and its manufacturing method

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