JPH11147973A - Method of treating thermosetting resin powder waste material and method of supplying the waste material to a furnace - Google Patents
Method of treating thermosetting resin powder waste material and method of supplying the waste material to a furnaceInfo
- Publication number
- JPH11147973A JPH11147973A JP31354697A JP31354697A JPH11147973A JP H11147973 A JPH11147973 A JP H11147973A JP 31354697 A JP31354697 A JP 31354697A JP 31354697 A JP31354697 A JP 31354697A JP H11147973 A JPH11147973 A JP H11147973A
- Authority
- JP
- Japan
- Prior art keywords
- thermosetting resin
- powder
- resin
- resin powder
- thermoplastic resin
- 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.)
- Pending
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
- Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- 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)
Abstract
(57)【要約】
【課題】 樹脂材料として再使用できるように、熱硬化
性樹脂粉体の廃材を固形物にする処理方法を提供すると
共に、炉に吹き込む燃料又は原料代替として、熱硬化性
樹脂粉体の廃材を炉に供給する方法の提供。
【解決手段】 熱硬化性樹脂粉体の廃材を樹脂材料とし
て再使用できるように固形物にする場合には、熱硬化性
樹脂粉体の廃材に熱可塑性樹脂を混合し、加熱して熱可
塑性樹脂を軟化・溶融させながら混練した後、混練物を
固形物にする。又、熱硬化性樹脂粉体の廃材を炉に供給
する場合には、熱硬化性樹脂粉体の廃材に熱可塑性樹脂
を混合し、加熱して熱可塑性樹脂を軟化・溶融させなが
ら混練した後、混練物を粒状化し、この粒状物を気流輸
送して炉に吹き込む。
PROBLEM TO BE SOLVED: To provide a processing method for turning waste material of thermosetting resin powder into a solid so that it can be reused as a resin material, and to use a thermosetting resin as a fuel or raw material substitute to be blown into a furnace Provision of a method for supplying resin powder waste to a furnace. SOLUTION: When a waste material of thermosetting resin powder is made into a solid so that it can be reused as a resin material, a thermoplastic resin is mixed with the waste material of thermosetting resin powder and heated to obtain a thermoplastic resin. After kneading while softening and melting the resin, the kneaded material is turned into a solid. When supplying the waste material of the thermosetting resin powder to the furnace, the thermoplastic resin is mixed with the waste material of the thermosetting resin powder, and the mixture is heated and kneaded while softening and melting the thermoplastic resin. The kneaded material is granulated, and the granulated material is pneumatically transported and blown into a furnace.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、合成樹脂の廃材を
再利用する技術に係り、粉体の状態で発生する熱硬化性
樹脂(熱硬化性樹脂粉体)の廃材を固形物にする方法及
びその熱硬化性樹脂粉体の廃材を燃料又は原料の代替材
として高炉などの炉に供給する方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for recycling synthetic resin waste, and a method for solidifying waste thermosetting resin (thermosetting resin powder) generated in powder form. And a method of supplying a waste material of the thermosetting resin powder to a furnace such as a blast furnace as a substitute for a fuel or a raw material.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】合成樹
脂は成形加工が容易であり、その上、化学的に安定であ
ると言う特性を有するため、その製品が大量に製造され
ている。これらの製品が廃材となった場合、その殆どが
再利用されることなく、埋め立て地などに投棄処分され
ている。しかし、年々、埋め立て地の確保が困難になる
と共に、合成樹脂は微生物によって分解されることもな
く、そのままの状態で残留してしまうので、埋め立て処
分に関わる種々の問題が発生している。このため、合成
樹脂の廃材を資源として再利用するための技術開発が切
望されている。2. Description of the Related Art Synthetic resins are easy to mold and have the property of being chemically stable, so that their products are manufactured in large quantities. When these products become waste, most of them are disposed of in landfills without being reused. However, it becomes difficult to secure landfill sites year by year, and the synthetic resin remains as it is without being decomposed by microorganisms. Therefore, various problems related to landfill disposal have occurred. For this reason, there is a strong need for the development of technology for reusing synthetic resin waste as a resource.
【0003】このような状況において、合成樹脂の廃材
を再利用する方法の一つとして、その廃材を粒状化し、
この粒状物を炭素材の代替材として高炉等へ吹込む再利
用方法が検討されており、これらの技術は特開平9−1
37926号公報などに開示されている。In such a situation, as one of the methods for recycling synthetic resin waste material, the waste material is granulated,
A method of reusing the granular material as a substitute for a carbon material into a blast furnace or the like has been studied.
No. 37926 discloses this.
【0004】ところで、合成樹脂のうち、熱硬化性樹脂
はその性質に基づいて耐熱性や耐薬品性が要求される用
途に供されており、その廃材としては、種々の形態のも
のが排出されるが、その廃材の一つとして、粉体状のも
のがある。[0004] Among the synthetic resins, thermosetting resins are used for applications requiring heat resistance and chemical resistance based on their properties, and various forms of waste materials are discharged. However, one of the waste materials is a powdery material.
【0005】しかし、この粉体は、熱可塑性樹脂の廃材
のように、溶融・成形が可能なものではないので、樹脂
材料としての再生利用は困難である。又、この粉体は非
常に細かい粉末であるため、取り扱いにくく、この点も
再利用の用途が開拓されない一因になっている。[0005] However, this powder cannot be melted and molded as in the case of waste thermoplastic resin, so it is difficult to recycle it as a resin material. Further, since this powder is a very fine powder, it is difficult to handle, and this is one of the reasons that the reuse application is not developed.
【0006】さらに、熱硬化性樹脂の廃材のうち、粉体
以外のものは、破砕して粒状化すれば、上記のような高
炉等への吹込みによる再利用も可能であるが、粉体のも
のは微粉末であるため、そのままの状態で高炉やスクラ
ップ溶解炉などの炉へ吹き込むと、操業上のトラブルが
発生する。Further, among waste materials of thermosetting resin, those other than powder can be reused by blowing them into a blast furnace as described above if they are crushed and granulated. Since it is a fine powder, if it is blown into a furnace such as a blast furnace or a scrap melting furnace as it is, operational problems will occur.
【0007】即ち、本発明者等の研究結果によれば、高
炉等へ合成樹脂の廃材を吹き込む場合、合成樹脂の粉体
が細かすぎると、貯槽内で棚吊りが発生して合成樹脂の
粉体が落下しなくなって貯留槽からの切り出しができな
くなったり、或いは、貯槽と高炉等の吹き込み部の間に
設けられている気流輸送配管のバルブや曲管部などに粉
体が付着して詰まりが発生したりする。このため、しば
しば、合成樹脂の粉体の吹き込みが中断され、吹き込み
材の供給が円滑に行われない。That is, according to the research results of the present inventors, when blowing synthetic resin waste into a blast furnace or the like, if the synthetic resin powder is too fine, shelves are suspended in the storage tank and the synthetic resin powder is generated. The body does not fall and cannot be cut out from the storage tank, or powder adheres and clogs the valve or curved pipe part of the airflow pipe installed between the storage tank and the blowing part of the blast furnace etc. Or occur. Therefore, the blowing of the synthetic resin powder is often interrupted, and the supply of the blowing material is not performed smoothly.
【0008】本発明は、熱硬化性樹脂粉体の廃材が有す
る上記の問題を解決するためになされたものであり、樹
脂材料として再使用できるように、熱硬化性樹脂粉体の
廃材を固化させる処理方法を提供すると共に、炉に吹き
込む燃料又は原料の代替として、熱硬化性樹脂粉体を炉
に供給する方法を提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems of waste thermosetting resin powder, and solidifies waste thermosetting resin powder so that it can be reused as a resin material. It is an object of the present invention to provide a method of supplying a thermosetting resin powder to a furnace as a substitute for fuel or a raw material to be blown into the furnace, while providing a processing method for causing the furnace to blow.
【0009】[0009]
【課題を解決するための手段】上記の目的を達成するた
めに、第一の発明に係る熱硬化性樹脂の処理方法におい
ては、熱硬化性樹脂粉体の廃材に熱可塑性樹脂を混合
し、加熱して熱可塑性樹脂を軟化・溶融させながら混練
した後、混練物を固形物にする。Means for Solving the Problems In order to achieve the above object, in the method for treating a thermosetting resin according to the first invention, a thermoplastic resin is mixed with waste material of the thermosetting resin powder, After kneading while heating to soften and melt the thermoplastic resin, the kneaded material is turned into a solid.
【0010】第二の発明に係る熱硬化性樹脂粉体の廃材
を炉に供給する方法においては、熱硬化性樹脂粉体の廃
材に熱可塑性樹脂を混合し、加熱して熱可塑性樹脂を軟
化・溶融させながら混練した後、混練物を粒状化し、こ
の粒状物を気流輸送して炉に吹き込む。In the method of supplying waste thermosetting resin powder to a furnace according to the second invention, the thermoplastic resin is mixed with the waste thermosetting resin powder and heated to soften the thermoplastic resin. After kneading while melting, the kneaded material is granulated, and the granulated material is pneumatically transported and blown into a furnace.
【0011】前述のように、熱硬化性樹脂粉体の廃材は
樹脂材料としての再生利用ができず、その上、微粉末で
あるため、他の用途への再利用が妨げられている。本発
明者は、この問題に対処し、熱硬化性樹脂の粉体を固め
て固形物にする検討を行った。しかし、熱硬化性樹脂の
廃材は加熱しても溶融しないので、熱可塑性樹脂の廃材
と同様の処理をして再生利用することはできない。As described above, the waste material of the thermosetting resin powder cannot be recycled as a resin material, and since it is a fine powder, it is prevented from being reused for other uses. The present inventor has dealt with this problem and has studied the solidification of thermosetting resin powder by solidifying the powder. However, since the waste material of the thermosetting resin does not melt even when heated, it cannot be recycled by performing the same treatment as the waste material of the thermoplastic resin.
【0012】そこで、本発明においては、熱硬化性樹脂
の粉体に熱可塑性樹脂を混合して加熱し、熱可塑性樹脂
を軟化・溶融させて、溶融状態又は半溶融状態の熱可塑
性樹脂と熱硬化性樹脂の粉体を混練する処理を行った
後、冷却して固化させ、固形物を得る。この際、熱硬化
性樹脂の粉体は溶融しないが、溶融した熱可塑性樹脂が
バインダーの役割をするので、粉体が固まる。Therefore, in the present invention, a thermoplastic resin is mixed with a thermosetting resin powder and heated to soften and melt the thermoplastic resin, and the thermoplastic resin in a molten state or a semi-molten state is mixed with the thermoplastic resin. After a process of kneading the curable resin powder, the mixture is cooled and solidified to obtain a solid. At this time, the powder of the thermosetting resin does not melt, but the melted thermoplastic resin acts as a binder, so that the powder hardens.
【0013】そして、熱可塑性樹脂の混合割合をある限
度以上にして処理すれば、再び溶融して成形することが
可能になる。このため、比較的強度が要求されない樹脂
製品であれば、上記粉体に熱可塑性樹脂を混合した処理
物をその成形原料として使用することができる。[0013] If the treatment is carried out with the mixing ratio of the thermoplastic resin being more than a certain limit, it becomes possible to melt and mold again. For this reason, if the resin product does not require relatively high strength, a processed product obtained by mixing the above powder with a thermoplastic resin can be used as a raw material for molding.
【0014】又、前述のように、熱硬化性樹脂粉体の廃
材を燃料又は原料代替の吹き込み材として使用すると、
吹き込み時にトラブルが発生するが、本発明者らの試験
結果によれば、吹き込み材がある程度以上の嵩密度を有
する粒状物であれば、トラブルは発生しないことが確認
されている。このため、本発明においては、まず、熱硬
化性樹脂粉体の廃材に熱可塑性樹脂を混合し、上記のよ
うにして加熱・混練した後、混練物を粒状化し、この粒
状物を気流輸送して炉に吹き込む。なお、混練物の粒状
化に際しては、混練物を冷却して固化させた後に破砕し
て粒状にしてもよく、或いは混練物を裁断した後に冷却
して固化させて粒状にしてもよい。Further, as described above, when waste material of thermosetting resin powder is used as a blowing material for fuel or raw material,
Although a trouble occurs at the time of blowing, according to the test results of the present inventors, it is confirmed that no trouble occurs if the blowing material is a granular material having a bulk density of a certain level or more. Therefore, in the present invention, first, a thermoplastic resin is mixed with the waste material of the thermosetting resin powder, and after heating and kneading as described above, the kneaded material is granulated, and the granular material is pneumatically transported. Into the furnace. When granulating the kneaded material, the kneaded material may be cooled and solidified and then crushed to be granulated, or the kneaded material may be cut and cooled and solidified to be granulated.
【0015】本発明を適用できる熱硬化性樹脂の粉体と
しては、不飽和ポリエステル樹脂、エポキシ樹脂、ウレ
タン樹脂、フェノール樹脂、ユリアメラミン樹脂、アル
キッドメラミン樹脂、アクリルメラミン樹脂などの粉
体、又は、それらの樹脂の混合物からなる粉体、又は、
上記樹脂にガラスなどのフィラー材が混合された粉体な
どが挙げられる。The thermosetting resin powder to which the present invention can be applied includes powders of unsaturated polyester resin, epoxy resin, urethane resin, phenol resin, urea melamine resin, alkyd melamine resin, acrylic melamine resin, etc. Powder consisting of a mixture of those resins, or
A powder obtained by mixing a filler material such as glass with the above resin may be used.
【0016】又、熱可塑性樹脂としては、ポリエチレ
ン、ポリプロピレン、ポリブテン、ポリスチレン、ポリ
エステル、又は、これらの共重合体等を用いることがで
きる。As the thermoplastic resin, polyethylene, polypropylene, polybutene, polystyrene, polyester, or a copolymer thereof can be used.
【0017】[0017]
【発明の実施の形態】図1は本発明により熱硬化性樹脂
粉体の廃材を固形物にする処理方法の一例を示す図であ
る。混合工程では、熱硬化性樹脂粉体の廃材に所定の大
きさ以下に破砕又は裁断した熱可塑性樹脂を所定の割合
で混合する。加熱・混練工程では、この混合物を加熱し
て熱可塑性樹脂を溶融し、熱硬化性樹脂の粉体を熱可塑
性樹脂の溶融物で練った混練物にする。冷却工程では、
混練物を水噴霧あるいは水中投入などの操作によって冷
却し、固化させる。そして、必要に応じて、破砕工程を
設け、固形物を所定の粒径になるように破砕し、熱硬化
性樹脂を主とする粒状物にする。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a view showing an example of a method for processing waste materials of thermosetting resin powder into solids according to the present invention. In the mixing step, a thermoplastic resin crushed or cut to a predetermined size or less is mixed with a waste material of the thermosetting resin powder at a predetermined ratio. In the heating / kneading step, the mixture is heated to melt the thermoplastic resin, and the thermosetting resin powder is kneaded with the thermoplastic resin melt. In the cooling process,
The kneaded material is cooled and solidified by an operation such as water spraying or water injection. Then, if necessary, a crushing step is provided, and the solid is crushed so as to have a predetermined particle size to obtain a granular material mainly composed of a thermosetting resin.
【0018】上記のようにして熱硬化性樹脂粉体の廃材
を粒状物にする場合には、混合する熱可塑性樹脂を5w
t%(熱硬化性樹脂:熱可塑性樹脂=95:5)以上に
する必要がある。熱可塑性樹脂が5%未満であると、加
熱・混練時にバインダーの役目をする溶融物が不足し、
脆い固形物が生成し、後のハンドリングの際に崩壊して
粉状物が発生する。なお、上記の処理物を樹脂材料とし
て再利用しようとする場合には、成形性をよくするため
に、熱可塑性樹脂の混合率を30wt%(熱硬化性樹
脂:熱可塑性樹脂=70:30)程度以上にする必要が
ある。When the waste material of the thermosetting resin powder is made into a granular material as described above, the thermoplastic resin to be mixed is 5 watts.
t% (thermosetting resin: thermoplastic resin = 95: 5) or more. When the content of the thermoplastic resin is less than 5%, a melt serving as a binder during heating and kneading is insufficient,
A brittle solid is produced which collapses during later handling to produce a powder. When the treated material is to be reused as a resin material, the mixing ratio of the thermoplastic resin is set to 30 wt% (thermosetting resin: thermoplastic resin = 70: 30) in order to improve moldability. It needs to be more than degree.
【0019】又、加熱・混練時の温度は、熱可塑性樹脂
の軟化点、好ましくは融点以上にする。しかし、必要以
上に温度を上げると、樹脂の分解が起こるので、加熱温
度の上限は350℃程度にすべきである。従って、加熱
・混練処理は、樹脂の種類によっても異なるが、通常、
160℃〜350℃、好ましくは、180℃〜300℃
程度の温度範囲で行う。The temperature at the time of heating and kneading is higher than the softening point, preferably the melting point, of the thermoplastic resin. However, if the temperature is raised more than necessary, the decomposition of the resin occurs. Therefore, the upper limit of the heating temperature should be about 350 ° C. Therefore, the heating and kneading process differs depending on the type of resin, but usually,
160 ° C to 350 ° C, preferably 180 ° C to 300 ° C
Perform in a temperature range of about
【0020】なお、熱硬化性樹脂粉体の廃材と熱可塑性
樹脂の加熱・混練処理に際し、木粉やガラス粉或いは熱
可塑性樹脂と同程度の融点を有する物質を混合してもよ
い。When heating and kneading the waste material of the thermosetting resin powder and the thermoplastic resin, wood powder, glass powder, or a substance having a melting point similar to that of the thermoplastic resin may be mixed.
【0021】図2は図1における加熱・混練工程で押出
機を使用した場合の処理方法の一例を示す図である。こ
押出機を使用する方法においては、まず、熱可塑性樹脂
材を破砕機11で5mm以下程度の大きさに破砕してお
く。次いで、破砕した熱可塑性樹脂と熱硬化性樹脂の粉
体をそれぞれ所定量ずつ秤量し、この二つの処理材を同
時に押出成形機12のホッパーへ装入する。二つの処理
材は押出成形機12のホッパーからシリンダーに入り、
その供給部でスクリューによってよく掻き混ぜられ、加
熱・溶融部へ送られる。加熱・溶融部では、熱可塑性樹
脂が溶融し、その溶融物と熱硬化性樹脂粉体が混練され
る。混練された処理材は、シリンダーの端部に取り付け
られているダイから押し出され、線状体に成形されて排
出される。FIG. 2 is a diagram showing an example of a processing method when an extruder is used in the heating / kneading step in FIG. In the method using this extruder, first, a thermoplastic resin material is crushed by a crusher 11 to a size of about 5 mm or less. Next, the crushed thermoplastic resin and thermosetting resin powder are each weighed by a predetermined amount, and the two treatment materials are simultaneously charged into the hopper of the extruder 12. The two treated materials enter the cylinder from the hopper of the extruder 12 and
In the supply section, the mixture is stirred well by a screw and sent to the heating / melting section. In the heating / melting section, the thermoplastic resin is melted, and the melt and the thermosetting resin powder are kneaded. The kneaded processing material is extruded from a die attached to the end of the cylinder, formed into a linear body, and discharged.
【0022】成形物は水噴霧などの冷却手段を備えた冷
却装置13で冷却され、固形物となる。固形物は破砕機
14で所定の粒径になるように破砕される。この粒状物
は、必要に応じて篩分けされ、貯留ホッパー20へ送ら
れる。The molded product is cooled by a cooling device 13 provided with a cooling means such as water spray and becomes a solid. The solid is crushed by the crusher 14 so as to have a predetermined particle size. The granules are sieved as required and sent to the storage hopper 20.
【0023】押出成形機を使用した場合には、加熱・混
練工程における混練が十分に行われると言う利点がある
外に、混練物を線状体などの形状に成形することができ
るので、固形物の破砕が容易になる。又、混練物を適宜
の太さの径に成形することができるので、所望の粒径を
有する粒状物が効率よく得られる。When an extruder is used, in addition to the advantage that the kneading in the heating / kneading step is sufficiently performed, the kneaded material can be formed into a shape such as a linear body. The crushing of objects becomes easier. In addition, since the kneaded material can be formed into an appropriate diameter, a granular material having a desired particle size can be obtained efficiently.
【0024】なお、本発明で使用できる押出成形機は合
成樹脂の押出成形や溶融紡糸などを行う際に用いられる
ものであって、スクリューが一軸ものでも、二軸のもの
でもよい。又、処理材のフィード方式は、上部から装入
する通常の方式であってもよいが、処理材の性状によっ
ては、圧縮しながら強制的に装入するフィード方式に
し、処理能力を向上させた方がよい。The extruder used in the present invention is used for extruding or melt-spinning a synthetic resin, and may have a single screw or a twin screw. In addition, the feed method of the processing material may be a normal method of loading from above, but depending on the properties of the processing material, a feed method of forcibly loading while compressing is used to improve the processing capacity. Better.
【0025】図3は熱硬化性樹脂粉体の廃材を炭素材の
代替材として高炉へ供給する方法の一例を示す図であ
る。熱硬化性樹脂粉体の廃材及び熱可塑性樹脂のそれぞ
れ所定量を、例えば、図2のように構成された粒状化装
置10へ送り、上記粉体を粒状化する。そして、この粒
状物を貯留ホッパー20へ送って一時貯留した後、順次
抜き出して吹き込みホッパー21へ導入し、キャリアガ
スによって気流輸送して高炉30へ供給する。この際、
樹脂の粒状物は気送管22を流れ、高炉30の羽口に設
けられている送風用のブローパイプ31に挿入された吹
き込みノズルからブローパイプ31中へ導入され、炉内
へ吹き込まれる。炉内へ吹き込まれた樹脂の粒状物は分
解して一酸化炭素及び水素ガスを発生し、鉄鉱石の還元
剤として作用すると共に、燃焼して燃焼熱を発生し、高
炉内の装入物を加熱、溶融し、炭素材の代替として有効
に利用される。FIG. 3 is a diagram showing an example of a method of supplying a waste material of thermosetting resin powder to a blast furnace as a substitute for a carbon material. A predetermined amount of each of the waste material of the thermosetting resin powder and the thermoplastic resin is sent to, for example, a granulating device 10 configured as shown in FIG. 2 to granulate the powder. Then, the particulate matter is sent to the storage hopper 20 to be temporarily stored, then sequentially extracted, introduced into the blowing hopper 21, and transported by a carrier gas in a gas stream to the blast furnace 30. On this occasion,
The resin particles flow through the air supply pipe 22, are introduced into the blow pipe 31 from a blow nozzle inserted into a blow pipe 31 for blowing provided at the tuyere of the blast furnace 30, and are blown into the furnace. The resin particles blown into the furnace decompose to generate carbon monoxide and hydrogen gas, act as a reducing agent for iron ore, and burn to generate heat of combustion, thereby reducing the charge in the blast furnace. Heats and melts and is effectively used as a substitute for carbon materials.
【0026】[0026]
【実施例】(粒状化試験)表1に示す6種類の熱硬化性
樹脂の粉体と熱可塑性樹脂を押出成形機を使用して混練
し、約12mmの太さの線状体に成形した。次いで、こ
れを冷却して固化させた後、破砕して粒状物にする処理
を行った。この粒状化処理においては、図2の装置と同
様の構成による装置を使用し、処理条件は表1に示すご
とくにした。なお、表1の押出成形機の欄には使用した
押出成形機のスクリューの数とその径を記載した。又、
熱可塑性樹脂の欄のPE、PP、PSは、それぞれポリ
エチレン、ポリプロピレン、ポリスチレンを示す。そし
て、評価欄の○は成形性がよく、かつ粒状化するための
破砕処理に問題がなかった場合、×は混練が不十分で成
形することがでず、粉体のままのものが存在していた場
合を示す。EXAMPLES (Granulation test) Six kinds of thermosetting resin powders and thermoplastic resin shown in Table 1 were kneaded using an extruder and formed into a linear body having a thickness of about 12 mm. . Next, after cooling and solidifying, it was crushed into particles. In this granulation process, an apparatus having the same configuration as the apparatus in FIG. 2 was used, and the processing conditions were as shown in Table 1. In the column of extruder in Table 1, the number and diameter of the screws of the extruder used were described. or,
PE, PP and PS in the column of thermoplastic resin indicate polyethylene, polypropylene and polystyrene, respectively. In the evaluation column, ○ indicates good moldability, and if there was no problem in the crushing treatment for granulation, x indicates insufficient kneading and molding could not be performed, and there was a powder as it was. Indicates the case where
【0027】表1によれば、熱可塑性樹脂の混合割合と
粒状化処理の評価との関係をみると、熱可塑性樹脂の混
合割合が5wt%(No.1)以上の場合には良好の結果
が得られたが、その混合割合が2wt%(No.20とNo.2
1)の場合には成形不良であった。この結果から、この
粒状物を燃料や原料の代替材として使用するために成形
して粒状化する場合には、熱可塑性樹脂の混合割合を5
wt%以上にする必要がある。According to Table 1, the relationship between the mixing ratio of the thermoplastic resin and the evaluation of the granulation treatment shows that when the mixing ratio of the thermoplastic resin is 5 wt% (No. 1) or more, good results are obtained. Was obtained, but the mixing ratio was 2 wt% (No. 20 and No. 2).
In the case of 1), molding was defective. From this result, when this granular material is molded and granulated for use as a substitute for fuel or raw material, the mixing ratio of the thermoplastic resin is set to 5%.
It must be at least wt%.
【0028】そして、処理温度については、表1に記載
した温度範囲内では、温度が原因となる不都合な問題は
起こらなかった。As for the treatment temperature, no inconvenience caused by the temperature occurred within the temperature range shown in Table 1.
【0029】[0029]
【表1】 [Table 1]
【0030】(高炉への吹込み試験)アルキッド樹脂の
粉体とポリエチレン樹脂を95:5の割合で混合し、こ
れを図2の装置と同様の構成による装置によって、加熱
・混練、成形、冷却、破砕の各処理を行い、6mm程度
の粒状物にした。次いで、この粒状物を貯留ホッパーに
一時貯留した後、吹き込みホッパーへ送り、次に記す条
件で気流輸送し、吹き込みノズルからブローパイプを経
由して高炉の羽口へ吹き込んだ。(Blow furnace injection test) Alkyd resin powder and polyethylene resin were mixed at a ratio of 95: 5, and the mixture was heated, kneaded, molded, and cooled by an apparatus having the same configuration as the apparatus shown in FIG. , And crushing to obtain a granular material of about 6 mm. Next, the particulate matter was temporarily stored in a storage hopper, sent to a blowing hopper, air-transported under the following conditions, and blown from a blowing nozzle into a tuyere of a blast furnace via a blow pipe.
【0031】吹き込み条件 キャリアガス:空気 合成樹脂粒状物の吹き込み量:60 kg/ min キャリアガスの流量:1200 Nm3 /hr なお、高炉の操業条件は下記の通りで行い、同時に他の
羽口から微粉炭の吹き込みも行った。Blowing conditions Carrier gas: air Blowing amount of synthetic resin granules: 60 kg / min Carrier gas flow rate: 1200 Nm 3 / hr The operating conditions of the blast furnace were as follows, and simultaneously from other tuyeres. Pulverized coal was also injected.
【0032】高炉の操業条件 出銑量 :9000 t/d コークス比:447 kg/t-銑鉄 送風量 :7260 Nm3 /min 酸素富化率:4 vol% 送風温度 :1200℃ 上記の条件による樹脂粒状物の吹き込みを8時間実施し
たが、貯留ホッパーや吹込みホッパーに棚吊りが起こっ
たり、気送管系統が詰まったりするようなトラブル発生
せず、順調な操業を継続することができた。Operating conditions of the blast furnace: Tapping rate: 9000 t / d Coke ratio: 447 kg / t-pig Iron Blowing rate: 7260 Nm 3 / min Oxygen enrichment rate: 4 vol% Blasting temperature: 1200 ° C. Resin under the above conditions Although the blowing of the granular material was performed for 8 hours, no troubles such as hanging of the storage hopper or the blowing hopper on the shelf or clogging of the pneumatic pipe system occurred, and the smooth operation could be continued.
【0033】[0033]
【発明の効果】本発明に係る熱硬化性樹脂粉体の廃材の
処理方法によれば、熱硬化性樹脂粉体の廃材に混合した
熱可塑性樹脂が溶融してバインダーの役割をなし、熱硬
化性樹脂の粉体が固められるので、熱硬化性樹脂粉体の
廃材を再利用可能な固形物にすることができる。According to the method for treating waste thermosetting resin powder according to the present invention, the thermoplastic resin mixed with the waste thermosetting resin powder melts to serve as a binder, and serves as a binder. Since the powder of the thermosetting resin is solidified, the waste material of the thermosetting resin powder can be made into a reusable solid.
【0034】本発明に係る熱硬化性樹脂粉体の廃材を炉
に供給する方法によれば、熱硬化性樹脂粉体の廃材に熱
可塑性樹脂を混合し、加熱・混練、固化、破砕して粒状
化し、この粒状物を気流輸送して吹き込むので、気送管
系統などが詰まったりするようなトラブル発生せず、吹
込み材の供給が円滑に行われる。According to the method of supplying waste thermosetting resin powder to a furnace according to the present invention, a thermoplastic resin is mixed with the waste thermosetting resin powder, and the mixture is heated, kneaded, solidified, and crushed. Since the particles are granulated, and the particles are pneumatically transported and blown, troubles such as clogging of a pneumatic pipe system or the like do not occur and the supply of the blowing material is performed smoothly.
【図1】本発明により熱硬化性樹脂粉体の廃材を固形物
にする処理方法の一例を示す図である。FIG. 1 is a view showing an example of a processing method for converting waste material of thermosetting resin powder into a solid material according to the present invention.
【図2】図1における加熱・混練工程で押出機を使用し
た場合の処理方法の一例を示す図である。FIG. 2 is a diagram showing an example of a processing method when an extruder is used in the heating / kneading step in FIG.
【図3】熱硬化性樹脂粉体の廃材を炭素材の代替材とし
て高炉へ供給する方法の一例を示す図である。FIG. 3 is a diagram showing an example of a method of supplying waste material of thermosetting resin powder to a blast furnace as a substitute for carbon material.
10 粒状化装置 11 破砕機 12 押出成形機 13 冷却装置 14 破砕機 20 貯留ホッパー 21 吹込みホッパー 30 高炉 31 ブローパイプ DESCRIPTION OF SYMBOLS 10 Granulation apparatus 11 Crusher 12 Extruder 13 Cooling apparatus 14 Crusher 20 Storage hopper 21 Blow hopper 30 Blast furnace 31 Blow pipe
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI // B29K 101:10 101:12 105:26 (72)発明者 浅川 幸彦 東京都千代田区丸の内一丁目1番2号日本 鋼管株式会社内──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI // B29K 101: 10 101: 12 105: 26 (72) Inventor Yukihiko Asakawa 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Japan Steel Pipe Inside the corporation
Claims (2)
を混合し、加熱して熱可塑性樹脂を軟化・溶融させなが
ら混練した後、混練物を固形物にすることを特徴とする
熱硬化性樹脂粉体の廃材の処理方法。1. A thermosetting method comprising mixing a thermoplastic resin with waste thermosetting resin powder, kneading the mixture while heating to soften and melt the thermoplastic resin, and then converting the kneaded material into a solid material. A method for treating curable resin powder waste.
を混合し、加熱して熱可塑性樹脂を軟化・溶融させなが
ら混練した後、混練物を粒状化し、この粒状物を気流輸
送して炉に吹き込むことを特徴とする熱硬化性樹脂粉体
の廃材を炉に供給する方法。2. A thermoplastic resin is mixed with waste material of thermosetting resin powder, and the mixture is heated and kneaded while softening and melting the thermoplastic resin. The kneaded material is granulated, and the granulated material is pneumatically transported. And supplying the waste material of the thermosetting resin powder to the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31354697A JPH11147973A (en) | 1997-11-14 | 1997-11-14 | Method of treating thermosetting resin powder waste material and method of supplying the waste material to a furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP31354697A JPH11147973A (en) | 1997-11-14 | 1997-11-14 | Method of treating thermosetting resin powder waste material and method of supplying the waste material to a furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11147973A true JPH11147973A (en) | 1999-06-02 |
Family
ID=18042633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP31354697A Pending JPH11147973A (en) | 1997-11-14 | 1997-11-14 | Method of treating thermosetting resin powder waste material and method of supplying the waste material to a furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11147973A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001232637A (en) * | 1999-12-13 | 2001-08-28 | Nippon Steel Corp | Method and apparatus for molding granulated waste plastic for chemical raw materials |
| JP2002038172A (en) * | 2000-07-24 | 2002-02-06 | Hideyo Kano | Waste plastic fuel |
| JP2002212326A (en) * | 2001-01-15 | 2002-07-31 | Ig Tech Res Inc | Recyclable rigid foamed resin |
| JP2002293974A (en) * | 2001-03-28 | 2002-10-09 | Ig Tech Res Inc | Method for producing recyclable hard foamed resin material |
| JP2006103336A (en) * | 1999-12-13 | 2006-04-20 | Nippon Steel Corp | Molding method of waste plastic granulation for chemical raw materials |
| WO2010030038A1 (en) * | 2008-09-12 | 2010-03-18 | Jfeスチール株式会社 | Method for producing pulverized waste plastic and solid fuel or mineral reduction material |
| JP2011056789A (en) * | 2009-09-10 | 2011-03-24 | Jfe Steel Corp | Method for manufacturing waste plastics pulverized powder, and ore reducing agent or solid fuel |
| JP2014030824A (en) * | 2005-08-29 | 2014-02-20 | Jfe Steel Corp | Mixed plastic powder and manufacturing method of the same |
-
1997
- 1997-11-14 JP JP31354697A patent/JPH11147973A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001232637A (en) * | 1999-12-13 | 2001-08-28 | Nippon Steel Corp | Method and apparatus for molding granulated waste plastic for chemical raw materials |
| JP2006103336A (en) * | 1999-12-13 | 2006-04-20 | Nippon Steel Corp | Molding method of waste plastic granulation for chemical raw materials |
| JP2002038172A (en) * | 2000-07-24 | 2002-02-06 | Hideyo Kano | Waste plastic fuel |
| JP2002212326A (en) * | 2001-01-15 | 2002-07-31 | Ig Tech Res Inc | Recyclable rigid foamed resin |
| JP2002293974A (en) * | 2001-03-28 | 2002-10-09 | Ig Tech Res Inc | Method for producing recyclable hard foamed resin material |
| JP2014030824A (en) * | 2005-08-29 | 2014-02-20 | Jfe Steel Corp | Mixed plastic powder and manufacturing method of the same |
| WO2010030038A1 (en) * | 2008-09-12 | 2010-03-18 | Jfeスチール株式会社 | Method for producing pulverized waste plastic and solid fuel or mineral reduction material |
| JP2010089500A (en) * | 2008-09-12 | 2010-04-22 | Jfe Steel Corp | Method for producing pulverized waste plastic and solid fuel or mineral reduction material |
| KR101134809B1 (en) * | 2008-09-12 | 2012-04-13 | 제이에프이 스틸 가부시키가이샤 | Method for producing pulverized waste plastic |
| JP2011056789A (en) * | 2009-09-10 | 2011-03-24 | Jfe Steel Corp | Method for manufacturing waste plastics pulverized powder, and ore reducing agent or solid fuel |
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