JP6739047B2 - Bamboo powder composite resin manufacturing method, bamboo powder resin mixed melt manufacturing method, bamboo powder resin mixed melt, and bamboo powder composite resin - Google Patents

Bamboo powder composite resin manufacturing method, bamboo powder resin mixed melt manufacturing method, bamboo powder resin mixed melt, and bamboo powder composite resin Download PDF

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JP6739047B2
JP6739047B2 JP2018094198A JP2018094198A JP6739047B2 JP 6739047 B2 JP6739047 B2 JP 6739047B2 JP 2018094198 A JP2018094198 A JP 2018094198A JP 2018094198 A JP2018094198 A JP 2018094198A JP 6739047 B2 JP6739047 B2 JP 6739047B2
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孝志 佐野
孝志 佐野
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本発明は竹粉複合樹脂の製造方法、竹粉樹脂混合溶融体の製造方法、竹粉樹脂混合溶融体及び竹粉複合樹脂に関する。詳しくは、多孔質微竹粉を高温・高圧溶融により樹脂と複合させた竹粉複合樹脂の製造方法、竹粉樹脂混合溶融体の製造方法、竹粉樹脂混合溶融体及び竹粉複合樹脂に関する。 The present invention relates to a method for producing a bamboo powder composite resin, a method for producing a bamboo powder resin mixed melt, a bamboo powder resin mixed melt, and a bamboo powder composite resin. More specifically, the present invention relates to a method for producing a bamboo powder composite resin, a method for producing a bamboo powder resin mixed melt, a bamboo powder resin mixed melt, and a bamboo powder composite resin, in which porous fine bamboo powder is combined with a resin by high temperature/high pressure melting.

樹脂に木質系バイオマスを複合したセルロース系複合樹脂には、通称ウッドプラスチックと言われるウッドデッキ等がある。これは安価な製造方法を目標に、原料にリサイクルウッドとリサイクルプラスチックを使用したものである。木粉をプラスチックと複合するには、プラスチック側からみて、木粉は細かくかつ水分を含まない、例えば平均粒度数10μm以下、含水率5%以下が良いとされてきた。すなわち、粒度が大きい、水分が多い場合は木紛がプラスチックの中にうまく混入しない。その結果、木粉ではせいぜい30〜50%までしか含有されなかった。さらに、木粉を30〜50%複合した成形体を得るには、押し出し成形かプレス成形で成形される簡単な形状の製品に限られていた。木粉複合樹脂は木のように見える良さと樹脂の良さを兼ねる利点があるが、逆にそのどちらでもない弱点もある。このように、品質維持や生産性に問題を抱えている。
最近ではセルロースナノファイバー(CNF)にして、高強度・高弾性・低熱膨張性に注目した技術が大きく取り上げられているが、まだ実用化には程遠い状態である。
Examples of the cellulose-based composite resin in which resin is combined with wood-based biomass include a wood deck commonly called wood plastic. This aims to use an inexpensive manufacturing method and uses recycled wood and recycled plastic as raw materials. In order to combine wood powder with plastic, it has been considered that wood powder is fine and does not contain water, for example, an average particle size of 10 μm or less and a water content of 5% or less from the plastic side. That is, when the particle size is large and the water content is high, the wood powder does not mix well into the plastic. As a result, wood flour contained only 30 to 50% at most. Further, in order to obtain a molded body in which 30 to 50% of wood powder is compounded, it has been limited to a product having a simple shape molded by extrusion molding or press molding. The wood-powder composite resin has the advantage of combining the goodness of a resin that looks like wood and the goodness of a resin, but on the other hand, it has a weakness that is neither of them. Thus, there are problems in quality maintenance and productivity.
Recently, a technique focusing on high strength, high elasticity, and low thermal expansion property using cellulose nanofiber (CNF) has been widely taken up, but it is far from practical use.

竹のファイバーに着目すると、水蒸気で竹を粉砕し、糸状に分解し、細かく切断して樹脂に複合しようとする試みも数件あるが、実用化できたものはまだない。従来の樹脂製造技術による混錬装置で、100℃程度で樹脂を溶かして竹紛を混合しただけでは、竹の低純度での混錬ができるだけで、溶融一体化した複合樹脂になっていない。なお、竹本来の成分から抗菌性を発揮させるために抗菌性充填剤を入れている試みも見られる。 Focusing on bamboo fibers, there have been several attempts to pulverize bamboo with steam, decompose it into filaments, and cut it into fine particles to combine it with resin, but none has yet been put to practical use. A conventional kneading apparatus using a resin manufacturing technique can melt bamboo at a temperature of about 100° C. and mix the bamboo powder, but the bamboo can be kneaded at a low purity and is not a melt-integrated composite resin. There are also attempts to add antibacterial fillers in order to exert antibacterial properties from the original ingredients of bamboo.

他方で、竹材は日本国内に多く存在し、プラスチックに混入できれば繊維強化剤になる期待もあるが、平均粒度400μm以下の細粉化が困難であり、含水率も大きく35%以下にすることは困難なため、プラスチックと複合するのに大きな壁になっていた。 On the other hand, there are many bamboo materials in Japan, and if they can be mixed with plastics, they are expected to become fiber reinforcing agents, but it is difficult to make fine powder with an average particle size of 400 μm or less, and it is not possible to increase the water content to 35% or less. Due to the difficulty, it was a big wall to combine with plastic.

ところで、発明者は特殊なフライス工具を有する特殊竹粉製造機を発明し、内部に維管束の多孔質を持つ竹を用いて、一次粉砕で平均粒度400μm、これを原料とした二次粉砕機による二次粉砕で平均粒度50μの竹粉を作成することにも成功した。当該フライス工具は、竹の端面を切削粉砕するもので、円筒状被切削物の端面の切削粉砕に好適である(特許文献1,2参照)。 By the way, the inventor invented a special bamboo powder manufacturing machine having a special milling tool, and using bamboo having a porous vascular bundle inside, an average particle size of 400 μm in primary crushing, and a secondary crusher using this as a raw material. We also succeeded in producing bamboo powder with an average particle size of 50μ by secondary pulverization with. The milling tool cuts and grinds the end surface of bamboo, and is suitable for cutting and grinding the end surface of a cylindrical workpiece (see Patent Documents 1 and 2).

また、(株)エムアンドエフ・テクノロジー社製の混合粉砕装置を用いて、セルロース系材料とプラスチックバインダーを混合粉砕すると、混合容器内において上記材料が混合粉砕され、剪断、摩擦及び圧縮による発熱により、含水成分が脱水される。次に、混合粉砕時の衝突エネルギーにより、最終的に微粉粒となり、急激な温度上昇が起こる。そして、従来の技術における単純混合と異なり、混合容器内が一瞬のうちに高温高圧の状態となる。次に、細胞内腔や細胞間隙等の空隙中に存在する自由水と、細胞壁中に含まれている結合水が抜けた隙間に、木材においてセルロースに次いで多い割合のリグニンが媒介となりバインダーの熱可塑性樹脂(ポリプロピレンPP、ポリエチレンPE、生分解性樹脂など)が入り込み、単純混合では全く見られない木材を構成するセルロース等と均一にそして強い結合力を持って溶融し一体化する。すなわちリグニンは、3つのモノグリノールの重合体からなる3次元網目状構造をした天然高分子なので、バインダーの高分子との親和性によって、脱水状態のセルロース成分に溶融したバインダーが含浸されたと考えることが出来る(特許文献3参照)。すなわち、上記混合粉砕装置を用いると、セルロース系材料とプラスチックとの混合溶融が可能である。
そして、かかる混合粉砕装置を用いて、パルプ及びケナフについてセルロース複合樹脂が製造されている(特許文献4,5参照)。
In addition, when a cellulosic material and a plastic binder are mixed and pulverized using a mixing and pulverizing device manufactured by M&F Technology Co., Ltd., the above materials are mixed and pulverized in a mixing container, and due to heat generated by shearing, friction and compression, water content is generated. The ingredients are dehydrated. Next, due to the collision energy at the time of mixing and pulverizing, the particles finally become fine powder particles, and a rapid temperature rise occurs. Then, unlike the simple mixing in the conventional technique, the inside of the mixing container is in a high temperature and high pressure state in an instant. Next, the free water existing in the voids such as cell lumens and intercellular spaces and the voids in which bound water contained in the cell wall escaped, the ratio of lignin, which is the second largest after cellulose in wood, mediated, and the heat of the binder A plastic resin (polypropylene PP, polyethylene PE, biodegradable resin, etc.) enters and melts and integrates uniformly and with a strong binding force with cellulose and the like that make up wood, which cannot be seen by simple mixing. In other words, since lignin is a natural polymer with a three-dimensional network structure composed of three monoglinol polymers, it can be considered that the molten cellulose component is impregnated into the dehydrated cellulose component due to the affinity with the binder polymer. (See Patent Document 3). That is, by using the above mixing and pulverizing device, it is possible to mix and melt the cellulosic material and the plastic.
Then, a cellulose composite resin is produced for pulp and kenaf using such a mixing and pulverizing device (see Patent Documents 4 and 5).

特許第5344644号公報Japanese Patent No. 5344644 実用新案登録第3176586号公報Utility model registration No. 3176586 特許第4489017号公報Japanese Patent No. 4489017 特開2011−116838号公報JP, 2011-116838, A 特許第5314867号公報Japanese Patent No. 5314867

そこで、発明者は、特殊なフライス工具を有する特殊竹粉製造機による微細竹粉の製造と、混合粉砕装置を用いたセルロース系材料とプラスチックとを混合溶融させる技術を用い、さらに、セルロース系材料として竹粉を用いることにより、上記壁を乗り越えて、強化プラスチックを形成できる可能性に想到した。
本発明は、粒度が大きくかつ水分含有率が高い竹粉を用い、セルロース系材料の含有率の高い竹粉複合樹脂、竹粉樹脂混合溶融体及びこれらの製造方法を提供すること、製造できる新な複合樹脂の範囲を拡大すること、そして、強度特性が良好でかつ再成形可能な成形体を提供することを目的とする。
Therefore, the inventor uses a technique of producing fine bamboo powder by a special bamboo powder producing machine having a special milling tool and a technique of mixing and melting a cellulosic material and a plastic using a mixing and pulverizing device, By using bamboo powder as the material, it has been conceived that the reinforced plastic can be formed by overcoming the wall.
The present invention provides a bamboo powder composite resin having a high content rate of a cellulosic material, a bamboo powder resin mixed melt, and a manufacturing method thereof, using bamboo powder having a large particle size and a high water content, It is an object of the present invention to expand the range of various composite resins and to provide a remoldable molded product having good strength characteristics.

本発明の第1の態様における竹粉複合樹脂の製造方法は、密閉型混合粉砕装置1の撹拌室3内で、樹脂粉末と竹粉を原料として、溶融混合して竹粉樹脂混合溶融体を製作し、竹粉樹脂混合溶融体を成形して竹粉複合樹脂を製造する竹粉複合樹脂の製造方法である。この製造方法では、例えば図8に示すように、竹粉は、平均粒度が1μm以上800μm以下に粉砕され(S001)、水分含水率が5〜40質量%の竹粉であり、溶融混合時(S005)の撹拌室3内の温度が150℃以上370℃以下、圧力が0.20MPa以上飽和水蒸気以下で、かつ、回転軸5の回転トルクが下降して極小値に達し、さらに上昇に転じた(S007)直後に回転を停止させて(S008)竹粉樹脂混合溶融体を製作する(S009)。その後、例えば図9に示すように、竹粉樹脂混合溶融体を粉砕し(S011)、成形して(S012)竹粉複合樹脂を製造する(S0013)。また、溶融混合が行われる密閉型混合粉砕装置1は、図4に示すように、複数の回転羽根10a〜10fが配設された回転軸5を有し、竹粉複合樹脂は、その撹拌室3内で、樹脂粉末と竹粉を原料として、回転軸5を回転させて溶融混合して製造される。 The method for producing a bamboo powder composite resin according to the first aspect of the present invention is a method for producing a bamboo powder resin mixed melt by melting and mixing resin powder and bamboo powder as raw materials in the stirring chamber 3 of the closed-type mixing and pulverizing device 1. It is a manufacturing method of a bamboo powder composite resin, which is manufactured and a bamboo powder resin mixed melt is molded to manufacture a bamboo powder composite resin. In this manufacturing method, for example, as shown in FIG. 8, bamboo powder is a bamboo powder having an average particle size of 1 μm or more and 800 μm or less (S001) and a water content of 5 to 40% by mass. In S005), the temperature in the stirring chamber 3 is 150° C. or more and 370° C. or less, the pressure is 0.20 MPa or more and saturated water vapor or less, and the rotation torque of the rotating shaft 5 decreases to reach the minimum value, and further increases. Immediately after (S007), the rotation is stopped (S008) to produce a bamboo powder resin mixed melt (S009). Then, for example, as shown in FIG. 9, the bamboo powder resin mixed melt is crushed (S011) and molded (S012) to produce a bamboo powder composite resin (S0013). Further, as shown in FIG. 4, the closed type mixing and pulverizing device 1 in which the melt mixing is performed has a rotating shaft 5 on which a plurality of rotating blades 10a to 10f are arranged, and the bamboo powder composite resin has its stirring chamber. In 3, the resin powder and the bamboo powder are used as raw materials, and the rotary shaft 5 is rotated to melt and mix them.

ここにおいて、竹粉複合樹脂とは、竹紛と樹脂が混じり合い一体化したものをいうが、ここでは、高温・高圧で混合溶融されたものを竹粉樹脂混合溶融体、その後粉砕、成形されたものを竹粉複合樹脂と称して区別する。なお、混合溶融後に加熱、冷却、加工、変形されたもの、他の樹脂に混入されたものも竹粉樹脂混合溶融体に含まれ、成形後に加熱、冷却、加工、変形されたもの、他の樹脂に混入されたものも竹粉複合樹脂に含まれる。
回転の停止後、竹粉樹脂混合溶融体として取り出すことが出来る。次に成型機の投入可能なサイズに粉砕して、プラスチック成型機にて成型されて、竹粉複合樹脂が製造される。竹粉樹脂混合溶融体は、各種成型機で成形される過程で再度溶融されて成形体としてのプラスチック製品になる。すなわち、混合粉砕装置から溶融体として取り出した竹粉樹脂混合溶融体にすることで、従来のバイオマス混練方式とは異なり、竹粉70%や60%という高比率のバイオマスを複合しながら、微小径ノズルから金型へ射出する射出成型機による成形が可能となり、他の成形も含め竹粉複合樹脂が生産される。また、直後とは、極小値を示してからの短時間の間を指し、少なくとも1秒から10分、より好ましくは1秒から2分、さらに好ましくは1秒から30秒が好ましい。
このように構成すると、内部に竹の維管束の多孔質を持ち、粒度が大きくかつ水分含有率が高い竹粉を用い、セルロース系材料の含有率の高い竹粉複合樹脂の製造方法を提供することができ、製造できる新たな複合樹脂の範囲を拡大することができる。
Here, the bamboo powder composite resin refers to a material in which bamboo powder and resin are mixed and integrated, but here, a material mixed and melted at high temperature and high pressure is a bamboo powder resin mixed melt, which is then crushed and molded. What is called "bamboo powder composite resin" is used to distinguish them. It should be noted that bamboo powder resin mixed melts include those that have been heated, cooled, processed and deformed after mixing and melting, and those that have been mixed with other resins, and those that have been heated, cooled, processed and deformed after molding, and other Those mixed with resin are also included in the bamboo powder composite resin.
After the rotation is stopped, it can be taken out as a bamboo powder resin mixed melt. Next, it is crushed to a size that can be put into a molding machine and molded with a plastic molding machine to produce a bamboo powder composite resin. The bamboo powder resin mixed melt is melted again in the process of being molded by various molding machines to be a plastic product as a molded body. That is, by using the bamboo powder resin mixed melt taken out as a melt from the mixing and pulverizing device, unlike the conventional biomass kneading method, while combining a high ratio of bamboo powder of 70% or 60%, a small diameter Molding with an injection molding machine that injects from a nozzle into a mold is possible, and bamboo powder composite resin is produced including other moldings. The term “immediately after” refers to a short time after the minimum value is shown, and it is preferably at least 1 second to 10 minutes, more preferably 1 second to 2 minutes, still more preferably 1 second to 30 seconds.
With this configuration, a bamboo powder having a porous vascular bundle of bamboo, a large particle size and a high water content is used, and a method for producing a bamboo powder composite resin having a high content of a cellulosic material is provided. Therefore, the range of new composite resins that can be manufactured can be expanded.

本発明の第2の態様における竹粉複合樹脂の製造方法は、第1の態様における竹粉複合樹脂の製造方法において、例えば図1、図2A及び図2Bに示すように、竹粉は、切れ刃であるチップ34が取り付けられる工具本体の端面35に、複数個のチップ34を放射状に並べて延びたチップ列を周方向に複数列備え、隣接する一対のチップ列のチップそれぞれが、回転中心軸からの径方向距離を交互に異にした千鳥状に配設されているフライス工具32を用いて粉砕された微細粉末であり、電子顕微鏡写真により竹維管束の多孔質構造が観測され、内部に10〜1011/gの乳酸菌が生育し、竹粉と樹脂の重量比が5:95〜95:5であることを特徴とする。
このように構成すると、竹粉複合樹脂の製造に適切な原料としての竹粉を提供できる。
The method for producing a bamboo powder composite resin according to the second aspect of the present invention is the same as the method for producing a bamboo powder composite resin according to the first aspect, for example, as shown in FIG. 1, FIG. 2A and FIG. The end surface 35 of the tool body to which the chips 34, which are blades, are attached, is provided with a plurality of chip rows in the circumferential direction in which a plurality of tips 34 are arranged in a radial pattern and extend. It is a fine powder pulverized by using a milling tool 32 arranged in a zigzag pattern in which the radial distance from is alternated, and the porous structure of the bamboo vascular bundle is observed by an electron micrograph and It is characterized in that 10 3 to 10 11 /g of lactic acid bacteria grow, and the weight ratio of bamboo powder and resin is 5:95 to 95:5.
According to this structure, it is possible to provide bamboo powder as a raw material suitable for producing a bamboo powder composite resin.

本発明の第3の態様における竹粉樹脂混合溶融体の製造方法は、第1の態様における竹粉複合樹脂の製造方法から、中間体としての竹粉樹脂混合溶融体を製造する工程を抽出したものであります。
このように構成すると、竹粉複合樹脂の成形に適切な材料としての竹粉樹脂混合溶融体を提供できる。
The method for producing a bamboo powder resin-mixed melt according to the third aspect of the present invention extracts the step of producing a bamboo powder resin-mixed melt as an intermediate from the method for producing a bamboo powder resin composite according to the first aspect. It is a thing.
According to this structure, it is possible to provide the bamboo powder resin mixed melt as a material suitable for molding the bamboo powder composite resin.

本発明の第4の態様における竹粉樹脂混合溶融体の製造方法は、第2の態様における竹粉複合樹脂の製造方法から、中間体としての竹粉樹脂混合溶融体を製造する工程を抽出したものであります。 The method for producing a bamboo powder resin mixed melt according to the fourth aspect of the present invention is the step of producing a bamboo powder resin mixed melt as an intermediate from the method for producing a bamboo powder composite resin according to the second aspect. It is a thing.

本発明の第5の態様における竹粉樹脂混合溶融体は、第3または第4の態様における竹粉樹脂混合溶融体の製造方法で製造されたことを特徴とするものであります。 The bamboo powder resin mixed melt according to the fifth aspect of the present invention is characterized by being manufactured by the method for manufacturing a bamboo powder resin mixed melt according to the third or fourth aspect.

本発明の第6の態様における竹粉複合樹脂は、第1または第2の態様における竹粉複合樹脂の製造方法で製造されたことを特徴とするものであります。
このように構成すると、粒度が大きくかつ水分含有率が高い竹粉を用い、セルロース系材料の含有率の高い竹粉複合樹脂を提供することができ、強度特性が良好でかつ再成形可能な成形体を提供することができる。
The bamboo powder composite resin according to the sixth aspect of the present invention is characterized by being manufactured by the method for manufacturing a bamboo powder composite resin according to the first or second embodiment.
With such a configuration, it is possible to provide a bamboo powder composite resin having a high content rate of a cellulosic material, by using bamboo powder having a large particle size and a high water content rate, and having a good strength property and a remoldable shape. The body can be provided.

本発明によれば、粒度が大きくかつ水分含有率が高い竹粉を用い、セルロース系材料の含有率の高い竹粉複合樹脂、竹粉樹脂混合溶融体及びこれらの製造方法を提供することができ、製造できる新たな複合樹脂の範囲を拡大することができ、そして、強度特性が良好でかつ再成形可能な成形体を提供することができる。 According to the present invention, it is possible to provide a bamboo powder composite resin having a high content rate of a cellulosic material, a bamboo powder resin mixed melt, and a manufacturing method thereof using bamboo powder having a large particle size and a high water content. The range of new composite resins that can be produced can be expanded, and a remoldable molded article having good strength characteristics can be provided.

特殊竹粉製造機の例の模式図である。It is a schematic diagram of an example of a special bamboo powder manufacturing machine. 特殊竹粉製造機が備えるフライス工具の例の模式断面図である。It is a schematic cross section of the example of the milling tool with which a special bamboo powder manufacturing machine is equipped. 特殊竹粉製造機が備えるフライス工具の例の模式正面図である。It is a model front view of the example of the milling tool with which a special bamboo powder manufacturing machine is equipped. 特殊竹粉製造機で製造した竹粉の電子顕微鏡写真の例である。It is an example of the electron micrograph of the bamboo powder manufactured with the special bamboo powder manufacturing machine. 密閉型混合粉砕装置の例の模式図である。It is a schematic diagram of an example of a closed type mixing and pulverizing device. 複数の回転羽が配設された回転軸の例の模式図である。It is a schematic diagram of an example of a rotating shaft in which a plurality of rotary wings are arranged. 水蒸気の解放機構の例の模式図である。It is a schematic diagram of an example of a release mechanism of water vapor. 回転トルクの時間変化の例を示す図である。It is a figure which shows the example of the time change of rotation torque. 竹粉樹脂混合溶融体の製造方法の手順の例を説明する図である。It is a figure explaining the example of the procedure of the manufacturing method of a bamboo powder resin mixed melt. 竹粉樹脂混合溶融体から竹粉複合樹脂への製造方法の手順の例を説明する図である。It is a figure explaining the example of the procedure of the manufacturing method from a bamboo powder resin mixed melt to a bamboo powder composite resin. 竹粉複合樹脂の電子顕微鏡写真の例である。It is an example of the electron micrograph of a bamboo powder composite resin. 竹粉複合樹脂からなる成形体を示す図である。It is a figure which shows the molded object which consists of a bamboo powder composite resin.

本実施の形態では、複数の回転羽根が配設された回転軸を有する密閉型混合粉砕装置の攪拌室内で、樹脂粉末と竹粉を原料として、回転軸を回転させて溶融混合して竹粉複合樹脂を製造する竹粉複合樹脂の製造方法の例について説明する。また、原料として、特殊なフライス工具を備える特殊竹粉製造機により製造された微細竹粉を使用する例について説明する。 In this embodiment, resin powder and bamboo powder are used as raw materials in a stirring chamber of a closed type mixing and pulverizing device having a rotary shaft in which a plurality of rotary blades are arranged, and the rotary shaft is rotated to melt and mix the bamboo powder. An example of a method for producing a bamboo powder composite resin for producing the composite resin will be described. Further, an example in which fine bamboo powder manufactured by a special bamboo powder manufacturing machine equipped with a special milling tool is used as a raw material will be described.

図1に本発明で使用する特殊竹粉製造機の例の模式図を示す。
本発明の竹粉複合樹脂の製造方法で用いる特殊竹粉製造機31は、乾式竹粉製造機に属する。孟宗竹又は真竹の外形8cm以上の竹(竹素材)Wの枝葉を落とし、良く洗浄して両端の外径を把握して位置決めし、右端のすり鉢状のフライス工具32の本体の端面35(33〜35は図2参照)に放射線状に超硬インサートチップ34を配置したカッター33を配し、これをカッター駆動部36で回転させて、左端から竹素材Wを回転させずにカッター33に向かって送り機構37で送り込みながら切削することで微細竹粉を作るものである(特許文献1,2参照)。竹素材Wは、支持手段38に支持され、スライド可能な基台39に搭載されてカッター33に向かって移動する。なお、本発明における竹粉は、これに限られない。また、生竹から粉砕した竹粉であれば特に制限されない。なお、Xは回転中心の軸線である。
FIG. 1 shows a schematic view of an example of a special bamboo powder manufacturing machine used in the present invention.
The special bamboo powder manufacturing machine 31 used in the method for manufacturing a bamboo powder composite resin of the present invention belongs to a dry bamboo powder manufacturing machine. Bamboo (bamboo material) W with an outer diameter of 8 cm or more of Moso bamboo or bamboo is dropped, washed well and grasped the outer diameters of both ends to be positioned, and the end face 35 (33 ~ of the mortar-shaped milling tool 32 on the right end 35 is a drawing (see FIG. 2) is provided with a cutter 33 in which the carbide insert tips 34 are arranged in a radial pattern, and is rotated by the cutter drive unit 36, and the bamboo material W is not rotated from the left end toward the cutter 33. Fine bamboo powder is produced by cutting while feeding by the feeding mechanism 37 (see Patent Documents 1 and 2). The bamboo material W is supported by the supporting means 38, mounted on a slidable base 39, and moves toward the cutter 33. The bamboo powder in the present invention is not limited to this. Further, it is not particularly limited as long as it is bamboo powder crushed from raw bamboo. In addition, X is an axis line of the rotation center.

図2A及び図2Bに特殊竹粉製造機が備えるフライス工具の例の模式図を示す。図2Aは回転中心軸を含む断面図、図2Bは正面図である。
フライス工具32は、切れ刃であるチップ34が取り付けられる工具本体の端面35に、複数個のチップ34を放射状に並べて、周方向に延びたチップ列を有するフライスカッター33を複数列備え、フライスカッター33は隣接する一対のチップ列のチップ34それぞれが、回転中心軸からの径方向距離を交互に異にした千鳥状に配設されている。本発明で用いる竹粉は、フライス工具32を用いて粉砕された微細粉末であり、水分含水率が5〜40質量%であり、電子顕微鏡写真により竹維管束の多孔質構造が観測され、内部に10〜1011/gの乳酸菌が生育し、竹粉と樹脂の重量比が5:95〜95:5である。なお、Yは竹素材Wの移動方向、Zはフライスカッターの回転方向である。
2A and 2B show schematic views of examples of milling tools provided in the special bamboo powder manufacturing machine. 2A is a cross-sectional view including the rotation center axis, and FIG. 2B is a front view.
The milling tool 32 is provided with a plurality of rows of milling cutters 33 each having a row of tips extending in the circumferential direction, in which a plurality of tips 34 are radially arranged on an end surface 35 of a tool body to which a tip 34 that is a cutting edge is attached. The chips 34 of a pair of adjacent chip rows 33 are arranged in a zigzag pattern in which radial distances from the rotation center axis are alternately different. The bamboo powder used in the present invention is a fine powder pulverized using a milling tool 32, has a water content of 5 to 40% by mass, and a porous structure of a bamboo vascular bundle is observed by an electron micrograph, Lactobacillus of 10 3 to 10 11 /g grows and the weight ratio of bamboo powder and resin is 5:95 to 95:5. Note that Y is the moving direction of the bamboo material W, and Z is the rotating direction of the milling cutter.

図3に特殊竹粉製造機で製造した竹粉の電子顕微鏡写真の例を示す。
竹素材Wは中空円筒状で、竹稈の内部に軸方向に無数の竹維管束(水分・養分の通り道)の管が開いているところを、軸に直角に切削して製造した竹粉には内部に20μmの蜂の巣状の多孔質になっている。
竹粉の粉末粒度は1〜800μmで、内部には粉砕直後は10〜10程度の数の乳酸菌が生息している。これを袋で密閉し、約2週間寝かせて、発酵を促進させて、乳酸菌数を10〜1011もの数に増殖させている。
Fig. 3 shows an example of an electron micrograph of bamboo powder manufactured by a special bamboo powder manufacturing machine.
The bamboo material W has a hollow cylindrical shape, and the inside of the bamboo culm is an innumerable bamboo vascular bundle (pathway for water and nutrients) that is cut at right angles to the axis to produce bamboo powder. Has a honeycomb-like porous structure of 20 μm inside.
Bamboo powder has a particle size of 1 to 800 μm, and lactic acid bacteria of a number of about 10 3 to 10 4 live in the inside immediately after crushing. This is sealed in a bag and left to stand for about 2 weeks to accelerate fermentation and grow the number of lactic acid bacteria to 10 8 to 10 11 .

本発明で用いる竹粉は、天然竹粉の枝葉を除いた竹稈を特殊竹粉製造機で粉砕した多孔質保持の微細竹粉であることが好ましい。この竹粉は、その色・形状の均質性が高いため、成形体としたときに色相が均一になる上に、成形時、マスターバッチや顔料を混合して成形体を着色しても均一になる。 The bamboo powder used in the present invention is preferably a fine bamboo powder that retains porosity obtained by crushing bamboo culms excluding the branches and leaves of natural bamboo powder with a special bamboo powder maker. Since this bamboo powder has a high degree of homogeneity in its color and shape, it has a uniform hue when formed into a molded product, and even when the molded product is colored by mixing a masterbatch or pigment during molding. Become.

本発明で用いる竹粉は、特殊竹粉製造機により粉砕した竹粉である。目視でわかる糸状の繊維がなく、竹維管束の多孔質が保持されている粉末であればよい。竹粉の寸法は特に制限はないが、400μm以下が好ましく、200μm以下がより好ましい。他の竹破砕機(通常チッパーやシュレッダーなどと称する)で製造した多孔質のない竹粉では樹脂成形時に物性強度が低下し、表面仕上げ品質が低下することがある。 The bamboo powder used in the present invention is bamboo powder pulverized by a special bamboo powder manufacturing machine. Any powder can be used as long as it has no thread-like fibers that can be visually recognized and the porosity of the bamboo fiber bundle is retained. The size of bamboo powder is not particularly limited, but is preferably 400 μm or less, more preferably 200 μm or less. Non-porous bamboo powder produced by another bamboo crushing machine (usually referred to as a chipper or shredder) may deteriorate the physical strength during resin molding and the surface finish quality.

本発明で用いる竹粉は、水分含有率が5〜30質量%であるものが好ましい。セルロースの水分含有率がこの範囲にあると、溶融混合時間が短くなり、生産性が良好である。一方、水分含有率が5質量%未満であると、時間をかけても撹拌室内部の圧力が上がらないので水を補充投入することがある。
また、35質量%を超えた水分含有率とすると、竹粉の脱水に時間がかかるため、溶融時間が長くなり、竹粉が分解され易くなることがある。水分含有率は8〜35質量%がより好ましく、10〜25質量%がさらに好ましい。
The bamboo powder used in the present invention preferably has a water content of 5 to 30 mass %. When the water content of the cellulose is within this range, the melt mixing time is shortened and the productivity is good. On the other hand, if the water content is less than 5% by mass, the pressure inside the stirring chamber does not rise even over time, so water may be replenished and added.
If the water content is more than 35% by mass, it takes a long time to dehydrate the bamboo powder, so that the melting time becomes long and the bamboo powder may be easily decomposed. The water content is more preferably 8 to 35% by mass, further preferably 10 to 25% by mass.

図4は本発明で用いる密閉型混合粉砕装置1の例の模式図である(特許文献3参照)。本発明で用いる密閉型混合粉砕装置1においては、機台ベース2上に横向に円筒形の撹拌室3と、材料投入部14およびらせん状羽根部材12が配設される材料供給室13が複数の脚部によって配置される。両端の脚部に配置された軸受4、4により回転軸5を水平に支持して、回転軸5が撹拌室3の中心と同軸的に貫挿配置され、回転軸の一端をプーリー6とVベルト7を介して駆動源としてのモーター8と回転連絡している。 FIG. 4 is a schematic view of an example of the closed type mixing and pulverizing apparatus 1 used in the present invention (see Patent Document 3). In the closed type mixing and pulverizing apparatus 1 used in the present invention, there are a plurality of laterally cylindrical stirring chambers 3 on a machine base 2 and a plurality of material supply chambers 13 in which a material feeding section 14 and a spiral blade member 12 are arranged. Placed by the legs of the. The rotating shaft 5 is horizontally supported by the bearings 4 and 4 arranged on the legs at both ends, and the rotating shaft 5 is coaxially inserted through the center of the stirring chamber 3, and one end of the rotating shaft is connected to the pulley 6 and the V. It is rotationally connected to a motor 8 as a drive source via a belt 7.

図5は複数の回転羽が配設された回転軸の例の模式図である。撹拌室3中を貫通して配置された回転軸5の外周には、例えば、計6枚の横断面形状矩形であるとともに、全体形状矩形の回転羽根10a〜10fが、回転軸5の円周方向の180度の角度間隔の部位における軸方向において対向して突設されている。そのうちの軸方向の両端部の回転羽根10aおよび10fは、図4の右側面から見た場合の時計回りに回転したとき、その前縁が撹拌室3の両端の垂直壁11、11の内面とほとんど隙間なく摺接するように回転軸5の外周に固着されている。また、中間部の4枚の回転羽根10b、10c、10d、10eは回転軸5の外周面に千鳥状に固着され、回転時の前縁が該撹拌室3の両端を向く方向に各々配置されている。 FIG. 5 is a schematic diagram of an example of a rotary shaft on which a plurality of rotary vanes are arranged. On the outer periphery of the rotary shaft 5 that is disposed so as to penetrate through the stirring chamber 3, for example, the rotary blades 10a to 10f having a total of six rectangular cross-sections and a rectangular overall shape are provided on the circumference of the rotary shaft 5. The projections are provided so as to face each other in the axial direction at portions at angular intervals of 180 degrees in the direction. The rotary blades 10a and 10f at both ends in the axial direction of the rotary blades 10a and 10f, when rotated clockwise as viewed from the right side of FIG. 4, have their front edges formed with the inner surfaces of the vertical walls 11, 11 at both ends of the stirring chamber 3. It is fixed to the outer circumference of the rotary shaft 5 so that it is in sliding contact with almost no gap. Further, the four rotary blades 10b, 10c, 10d, 10e in the middle portion are fixed to the outer peripheral surface of the rotary shaft 5 in a zigzag manner, and the front edges of the rotary blades are arranged so as to face both ends of the stirring chamber 3. ing.

撹拌室3の両端の垂直壁11のモーター8側は、撹拌室3の一方の端壁に開設された撹拌室3の材料供給口であり、12は回転軸5の外周に形成されたらせん状の材料供給羽根部材であり、13は供給スクリューを包囲している材料供給室、14は材料供給室13の上方に設けられた材料投入部であり、材料投入部14には材料を投入した後溶融混合時に密閉性を保ち得る開閉自在のシャッター15が設けられている。 The motor 8 side of the vertical walls 11 at both ends of the stirring chamber 3 is a material supply port of the stirring chamber 3 opened in one end wall of the stirring chamber 3, and 12 is a spiral formed on the outer circumference of the rotating shaft 5. Is a material supply blade member, 13 is a material supply chamber that surrounds the supply screw, 14 is a material feeding portion provided above the material feeding chamber 13, and after feeding the material into the material feeding portion 14. A shutter 15 that can be opened and closed so as to maintain hermeticity during melt mixing is provided.

図6は水蒸気の解放機構20例の拡大模式図である。本発明で用いられる密閉型混合粉砕装置1には、回転軸5の両端に、水蒸気の解放機構20が設けられている。水蒸気の解放機構20を構成する回転軸の部分にはらせん状の溝22が切られており、回転軸5が回転したときに、外部から空気が撹拌室3内部に送り込まれるように右ネジ、あるいは左ネジの方向にらせん状の溝22が切られている。空気流入方向24(矢印)は外部から撹拌室内部へ送り込まれる空気の方向を示している。また、本発明において、溶融混合時、撹拌室3内部は非常な高圧力状態となるため、撹拌室内部の高圧力水蒸気は、水蒸気流出方向23(矢印)へ向かい外部に漏れ出ようとする。しかし、水蒸気の解放機構20において、回転軸5に切ってあるらせん状の溝22の最外周部と外壁部との隙間の距離がわずかであるため、この部分で、両者はぶつかり合い、いずれ均衡を保つようになる。 FIG. 6 is an enlarged schematic view of 20 examples of the water vapor release mechanism. The closed type mixing and pulverizing apparatus 1 used in the present invention is provided with water vapor release mechanisms 20 at both ends of the rotary shaft 5. A spiral groove 22 is cut in a part of the rotary shaft that constitutes the water vapor release mechanism 20, and when the rotary shaft 5 rotates, a right-hand screw so that air is sent into the stirring chamber 3 from the outside, Alternatively, a spiral groove 22 is cut in the direction of the left screw. The air inflow direction 24 (arrow) indicates the direction of air sent into the stirring chamber from the outside. Further, in the present invention, since the inside of the stirring chamber 3 is in an extremely high pressure state during melt mixing, the high-pressure steam inside the stirring chamber tends to leak outward toward the steam outflow direction 23 (arrow). However, in the water vapor release mechanism 20, since the distance between the outermost peripheral portion of the spiral groove 22 cut on the rotary shaft 5 and the outer wall portion is small, both of them collide with each other at this portion and eventually the balance is reached. Will be kept.

回転羽根が配置された回転軸5は駆動源であるモーター8に連結されているが、本発明で用いる密閉型混合粉砕装置1においては、モーター8にかかる回転トルクを計測するトルクメーター(図示しない)が設置され、制御盤21(図4参照)にて回転トルクがモニターできる。本発明の竹粉複合樹脂の製造方法においては、該トルクメーターから計測される回転羽根10aないし10fが配設された回転軸5の回転トルクの変化を計測し、溶融混合の終了時点を判断する。 The rotary shaft 5 on which the rotary blades are arranged is connected to a motor 8 which is a drive source. In the closed type mixing and pulverizing apparatus 1 used in the present invention, a torque meter (not shown) for measuring the rotary torque applied to the motor 8 is used. ) Is installed, the rotational torque can be monitored on the control panel 21 (see FIG. 4). In the method of manufacturing a bamboo powder composite resin of the present invention, the change in the rotation torque of the rotary shaft 5 provided with the rotary blades 10a to 10f measured by the torque meter is measured to determine the end point of the melt mixing. ..

図7は回転トルクTの時間変化の例を示す図である。密閉型混合粉砕装置1内における材料の混合粉砕および乾燥状態に応じてモーター8の主軸にかかる回転トルクTが上昇して最大値M(時間t)に達した後、低下して最小値I(時間t)に達した後、一定時間tが経過したら、密閉型混合粉砕装置1の取出部17(図4参照)より混合粉砕、脱水され、樹脂が含浸された、竹粉と樹脂の混合溶融体を取り出す。回転トルクの計測値に応じた終了操作の措置は、初めて扱う素材のときには必須であるものの、同じ素材を定常的に用いる場合は、必ずしも毎回計測する必要はなく、実績より溶融混合の必要時間を決定しておき、その決められた溶融混合時間により終了時点を決めてもよい。 FIG. 7 is a diagram showing an example of the change over time of the rotational torque T. The rotation torque T applied to the main shaft of the motor 8 increases according to the mixing and crushing and drying conditions of the material in the closed-type mixing and crushing device 1, reaches a maximum value M (time t M ), and then decreases to a minimum value I. After a lapse of a certain time t after reaching (time t I ), the mixed powder is pulverized and dehydrated by the take-out section 17 (see FIG. 4) of the closed-type mixing and pulverizing apparatus 1 to impregnate the resin with the bamboo powder and the resin. Take out the mixed melt. The measure of the ending operation according to the measured value of the rotating torque is indispensable for the material to be handled for the first time, but when the same material is used constantly, it is not always necessary to measure each time, and the required time for melting and mixing is based on actual results. It may be determined in advance, and the end point may be determined according to the determined melt mixing time.

本発明における竹粉複合樹脂の製造方法において、竹粉と樹脂が、密閉型混合粉砕装置1の撹拌室3内で溶融混合される温度圧力条件は、温度範囲は150〜370℃であり、200〜370℃がより好ましく、250〜370℃がさらに好ましい、また、圧力範囲は0.20MPa〜溶融混合温度における飽和水蒸気圧であり、2.00MPa〜溶融混合温度における飽和水蒸気圧がより好ましい。本発明においては、水の超臨界状態である温度375℃、圧力22.00MPa条件よりわずかに温度または圧力、あるいは両者が低い水の亜臨界状態で溶融混合が行われるとより一層好ましい。 In the method for producing a bamboo powder composite resin according to the present invention, the temperature and pressure conditions under which the bamboo powder and the resin are melt-mixed in the stirring chamber 3 of the closed-type mixing and pulverizing apparatus 1 are in the temperature range of 150 to 370° C. -370 degreeC is more preferable, 250-370 degreeC is still more preferable, Moreover, a pressure range is 0.20MPa-saturated steam pressure in a melt-mixing temperature, and its saturated steam-pressure in a melt-mixing temperature is more preferable. In the present invention, it is even more preferable to carry out the melt mixing in a subcritical state of water in which the temperature or pressure is slightly lower than the temperature of 375° C., which is a supercritical state of water, and the pressure of 22.00 MPa.

本発明における飽和水蒸気圧とは、溶融混合時において、溶融混合温度が一定であり、撹拌室の内部容積に変化がなければ、該撹拌室内部の水蒸気圧力は飽和水蒸気圧を超えることはない。 The saturated steam pressure in the present invention means that the steam pressure in the stirring chamber does not exceed the saturated steam pressure as long as the melting and mixing temperature is constant during melt mixing and the internal volume of the stirring chamber does not change.

図8は本発明の竹粉樹脂混合溶融体の製造方法の手順の例を説明する図である。用意した竹粉は特殊竹粉製造機31により切削、粉砕し、粉砕された乳酸発酵微粉末を得る(S001)。次に、竹粉と樹脂を密閉型混合粉砕装置に投入する(S002)。竹粉と樹脂は、投入前にブレンダー等で予備混合しておいてもよいし、撹拌室3に順番に投入してもよい。予備混合なしに直接竹粉と樹脂を撹拌室3に投入する際は、撹拌室3内部の回転羽根10aないし10fを低速で回転させながら投入することが好ましい。竹粉と樹脂を撹拌室3に投入後、該撹拌室3を密閉状態にし、回転羽根10aないし10fを高速回転させる(S003)。竹粉と樹脂は強力な剪断力を受け、撹拌室3内部の温度は急上昇する。温度の急上昇に伴い、竹粉が含有している水分が蒸発し、水蒸気と化し、撹拌室3内部が水蒸気で充満され内部圧力が急激に上昇する(S004)。さらに、撹拌室3内部の温度が樹脂の軟化温度、溶融温度を超えることにより、樹脂の軟化あるいは溶融が開始し、竹粉と樹脂の溶融混合が開始する(S005)。 FIG. 8: is a figure explaining the example of the procedure of the manufacturing method of the bamboo powder resin mixed melt of this invention. The prepared bamboo powder is cut and crushed by the special bamboo powder maker 31 to obtain crushed lactic acid fermentation fine powder (S001). Next, the bamboo powder and the resin are put into a closed type mixing and pulverizing device (S002). The bamboo powder and the resin may be premixed with a blender or the like before being charged, or may be sequentially charged into the stirring chamber 3. When the bamboo powder and the resin are directly charged into the stirring chamber 3 without premixing, it is preferable that the rotating blades 10a to 10f inside the stirring chamber 3 are rotated at a low speed. After the bamboo powder and the resin are put into the stirring chamber 3, the stirring chamber 3 is hermetically closed and the rotary blades 10a to 10f are rotated at high speed (S003). The bamboo powder and the resin receive a strong shearing force, and the temperature inside the stirring chamber 3 rapidly rises. As the temperature rises sharply, the water content of the bamboo powder evaporates and becomes steam, and the inside of the stirring chamber 3 is filled with steam and the internal pressure rises rapidly (S004). Further, when the temperature inside the stirring chamber 3 exceeds the softening temperature and the melting temperature of the resin, the softening or melting of the resin starts, and the melt mixing of the bamboo powder and the resin starts (S005).

本発明の竹粉複合樹脂の製造方法においては、回転羽根10aないし10fが配設された回転軸5の回転トルクを計測する(S006)ことで、溶融混合の進行状況を把握し、溶融混合の停止を見極めることができる。すなわち、回転羽根10aないし10fの回転数の高まりとともに回転トルクが上昇するが、被混練物の温度の上昇に伴い、樹脂の熱溶融が開始するため、一度最大値に達した回転トルクは、該樹脂の熱溶融の進行とともに低下し続ける。このとき、竹粉と樹脂との溶融混合が始まっており、竹粉と樹脂との界面における相互作用力が増大することにより、回転トルクはいったん極小値を示した後に反転して再上昇を始める(S007)。本発明においては、回転トルクが再上昇し始めた直後に回転軸5の回転を停止する(S008)。本発明において、撹拌室3内の温度は、回転トルクが上昇→低下→上昇と変動している間も上昇を続けるが、溶融混合は、回転トルクの再上昇後、被混練物の熱分解温度に達する前に停止することが好ましい。回転停止後、取出部17を開放して、竹粉と樹脂との混合溶融体を取り出す(S009)。そして、空気中で冷却されて固化する。この混合溶融体は竹粉複合樹脂製造の必然の過程であり、後述する図9における(S011)で粉砕されたチップは言わば通常の樹脂原料のペレットに相当するものである。このように、高温・高圧で混合溶融されたものを竹粉樹脂混合溶融体という。なお、混合溶融後に加熱、冷却、加工、変形されたもの、他の樹脂に混入されたものも竹粉樹脂混合溶融体に含まれる。 In the method for producing a bamboo powder composite resin of the present invention, the progress of melt mixing is grasped by measuring the rotation torque of the rotary shaft 5 on which the rotary blades 10a to 10f are arranged (S006), and You can identify the stoppage. That is, the rotational torque increases as the number of rotations of the rotary blades 10a to 10f increases, but the thermal melting of the resin starts with the increase in the temperature of the material to be kneaded. It keeps decreasing as the heat melting of the resin progresses. At this time, the melt mixing of the bamboo powder and the resin has started, and the interaction torque at the interface between the bamboo powder and the resin increases, so that the rotational torque once exhibits a minimum value, then reverses and begins to rise again. (S007). In the present invention, the rotation of the rotary shaft 5 is stopped immediately after the rotation torque starts to rise again (S008). In the present invention, the temperature in the agitation chamber 3 continues to rise even while the rotational torque fluctuates from rising → lowering → rising, but in the melt mixing, the thermal decomposition temperature of the material to be kneaded after re-raising the rotating torque. It is preferable to stop before reaching. After the rotation is stopped, the take-out portion 17 is opened and the mixed melt of bamboo powder and resin is taken out (S009). Then, it is cooled in the air and solidified. This mixed melt is an inevitable process of manufacturing the bamboo powder composite resin, and the chips crushed in (S011) in FIG. 9 described later correspond to pellets of a normal resin raw material. Such a mixture melted at high temperature and high pressure is called a bamboo powder resin mixed melt. Bamboo powder resin mixed melts include those that have been heated, cooled, processed and deformed after mixing and melting, and those that have been mixed with other resins.

溶融混合の際、竹粉と樹脂からなる被混練物は酸化分解から保護されている必要がある。特に、酸素による酸化の抑制は、被混練物の構造物性変化を抑制するために重要である。そのため、本発明の竹粉複合樹脂の製造方法においては、水蒸気の解放機構20において、水蒸気の流出入の均衡を保った状態、すなわち、撹拌室3内部から流出する水蒸気と外部から撹拌室内へ流入する空気とが解放機構20で釣り合い均衡状態を保つことにより、撹拌室3内部への空気の流入を防ぐようにすることが好ましい。本発明の製造方法においては、混合開始直後、撹拌室3内の圧力は急激に上昇し、その時点では、水蒸気の解放機構20において、水蒸気の流出入は均衡を保った状態にはなく、撹拌室3内部の水蒸気は解放機構より外部に流出する。この間、撹拌室内部の圧力は減少傾向を示し、最終的に均衡状態に達して、一定圧力を保持するようになる。また、本発明の製造方法においては、撹拌室3内部が水の亜臨界状態となることがある。水の亜臨界状態とは、水の超臨界点(温度375℃、圧力22.00MPa)よりも低い状態をいい、亜臨界水は酸化性が非常に強い。 During melt mixing, the material to be kneaded, which is composed of bamboo powder and resin, must be protected from oxidative decomposition. In particular, suppression of oxidation by oxygen is important for suppressing changes in the physical properties of the material to be kneaded. Therefore, in the method for producing a bamboo powder composite resin of the present invention, in the steam releasing mechanism 20, a state in which the steam inflow and outflow are balanced, that is, the steam flowing out of the stirring chamber 3 and flowing into the stirring chamber from the outside. It is preferable to prevent the inflow of air into the stirring chamber 3 by maintaining a balanced state of balance with the air to be released by the release mechanism 20. In the production method of the present invention, immediately after the start of mixing, the pressure in the stirring chamber 3 rapidly rises, and at that time, the steam inflow and outflow is not in a balanced state in the steam releasing mechanism 20, and the stirring is not performed. The water vapor inside the chamber 3 flows out from the release mechanism. During this time, the pressure inside the stirring chamber tends to decrease and finally reaches an equilibrium state to maintain a constant pressure. Further, in the manufacturing method of the present invention, the inside of the stirring chamber 3 may be in a subcritical state of water. The subcritical state of water is a state lower than the supercritical point of water (temperature 375° C., pressure 22.00 MPa), and the subcritical water has a very strong oxidizing property.

本発明の竹粉樹脂混合溶融体の製造方法においては、撹拌室の圧力を保持した状態で、回転トルクが極小値を示した直後、すなわち、極小値を示してから、少なくとも1秒から10分、より好ましくは1秒から2分、さらに好ましくは1秒から30秒、酸素の流入を防止し、竹粉と樹脂を酸素酸化や水和による分解から保護しながら溶融混合を行うことが好ましい。また、装置の強度の問題から、撹拌室内の圧力が23.00MPa付近より高いと、急激な圧力上昇に耐え切れず撹拌室そのものが破損する等のトラブルが発生する確率が高くなる。装置の強度を上げればよいが、そのための費用が非常にかかるため経済的に好ましくない。 In the manufacturing method of the bamboo powder resin mixed melt of the present invention, at least 1 second to 10 minutes immediately after the rotational torque shows the minimum value in the state where the pressure in the stirring chamber is maintained, that is, after the minimum value is shown. It is preferable to perform the melt mixing for 1 second to 2 minutes, more preferably for 1 second to 30 seconds while preventing the inflow of oxygen and protecting the bamboo powder and the resin from decomposition by oxygen oxidation or hydration. Further, due to the problem of the strength of the apparatus, if the pressure in the stirring chamber is higher than around 23.00 MPa, there is a high probability that troubles such as the stirring chamber itself being damaged without being able to withstand a rapid pressure increase will occur. Although it is necessary to increase the strength of the device, it is economically not preferable because the cost is very high.

図9は竹粉樹脂混合溶融体から竹粉複合樹脂への製造方法の手順の例を説明する図である。まず、粉砕機を用いて混合溶融体を粉砕する(S011)。次に、粉砕された混合溶融体を成形機に投入して成形する(S012)。この竹粉複合樹脂を使用すると、押し出し成形、プレス成形の他に、射出成形も可能である。このようにして、成形体を得ることができる(S013)。このように、竹粉樹脂混合溶融体から粉砕、成形されたものを竹粉複合樹脂という。なお、成形後に加熱、冷却、加工、変形されたもの、他の樹脂に他の樹脂に混入されたものも竹粉複合樹脂に含まれる。
密閉型混合粉砕装置において高濃度の竹粉を混合溶融体として製造し、粉砕ペレット化しておけば、これと通常の純粋樹脂ペレットと適切な割合で混合して、樹脂成型機に掛ければ竹粉複合濃度の異なる(濃度の低い)竹粉複合樹脂成形体を製造することが出来る。
かかる竹粉複合樹脂からなる成形体は、従来の木紛複合樹脂に比較して曲げ強度が高く、成形性も良いことから、食器、トレーに限られず、家具、建材、玩具に使用でき、乗り物、電子機器、電子部品、楽器、医療機器等への応用も期待される。
特に航空機の機体に多用され、乗用車にも用途拡大しつつある強化プラスチックに使用されている熱硬化性プラスチックの代替への期待が高まっており、強化プラスチック協会との連携で試作が始まる可能性が高まっている。実現すればコストダウンのみならず、熱可塑性プラスチックなのでリサイクルも可能となり、地球温暖化対策にも貢献できる。
FIG. 9: is a figure explaining the example of the procedure of the manufacturing method from a bamboo powder resin mixed melt to a bamboo powder composite resin. First, the mixed melt is crushed using a crusher (S011). Next, the pulverized mixed melt is put into a molding machine and molded (S012). When this bamboo powder composite resin is used, injection molding is possible in addition to extrusion molding and press molding. In this way, a molded body can be obtained (S013). Thus, what is crushed and molded from the bamboo powder resin mixed melt is called bamboo powder composite resin. Bamboo powder composite resins include those that are heated, cooled, processed and deformed after molding, and those that are mixed with other resins in other resins.
If high-concentration bamboo powder is produced as a mixed melt in a closed-type mixing and pulverizing device and crushed and pelletized, it is mixed with normal pure resin pellets at an appropriate ratio, and then applied to a resin molding machine to produce bamboo powder. Bamboo powder composite resin moldings having different composite concentrations (low concentrations) can be produced.
Molded products made from such a bamboo powder composite resin have higher bending strength and better moldability than conventional wood powder composite resins, so they can be used not only for tableware and trays but also for furniture, building materials, toys, and vehicles. It is also expected to be applied to electronic equipment, electronic parts, musical instruments, medical equipment, etc.
In particular, there is growing hope for a substitute for the thermosetting plastics used in reinforced plastics that are widely used in aircraft fuselage and are expanding in use in passenger cars, and it is possible that prototypes will begin in collaboration with the Reinforced Plastics Association. It is rising. If realized, not only will costs be reduced, but it will also be possible to recycle because it is a thermoplastic, which will contribute to global warming countermeasures.

本発明において、竹粉複合樹脂は竹粉を複合する量次第で、曲げ強度・引張強度・耐熱性等で物性強度が1.5倍〜4倍に増す。従って従来添加剤により強度増加を図るために添加剤を入れていた場合は、竹粉による強度増により添加剤を減量することができる。また竹粉複合により衝撃性の低下が起きることがあり、この場合は竹粉と樹脂以外の各種添加剤を適宜加えることで、ゴム系のエラストマーを添加するか、竹粉量を増やすことなどで補うことができる。 In the present invention, the bamboo powder composite resin has a physical strength increased by 1.5 to 4 times in bending strength, tensile strength, heat resistance, etc. depending on the amount of the bamboo powder composited. Therefore, when an additive is conventionally added to increase the strength by the additive, the amount of the additive can be reduced by increasing the strength with the bamboo powder. In addition, the impact resistance may decrease due to the combination of bamboo powder, and in this case, by adding various additives other than bamboo powder and resin appropriately, it is possible to add a rubber elastomer or increase the amount of bamboo powder. Can be supplemented.

次に本発明を実施例によりさらに詳細に説明するが、本発明はこれらに何ら限定されるものではない。
本発明で用いる竹粉は、天然竹粉の枝葉を除いた竹稈を特殊竹粉製造機31で粉砕した多孔質保持の微細竹粉である。竹維管束の多孔質が保持されている粉末で平均粒度約300μmの竹粉である。含水率は約35%である。
かかる竹粉を樹脂(PE又はPP)粉末と共に密閉型混合粉砕装置1の撹拌室3に投入し、混合溶融して竹粉樹脂混合溶融体を得た。
Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited thereto.
The bamboo powder used in the present invention is a fine bamboo powder that retains its porosity obtained by crushing bamboo culms excluding the branches and leaves of natural bamboo powder with a special bamboo powder manufacturing machine 31. It is a powder that retains the porosity of the bamboo vascular bundle and has an average particle size of about 300 μm. The water content is about 35%.
The bamboo powder and the resin (PE or PP) powder were put into the stirring chamber 3 of the closed type mixing and pulverizing apparatus 1 and mixed and melted to obtain a bamboo powder resin mixed melt.

得られた竹粉樹脂混合溶融体を、破砕機を用いて25mm程度に破砕して竹粉樹脂混合溶融体ペレットを得た。得られた竹粉樹脂混合溶融体ペレット各を射出成形機に各々投入し、射出成形して板状の試験片を得た。そして、JIS規格に従って、各試験片の破断直前の最大荷重(曲げ弾性率)等を測定し、表1に併記した。 The obtained bamboo powder resin mixed melt was crushed to about 25 mm using a crusher to obtain bamboo powder resin mixed melt pellets. Each of the obtained bamboo powder resin mixed melt pellets was placed in an injection molding machine and injection-molded to obtain a plate-shaped test piece. Then, according to the JIS standard, the maximum load (flexural modulus) immediately before fracture of each test piece was measured, and the results are shown in Table 1.

Figure 0006739047
Figure 0006739047

表1は竹粉複合による樹脂の物性強度増加の例を示す表である。
竹粉複合により、PP(ポリプロピレン)100%、竹粉60%−PP40%、竹粉70%−PP30%と竹粉含有率の増加とともに、MFR(マテリアルフロー)は低下するが、密度・引張降伏強さ・曲げ弾性率・曲げ強さは上昇しており、引張・曲げ強さは向上することがわかる。特に曲げ弾性率については、竹粉70%で4170MPaとPP100%に比して4倍以上になっている。また、竹粉含有率の増加とともに、衝撃強さ(デュロメータ硬さ)は低下するが、添加剤(エラストマー)の増加又は竹粉量の増加により復元する、表面硬さは軟化する、荷重たわみ温度は高くなる。
Table 1 is a table showing an example of the increase in the physical strength of the resin due to the composite of bamboo powder.
With the combination of bamboo powder, PP (polypropylene) 100%, bamboo powder 60%-PP40%, bamboo powder 70%-PP30%, and MFR (material flow) decrease with increasing bamboo powder content, but density and tensile yield It can be seen that the strength, flexural modulus, and flexural strength have increased, while the tensile and flexural strength has improved. In particular, the bending elastic modulus of bamboo powder 70% is 4170 MPa, which is four times or more that of PP 100%. Moreover, impact strength (durometer hardness) decreases with an increase in the content of bamboo powder, but it is restored by an increase in the amount of additives (elastomer) or the amount of bamboo powder, the surface hardness softens, the deflection temperature under load. Will be higher.

図10に竹粉複合樹脂の電子顕微鏡写真の例を示す。竹粉70%とPP30%を混合溶融させた複合樹脂の写真である。図右下のスケールの全長が50μmである。竹粉とPPを水の亜臨界状態で混合溶融させると、竹粉の多孔質の孔にPPが入り込み、常温に戻るときに固化する。これにより、樹脂単体としての力学特性と熱特性が向上する。熱特性については表1の荷重たわみ温度がPP100%では91℃であるが竹粉70%では149℃と大幅に向上していることで示されている。
すなわち、竹粉含有率の増加は曲げ強度を上げ、熱特性を向上させ、同時に抗菌性を発揮する。
FIG. 10 shows an example of an electron micrograph of the bamboo powder composite resin. It is a photograph of a composite resin obtained by mixing and melting bamboo powder 70% and PP 30%. The total length of the scale at the lower right of the figure is 50 μm. When bamboo powder and PP are mixed and melted in a subcritical state of water, PP enters the porous pores of bamboo powder and solidifies when the temperature returns to room temperature. As a result, the mechanical properties and thermal properties of the resin alone are improved. Regarding the thermal characteristics, it is shown that the deflection temperature under load in Table 1 is 91°C when PP is 100%, but is significantly improved to 149°C when bamboo powder is 70%.
That is, the increase in the content of bamboo powder increases the bending strength, improves the thermal characteristics, and simultaneously exhibits the antibacterial property.

図10に示すように、本実施例に係る竹粉複合樹脂では微細竹粉の多孔質部分まで熱可塑性のプラスチックが溶融浸潤されている。従来のFRP(炭素繊維強化プラスチック)では炭素繊維網にプラスチックを浸潤させるのはかなり困難であり、このため航空機のボデイに使用するシート状にするのも相当困難であると推測される。しかしながら、本実施例では溶融混合段階で既に微細竹粉にプラスチックが浸潤されており、射出成型可能なので、シート状にすることも容易と推測される。また、FRPは熱硬化性のエポキシ樹脂等を使用するので、リサイクルできないが、本実施例では熱可塑性樹脂を使用するのでリサイクル可能であり、環境省が地球温暖化ガス対策に推奨するリサイクル可能型バイオマスプラスチックの利用拡大に大いに寄与できる。
竹粉複合量が変わる都度、密閉型混合粉砕装置で竹粉樹脂混合溶融体を製造するよりも、竹粉濃度を70%以上でも可能な高濃度に混合溶融体を標準として製造し、これをマザーペレットとして、成型機にて成型時に樹脂をしかるべき量を添加して成形体の竹粉複合量の異なるものを得ることが出来る。
As shown in FIG. 10, in the bamboo powder composite resin according to this example, the thermoplastic plastic was melt-infiltrated to the porous portion of the fine bamboo powder. With conventional FRP (carbon fiber reinforced plastic), it is quite difficult to infiltrate the plastic into the carbon fiber network, and therefore it is presumed that it is considerably difficult to form a sheet for use in the body of an aircraft. However, in this embodiment, since the fine bamboo powder has been infiltrated with the plastic at the melt mixing stage and injection molding is possible, it is presumed that it is easy to form a sheet. Further, FRP cannot be recycled because it uses a thermosetting epoxy resin, but in this example, it is recyclable because it uses a thermoplastic resin, and is a recyclable type recommended by the Ministry of the Environment as a measure against global warming gas. It can greatly contribute to expanding the use of biomass plastics.
Each time the combined amount of bamboo powder changes, a mixed melt is manufactured as a standard to a high concentration that allows a bamboo powder concentration of 70% or more, rather than a bamboo powder resin mixed melt produced by a closed-type mixing and pulverizing device. As the mother pellets, a proper amount of resin can be added at the time of molding by a molding machine to obtain molded bodies having different combined amounts of bamboo powder.

本発明の竹粉樹脂混合溶融体を用いて、各種成形方法により成形体を製造することができる。成形方法としては、一般的な成形方法を用いることができ、特に制限されない。例えば、射出成形法、押出成形法、圧縮成形法、回転成形法、中空成形法(ブロー成形法)、ダイ成形法、インフレーション成形法、カレンダー成形法等を挙げることができるが、これらの方法に制限されることはない。また、成形体の形状も特に制限されず、どのような形状のものを、どのような成形方法で製造してもよい。物性・品質等を総合的に判断して竹粉の複合量を判断することが重要である。 A molded body can be manufactured by various molding methods using the bamboo powder resin mixed melt of the present invention. As a molding method, a general molding method can be used and is not particularly limited. For example, injection molding method, extrusion molding method, compression molding method, rotational molding method, hollow molding method (blow molding method), die molding method, inflation molding method, calender molding method and the like can be mentioned. There is no limit. Further, the shape of the molded body is not particularly limited, and any shape may be manufactured by any molding method. It is important to judge the composite amount of bamboo powder by comprehensively judging the physical properties and quality.

図11に竹粉複合樹脂からなる成形体40の写真の例を示す。
竹粉70%−PP30%において、図中の試験片のような複雑な形状でも、容易に射出成型可能である。
実施例の結果から、本製造方法により得られた竹粉樹脂混合溶融体である熱可塑性樹脂組成物は、射出成形により問題なく成形を行うことができ、優れた成形性を有していた。
FIG. 11 shows an example of a photograph of a molded body 40 made of a bamboo powder composite resin.
Bamboo powder 70%-PP30% can be easily injection-molded even with a complicated shape such as the test piece in the figure.
From the results of the examples, the thermoplastic resin composition, which is the bamboo powder resin mixed melt obtained by the present production method, could be molded by injection molding without any problem, and had excellent moldability.

木材と樹脂との複合材料は、従来はウッドプラスチックとして世の中に知られていた。しかしながら、木材と樹脂の親和性は大きくなく、せいぜい木材の含有率は30〜50%止まりであった。また、溶融せず、混在しているだけなので、成形方法が単純なプレス成形や押し出し成形に限られ、射出成形はできなかった。 The composite material of wood and resin was conventionally known as wood plastic. However, the affinity between wood and resin is not so great that the content of wood is at most 30 to 50%. Further, since they are not melted but only mixed, the molding method is limited to simple press molding and extrusion molding, and injection molding cannot be performed.

ところが、竹材を用いると、60〜70%混入でき、さらに60〜70%においても射出成形が可能になる。また竹材は水分が35%と大きいが、混合溶融時に高温になり揮発するので問題ない。それどころか、水分がないと圧力が上がらないので、混合溶融に不利である。かえってある程度は水分を含んでいた方が良いのである。また、竹材を混入するとプラスチックの強度が上がる。高機能プラスチックとなる。さらに、竹材の含有率を多くすることができるので、新規・多様な、高機能プラスチックを開発できる可能性が広がった。また、EUでは生分解能を有する複合樹脂の開発が進んでいるが、ポリ乳酸と竹を組み合わせると、生分解能を維持でき、EUの規格にも適合できるようになり、望ましい方向にある。また、プラスチックについても、ポリエチレン、ポリプロピレンだけでなく、熱可塑性プラスチック全般に適用できる。また、本発明をバイオマスプラスチックに利用すると、一般社団法人日本有機資源協会、一般財団法人バイオインダストリアル協会のバイオマス資源の規格の範囲、製品の種類を拡大できる。また、射出成型が可能なので、多様な成形に適用でき、飛躍的に用途も拡大できる。そして、製品開発のコストアップを小さくできる。 However, when bamboo material is used, 60 to 70% can be mixed, and even 60 to 70% can be injection-molded. Further, the bamboo material has a large water content of 35%, but there is no problem because it volatilizes at a high temperature when mixed and melted. On the contrary, the pressure does not rise without water, which is disadvantageous for mixing and melting. On the contrary, it is better to contain water to some extent. Moreover, the strength of plastic increases when bamboo is mixed. High-performance plastic. Furthermore, since the content of bamboo can be increased, the possibility of developing new and diverse high-performance plastics has expanded. Further, in EU, a composite resin having biodegradability is under development, but when polylactic acid and bamboo are combined, the biodegradability can be maintained and the standard of EU can be satisfied, which is in a desirable direction. As for plastics, not only polyethylene and polypropylene but also thermoplastics in general can be applied. When the present invention is applied to biomass plastics, the scope of biomass resource standards and product types of the Japan Organic Resources Association and the Bioindustrial Association can be expanded. Also, since injection molding is possible, it can be applied to various moldings, and the applications can be dramatically expanded. And the cost increase of product development can be reduced.

以上により、本発明によれば、内部に多孔質を持ち、粒度が大きくかつ水分含有率が高い竹粉を用い、セルロース系材料の含有率の高い竹粉複合樹脂、竹粉樹脂混合溶融体及びこれらの製造方法を提供することができる。また、製造できる新な複合樹脂の範囲を拡大することができ、そして、強度特性が良好でかつ再成形可能な成形体を提供することができる。 As described above, according to the present invention, a bamboo powder composite resin having a high content rate of a cellulosic material, a bamboo powder resin mixed melt, and a porous material having a large particle size and a high water content rate are used according to the present invention. It is possible to provide these manufacturing methods. In addition, the range of new composite resins that can be manufactured can be expanded, and a molded product that has good strength characteristics and can be remolded can be provided.

本発明は、成形体の強度特性が良好でかつ再成形可能なセルロース複合樹脂に利用できる。また、建材や乗り物の材料として利用できる。 INDUSTRIAL APPLICABILITY The present invention can be utilized for a remoldable cellulose composite resin in which the molded body has good strength characteristics. It can also be used as a building material or a vehicle material.

1 密閉型混合粉砕装置
2 機台ベース
3 撹拌室
4 軸受
5 回転軸
6 プーリー
7 Vベルト
8 モーター
10a〜10f 回転羽根
11 撹拌室の垂直壁
12 らせん状羽根部材
13 材料供給室
14 材料投入部
15 シャッター
17 取出部
20 水蒸気の解放機構
21 制御盤
22 らせん状溝
23 水蒸気流出方向
24 空気流入方向
31 特殊竹粉製造機
32 フライス工具
33 フライスカッター
34 チップ
35 フライス工具本体の端面
36 カッター駆動部
37 竹素材送り機構
38 支持手段
39 基台
40 成形体
I 回転トルクの最小値
M 回転トルクの最大値
t 回転トルクが最小値に達した後の一定時間
tI 回転トルクが最小値のときの時間
tM 回転トルクが最大値のときの時間
T 回転トルク
W 竹素材
X 回転中心の軸線
Y 竹素材の移動方向
Z フライスカッターの回転方向

1 Closed Type Mixing and Grinding Device 2 Machine Base 3 Stirring Chamber 4 Bearing 5 Rotating Shaft 6 Pulley 7 V Belt 8 Motors 10a to 10f Rotating Blade 11 Vertical Wall 12 of Stirring Chamber 12 Helical Blade Member 13 Material Supply Chamber 14 Material Feeding Port 15 Shutter 17 Extraction part 20 Water vapor release mechanism 21 Control panel 22 Helical groove 23 Water vapor outflow direction 24 Air inflow direction 31 Special bamboo powder making machine 32 Milling tool 33 Milling cutter 34 Tip 35 End face of milling tool body 36 Cutter driving part 37 Bamboo Material feeding mechanism 38 Support means 39 Base 40 Formed body I Minimum value of rotational torque M Maximum value of rotational torque t Constant time after rotational torque reaches minimum value tI Time when rotational torque is minimum value tM Rotational torque Is the maximum time T Rotation torque W Bamboo material X Axis of rotation Y Y Bamboo material movement direction Z Milling cutter rotation direction

Claims (6)

複数の回転羽根が配設された回転軸を有する密閉型の攪拌室内で、樹脂粉末と竹粉を原 料として、前記回転軸を回転させて溶融混合して竹粉樹脂混合溶融体を製作し、前記竹粉 樹脂混合溶融体を成形して竹粉複合樹脂を製造する竹粉複合樹脂の製造方法において;
前記竹粉は、平均粒度が1μm以上800μm以下に粉砕され、水分含水率が5〜40 質量%の竹粉であり、前記溶融混合時の前記攪拌室内の温度が150℃以上370℃以下、圧力が0.20MPa以上飽和水蒸気以下で、かつ、前記回転軸の回転トルクが下降して極小値に達し、さらに上昇に転じた直後に前記回転を停止させて竹粉樹脂混合溶融体を製作し、さらに前記竹粉樹脂混合溶融体を粉砕し、成形して竹粉複合樹脂を製造することを特徴とし;
前記竹粉と前記樹脂粉末の重量比が5:95〜70:30である;
竹粉複合樹脂の製造方法。
In a closed type stirring chamber having a rotary shaft with a plurality of rotary blades, resin powder and bamboo powder are used as raw materials, and the rotary shaft is rotated to melt and mix to produce a bamboo powder resin mixed melt. In the method for producing a bamboo powder composite resin, the bamboo powder resin mixed melt is molded to produce a bamboo powder composite resin;
The bamboo powder is a bamboo powder having an average particle size of 1 μm or more and 800 μm or less and a water content of 5 to 40% by mass, and the temperature in the stirring chamber at the time of the melt mixing is 150° C. or more and 370° C. or less, and pressure. Is 0.20 MPa or more and saturated water vapor or less, and the rotation torque of the rotary shaft decreases to reach a minimum value, and immediately after the rotation torque starts to increase, the rotation is stopped to produce a bamboo powder resin mixed melt, Further, the bamboo powder resin mixed melt is pulverized and molded to produce a bamboo powder composite resin ;
The weight ratio of the bamboo powder and the resin powder is 5:95 to 70:30;
Bamboo powder composite resin manufacturing method.
前記竹粉は、切れ刃であるチップが取り付けられる工具本体の端面に、複数個のチップ を放射状に並べて延びたチップ列を周方向に複数列備え、隣接する一対のチップ列のチッ プそれぞれが、回転中心軸からの径方向距離を交互に異にした千鳥状に配設されているフ ライス工具を用いて粉砕された微細粉末であり、電子顕微鏡写真により竹維管束の多孔質 構造が観測され、内部に10〜1011/gの乳酸菌が生育することを特徴とする;
請求項1に記載の竹粉複合樹脂の製造方法。
The bamboo powder is provided with a plurality of rows of chips in the circumferential direction, which are formed by arranging a plurality of chips in a radial pattern on the end surface of the tool body to which the chips, which are cutting edges, are attached. , A fine powder crushed by using a stylus-shaped friece tool arranged in different radial distances from the rotation center axis, and the porous structure of the bamboo vascular bundle was observed by an electron micrograph. is characterized in that the lactic acid bacteria of the interior 10 3 ~10 11 / g are growing;
The method for producing the bamboo powder composite resin according to claim 1.
複数の回転羽根が配設された回転軸を有する密閉型の攪拌室内で、樹脂粉末と竹粉を原 料として、前記回転軸を回転させて溶融混合して竹粉樹脂混合溶融体を製造する竹粉樹脂混合溶融体の製造方法において;
前記竹粉は、平均粒度が1μm以上800μm以下に粉砕され、水分含水率が5〜40質量%の竹粉であり、前記溶融混合時の前記攪拌室内の温度が150℃以上370℃以下、圧力が0.20MPa以上飽和水蒸気以下で、かつ、前記回転軸の回転トルクが下降して極小値に達し、さらに上昇に転じた直後に前記回転を停止させて竹粉樹脂混合溶融体を製作することを特徴とし;
前記竹粉と前記樹脂粉末の重量比が5:95〜70:30である;
竹粉樹脂混合溶融体の製造方法。
In sealed stirring chamber having an axis of rotation in which a plurality of rotating blades are provided, the resin powder and bamboo powder as raw materials, the production of bamboo powder resin mixture melt was melt-mixed by rotating the rotary shaft In the manufacturing method of the bamboo powder resin mixed melt ;
The bamboo powder is a bamboo powder having an average particle size of 1 μm or more and 800 μm or less and a moisture content of 5 to 40% by mass, and the temperature in the stirring chamber at the time of the melt mixing is 150° C. or more and 370° C. or less and pressure. Is 0.20 MPa or more and saturated water vapor or less, and the rotation torque of the rotary shaft decreases to reach a minimum value, and immediately after the rotation torque increases, the rotation is stopped to produce a bamboo powder resin mixed melt. Characterized by;
The weight ratio of the bamboo powder and the resin powder is 5:95 to 70:30;
Bamboo powder resin mixed melt manufacturing method.
前記竹粉は、切れ刃であるチップが取り付けられる工具本体の端面に、複数個のチップ を放射状に並べて延びたチップ列を周方向に複数列備え、隣接する一対のチップ列のチッ プそれぞれが、回転中心軸からの径方向距離を交互に異にした千鳥状に配設されているフ ライス工具を用いて粉砕された微細粉末であり、電子顕微鏡写真により竹維管束の多孔質 構造が観測され、内部に10〜1011/gの乳酸菌が生育することを特徴とする;
請求項3に記載の竹粉樹脂混合溶融体の製造方法。
The bamboo powder is provided with a plurality of rows of chips in the circumferential direction, which are formed by arranging a plurality of chips in a radial pattern on the end surface of the tool body to which the chips, which are cutting edges, are attached. , A fine powder crushed by using a stylus-shaped friece tool arranged in different radial distances from the rotation center axis, and the porous structure of the bamboo vascular bundle was observed by an electron micrograph. is characterized in that the lactic acid bacteria of the interior 10 3 ~10 11 / g are growing;
A method for producing the bamboo powder resin mixed melt according to claim 3.
竹紛と樹脂粉末が、高温・高圧で混合溶融されて、混じり合い一体化した竹粉樹脂混合溶融体であって;
前記高温・高圧で混合溶融される時の温度範囲は150〜370℃であり、圧力範囲 は0.20MPa〜溶融混合温度における飽和水蒸気圧であり、
微細竹粉の多孔質部分まで熱可塑性の樹脂が溶融浸潤されており、前記竹粉と前記樹脂粉末の重量比が5:95〜70:30であることを特徴とする;
竹粉樹脂混合溶融体。
A bamboo-powder-resin mixed melt in which bamboo powder and resin powder are mixed and melted at high temperature and high pressure, and mixed and integrated;
The temperature range at the time of mixing and melting at the high temperature and high pressure is 150 to 370° C., the pressure range is 0.20 MPa to the saturated steam pressure at the melting and mixing temperature,
The thermoplastic resin is melt-infiltrated to the porous portion of the fine bamboo powder, and the weight ratio of the bamboo powder and the resin powder is 5:95 to 70:30;
Bamboo powder resin mixed melt.
請求項5に記載の竹粉樹脂混合溶融体を粉砕し、射出成形して製造することを特徴とする;The bamboo powder resin-mixed melt according to claim 5 is crushed and injection-molded to produce the product.
竹粉複合樹脂の製造方法。Bamboo powder composite resin manufacturing method.
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