JP2008075014A - Paper-containing resin composition and molded product thereof, and method for producing them - Google Patents
Paper-containing resin composition and molded product thereof, and method for producing them Download PDFInfo
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- JP2008075014A JP2008075014A JP2006257373A JP2006257373A JP2008075014A JP 2008075014 A JP2008075014 A JP 2008075014A JP 2006257373 A JP2006257373 A JP 2006257373A JP 2006257373 A JP2006257373 A JP 2006257373A JP 2008075014 A JP2008075014 A JP 2008075014A
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- 239000011342 resin composition Substances 0.000 title claims abstract description 102
- 238000004519 manufacturing process Methods 0.000 title claims description 31
- 229920005989 resin Polymers 0.000 claims abstract description 103
- 239000011347 resin Substances 0.000 claims abstract description 103
- -1 polypropylene Polymers 0.000 claims abstract description 74
- 238000012360 testing method Methods 0.000 claims abstract description 30
- 239000004743 Polypropylene Substances 0.000 claims abstract description 29
- 229920001155 polypropylene Polymers 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 21
- 150000007519 polyprotic acids Polymers 0.000 claims abstract description 19
- 150000001341 alkaline earth metal compounds Chemical class 0.000 claims abstract description 17
- 150000008065 acid anhydrides Chemical class 0.000 claims abstract description 16
- 229920013716 polyethylene resin Polymers 0.000 claims abstract description 15
- 239000004698 Polyethylene Substances 0.000 claims description 46
- 229920000573 polyethylene Polymers 0.000 claims description 46
- 238000010298 pulverizing process Methods 0.000 claims description 21
- 239000002699 waste material Substances 0.000 claims description 20
- 239000000395 magnesium oxide Substances 0.000 claims description 19
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 19
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 19
- 229920001131 Pulp (paper) Polymers 0.000 claims description 18
- 238000004898 kneading Methods 0.000 claims description 18
- 239000011122 softwood Substances 0.000 claims description 17
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical group O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 claims description 16
- 230000003472 neutralizing effect Effects 0.000 claims description 15
- 239000011802 pulverized particle Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 14
- 239000000155 melt Substances 0.000 claims description 14
- 239000010893 paper waste Substances 0.000 claims description 12
- 238000005520 cutting process Methods 0.000 claims description 9
- 150000007524 organic acids Chemical class 0.000 claims description 9
- 239000000945 filler Substances 0.000 claims description 8
- 238000001746 injection moulding Methods 0.000 claims description 8
- 230000032050 esterification Effects 0.000 claims description 6
- 238000005886 esterification reaction Methods 0.000 claims description 6
- 150000002681 magnesium compounds Chemical class 0.000 claims description 3
- 238000002156 mixing Methods 0.000 abstract description 12
- 239000002245 particle Substances 0.000 abstract description 11
- 239000000203 mixture Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 6
- 238000000034 method Methods 0.000 description 23
- 239000000835 fiber Substances 0.000 description 18
- 235000013336 milk Nutrition 0.000 description 11
- 239000008267 milk Substances 0.000 description 11
- 210000004080 milk Anatomy 0.000 description 11
- 238000011156 evaluation Methods 0.000 description 10
- 238000000465 moulding Methods 0.000 description 10
- 239000003795 chemical substances by application Substances 0.000 description 8
- 238000007639 printing Methods 0.000 description 8
- 238000002845 discoloration Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 239000006185 dispersion Substances 0.000 description 6
- 238000002347 injection Methods 0.000 description 6
- 239000007924 injection Substances 0.000 description 6
- 238000009966 trimming Methods 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 238000005452 bending Methods 0.000 description 5
- 230000020169 heat generation Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 239000002985 plastic film Substances 0.000 description 4
- 229920006255 plastic film Polymers 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 150000008064 anhydrides Chemical class 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 235000013312 flour Nutrition 0.000 description 3
- 238000003475 lamination Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000012752 auxiliary agent Substances 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009864 tensile test Methods 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 2
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 description 1
- 206010037660 Pyrexia Diseases 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000000805 composite resin Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- UAUDZVJPLUQNMU-KTKRTIGZSA-N erucamide Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(N)=O UAUDZVJPLUQNMU-KTKRTIGZSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000005001 laminate film Substances 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 description 1
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920005668 polycarbonate resin Polymers 0.000 description 1
- 239000004431 polycarbonate resin Substances 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920005990 polystyrene resin Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000007655 standard test method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229940014800 succinic anhydride Drugs 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Classifications
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- 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
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
本発明は、液体容器の印刷断裁屑又は回収された液体容器などの再生困難なラミネート紙を粉砕して樹脂原料と混合してなる紙含有樹脂組成物に関する。さらに詳しくは、粒径の粗い粉砕物と樹脂原料との混練性を改善することで、ラミネート紙の未分散物をなくして均一に混合分散させ、その結果、紙含有樹脂組成物の流動性を改善することによって、ラミネート紙の含有率を増加させることができる紙含有ポリオレフィン樹脂組成物に関する。 The present invention relates to a paper-containing resin composition obtained by pulverizing laminated paper that is difficult to regenerate, such as printing cutting waste from a liquid container or a collected liquid container, and mixing it with a resin raw material. More specifically, by improving the kneadability between the coarsely pulverized pulverized product and the resin raw material, the undispersed laminate paper is eliminated and uniformly mixed and dispersed. As a result, the fluidity of the paper-containing resin composition is improved. The present invention relates to a paper-containing polyolefin resin composition capable of increasing the content of laminated paper by improving.
従来、湿式によるラミネート古紙を再利用する方法が行われている。また、プラスチックフィルムラミネート紙の乾式再利用に関して幾つかの方法が提案されている。乾式再利用の方法は、大別して、粉砕(粉砕機と粉砕粒径)、熱可塑性樹脂との混練(混練薬品と樹脂配合率)、造粒に関する提案であり、いずれの方法も紙と樹脂との混合分散を高めることによって成形性を改善することを目的としている。樹脂と紙粉砕物との混合組成物は、紙の粉砕粒度が粗くなるに従い、また紙粉砕物の比率が増加するに従い、その流動性が低下することが知られている。 Conventionally, a method of reusing waste laminated paper has been performed. Several methods have been proposed for dry reuse of plastic film laminated paper. The dry recycling methods are roughly divided into proposals for pulverization (pulverizer and pulverized particle size), kneading with thermoplastic resin (mixing chemical and resin blending ratio), and granulation. The purpose of this is to improve the moldability by increasing the mixing and dispersion. It is known that the fluidity of the mixed composition of resin and pulverized paper decreases as the pulverized particle size of the paper becomes coarse and the ratio of the pulverized paper increases.
樹脂との混練性を高める粉砕方法については、例えば、プラスチックフィルムラミネート紙を、その細断物の粒径が0.05mm〜0.3mmの範囲に中心値を有し、紙の繊維を解繊させないように切断して該細断物とする方法(例えば、特許文献1を参照。)、粒径3mm程度の燐片状に粗粉砕した後、衝撃粉砕する方法(例えば、特許文献2を参照。)、粉砕物の粒径を一辺が5mm以下、好ましくは1mm以下に微粉砕し、繊維を綿状に解繊させることによって、紙と樹脂との分散性を高めるとする方法(例えば、特許文献3を参照。)、ポリプロピレンラミネート古紙を3mm角に粉砕した後、100メッシュパスの微粉砕したものを使用する方法(例えば、特許文献4を参照。)などがある。 As for the pulverization method for improving the kneadability with resin, for example, plastic film laminated paper has a median value in the range of 0.05 mm to 0.3 mm in the particle size of the shredded product, and the fiber of the paper is defibrated. A method of cutting the material so as not to cause the shredded product (see, for example, Patent Document 1), a method of roughly pulverizing into a flake shape having a particle size of about 3 mm, and then impact-pulverizing (for example, see Patent Document 2) ), A method of improving the dispersibility of paper and resin by finely pulverizing the particle size of the pulverized product to 5 mm or less, preferably 1 mm or less on one side and defibrating the fibers into a cotton-like shape (for example, patents) Reference 3), and a method of using finely pulverized 100-mesh pass after pulverizing polypropylene laminated waste paper to 3 mm square (for example, see Patent Document 4).
一方、混練薬品については、両面又は片面にポリエチレン樹脂層やポリプロピレン樹脂層を有する複合紙の細断物に、比重差の少ない細断したポリエチレン樹脂やポリプロピレン樹脂を用いて紙−樹脂の混合時の偏り分散を防止する方法(例えば、特許文献5を参照。)、不要となったプラスチックラミネート紙や樹脂塗布紙をペレット樹脂のメルトフローレイト(MFR)を5〜50に規定することによって再利用する方法(例えば、特許文献6を参照。)がある。 On the other hand, with regard to kneading chemicals, a shredded composite paper having a polyethylene resin layer or a polypropylene resin layer on both sides or one side is used for a paper-resin mixing using a shredded polyethylene resin or polypropylene resin with a small specific gravity difference. A method of preventing uneven dispersion (see, for example, Patent Document 5), and reusing unnecessary plastic-laminated paper and resin-coated paper by defining the pellet resin melt flow rate (MFR) to 5-50. There is a method (for example, refer to Patent Document 6).
多塩基酸無水物によるエステル化については、ポリオレフィン、木粉・木質パルプなどの木質系材料、多塩基酸無水物及び有機過酸化物を含有させたポリオレフィン樹脂複合材を製造する方法があり、加熱混練により成形加工性及び機械強度が高まるとしている(例えば、特許文献7を参照。)。また、木粉入り樹脂組成物に関して、特に加熱加圧時における木粉の熱分解により生成する有機酸の中和剤として酸化マグネシウムを添加して、射出成形等の金型の腐食を防止する方法がある(例えば、特許文献8を参照。)。 For esterification with polybasic acid anhydrides, there is a method for producing polyolefin resin composites containing polyolefin, wood-based materials such as wood flour and wood pulp, polybasic acid anhydrides and organic peroxides, and heating. It is said that molding processability and mechanical strength are increased by kneading (see, for example, Patent Document 7). In addition, with respect to resin compositions containing wood flour, in particular, a method for preventing corrosion of molds such as injection molding by adding magnesium oxide as a neutralizing agent for organic acids generated by thermal decomposition of wood flour during heating and pressing. (For example, refer to Patent Document 8).
湿式によるラミネート古紙の再利用する方法では、紙とフィルムを分離する必要があることと、分離回収された繊維分の歩留まりが低いこと、また、更に分離されたラミネートフィルムの焼却、埋め立てなどの処理が必要であることの理由によって、ラミネート古紙全体を効率よく再利用する方法については実用化されていない。さらにラミネート古紙を分離せずにそのまま再利用する方法についても実用化されていない。 In the method of reusing recycled waste paper by wet method, it is necessary to separate the paper and film, the yield of separated and recovered fibers is low, and further processing such as incineration and landfilling of the separated laminated film However, a method for efficiently reusing the entire laminated waste paper has not been put into practical use. Furthermore, a method for reusing recycled laminated paper as it is without separation has not been put to practical use.
特許文献1、2又は3で示された方法は、何れも紙の粉砕粒径を細かくすることによって、又は粉砕物の形状を規定することによって、樹脂中での繊維の混合分散を高めるものである。しかし粒径を細かくする程、プラスチックフィルムラミネート紙に含まれる比較的融点の低いポリエチレンが粉砕時の発熱によって溶融し、スクリーンの目詰りを発生させるなどの粉砕効率を著しく低下させるという欠点がある。特許文献4で示された方法でも、ラミネート紙を粉砕する場合には、粉砕粒径が細かくなる程、ラミネートされた樹脂の熱溶融によるスクリーン又は平網の目詰まりが起き易く、粉砕機内部の温度上昇による固定刃と回転刃の接触などの問題が発生する。 Each of the methods disclosed in Patent Documents 1, 2, or 3 enhances the mixing and dispersion of fibers in the resin by reducing the pulverized particle size of the paper or by defining the shape of the pulverized product. is there. However, the finer the particle size, there is a disadvantage that the polyethylene having a relatively low melting point contained in the plastic film laminated paper melts due to heat generated during crushing, and the crushing efficiency is remarkably reduced, such as clogging of the screen. Even in the method shown in Patent Document 4, when the laminated paper is pulverized, the smaller the pulverized particle size, the more easily clogging of the screen or the flat net due to heat melting of the laminated resin occurs. Problems such as contact between the fixed blade and the rotary blade due to temperature rise occur.
プラスチックフィルムラミネート紙が、針葉樹漂白化学パルプを主体とするラミネート紙である場合、紙の強度は高いが、坪量が高く、紙の両面が厚いポリエチレンなどの樹脂層で被覆され、剛度も高く、微粉砕が困難である。微粉砕が困難な理由としては、特許文献1、2、3又は4の場合と同様であり、比較的融点の低いポリエチレンなどの樹脂が粉砕時の発熱によって溶融し、スクリーンの目詰りを誘発し、粉砕効率を著しく低下させることが挙げられる。したがって、粒径の粗いラミネート紙の粉砕物と樹脂との混練分散性を向上させ、紙配合率の高い樹脂組成物を射出成形などに利用する技術の確立が課題となっている。 When the plastic film laminated paper is a laminated paper mainly composed of softwood bleached chemical pulp, the strength of the paper is high, but the basis weight is high, both sides of the paper are covered with a resin layer such as thick polyethylene, and the rigidity is also high, It is difficult to pulverize. The reason why fine pulverization is difficult is the same as in Patent Documents 1, 2, 3 or 4, and a resin such as polyethylene having a relatively low melting point melts due to heat generated during pulverization, thereby causing clogging of the screen. , Remarkably reducing the pulverization efficiency. Therefore, establishment of a technique for improving the kneading dispersibility of the pulverized laminate paper having a coarse particle size and the resin and utilizing a resin composition having a high paper blending ratio for injection molding is a problem.
本発明の第一の目的は、従来焼却若しくは繊維分しか利用されていなかった、液体容器の印刷断裁屑及び/又は回収された液体容器の長繊維の針葉樹漂白化学パルプを多く含む再生困難なラミネート紙を、紙とフィルムとを分離せずにそのまま全体として再利用して、資源の有効活用を目指した紙含有樹脂組成物を提供することにある。すなわち、ラミネート紙の粉砕粒径を細かくすることなく、粒径の粗い粉砕物と樹脂原料との混練性を改善することで、ラミネート紙の未分散物をなくして均一に混合分散し、その結果、紙含有樹脂組成物の流動性を改善することによって、ラミネート紙の含有率を増加させても射出成形などの成形性が良好な紙含有樹脂組成物を提供することにある。 The first object of the present invention is a hard-to-regenerate laminate that contains a large amount of printing wastes from liquid containers and / or long-fiber softwood bleached chemical pulp collected from liquid containers, which has conventionally been used only for incineration or fiber content. An object of the present invention is to provide a paper-containing resin composition aiming at effective utilization of resources by reusing paper as it is as a whole without separating paper and film. That is, without reducing the pulverized particle size of the laminated paper, by improving the kneadability between the coarsely pulverized pulverized product and the resin raw material, the laminated paper is uniformly mixed and dispersed without any undispersed material. An object of the present invention is to provide a paper-containing resin composition having good moldability such as injection molding even when the content of laminated paper is increased by improving the fluidity of the paper-containing resin composition.
本発明の第二の目的は、本発明に係る紙含有樹脂組成物を用いて、ラミネート紙の含有率が高く、変色及び臭気がなく、吸水率が少なく、衝撃強度に優れた紙含有樹脂成形品を提供することにある。 A second object of the present invention is to use a paper-containing resin composition according to the present invention, a high content of laminated paper, no discoloration and odor, low water absorption, and excellent impact strength. Is to provide goods.
本発明の第三の目的は、二軸押出機を用いた混練を行うことによって、ラミネート紙の未分散がなく、均一に混合分散された紙含有樹脂組成物を得るための製造方法を提供することにある。 The third object of the present invention is to provide a production method for obtaining a paper-containing resin composition in which laminated paper is not dispersed and is uniformly mixed and dispersed by kneading using a twin-screw extruder. There is.
本発明の第四の目的は、本発明の紙含有樹脂組成物を用いて、良好に成形された紙含有樹脂成形品を得るための製造方法を提供することにある。 The fourth object of the present invention is to provide a production method for obtaining a well-formed paper-containing resin molded article using the paper-containing resin composition of the present invention.
本発明者らは、紙の粉砕物に使用する紙の組成と該粉砕物との関係、及び樹脂を混合したときの作業性と紙含有樹脂組成物の品質との関係について鋭意検討を進めた結果、前記目的を同時に達成できることを見出し、本発明に至った。 The present inventors diligently investigated the relationship between the composition of the paper used for the pulverized paper and the pulverized product, and the relationship between the workability when the resin was mixed and the quality of the paper-containing resin composition. As a result, the inventors have found that the above objects can be achieved at the same time, and have reached the present invention.
本発明に係る紙含有樹脂組成物は、多塩基酸無水物でエステル化された紙の粉砕物、ポリプロピレン樹脂、ポリエチレン樹脂及びアルカリ土類金属化合物を少なくとも含有し、前記粉砕物及び前記ポリプロピレン樹脂が主要成分であり、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minであることを特徴とする。 The paper-containing resin composition according to the present invention contains at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin, and an alkaline earth metal compound. It is a main component and is characterized in that the melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c is 2.0 to 25.0 g / 10 min.
本発明に係る紙含有樹脂組成物では、前記多塩基酸無水物が無水マレイン酸であり、かつ、エステル化によって導入された無水マレイン酸の割合がパルプ成分に対して0.1〜5質量%であることが好ましい。紙含有樹脂組成物の流動性が改善され、吸水率も少なくなる。ラミネート紙の未分散がなく均一に混合分散されやすい。 In the paper-containing resin composition according to the present invention, the polybasic acid anhydride is maleic anhydride, and the proportion of maleic anhydride introduced by esterification is 0.1 to 5% by mass with respect to the pulp component. It is preferable that The fluidity of the paper-containing resin composition is improved and the water absorption rate is reduced. There is no undispersed laminate paper and it is easy to mix and disperse uniformly.
本発明に係る紙含有樹脂組成物では、前記アルカリ土類金属化合物がマグネシウム化合物であり、かつ、酸化マグネシウム換算で全質量に対し0.1〜5質量%含有していることが好ましい。有機酸を中和することによって、変色及び臭気の発生を抑えることが可能となる。 In the paper-containing resin composition according to the present invention, it is preferable that the alkaline earth metal compound is a magnesium compound and is contained in an amount of 0.1 to 5% by mass with respect to the total mass in terms of magnesium oxide. By neutralizing the organic acid, it is possible to suppress discoloration and odor generation.
本発明に係る紙含有樹脂組成物では、前記紙が針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙であり、かつ、前記ポリエチレン樹脂が前記ポリエチレンフィルムラミネート紙の由来であることが好ましい。ミルクカートンやその裁断屑を再利用するものであり、針葉樹漂白化学パルプを多く含有することで、紙含有樹脂組成物の強度が高まる。 In the paper-containing resin composition according to the present invention, the paper is a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp, and the polyethylene resin is derived from the polyethylene film laminated paper. It is preferable that Milk cartons and their cut waste are reused, and the strength of the paper-containing resin composition is increased by containing a large amount of softwood bleached chemical pulp.
本発明に係る紙含有樹脂組成物では、前記粉砕物と填料とを含む紙素材の合計量が、51質量%以上であることが好ましい。すなわち、環境配慮型紙含有樹脂組成物とすることができる。 In the paper-containing resin composition according to the present invention, the total amount of the paper material including the pulverized material and the filler is preferably 51% by mass or more. That is, it can be set as an environment-friendly paper-containing resin composition.
本発明に係る紙含有樹脂成形品は、多塩基酸無水物でエステル化された紙の粉砕物、ポリプロピレン樹脂、ポリエチレン樹脂及びアルカリ土類金属化合物を少なくとも含有し、前記粉砕物及び前記ポリプロピレン樹脂が主要成分であり、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minであることを特徴とする。 The paper-containing resin molded product according to the present invention contains at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin, and an alkaline earth metal compound, and the pulverized product and the polypropylene resin are It is a main component and is characterized in that the melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c is 2.0 to 25.0 g / 10 min.
本発明に係る紙含有樹脂成形品では、前記紙が針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙であり、かつ、前記ポリエチレン樹脂が前記ポリエチレンフィルムラミネート紙の由来であることが好ましい。ミルクカートンやその裁断屑を再利用するものであり、針葉樹漂白化学パルプを多く含有することで、紙含有樹脂組成物の強度が高まる。 In the paper-containing resin molded product according to the present invention, the paper is a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp, and the polyethylene resin is derived from the polyethylene film laminated paper. It is preferable that Milk cartons and their cut waste are reused, and the strength of the paper-containing resin composition is increased by containing a large amount of softwood bleached chemical pulp.
本発明に係る紙含有樹脂組成物の製造方法は、針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙を粉砕して紙の粉砕物を得る工程と、多塩基酸無水物で前記粉砕物をエステル化させる工程と、アルカリ土類金属化合物で有機酸を中和する工程と、少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂組成物を得る工程と、を有することを特徴とする。 The method for producing a paper-containing resin composition according to the present invention includes a step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp to obtain a pulverized paper, and a polybasic acid A step of esterifying the pulverized product with an anhydride, a step of neutralizing an organic acid with an alkaline earth metal compound, and at least the pulverized product and a polypropylene resin are kneaded with a twin screw extruder, and ASTM-D1238- And a step of obtaining a paper-containing resin composition having a melt mass flow rate (MFR) specified in 04c (test temperature = 190 ° C., test load = 10 kg) of 2.0 to 25.0 g / 10 min. To do.
本発明に係る紙含有樹脂組成物の製造方法では、前記粉砕物の粉砕粒径が0.5〜2.5mmであることが好ましい。良好な混練性が得られるとともに、粉砕が容易でロングラン操業が可能である。 In the method for producing a paper-containing resin composition according to the present invention, the pulverized product preferably has a pulverized particle size of 0.5 to 2.5 mm. Good kneadability can be obtained, pulverization is easy, and long run operation is possible.
本発明に係る紙含有樹脂組成物の製造方法では、前記ポリエチレンフィルムラミネート紙が、液体容器用のポリエチレンフィルムラミネート紙、該ポリエチレンフィルムラミネート紙の断裁屑及び/又は該ポリエチレンフィルムラミネート紙の回収古紙であることが好ましい。すなわち、資源の有効活用の効率が高まる。 In the method for producing a paper-containing resin composition according to the present invention, the polyethylene film laminated paper is a polyethylene film laminated paper for a liquid container, cutting waste of the polyethylene film laminated paper, and / or recovered waste paper of the polyethylene film laminated paper. Preferably there is. That is, the efficiency of effective use of resources increases.
本発明に係る紙含有樹脂成形品の製造方法は、針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙を粉砕して紙の粉砕物を得る工程と、多塩基酸無水物で前記粉砕物をエステル化させる工程と、アルカリ土類金属化合物で有機酸を中和する工程と、少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、紙含有樹脂組成物を得る工程と、該紙含有樹脂組成物を射出成形機によって成形して、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂成形品を得る工程と、を有することを特徴とする。 The method for producing a paper-containing resin molded product according to the present invention includes a step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp to obtain a pulverized paper product, and a polybasic acid A step of esterifying the pulverized product with an anhydride, a step of neutralizing an organic acid with an alkaline earth metal compound, and at least the pulverized product and a polypropylene resin are kneaded with a twin screw extruder, and a paper-containing resin composition And a melt mass flow rate (MFR) defined by ASTM-D1238-04c (test temperature = 190 ° C., test load = 10 kg) is obtained by molding the paper-containing resin composition with an injection molding machine. And a step of obtaining a paper-containing resin molded product of 0 to 25.0 g / 10 min.
本発明に係る紙含有樹脂成形品の製造方法では、前記粉砕物の粉砕粒径が0.5〜2.5mmであることが好ましい。良好な混練性が得られるとともに、粉砕が容易でロングラン操業が可能である。 In the method for producing a paper-containing resin molded product according to the present invention, the pulverized product preferably has a pulverized particle size of 0.5 to 2.5 mm. Good kneadability can be obtained, pulverization is easy, and long run operation is possible.
本発明に係る紙含有樹脂成形品の製造方法では、前記ポリエチレンフィルムラミネート紙が、液体容器用のポリエチレンフィルムラミネート紙、該ポリエチレンフィルムラミネート紙の断裁屑及び/又は該ポリエチレンフィルムラミネート紙の回収古紙であることが好ましい。すなわち、資源の有効活用の効率が高まる。 In the method for producing a paper-containing resin molded product according to the present invention, the polyethylene film laminated paper is a polyethylene film laminated paper for a liquid container, cutting waste of the polyethylene film laminated paper, and / or recovered waste paper of the polyethylene film laminated paper. Preferably there is. That is, the efficiency of effective use of resources increases.
本発明に係る紙含有樹脂成形品の製造方法では、前記紙含有樹脂組成物を得る工程及び/又は前記紙含有樹脂成形品を得る工程において、流動性向上剤を添加することが好ましい。混練時の発熱及び/又は成形時の発熱が抑制され、成形性が向上する。 In the method for producing a paper-containing resin molded product according to the present invention, it is preferable to add a fluidity improver in the step of obtaining the paper-containing resin composition and / or the step of obtaining the paper-containing resin molded product. Heat generation during kneading and / or heat generation during molding is suppressed, and moldability is improved.
本発明の紙含有樹脂組成物によって、従来焼却若しくは繊維分しか利用されていなかった、液体容器の印刷断裁屑及び/又は回収された液体容器の全体が再利用できる。特に液体容器には、長繊維の針葉樹漂白化学パルプを多く含む再生困難なラミネート紙が使用されており、その全体が再利用できる。すなわち、本発明の紙含有樹脂組成物は、ラミネート紙の粉砕粒径を細かくすることなく、粒径の粗い粉砕物と樹脂原料との混練性を改善することで、ラミネート紙の未分散物をなくして均一に混合分散させ、その結果、紙含有樹脂組成物の流動性を改善することによって、ラミネート紙の含有率を増加させても射出成形などの成形性が良好である。 With the paper-containing resin composition of the present invention, the entire printing waste and / or the recovered liquid container of the liquid container, which has conventionally been used only for incineration or fiber, can be reused. In particular, the liquid container is made of hard-to-recycle laminated paper containing a lot of long-fiber softwood bleached chemical pulp, and the whole can be reused. That is, the paper-containing resin composition of the present invention improves the kneadability between the coarsely pulverized product and the resin raw material without reducing the pulverized particle size of the laminated paper, thereby reducing the undispersed material of the laminated paper. Without being mixed and dispersed uniformly, as a result, by improving the fluidity of the paper-containing resin composition, the moldability such as injection molding is good even when the content of the laminated paper is increased.
本発明の紙含有樹脂成形品は、本発明に係る紙含有樹脂組成物を用いることで、ラミネート紙の含有率を高くすることができ、しかも変色及び臭気がなく、衝撃強度に優れる。 By using the paper-containing resin composition according to the present invention, the paper-containing resin molded product of the present invention can increase the content of the laminated paper, and is excellent in impact strength without discoloration and odor.
本発明の紙含有樹脂組成物の製造方法では、多塩基酸無水物及びアルカリ土類金属化合物による反応を起こし、かつ、二軸押出機を用いた混練を行うことによって、ラミネート紙の未分散がなく均一に混合分散された流動性の良好な紙含有樹脂組成物を得ることができる。 In the method for producing the paper-containing resin composition of the present invention, the reaction with the polybasic acid anhydride and the alkaline earth metal compound is caused, and kneading using a twin-screw extruder is performed so that the undispersed laminate paper is removed. A paper-containing resin composition having good fluidity that is uniformly mixed and dispersed can be obtained.
本発明の紙含有樹脂成形品の製造方法では、本発明の紙含有樹脂組成物を用いて、良好に成形された紙含有樹脂成形品を得ることができる。 In the method for producing a paper-containing resin molded article of the present invention, a paper-containing resin molded article that has been well molded can be obtained using the paper-containing resin composition of the present invention.
本発明の詳細について説明するが、本発明は次の実施形態に限定して解釈されるものではない。 The details of the present invention will be described, but the present invention is not construed as being limited to the following embodiments.
本実施形態に係る紙含有樹脂組成物は、多塩基酸無水物でエステル化された紙の粉砕物、ポリプロピレン樹脂、ポリエチレン樹脂及びアルカリ土類金属化合物を少なくとも含有し、前記粉砕物及び前記ポリプロピレン樹脂が主要成分であり、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである。前記紙は、針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたラミネート紙、又は、該ラミネート紙とラミネート前のその原紙とを組み合わせたものである。 The paper-containing resin composition according to this embodiment contains at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin, and an alkaline earth metal compound, and the pulverized material and the polypropylene resin. Is the main component, and the melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) specified by ASTM-D1238-04c is 2.0 to 25.0 g / 10 min. The paper is a laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp, or a combination of the laminated paper and the base paper before lamination.
ラミネート紙は、原紙の片面又は両面に膜厚20〜50μmのポリエチレン樹脂がラミネートされている。ここでラミネート紙は、液体容器用のラミネート紙、ラミネート紙の断裁屑又はラミネート紙の回収古紙のそれぞれ単独の使用、或いは、ラミネート紙及びラミネート紙の断裁屑の組み合わせの使用、ラミネート紙及びラミネート紙の回収古紙の組み合わせの使用、ラミネート紙の断裁屑及びラミネート紙の回収古紙の組み合わせの使用、又は、ラミネート紙及びラミネート紙の断裁屑及びラミネート紙の回収古紙の組み合わせの使用の各形態とすることが好ましい。資源の有効活用の効率が高まる。その代表例は、いわゆるミルクカートンと呼ばれる液体容器用のラミネート紙であり、又はその印刷断裁屑(以下、「印刷トリミング屑」という。)であり、又は、牛乳パックなどの回収古紙でもよい(以後、これらを総称して「ラミネート古紙」と呼ぶ。)。原紙は、坪量が300〜500g/m2、紙厚が0.4〜0.6mm、密度が0.7〜0.6g/cm3の範囲にあることが好ましい。ラミネート紙の原紙を構成するパルプは、針葉樹漂白化学パルプ(NBKP)を主体とし、その原紙中のNBKPの配合率は、少なくとも50質量%以上である。より好ましくは、80質量%以上である。NBKPが50質量%未満の配合率では、本実施形態の紙含有樹脂組成物の強度適性が不十分となりやすい。ラミネートされたフィルムの材料としては、例えば、低密度ポリエチレン樹脂又は高密度ポリエチレン樹脂である。 The laminated paper has a polyethylene resin having a film thickness of 20 to 50 μm laminated on one or both sides of the base paper. Here, the laminated paper is a single use of a laminated paper for a liquid container, a laminated paper cutting waste or a recycled waste paper of a laminated paper, or a combination of laminated paper and laminated paper cutting waste, a laminated paper and a laminated paper. Use of a combination of recovered recovered paper, use of a combination of cut waste of laminated paper and recovered recovered paper of laminated paper, or use of a combination of recovered waste paper of laminated paper and laminated paper and recovered recovered paper of laminated paper Is preferred. Increases the efficiency of effective use of resources. A typical example thereof is a laminated paper for a liquid container called a so-called milk carton, or printing cut waste (hereinafter referred to as “print trimming waste”), or recovered paper such as a milk pack (hereinafter referred to as “milk trimming waste”). These are collectively called “laminated waste paper”.) The base paper preferably has a basis weight of 300 to 500 g / m 2 , a paper thickness of 0.4 to 0.6 mm, and a density of 0.7 to 0.6 g / cm 3 . The pulp constituting the base paper of the laminate paper is mainly softwood bleached chemical pulp (NBKP), and the blending ratio of NBKP in the base paper is at least 50% by mass or more. More preferably, it is 80 mass% or more. If the NBKP content is less than 50% by mass, the strength suitability of the paper-containing resin composition of the present embodiment tends to be insufficient. As a material of the laminated film, for example, a low density polyethylene resin or a high density polyethylene resin is used.
ラミネート紙を粉砕することによって粉砕物を得る。なお、ラミネート紙にその原紙を混ぜたものを粉砕することによって粉砕物を得てもよい。これによって、粉砕物には、必ず、ラミネート紙のポリエチレンフィルムに由来するポリエチレンが含まれることとなる。本実施形態に係る紙含有樹脂組成物に含まれるポリエチレンの含有量は、例えば2〜10質量%であり、好ましくは4〜8質量%である。この含有量は、紙粉砕物の配合量、ラミネート前の原紙の添加量によって適宜調整できる。粉砕物の粉砕粒径は、その後の混錬条件の影響も受けるが、0.5〜2.5mmであることが好ましい。より好ましくは、1.0〜2.0mmである。紙粉砕物の粒径は、所定のスクリーンを通過して得られるスクリーンの径で定義される(以下、単に「粒径」という。)。樹脂との混練性を良好にする為には、紙の粉砕粒径が一般的に細かい程よい。粉砕粒径を2.5mm以下とすることで良好な混練性が得られやすい。ポリエチレンなどの熱溶融しやすい樹脂をラミネートしたラミネート紙を粉砕する場合には、粉砕粒径が細かくなる程、樹脂の熱溶融によるスクリーン又は平網の目詰まりが起き易く、粉砕機内部の温度上昇による固定刃と回転刃の接触などの問題が発生しやすい。本発明者らの実験によれば、特に0.5mm未満の粒径に粉砕する場合には、粉砕機の操業が著しく困難となる結果であった。しかし、0.5mm以上の粒径では、この種のトラブルはほとんど発生することなくロングラン操業が可能になり、粉砕効率も向上した。 A pulverized product is obtained by pulverizing the laminated paper. In addition, you may obtain a pulverized material by grind | pulverizing what mixed the base paper with the laminate paper. Thus, the pulverized product always contains polyethylene derived from the polyethylene film of the laminated paper. The content of polyethylene contained in the paper-containing resin composition according to this embodiment is, for example, 2 to 10% by mass, and preferably 4 to 8% by mass. This content can be appropriately adjusted depending on the blended amount of the pulverized paper and the amount of base paper added before lamination. The pulverized particle size of the pulverized product is preferably 0.5 to 2.5 mm, although it is affected by the subsequent kneading conditions. More preferably, it is 1.0-2.0 mm. The particle diameter of the pulverized paper is defined by the diameter of the screen obtained by passing through a predetermined screen (hereinafter simply referred to as “particle diameter”). In order to improve the kneadability with the resin, the finer the particle size of the paper, the better. By setting the pulverized particle size to 2.5 mm or less, good kneadability is easily obtained. When crushing laminated paper that is laminated with heat-meltable resin such as polyethylene, the crushing of the screen or flat screen due to heat melting of the resin is more likely to occur as the pulverized particle size becomes smaller, and the temperature inside the crusher rises. Problems such as contact between the fixed blade and the rotary blade due to the above are likely to occur. According to the experiments by the present inventors, particularly when pulverizing to a particle size of less than 0.5 mm, the operation of the pulverizer becomes extremely difficult. However, when the particle size is 0.5 mm or more, this type of trouble hardly occurs and a long run operation is possible, and the grinding efficiency is improved.
本実施形態で紙の粉砕物とともに添加されている樹脂は、ポリプロピレン樹脂(PP樹脂)又はこれの変性樹脂である。本実施形態では、ポリプロピレン樹脂又はこれの変性樹脂とともに下記の樹脂を添加しても良い。例えば、ポリエチレン樹脂、ポリスチレン樹脂、アクリロニトリル・ブタジエン・スチレン樹脂、アクリロニトリル・スチレン樹脂、ウレタン樹脂、ポリエステル樹脂、ポリカーボネート樹脂又はこれらの変性樹脂などの汎用樹脂である。これらの樹脂は、新規合成品、使用済み成形物の粉砕物又はリサイクル物でも良く、更に単独若しくは混合物であってもよい。 In this embodiment, the resin added together with the pulverized paper is a polypropylene resin (PP resin) or a modified resin thereof. In the present embodiment, the following resin may be added together with the polypropylene resin or the modified resin thereof. Examples thereof include general-purpose resins such as polyethylene resins, polystyrene resins, acrylonitrile / butadiene / styrene resins, acrylonitrile / styrene resins, urethane resins, polyester resins, polycarbonate resins, and modified resins thereof. These resins may be newly synthesized products, pulverized products or recycled products of used molded products, and may be used alone or as a mixture.
本実施形態に係る紙含有樹脂組成物は、粉砕物及びポリプロピレン樹脂が主要成分であり、これらの合計含有量は、85〜98質量%とすることが好ましく、より好ましくは90〜95質量%である。85質量%未満の場合は、流動性及び分散性で劣る場合があり、98質量%を超えると色の変色が目立ちやすい場合がある。ここで、粉砕物の含有量は50〜70質量%とすることが好ましく、より好ましくは55〜60質量%である。50質量%未満の場合は、粉砕物の混入量が減ってリサイクル効率が劣り、70質量%を超えると流動性及び分散性で劣る場合がある。また、ポリプロピレン樹脂の含有量は15〜48質量%とすることが好ましく、より好ましくは25〜43質量%である。15質量%未満の場合は、強度が低下する場合があり、48質量%を超えると粉砕物の混入量が減ってリサイクル効率が劣る。 In the paper-containing resin composition according to this embodiment, a pulverized product and a polypropylene resin are main components, and the total content thereof is preferably 85 to 98% by mass, more preferably 90 to 95% by mass. is there. If it is less than 85% by mass, the fluidity and dispersibility may be inferior, and if it exceeds 98% by mass, the color change may be noticeable. Here, the content of the pulverized product is preferably 50 to 70% by mass, and more preferably 55 to 60% by mass. When the amount is less than 50% by mass, the amount of pulverized material mixed is reduced, resulting in poor recycling efficiency. When the amount exceeds 70% by mass, fluidity and dispersibility may be inferior. Moreover, it is preferable that content of a polypropylene resin shall be 15-48 mass%, More preferably, it is 25-43 mass%. If the amount is less than 15% by mass, the strength may decrease. If the amount exceeds 48% by mass, the amount of pulverized material mixed in decreases, resulting in poor recycling efficiency.
本実施形態で使用する多塩基酸無水物は、例えば無水マレイン酸、無水フタル酸又は無水コハク酸などがあり、そして樹脂と混練する前のラミネート紙の粉砕物に選択的に付加され、主としてパルプ繊維中のセルロース、ヘミセルロースをエステル化することによって、紙の粉砕粒径を細かくすることなく、粒径が粗い粉砕物の流動性の向上に効果がある。これらのうち無水マレイン酸がより好ましく、添加量は0.1〜5質量%の範囲で選ばれる。より好ましくは、0.5〜3質量%である。この量が0.1質量%未満では流動性向上の効果が不十分な場合があり、5質量%を超えると紙含有樹脂組成物及び紙含有樹脂成形品の物性が低下する場合がある。 The polybasic acid anhydride used in the present embodiment is, for example, maleic anhydride, phthalic anhydride or succinic anhydride, and is selectively added to the pulverized laminate paper before kneading with the resin. By esterifying cellulose and hemicellulose in the fiber, it is effective in improving the fluidity of the pulverized product having a coarse particle size without reducing the pulverized particle size of the paper. Among these, maleic anhydride is more preferable, and the addition amount is selected in the range of 0.1 to 5% by mass. More preferably, it is 0.5-3 mass%. If this amount is less than 0.1% by mass, the effect of improving the fluidity may be insufficient, and if it exceeds 5% by mass, the physical properties of the paper-containing resin composition and the paper-containing resin molded product may be deteriorated.
本実施形態で使用するアルカリ土類金属化合物は、例えば酸化マグネシウム、酸化カルシウム、酸化亜鉛などがあり、樹脂と混練するときに添加され、パルプ中の水分と反応し水酸化物に変化した後、エステル化後に残留した多塩基酸及び/又はパルプの熱分解によって生じる有機酸を中和することによって、臭気・ガスの発生を防止するのに有効である。これらのうち酸化マグネシウムがより好ましく、添加量は、本実施形態に係る紙含有樹脂組成物の全質量に対して0.1〜5質量%の範囲で選ばれる。より好ましくは、0.5〜3質量%である。この量が0.1質量%未満では中和の効果が不十分の場合があり、5質量%を超えると紙含有樹脂組成物及び紙含有樹脂成形品の物性が低下する場合があり、また経済的に好ましくなくなる。なお、紙含有樹脂組成物を形成した場合、例えば酸化マグネシウムを添加すると、上記中和反応によって酸化マグネシウムはマグネシウム化合物となっているが、紙含有樹脂組成物の状態から酸化マグネシウムの含有量を測定する場合には、酸化マグネシウム換算で求める。 The alkaline earth metal compound used in the present embodiment includes, for example, magnesium oxide, calcium oxide, zinc oxide and the like, added when kneading with a resin, and after reacting with moisture in the pulp and changing to a hydroxide, By neutralizing the polybasic acid remaining after esterification and / or the organic acid generated by thermal decomposition of the pulp, it is effective to prevent the generation of odor and gas. Among these, magnesium oxide is more preferable, and the addition amount is selected in the range of 0.1 to 5% by mass with respect to the total mass of the paper-containing resin composition according to the present embodiment. More preferably, it is 0.5-3 mass%. If this amount is less than 0.1% by mass, the neutralization effect may be insufficient. If it exceeds 5% by mass, the physical properties of the paper-containing resin composition and the paper-containing resin molded product may be reduced, and the economy may be reduced. Is not preferable. When a paper-containing resin composition is formed, for example, when magnesium oxide is added, magnesium oxide is converted to a magnesium compound by the neutralization reaction, but the content of magnesium oxide is measured from the state of the paper-containing resin composition. If so, obtain it in terms of magnesium oxide.
本実施形態の紙含有樹脂組成物では、必要に応じて、紙粉砕物及び樹脂以外の成分を含有させてもよい。例えば、流動性向上剤を添加してもよい。 In the paper-containing resin composition of the present embodiment, components other than the pulverized paper and resin may be included as necessary. For example, a fluidity improver may be added.
本実施形態において使用される流動性向上剤の添加は、粉砕された紙粉砕物と樹脂を混練するときに配合する場合、又は紙含有樹脂組成物を成形するときに配合する場合のいずれの場合でもよい。流動性向上剤を含有させることで、成形時の発熱が防止され、成形時の成形性が向上する。なお、混練するときに流動性向上剤を配合する場合、成形時での効果だけでなく、混練時の摩擦による発熱を防止する効果も得られる。流動性向上剤は、成形時の摩擦による発熱を防止し、紙含有樹脂組成物の流動性を向上するものであれば特に制限はなく、例えば、ポリエチレンワックス、低密度ポリエチレン、ステアリン酸、ステアリン酸亜鉛、ステアリン酸カルシウムなどの高級脂肪酸又はその塩、各種高級脂肪酸エステルが挙げられる。流動性向上剤の融点が100℃以下であることが好ましく、例えば、エルカ酸アミド、オレイン酸アミド、ステアリン酸アミドなどの脂肪酸アミドが挙げられる。これらを1種類用いてもよいし、2種類以上を併用してもよい。 The addition of the fluidity improver used in the present embodiment is either when blended when kneaded the pulverized paper pulverized product and the resin, or when blended when molding the paper-containing resin composition But you can. By containing a fluidity improver, heat generation during molding is prevented, and moldability during molding is improved. In addition, when mix | blending a fluidity improver at the time of kneading | mixing, not only the effect at the time of shaping | molding but the effect which prevents the heat_generation | fever by friction at the time of kneading | mixing is also acquired. The fluidity improver is not particularly limited as long as it prevents heat generation due to friction during molding and improves the fluidity of the paper-containing resin composition. For example, polyethylene wax, low density polyethylene, stearic acid, stearic acid Examples include higher fatty acids such as zinc and calcium stearate or salts thereof, and various higher fatty acid esters. The melting point of the fluidity improver is preferably 100 ° C. or lower, and examples thereof include fatty acid amides such as erucic acid amide, oleic acid amide, and stearic acid amide. One kind of these may be used, or two or more kinds may be used in combination.
また、必要に応じて相溶化剤、樹脂の酸化防止剤、帯電防止剤などの助剤を本発明の効果に影響を与えない範囲で添加してもよい。白色度を高くするために、酸化チタン、タルク、炭酸カルシウムなどの填料を少量添加してもよい。 Moreover, you may add auxiliary agents, such as a compatibilizing agent, resin antioxidant, and an antistatic agent, as needed, in the range which does not affect the effect of this invention. In order to increase the whiteness, a small amount of filler such as titanium oxide, talc, calcium carbonate may be added.
本実施形態に係る紙含有樹脂組成物では、紙の粉砕物と填料とを含む紙素材の合計量が、51質量%以上であることが好ましい。環境配慮型紙含有樹脂組成物とすることができる。より好ましくは、51〜70質量%である。紙含有樹脂組成物中の紙素材以外の成分は、樹脂を主成分とする。紙の粉砕物には、ラミネート紙の場合は、その構成するすべての成分を含む。例えば、NBKP、NBKP以外のパルプ、原紙中の樹脂分、原紙中の填料、ラミネートフィルムを含む。填料は、紙粉砕物と樹脂を混練するときに、必要に応じて添加されるものである。 In the paper-containing resin composition according to the present embodiment, the total amount of paper materials including the pulverized paper material and the filler is preferably 51% by mass or more. It can be set as an environment-friendly paper-containing resin composition. More preferably, it is 51-70 mass%. Components other than the paper material in the paper-containing resin composition are mainly composed of a resin. In the case of a laminated paper, the pulverized paper includes all the constituents. For example, NBKP, pulp other than NBKP, resin content in base paper, filler in base paper, and laminate film are included. The filler is added as necessary when the pulverized paper and the resin are kneaded.
本実施形態の紙含有樹脂組成物は、二軸押出機で混練することが好ましく、このとき未分散物が少なくなり、均質化されやすい。二軸押出機による処理は、1回よりも2回以上の方がより均質化させることができるため好ましい。このとき、100〜200℃の温度で混練することがより好ましい。二軸押出機で混練する前に、所定の割合になるように計量された紙粉砕物及び樹脂並びに必要に応じて添加する流動性向上剤などの助剤をヘンシェルミキサーなどの混合機で予め均一に混合しておくことが好ましい。二軸押出機のスクリューによる流動、混練作用によって、繊維の解繊と切断とがなされ、紙含有樹脂組成物の分散性と流動性が改善される。 The paper-containing resin composition of the present embodiment is preferably kneaded with a twin-screw extruder, and at this time, the amount of undispersed material is reduced and is easily homogenized. The treatment with a twin screw extruder is preferable because it can be more homogeneous twice or more than once. At this time, it is more preferable to knead | mix at the temperature of 100-200 degreeC. Before kneading with a twin screw extruder, paper pulverized material and resin weighed to a predetermined ratio, and auxiliary agents such as a fluidity improver to be added as necessary are uniformly mixed in a mixer such as a Henschel mixer. It is preferable to mix them. The fibers are defibrated and cut by the flow and kneading action of the screw of the twin screw extruder, and the dispersibility and fluidity of the paper-containing resin composition are improved.
本実施形態に係る紙含有樹脂組成物は、ASTM−D1238−04cで規定したMFR(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである。好ましくは、5.0〜22.0g/10minである。MFRがこの範囲に入る紙含有樹脂組成物は、NBKPを50質量%以上含有する原紙をベースとした紙の粉砕物を含有しているにもかかわらず、紙粉砕物と樹脂とが十分に均一分散されている。MFRが2.0g/10min未満であると、紙粉砕物と樹脂との分散が不十分である。また、NBKPを多く含有している本実施形態では、紙粉砕物と樹脂との分散が十分に為されると、MFRは25.0g/10minに近づく。このMFRの値は、二軸押出機で混練するときに、流動性向上剤の添加の有無によって大きく影響を受けない。また、JIS K 7209:2000「プラスチック−吸水率の求め方」D法に準じて測定した吸水率が、0.10未満であることが好ましい。JIS K 7113:1995「プラスチックの引張試験方法」に準じて測定した引張強度が、33MPa以上であることが好ましい。さらにJIS K 7203:1995「硬質プラスチックの曲げ試験方法」に準じて測定した曲げ強度が、63MPa以上であることが好ましい。 In the paper-containing resin composition according to this embodiment, the MFR (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c is 2.0 to 25.0 g / 10 min. Preferably, it is 5.0-22.0 g / 10min. The paper-containing resin composition whose MFR falls within this range is sufficiently uniform between the pulverized paper and the resin even though it contains a pulverized paper based on a base paper containing NBKP of 50% by mass or more. Is distributed. When the MFR is less than 2.0 g / 10 min, dispersion of the pulverized paper and the resin is insufficient. Further, in the present embodiment containing a large amount of NBKP, when the pulverized paper and the resin are sufficiently dispersed, the MFR approaches 25.0 g / 10 min. The value of this MFR is not greatly affected by the presence or absence of the addition of a fluidity improver when kneading with a twin screw extruder. Moreover, it is preferable that the water absorptivity measured according to JIS K 7209: 2000 "Plastics-Determination of water absorptivity" D method is less than 0.10. The tensile strength measured according to JIS K 7113: 1995 “Plastic Tensile Test Method” is preferably 33 MPa or more. Furthermore, it is preferable that the bending strength measured according to JIS K 7203: 1995 “Bending test method of hard plastic” is 63 MPa or more.
このように本実施形態に係る紙含有樹脂組成物は、針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙を粉砕して紙の粉砕物を得る工程と、多塩基酸無水物で前記粉砕物をエステル化させる工程と、アルカリ土類金属化合物で有機酸を中和する工程と、少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂組成物を得る工程と、を有する製造方法で得ることができる。なお、ラミネート紙に、ラミネート前のその原紙を添加して使用してもよい。 Thus, the paper-containing resin composition according to this embodiment includes a step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp to obtain a pulverized paper, and a polybasic A step of esterifying the pulverized product with an acid anhydride, a step of neutralizing an organic acid with an alkaline earth metal compound, and at least the pulverized product and a polypropylene resin are kneaded with a twin screw extruder, and ASTM-D1238. And a step of obtaining a paper-containing resin composition having a melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) of 2.0 to 25.0 g / 10 min as defined in -04c. Obtainable. The base paper before lamination may be added to the laminated paper.
次に本実施形態に係る紙含有樹脂成形品は、針葉樹漂白化学パルプを50質量%以上含有する原紙をベースとしたポリエチレンフィルムラミネート紙を粉砕して紙の粉砕物を得る工程と、多塩基酸無水物で前記粉砕物をエステル化させる工程と、アルカリ土類金属化合物で有機酸を中和する工程と、少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、紙含有樹脂組成物を得る工程と、該紙含有樹脂組成物を射出成形機によって成形して、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂成形品を得る工程と、を有する製造方法で得ることができる。ここで、紙含有樹脂組成物を得る工程及び/又は紙含有樹脂成形品を得る工程において、流動性向上剤を添加することが好ましい。 Next, the paper-containing resin molded product according to this embodiment includes a step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by mass or more of softwood bleached chemical pulp to obtain a pulverized paper product, and a polybasic acid A step of esterifying the pulverized product with an anhydride, a step of neutralizing an organic acid with an alkaline earth metal compound, and at least the pulverized product and a polypropylene resin are kneaded with a twin screw extruder, and a paper-containing resin composition And a melt mass flow rate (MFR) defined by ASTM-D1238-04c (test temperature = 190 ° C., test load = 10 kg) is obtained by molding the paper-containing resin composition with an injection molding machine. And a step of obtaining a paper-containing resin molded product having a size of 0 to 25.0 g / 10 min. Here, it is preferable to add a fluidity improver in the step of obtaining the paper-containing resin composition and / or the step of obtaining the paper-containing resin molded product.
このようにして得られた本実施形態に係る紙含有樹脂成形品は、多塩基酸無水物でエステル化された紙の粉砕物、ポリプロピレン樹脂、ポリエチレン樹脂及びアルカリ土類金属化合物を少なくとも含有し、粉砕物及びポリプロピレン樹脂が主要成分であり、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである。前記紙は好ましくは、NBKPを50質量%以上含有する。また、MFRは、より好ましくは5.0〜22.0g/10minである。紙含有樹脂組成物のMFRの値と紙含有樹脂成形品にした後のMFRの値は、ほぼ同等となる。この紙含有樹脂成形品は、変色及び臭気がなく、衝撃強度が優れる。 The paper-containing resin molded article according to this embodiment thus obtained contains at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin, and an alkaline earth metal compound, The pulverized product and the polypropylene resin are main components, and the melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c is 2.0 to 25.0 g / 10 min. The paper preferably contains 50% by mass or more of NBKP. Further, the MFR is more preferably 5.0 to 22.0 g / 10 min. The MFR value of the paper-containing resin composition and the MFR value after making the paper-containing resin molded product are substantially the same. This paper-containing resin molded product is free from discoloration and odor and has excellent impact strength.
本実施形態の紙含有樹脂成形品では、含有されているラミネート紙が、液体容器用のポリエチレンフィルムラミネート紙、該ポリエチレンフィルムラミネート紙の断裁屑及び/又は該ポリエチレンフィルムラミネート紙の回収古紙であることを含み、資源の有効活用がなされる。また、紙含有樹脂成形品中の紙の粉砕物と填料とを含む紙素材の合計量が、51質量%以上であることが好ましく、環境配慮型となる。紙含有樹脂成形品としては、例えば、皿、コップ、ボウル、スプーン、櫛などがある。 In the paper-containing resin molded product of the present embodiment, the laminated paper contained is a polyethylene film laminated paper for liquid containers, cutting scraps of the polyethylene film laminated paper, and / or recovered waste paper of the polyethylene film laminated paper. And effective use of resources. Moreover, it is preferable that the total amount of the paper material including the pulverized paper and the filler in the paper-containing resin molded product is 51% by mass or more, which is an environment-friendly type. Examples of the paper-containing resin molded product include a dish, a cup, a bowl, a spoon, and a comb.
次に、実施例を挙げて本発明をより具体的に説明するが、本発明はこれら実施例に限定されるものではない。また、例中の「%」は特に断らない限り「質量%」を示す。 Next, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to these examples. Further, “%” in the examples represents “% by mass” unless otherwise specified.
(実施例1)
[紙粉砕物の製造]
ポリエチレンフィルムラミネート紙の原紙が、NBKPを90質量%含有し、坪量393g/m2、厚さ0.48mm、密度0.82g/cm3のミルクカートン印刷トリミング屑を粉砕機(型式 BO−2575及びHaA−2542:ホーライ社製)にて粉砕し、0.5mmφのスクリーンを通過させポリエチレンフィルムラミネート紙の粉砕物を得た。
[紙含有樹脂組成物の製造]
次いで、無水マレイン酸(商品名 無水マレイン酸:日本油脂社製)をパルプ成分に対し0.5質量%となる量を加え、上記粉砕物に酸化チタン(商品名 タイペークA-220:石原産業社製)、変性PP樹脂(商品名 ユーメックス1010:サンノプコ社製)及びPP樹脂(商品名 J-5051HP:出光石油化学社製)を加え、更に中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を全質量に対し0.5質量%となる量を加え、ヘンシェルミキサーで均一に混合し、その後デスクペレッター(型式 F−60:不二パウダル社製)及び二軸押出機に投入してペレット化し、紙含有樹脂組成物を得た。この紙含有樹脂組成物の中の紙比率は、55質量%であった。
[評価用射出成形品の製造]
紙含有樹脂組成物から、シリンダー設定温度180℃の射出成形機(型式 J35ELII:日本製鋼所社製)を用いて評価用射出成形品を作製した。
(Example 1)
[Manufacture of crushed paper]
The base paper of the polyethylene film laminated paper contains 90% by mass of NBKP, grinds the milk carton printing trimming waste having a basis weight of 393 g / m 2 , a thickness of 0.48 mm, and a density of 0.82 g / cm 3 (model BO-2575). And HaA-2542: manufactured by Horai Co., Ltd.) and passed through a 0.5 mmφ screen to obtain a pulverized polyethylene film laminated paper.
[Production of paper-containing resin composition]
Subsequently, maleic anhydride (trade name: maleic anhydride: manufactured by Nippon Oil & Fats Co., Ltd.) was added in an amount of 0.5% by mass with respect to the pulp component, and titanium oxide (trade name: Typaque A-220: Ishihara Sangyo Co., Ltd.) was added to the pulverized product. Manufactured), modified PP resin (trade name: Umex 1010: manufactured by San Nopco) and PP resin (trade name: J-5051HP: manufactured by Idemitsu Petrochemical Co., Ltd.), and magnesium oxide (trade name: magnesium oxide: Tomita Pharmaceutical) Add 0.5% by mass to the total mass, mix uniformly with a Henschel mixer, and then put into a desk pelleter (model F-60: manufactured by Fuji Powder Co., Ltd.) and a twin screw extruder. And pelletized to obtain a paper-containing resin composition. The paper ratio in this paper-containing resin composition was 55% by mass.
[Manufacture of injection molded products for evaluation]
From the paper-containing resin composition, an injection molded product for evaluation was produced using an injection molding machine (model J35ELII: manufactured by Nippon Steel Works) with a cylinder set temperature of 180 ° C.
(実施例2)
実施例1の紙粉砕物の製造において、スクリーンを0.5mmφのスクリーンから1.0mmφのスクリーンに変更し、無水マレイン酸(商品名 無水マレイン酸:日本油脂社製)をパルプ成分に対し0.5質量%から1.5質量%となる量に変更し、中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を全質量に対し0.5質量%から1.5質量%となる量に変更した以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。この紙含有樹脂組成物の中の紙比率は、55質量%であった。
(Example 2)
In the production of the pulverized paper of Example 1, the screen was changed from a 0.5 mmφ screen to a 1.0 mmφ screen, and maleic anhydride (trade name: maleic anhydride: manufactured by NOF Corporation) was adjusted to 0.000 with respect to the pulp components. The amount is changed from 5% by mass to 1.5% by mass, and magnesium oxide (trade name: Magnesium oxide: manufactured by Tomita Pharmaceutical Co., Ltd.) as a neutralizing agent is 0.5% by mass to 1.5% by mass with respect to the total mass. A paper-containing resin composition and an evaluation injection-molded product were obtained in the same manner except that the amount was changed. The paper ratio in this paper-containing resin composition was 55% by mass.
(実施例3)
実施例2の紙粉砕物の製造において、粉砕物の原料を、ミルクカートン印刷トリミング屑から、ポリエチレンフィルムラミネート紙の原紙がNBKPを80質量%含有し、坪量362g/m2、厚さ0.47mm、密度0.78g/cm3の回収牛乳パックに変更した以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。この紙含有樹脂組成物の中の紙比率は、55質量%であった。
(Example 3)
In the production of the paper pulverized product of Example 2, the raw material of the pulverized product was made from milk carton printing trimming waste, the base paper of the polyethylene film laminated paper contained 80% by mass of NBKP, the basis weight was 362 g / m 2 , and the thickness was 0.00. A paper-containing resin composition and an evaluation injection-molded product were obtained in the same manner except that the recovered milk pack was changed to 47 mm and density 0.78 g / cm 3 . The paper ratio in this paper-containing resin composition was 55% by mass.
(実施例4)
実施例3の紙含有樹脂組成物の製造において、紙粉砕物の配合量を、紙含有樹脂組成物の中の紙比率が55質量%となる量から紙含有樹脂組成物の中の紙比率が60質量%となる量に変更し、実施例3の紙粉砕物の製造において、スクリーンを1.0mmφのスクリーンから2.0mmφのスクリーンに変更し、無水マレイン酸(商品名 無水マレイン酸:日本油脂社製)をパルプ成分に対し1.5質量%から2.0質量%となる量に変更し、中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を全質量に対し1.5質量%から2.0質量%となる量に変更した以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。
Example 4
In the production of the paper-containing resin composition of Example 3, the blended amount of the paper pulverized product was changed from the amount that the paper ratio in the paper-containing resin composition was 55% by mass to the paper ratio in the paper-containing resin composition. In the production of the pulverized paper of Example 3, the screen was changed from a 1.0 mmφ screen to a 2.0 mmφ screen in the production of the crushed paper of Example 3, and maleic anhydride (trade name: maleic anhydride: Nippon Oil & Fats) The product was changed from 1.5% by mass to 2.0% by mass with respect to the pulp component, and magnesium oxide (trade name: Magnesium oxide: manufactured by Tomita Pharmaceutical Co., Ltd.) as a neutralizing agent was 1. A paper-containing resin composition and an evaluation injection molded product were obtained in the same manner except that the amount was changed from 5% by mass to 2.0% by mass.
(比較例1)
実施例1の紙粉砕物の製造において、スクリーンを0.5mmφのスクリーンから3.0mmφのスクリーンに変更し、中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を無添加とした以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。この紙含有樹脂組成物の中の紙比率は、55質量%であった。
(Comparative Example 1)
In the production of the pulverized paper of Example 1, the screen was changed from a 0.5 mmφ screen to a 3.0 mmφ screen, and magnesium oxide (trade name magnesium oxide: manufactured by Tomita Pharmaceutical Co., Ltd.) was not added as a neutralizing agent. Except for the above, a paper-containing resin composition and an evaluation injection-molded product were obtained in the same manner. The paper ratio in this paper-containing resin composition was 55% by mass.
(比較例2)
実施例1の紙含有樹脂組成物の製造において、無水マレイン酸(商品名 無水マレイン酸:日本油脂社製)をパルプ成分に対し0.5質量%から無添加に変更し、中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を全質量に対し0.5質量%から無添加に変更したとした以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。
(Comparative Example 2)
In the production of the paper-containing resin composition of Example 1, maleic anhydride (trade name: maleic anhydride: manufactured by Nippon Oil & Fats Co., Ltd.) was changed from 0.5% by mass to no addition to the pulp component, and oxidized as a neutralizing agent. A paper-containing resin composition and an injection-molded product for evaluation were obtained in the same manner except that magnesium (trade name: magnesium oxide: manufactured by Tomita Pharmaceutical Co., Ltd.) was changed from 0.5% by mass to no additive with respect to the total mass. .
(比較例3)
実施例3の紙含有樹脂組成物の製造において、無水マレイン酸(商品名 無水マレイン酸:日本油脂社製)をパルプ成分に対し1.5質量%から無添加に変更し、中和剤として酸化マグネシウム(商品名 酸化マグネシウム:富田製薬社製)を全質量に対し1.5質量%から無添加に変更したとした以外は同じ方法で、紙含有樹脂組成物及び評価用射出成形品を得た。
(Comparative Example 3)
In the production of the paper-containing resin composition of Example 3, maleic anhydride (trade name: maleic anhydride: manufactured by Nippon Oil & Fats Co., Ltd.) was changed from 1.5% by mass to no addition to the pulp component, and oxidized as a neutralizing agent. A paper-containing resin composition and an injection molded product for evaluation were obtained in the same manner except that magnesium (trade name: magnesium oxide: manufactured by Tomita Pharmaceutical Co., Ltd.) was changed from 1.5% by mass to no additive with respect to the total mass. .
上記実施例1〜4、比較例1〜3で用いたラミネート古紙、得られた紙粉砕物及び紙含有樹脂組成物並びに評価用射出成形品の評価は下記の方法で行い、結果を表1に示した。 The laminated waste paper used in Examples 1 to 4 and Comparative Examples 1 to 3, the obtained paper pulverized product, the paper-containing resin composition, and the evaluation injection molded product were evaluated by the following methods, and the results are shown in Table 1. Indicated.
<紙比率>
紙含有樹脂組成物の中の紙の占める割合を紙比率と表示し、ここでは紙と炭酸カルシウムなどの填料の合計量を紙素材分とした。
<Paper ratio>
The ratio of the paper in the paper-containing resin composition is indicated as the paper ratio, and here, the total amount of paper and fillers such as calcium carbonate is defined as the paper material.
<MFR>
ASTM D1238-04c「Standard Test Method for Flow Rates of Thermoplastics by Extrusion Plastometer」に準じて測定。試験温度=190℃、試験荷重=10kg。紙含有樹脂組成物について測定した。
<MFR>
Measured according to ASTM D1238-04c, “Standard Test Method for Flow Rates of Thermoplastics by Extraction Plasometer”. Test temperature = 190 ° C., test load = 10 kg. It measured about the paper containing resin composition.
<繊維分散性>
紙含有樹脂組成物に所定量のカーボンブラックを配合して評価用射出成形品を作製し、繊維の分散の程度を次の基準で評価した。
×:繊維の未分散多数、劣り実用に耐えない。
△:繊維の未分散ややあり、やや劣り実用に耐えない。
○:繊維の未分散なし、優れる。
<Fiber dispersibility>
A predetermined amount of carbon black was blended with the paper-containing resin composition to produce an evaluation injection molded product, and the degree of fiber dispersion was evaluated according to the following criteria.
X: Many undispersed fibers, inferior to practical use.
Δ: Some undispersed fibers, slightly inferior and not practical.
○: No undispersed fiber, excellent.
<成形性>
紙含有樹脂組成物から成形品を作製する成形加工のときの作業性を次の基準で評価した。
×:成形品が得られなかった、
△:成形性が不良であり、実用に耐えない、
○:成形性が良好。
<Moldability>
Workability at the time of molding processing for producing a molded product from the paper-containing resin composition was evaluated according to the following criteria.
X: The molded product was not obtained.
Δ: Formability is poor and cannot be practically used.
○: Good formability.
<変色>
成形品を視感にて次の基準で判定した。
×:明らかな黄色味あり、劣り実用に耐えない、
△:黄色味ややあり、劣り実用に耐えない、
○:黄色身がなく、優れる。
<Discoloration>
The molded product was judged based on the following criteria based on visual sensation.
×: Obvious yellowish, inferior to practical use,
Δ: Slightly yellowish, inferior to practical use,
○: Excellent without yellow.
<臭気>
成形品の臭気を次の基準で判定した。
△:紙焼けの臭気がややあり、劣り実用に耐えない、
○:臭気なく、優れる。
<Odor>
The odor of the molded product was determined according to the following criteria.
Δ: Slightly burnt odor, inferior to practical use
○: Excellent without odor.
<引張強度>
JIS K 7113:1995「プラスチックの引張試験方法」に準じて測定した。
<Tensile strength>
Measured according to JIS K 7113: 1995 “Plastic Tensile Test Method”.
<曲げ強度>
JIS K 7203:1995「硬質プラスチックの曲げ試験方法」に準じて測定した。
<Bending strength>
Measured according to JIS K 7203: 1995 “Bending test method of hard plastic”.
<IZOD(アイゾット衝撃強度)>
ASTM D256−04「Test Methods for Determination of thwPendulum Impact Resistance of Notched Specimens of Plastics」(ノッチなし)に準じて測定した。
<IZOD (Izod impact strength)>
Measured according to ASTM D256-04 “Test Methods for Determination of the Pendulum Impact Resistance of Notched Specimens of Plastics” (no notch).
<吸水率>
JIS K 7209:2000「プラスチック−吸水率の求め方」D法 に準じて測定した。
<Water absorption rate>
Measured according to JIS K 7209: 2000 “Plastics—How to Obtain Water Absorption” Method D.
実施例1及び2では、ポリエチレンフィルムラミネート紙の原紙のNBKPが90質量%のミルクカートン印刷トリミング屑を使用して紙含有樹脂組成物を作製した。いずれの紙含有樹脂組成物も、NBKPの含有量が高いにもかかわらず、粉砕物のエステル化と二軸押出機の混練によって均一分散できたため、繊維分散性と成形性が良好であり、得られた成形品は、変色及び臭気もなかった。 In Examples 1 and 2, a paper-containing resin composition was prepared using milk carton printing trimming waste having NBKP of 90% by mass of the base film of polyethylene film laminated paper. All of the paper-containing resin compositions had good fiber dispersibility and moldability because they could be uniformly dispersed by esterification of the pulverized product and kneading by the twin screw extruder, despite the high NBKP content. The molded product obtained was neither discolored nor odorous.
実施例3及び4では、ポリエチレンフィルムラミネート紙の原紙のNBKPが80質量%の回収牛乳パックを使用して紙含有樹脂組成物を作製した。NBKPの含有量が高いにもかかわらず、粉砕物のエステル化と二軸押出機の混練によって均一分散できたため、繊維分散性と成形性が良好であり、得られた成形品は、変色及び臭気もなかった。 In Examples 3 and 4, a paper-containing resin composition was prepared using a recovered milk pack having an NBKP of 80% by mass as a base film of polyethylene film laminated paper. Despite having a high NBKP content, uniform dispersion was achieved by esterification of the pulverized product and kneading by a twin-screw extruder. Therefore, the fiber dispersibility and moldability were good, and the obtained molded product had discoloration and odor. There was not.
比較例1では、MFRの値が5g/10minであるが、ミルクカートン印刷トリミング屑の粉砕粒径が大きい為、分散性が不十分となり繊維分散性と成形性が不良であった。また中和剤を添加しなかった為、得られた成形品は、変色及び臭気が見られた。 In Comparative Example 1, the MFR value was 5 g / 10 min. However, since the pulverized particle size of the milk carton printing trimming waste was large, the dispersibility was insufficient and the fiber dispersibility and moldability were poor. Moreover, since the neutralizing agent was not added, the obtained molded product showed discoloration and odor.
機械的強度、特に引張強度、曲げ強度及び吸水率は、比較例と比べると実施例では良好であった。 The mechanical strength, particularly tensile strength, bending strength, and water absorption were better in the examples than in the comparative examples.
Claims (14)
前記粉砕物及び前記ポリプロピレン樹脂が主要成分であり、
ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minであることを特徴とする紙含有樹脂組成物。 Containing at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin and an alkaline earth metal compound;
The pulverized product and the polypropylene resin are main components,
A paper-containing resin composition having a melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c of 2.0 to 25.0 g / 10 min.
前記粉砕物及び前記ポリプロピレン樹脂が主要成分であり、
ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minであることを特徴とする紙含有樹脂成形品。 Containing at least a pulverized paper esterified with a polybasic acid anhydride, a polypropylene resin, a polyethylene resin and an alkaline earth metal compound;
The pulverized product and the polypropylene resin are main components,
A paper-containing resin molded product having a melt mass flow rate (MFR) defined by ASTM-D1238-04c (test temperature = 190 ° C., test load = 10 kg) of 2.0 to 25.0 g / 10 min.
多塩基酸無水物で前記粉砕物をエステル化させる工程と、
アルカリ土類金属化合物で有機酸を中和する工程と、
少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂組成物を得る工程と、
を有することを特徴とする紙含有樹脂組成物の製造方法。 A step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by weight or more of softwood bleached chemical pulp to obtain a pulverized paper,
Esterifying the pulverized product with a polybasic acid anhydride;
Neutralizing the organic acid with an alkaline earth metal compound;
At least the pulverized product and the polypropylene resin are kneaded by a twin screw extruder, and a melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c is 2.0 to 25. Obtaining a paper-containing resin composition that is 0.0 g / 10 min;
A method for producing a paper-containing resin composition, comprising:
多塩基酸無水物で前記粉砕物をエステル化させる工程と、
アルカリ土類金属化合物で有機酸を中和する工程と、
少なくとも前記粉砕物とポリプロピレン樹脂とを、二軸押出機で混練し、紙含有樹脂組成物を得る工程と、
該紙含有樹脂組成物を射出成形機によって成形して、ASTM−D1238−04cで規定したメルトマスフローレイト(MFR)(試験温度=190℃、試験荷重=10kg)が2.0〜25.0g/10minである紙含有樹脂成形品を得る工程と、
を有することを特徴とする紙含有樹脂成形品の製造方法。 A step of pulverizing a polyethylene film laminated paper based on a base paper containing 50% by weight or more of softwood bleached chemical pulp to obtain a pulverized paper,
Esterifying the pulverized product with a polybasic acid anhydride;
Neutralizing the organic acid with an alkaline earth metal compound;
Kneading at least the pulverized product and polypropylene resin with a twin-screw extruder to obtain a paper-containing resin composition;
The paper-containing resin composition was molded by an injection molding machine, and the melt mass flow rate (MFR) (test temperature = 190 ° C., test load = 10 kg) defined by ASTM-D1238-04c was 2.0 to 25.0 g / Obtaining a paper-containing resin molded product that is 10 min;
A method for producing a paper-containing resin molded product, comprising:
14. The paper-containing resin molded article according to claim 11, wherein a fluidity improver is added in the step of obtaining the paper-containing resin composition and / or the step of obtaining the paper-containing resin molded article. Manufacturing method.
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JP2009161700A (en) * | 2008-01-09 | 2009-07-23 | Hokuetsu Paper Mills Ltd | Paper-containing resin composition, molded article of the same, and methods for producing them |
WO2013141548A1 (en) * | 2012-03-19 | 2013-09-26 | 주식회사 에스에이치글로벌 | Plastic, for automotive interior parts, manufactured from biomass pellets, and method for manufacturing the plastic |
KR20160139429A (en) * | 2015-05-27 | 2016-12-07 | (주) 케이엠팩 | Resin composition for tray comprising the pellet powder manufactured using polyethylene separated from milk carton paper and the tray manufactured using the same |
JP2017002312A (en) * | 2012-02-14 | 2017-01-05 | ウェヤーハウザー・エヌアール・カンパニー | Composite polymer |
CN114729169A (en) * | 2019-11-18 | 2022-07-08 | 赛佩荷兰服务有限公司 | Non-corrosive fiber reinforced polymer composition |
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