JP6561537B2 - MOLDING MATERIAL AND METHOD FOR PRODUCING MOLDING MATERIAL - Google Patents
MOLDING MATERIAL AND METHOD FOR PRODUCING MOLDING MATERIAL Download PDFInfo
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- 238000004880 explosion Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 9
- 238000005422 blasting Methods 0.000 claims description 7
- 238000010025 steaming Methods 0.000 claims description 3
- 238000000227 grinding Methods 0.000 claims description 2
- 238000007561 laser diffraction method Methods 0.000 claims description 2
- 238000002356 laser light scattering Methods 0.000 claims description 2
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
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- 241001442228 Eucalyptus grandis x Eucalyptus urophylla Species 0.000 description 4
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
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- 244000193510 Larix occidentalis Species 0.000 description 2
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- YSGSDAIMSCVPHG-UHFFFAOYSA-N valyl-methionine Chemical compound CSCCC(C(O)=O)NC(=O)C(N)C(C)C YSGSDAIMSCVPHG-UHFFFAOYSA-N 0.000 description 2
- 241000208140 Acer Species 0.000 description 1
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- 229920002488 Hemicellulose Polymers 0.000 description 1
- 241000218652 Larix Species 0.000 description 1
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- 239000004640 Melamine resin Substances 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 241000218595 Picea sitchensis Species 0.000 description 1
- 235000008565 Pinus banksiana Nutrition 0.000 description 1
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- 241001236215 Pinus parviflora Species 0.000 description 1
- 235000008577 Pinus radiata Nutrition 0.000 description 1
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- 241001600434 Plectroglyphidodon lacrymatus Species 0.000 description 1
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- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
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- 241000736892 Thujopsis dolabrata Species 0.000 description 1
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- 241000190021 Zelkova Species 0.000 description 1
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- 229920006167 biodegradable resin Polymers 0.000 description 1
- QUDWYFHPNIMBFC-UHFFFAOYSA-N bis(prop-2-enyl) benzene-1,2-dicarboxylate Chemical compound C=CCOC(=O)C1=CC=CC=C1C(=O)OCC=C QUDWYFHPNIMBFC-UHFFFAOYSA-N 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
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- 238000010101 extrusion blow moulding Methods 0.000 description 1
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- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000017985 rocky mountain lodgepole pine Nutrition 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
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Landscapes
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Description
本発明は、木質系バイオマスを原料とする成形用材料、及びその製造方法に関するものである。 The present invention relates to a molding material using woody biomass as a raw material and a method for producing the same.
産業資源として、木材に代表されるバイオマス材が注目されている。バイオマス材とは、植物などの生物を由来とした材料を意味する。バイオマス材は有機物であるため、燃焼させると二酸化炭素が排出される。しかしこれに含まれる炭素は、そのバイオマスが成長過程で光合成により大気中から吸収した二酸化炭素に由来するため、バイオマス材を使用しても全体として見れば大気中の二酸化炭素量を増加させていないと考えてよいとされる。この性質をカーボンニュートラルと呼ぶ。 Biomass materials represented by wood are attracting attention as industrial resources. The biomass material means a material derived from a living organism such as a plant. Since the biomass material is organic, carbon dioxide is emitted when it is burned. However, the carbon contained in this is derived from carbon dioxide absorbed from the atmosphere by photosynthesis during the growth process, so using biomass materials does not increase the amount of carbon dioxide in the atmosphere as a whole It can be considered that. This property is called carbon neutral.
地球温暖化問題等の地球環境問題を背景として、省資源化、及び廃棄物の原材料を目指すマテリアルリサイクル、そして、生分解性プラスチックに代表される環境循環サイクルの推進が急務となっており、我が国でも改正リサイクル法やグリーン購入法等が整備され、これに対応した製品のニーズも高まっている。 Against the backdrop of global environmental issues such as global warming issues, there is an urgent need to conserve resources, material recycling aiming at raw materials for waste, and promotion of the environmental circulation cycle represented by biodegradable plastics. However, the revised Recycling Law and the Green Purchasing Law have been put in place, and the need for products that respond to these laws is increasing.
こうした状況において、自動車部品の材料から日用品まで幅広く使用されている樹脂成型品にバイオマス材を配合することは、カーボンニュートラルの理念の実践を促進するところであり、バイオマス材として最も多量に存在する木材を成形用材料として使用する、あるいは他の樹脂材料に配合することは、近年の環境循環サイクルの推進に合致するところである。 Under these circumstances, blending biomass materials into resin molded products that are widely used from automotive parts materials to daily necessities promotes the practice of the carbon neutral philosophy. Use as a molding material or blending with other resin materials is in line with the promotion of environmental circulation cycles in recent years.
しかしながら、木材を処理することなくそのまま粉砕したものでは、成形性が不十分であり、他の熱可塑性樹脂との混合も困難である。そこで、特許文献1には、木質系材料を水蒸気存在下で加熱および加圧後急激に減圧して爆砕し得られる粉末状の爆砕材料、樹脂、粉末状の木質系材料とを混合して成形することにより木質系成形体を製造する方法、特許文献2には、リグノセルロース含有材料を水蒸気処理(爆砕処理も含まれる)して粒径が45μm以上180μm以下の粉末としたリグノセルロース系熱可塑性材料が記載されている。 However, if the wood is pulverized as it is without being treated, the moldability is insufficient and mixing with other thermoplastic resins is difficult. Therefore, in Patent Document 1, a woody material is heated and pressurized in the presence of water vapor and then mixed with a powdery explosion material, a resin, and a powdery woody material obtained by abrupt decompression and explosion. Patent Document 2 discloses a method for producing a wood-based molded body by performing steam treatment (including explosive treatment) on a lignocellulose-containing material to obtain a powder having a particle size of 45 μm or more and 180 μm or less. The materials are listed.
しかしながら、特許文献1は未処理の粉末状の木質系材料を多量に含むため成形性が不十分であり、特許文献2のリグノセルロース系熱可塑性材料も成形性の点で不十分である。 However, since Patent Document 1 contains a large amount of untreated powdery woody material, the moldability is insufficient, and the lignocellulosic thermoplastic material of Patent Document 2 is also insufficient in terms of moldability.
そこで、本発明の課題は、木材を原料として成形性に優れる成形用材料を提供することである。 Then, the subject of this invention is providing the molding material which is excellent in a moldability from wood.
本発明者らは、木材を温度170〜230℃、圧力0.8〜3MPaで、5〜20分間、水蒸気処理した後、瞬時に圧解放して爆砕処理することによって得られ、平均粒径を30μm以下とした爆砕処理物が良好な成形性を有する成形用材料となることを見出した。 The inventors obtained a wood by steaming at a temperature of 170 to 230 ° C. and a pressure of 0.8 to 3 MPa for 5 to 20 minutes, and then instantaneously releasing the pressure to perform a blasting treatment. It has been found that an explosion-treated product having a size of 30 μm or less becomes a molding material having good moldability.
本発明によれば、木材質系バイオマスを原料として良好な成形性を有する成形用材料を得ることができる。 According to the present invention, a molding material having good moldability can be obtained using woody biomass as a raw material.
本発明は、木材を爆砕処理して得られる爆砕物から成る成形用材料である。本発明の爆砕処理は、木材を温度170〜230℃、圧力0.8〜3MPaで、保持時間5〜20分間水蒸気処理した後、瞬時に圧解放するものである。このような条件で爆砕処理を行うことにより、木材中のリグニンやヘミセルロースが部分的に分解及び/または変性することによって、粉砕性が向上し、結果的に微粒子化が容易となるので、成形用材料として好適となる。 The present invention is a molding material comprising a blasted product obtained by blasting wood. In the blasting treatment of the present invention, the wood is steam-treated at a temperature of 170 to 230 ° C. and a pressure of 0.8 to 3 MPa at a holding time of 5 to 20 minutes, and then the pressure is instantaneously released. By performing the blasting treatment under such conditions, lignin and hemicellulose in the wood are partially decomposed and / or modified, so that pulverization is improved, and as a result, micronization becomes easy. Suitable as a material.
温度が170℃未満であるとリグニンの分解が不十分となり粉砕性が十分に向上しない。また、230℃を超えるとセルロースの分解が過度になり収率が低下する。 When the temperature is lower than 170 ° C., the lignin is not sufficiently decomposed and the pulverization property is not sufficiently improved. Moreover, when it exceeds 230 degreeC, decomposition | disassembly of a cellulose will become excessive and a yield will fall.
保持時間が5分以内であるとリグニンの分解が不十分となり粉砕性が十分に向上しない。また、20分を超えるとリグニンが縮合するためリグニンが分解し難くなり粉砕性が十分に向上しない。 When the holding time is within 5 minutes, the lignin is not sufficiently decomposed and the grindability is not sufficiently improved. On the other hand, if it exceeds 20 minutes, the lignin is condensed, so that the lignin is hardly decomposed and the grindability is not sufficiently improved.
本発明において、木材1質量部に対して水を0〜1000質量部添加して水蒸気処理を行うことが好ましい。 In the present invention, it is preferable to add 0 to 1000 parts by mass of water to 1 part by mass of wood to perform steam treatment.
原料の木材としては、例えば、広葉樹、針葉樹、のいずれもが使用できる。消化性の観点からは広葉樹が好ましい。具体的には、広葉樹としては、ブナ、シナ、シラカバ、ポプラ、ユーカリ、アカシア、ナラ、イタヤカエデ、センノキ、ニレ、キリ、ホオノキ、ヤナギ、セン、ウバメガシ、コナラ、クヌギ、トチノキ、ケヤキ、ミズメ、ミズキ、アオダモ等が例示される。針葉樹としては、スギ、エゾマツ、カラマツ、クロマツ、トドマツ、ヒメコマツ、イチイ、ネズコ、ハリモミ、イラモミ、イヌマキ、モミ、サワラ、トガサワラ、アスナロ、ヒバ、ツガ、コメツガ、ヒノキ、イチイ、イヌガヤ、トウヒ、イエローシーダー(ベイヒバ)、ロウソンヒノキ(ベイヒ)、ダグラスファー(ベイマツ)、シトカスプルース(ベイトウヒ)、ラジアータマツ、イースタンスプルース、イースタンホワイトパイン、ウェスタンラーチ、ウェスタンファー、ウェスタンヘムロック、タマラック等が例示される。 As the raw material wood, for example, either hardwood or softwood can be used. From the viewpoint of digestibility, hardwood is preferable. Specifically, the broad-leaved trees include beech, china, birch, poplar, eucalyptus, acacia, oak, itayaka maple, senoki, elm, giraffe, honoki, willow, sen, basamushi, konara, kunugi, tochinoki, zelkova, mizume, mizuzuki Aodamo etc. are exemplified. As conifers, cedar, spruce, larch, black pine, todomatsu, himekomatsu, yew, neko, spruce, iramimi, fir, sawara, togasawara, asunaro, hiba, tsuga, kotsutsuga, hinoki, yew, yellowtail, spruce (Beihiba), Lawson Hinoki (Beihi), Douglas Fir (Beimatsu), Sitka Spruce (Beisuhi), Radiata Pine, Eastern Spruce, Eastern White Pine, Western Larch, Western Fir, Western Hemlock, Tamarack and the like.
本発明において、原料の木材は0.1〜100mmのサイズに粉砕された粉砕物を使用することが好ましく、0.1〜50mmのサイズのものを使用することがさらに好ましい。なお、本発明において、木材の粉砕物のサイズとは、篩い分け器の円形の穴の大きさによって篩い分けされたものである。木材を粉砕するための装置としては、ナイフ切削型バイオマス燃料用チッパーで粉砕処理することが好ましい。また、樹皮が混入していてもよい。 In the present invention, the raw material wood is preferably a pulverized product pulverized to a size of 0.1 to 100 mm, more preferably 0.1 to 50 mm. In the present invention, the size of the pulverized product of wood is a size that is sieved according to the size of the circular hole of the sieve. As an apparatus for pulverizing wood, it is preferable to perform pulverization with a knife cutting type biomass fuel chipper. Moreover, the bark may be mixed.
爆砕処理を行うための装置としては、バルメット、日東高圧(株)、日本電熱(株)、(株)ヤスジマ、日本化学機械製造(株)のバッチ式の爆砕処理装置、あるいはバルメット、アンドリッツの連続式の爆砕処理装置等が挙げられる。 As a device for performing the explosion treatment, a batch type explosion treatment device of Valmet, Nitto High Pressure Co., Ltd., Nippon Electric Heat Co., Ltd., Yasima Co., Ltd., Nippon Chemical Machinery Manufacturing Co., Ltd., or Valmet, Andritz Examples include a continuous explosion treatment apparatus.
本発明において、爆砕処理物の平均粒径を30μm以下とする必要がある。なお、平均粒径とは、レーザー光散乱法(レーザー回折法)により測定した体積50%平均粒子径(D50)であり、レーザー回折/散乱式粒度分布測定器(マルバーン(株)製、機器名:マスターサイザー2000)等で測定することができる。爆砕物の平均粒径が30μmを超えると、成形性が低下する。 In the present invention, it is necessary that the average particle size of the blasted product is 30 μm or less. The average particle diameter is a 50% volume average particle diameter (D50) measured by a laser light scattering method (laser diffraction method), and is a laser diffraction / scattering type particle size distribution measuring instrument (Malvern Co., Ltd., product name). : Mastersizer 2000) or the like. If the average particle size of the blasted product exceeds 30 μm, the moldability is lowered.
爆砕処理物の平均粒径を30μm以下に粉砕するための装置としては、湿式粉砕機としては、マスコロイダー(増幸産業(株)製)、等、乾式粉砕機としては、セレンミラー(増幸産業(株)社製)、等、が挙げられる。 As an apparatus for pulverizing the average particle size of the crushed material to 30 μm or less, as a wet pulverizer, a mass colloider (manufactured by Masuko Sangyo Co., Ltd.), etc. Etc.).
本発明の成型用材料は、熱可塑性樹脂と混合して使用してもよい。で熱可塑性樹脂としては、例えば、ポリエチレン、ポリプロピレン、L−LDPEが挙げられるが、これらに限定されず、熱により可塑化し成形が可能である樹脂であればいずれも用いることができる。中でも、ポリエチレン及びポリプロピレンは成形性の観点から好ましい。 The molding material of the present invention may be used by mixing with a thermoplastic resin. Examples of the thermoplastic resin include, but are not limited to, polyethylene, polypropylene, and L-LDPE, and any resin that can be plasticized and molded by heat can be used. Among these, polyethylene and polypropylene are preferable from the viewpoint of moldability.
また、熱可塑性を有する生分解性樹脂と混合してもよく、例えば、ポリ乳酸(PLA)、ポリブチレンサクシネート、ポリエチレンサクシネート、ポリグリコール、ポリカプロラクトン、ポリビニルアルコール等、を使用できる。 Moreover, you may mix with the biodegradable resin which has thermoplasticity, for example, polylactic acid (PLA), polybutylene succinate, polyethylene succinate, polyglycol, polycaprolactone, polyvinyl alcohol etc. can be used.
また、熱硬化性樹脂と混合してもよく、例えば、フェノール樹脂、ユリア樹脂、メラミン樹脂、不飽和ポリエステル樹脂、エポキシ樹脂、ジアリルフタレート樹脂、ポリウレタン樹脂、ケイ素樹脂、ポリイミド樹脂等の熱硬化性樹脂等、を使用できる。 Further, it may be mixed with a thermosetting resin, for example, a thermosetting resin such as phenol resin, urea resin, melamine resin, unsaturated polyester resin, epoxy resin, diallyl phthalate resin, polyurethane resin, silicon resin, polyimide resin, etc. Etc., can be used.
本発明の成形用材料を用いて、種々の成形物品を製造することができる。成形には、熱可塑性樹脂の成形に用いられる通常の方法を用いることができ、例えば、これらに限定されないが、射出成形、押出成形、ブロー成形などを行うことができる。 Various molded articles can be produced using the molding material of the present invention. The molding can be performed by a usual method used for molding a thermoplastic resin. For example, but not limited to, injection molding, extrusion molding, blow molding and the like can be performed.
本発明の成形用材料は、各種フィルム、建築材料、容器、自動車の内装部品、等に使用することが可能である。 The molding material of the present invention can be used for various films, building materials, containers, automobile interior parts, and the like.
以下、本発明を実施例及び比較例をあげてより具体的に説明するが、本発明はこれらに限定されるものではない。なお、特に断らない限り、部および%は質量部および質量%を示す。 EXAMPLES Hereinafter, although an Example and a comparative example are given and this invention is demonstrated more concretely, this invention is not limited to these. In addition, unless otherwise indicated, a part and% show a mass part and mass%.
[実施例1]
ユーカリ ユーログランディスのチップをカッターミル(商品名:P−15、フリッチュ社製)で6mm以下に粉砕した。粉砕物の固形分100gに対して水を800g加え、蒸気爆砕装置(日東高圧(株)製)を用いて200℃まで加温し、圧力1.6MPa、10分間保持して水蒸気処理した後、瞬時に圧解放して爆砕処理を行った。得られた爆砕処理物に水を加えて濃度5%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMKG−C #80、増幸産業(株)製、クリアランス60μm)で粉砕した。得られた粉砕処理物の平均粒径を下記の方法にて測定し、結果を表1に示した。
次に粉砕処理物を超純水で濃度0.2%に希釈し、メンブレンフィルター(使用フィルター:ADVANTEC H020A047A(親水性PTFE)、pore0.2μm、Φ47mm)で濾過した。得られた濾過物を濾紙に挟んで50tプレスで、1回目:120℃、2kgf/cm2、10分、2回目:180℃、5kgf/cm2、10分、の2回のホットプレスを行い、成形物を得た。得られた成形物の成形性、密度を下記の方法にて測定し、結果を表1に示した。
・粉砕処理物の平均粒径:レーザー回折/散乱式粒度分布測定器(商品名:マスターサイザー2000、マルバーン(株)製)を用いて、体積累積分布の50%点を平均粒径とした。
・成形性:成形物を目視にて、以下の基準で成形性を評価した。◎;均一なシート状に成形できる、Δ;シート状に成形できるが、不均一、×;シート状に成形できない。
・密度:成形物のノギスで厚さを測定し、その重量とから密度を算出した。
[Example 1]
Eucalyptus Eurograndis chips were pulverized to 6 mm or less with a cutter mill (trade name: P-15, manufactured by Fritsch). After adding 800 g of water to 100 g of the solid content of the pulverized product and heating it to 200 ° C. using a steam explosion device (manufactured by Nitto High Pressure Co., Ltd.), maintaining the pressure at 1.6 MPa for 10 minutes and steaming, The pressure was released immediately and the blasting process was performed. Water was added to the obtained crushed material to obtain a slurry having a concentration of 5%, and pulverized with a wet pulverizer (trade name: Mascolloider MKG-C # 80, manufactured by Masuko Sangyo Co., Ltd., clearance 60 μm). The average particle size of the obtained pulverized product was measured by the following method, and the results are shown in Table 1.
Next, the pulverized product was diluted with ultrapure water to a concentration of 0.2% and filtered with a membrane filter (filter used: ADVANTEC H020A047A (hydrophilic PTFE), pore 0.2 μm, Φ47 mm). The obtained filtrated material is sandwiched between filter papers and subjected to two hot presses at a first time: 120 ° C., 2 kgf / cm 2 , 10 minutes, second time: 180 ° C., 5 kgf / cm 2 , 10 minutes. A molded product was obtained. The moldability and density of the obtained molded product were measured by the following methods, and the results are shown in Table 1.
-Average particle diameter of pulverized product: Laser diffraction / scattering particle size distribution analyzer (trade name: Mastersizer 2000, manufactured by Malvern Co., Ltd.) was used, and the 50% point of the volume cumulative distribution was defined as the average particle diameter.
Moldability: The moldability was evaluated by visual observation of the molded product according to the following criteria. A: Can be formed into a uniform sheet, Δ: Can be formed into a sheet, but non-uniform, x: Cannot be formed into a sheet.
Density: The thickness was measured with a caliper of the molded product, and the density was calculated from the weight.
[実施例2]
実施例1で得た爆砕処理物に水を加えて濃度10%のスラリーとして粉砕した以外は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Example 2]
A molded product was obtained in the same manner as in Example 1 except that water was added to the explosion-treated product obtained in Example 1 and pulverized as a slurry having a concentration of 10%. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
[比較例1]
実施例1で得た爆砕処理物に水を加えて濃度5%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMK−E #46、増幸産業(株)製、クリアランス100μm)で粉砕した。得られた粉砕処理物は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Comparative Example 1]
Water was added to the crushed material obtained in Example 1 and the mixture was pulverized as a slurry having a concentration of 5% with a wet pulverizer (trade name: Mascolloider MK-E # 46, manufactured by Masuko Sangyo Co., Ltd., clearance 100 μm). The obtained pulverized product was obtained in the same manner as in Example 1. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
[比較例2]
実施例1で得た爆砕処理物に水を加えて濃度10%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMK−E #46、増幸産業(株)製、クリアランス100μm)で粉砕した。得られた粉砕処理物は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Comparative Example 2]
Water was added to the crushed material obtained in Example 1, and the mixture was pulverized as a slurry having a concentration of 10% with a wet pulverizer (trade name: Mascolloider MK-E # 46, manufactured by Masuko Sangyo Co., Ltd., clearance 100 μm). The obtained pulverized product was obtained in the same manner as in Example 1. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
[比較例3]
ユーカリ ユーログランディスのチップをカッターミル(商品名:P−15、フリッチュ社製)で6mm以下に粉砕した。この粉砕物に水を加えて濃度5%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMKG−C #80、増幸産業(株)製、クリアランス60μm)で粉砕した。得られた粉砕処理物は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Comparative Example 3]
Eucalyptus Eurograndis chips were pulverized to 6 mm or less with a cutter mill (trade name: P-15, manufactured by Fritsch). Water was added to the pulverized product, and the mixture was pulverized as a slurry having a concentration of 5% with a wet pulverizer (trade name: Mascolloider MKG-C # 80, manufactured by Masuko Sangyo Co., Ltd., clearance 60 μm). The obtained pulverized product was obtained in the same manner as in Example 1. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
[比較例4]
ユーカリ ユーログランディスのチップをカッターミル(商品名:P−15、フリッチュ社製)で6mm以下に粉砕した。この粉砕物に水を加えて濃度10%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMKG−C #80、増幸産業(株)製、クリアランス60μm)で粉砕した。得られた粉砕処理物は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Comparative Example 4]
Eucalyptus Eurograndis chips were pulverized to 6 mm or less with a cutter mill (trade name: P-15, manufactured by Fritsch). Water was added to the pulverized product, and the mixture was pulverized as a slurry having a concentration of 10% with a wet pulverizer (trade name: Mascolloider MKG-C # 80, manufactured by Masuko Sangyo Co., Ltd., clearance 60 μm). The obtained pulverized product was obtained in the same manner as in Example 1. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
[比較例5]
ユーカリ ユーログランディスを原料として製造したクラフトパルプをカッターミル(商品名:P−15、フリッチュ社製)で6mm以下に粉砕した。この粉砕物に水を加えて濃度5%のスラリーとして、湿式粉砕機(商品名:マスコロイダーMKG−C #80、増幸産業(株)製、クリアランス60μm)で粉砕した。得られた粉砕処理物は、実施例1と同様にして成形物を得た。粉砕処理物の平均粒径、成形物の成形性、密度を表1に示した。
[Comparative Example 5]
Kraft pulp manufactured using Eucalyptus Eurograndis as a raw material was pulverized to 6 mm or less with a cutter mill (trade name: P-15, manufactured by Fritsch). Water was added to the pulverized product, and the mixture was pulverized as a slurry having a concentration of 5% with a wet pulverizer (trade name: Mascolloider MKG-C # 80, manufactured by Masuko Sangyo Co., Ltd., clearance 60 μm). The obtained pulverized product was obtained in the same manner as in Example 1. Table 1 shows the average particle diameter of the pulverized product, the moldability and the density of the molded product.
表1に示されるように、実施例1〜2の平均粒径が30μm以下である爆砕処理物は成形性が良好であった。比較例1〜2の平均粒径が30μmを超えた爆砕処理物は成形性が劣っていた。また、比較例3〜4の未処理の粉砕物、比較例4のクラフトパルプも成形性が劣っていた。また、爆砕処理することによって、粉砕処理時の消費電力は低減された。 As shown in Table 1, the explosive treatment product having an average particle size of Examples 1 and 2 of 30 μm or less had good moldability. The explosive treatment product in which the average particle size of Comparative Examples 1 and 2 exceeded 30 μm was inferior in moldability. Moreover, the unprocessed ground material of Comparative Examples 3 to 4 and the kraft pulp of Comparative Example 4 were also inferior in moldability. Moreover, the power consumption at the time of a grinding | pulverization process was reduced by carrying out a blasting process.
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