JPH04156302A - Manufacture of thermoplastic wood-based material composition excellent in heat fluidity - Google Patents
Manufacture of thermoplastic wood-based material composition excellent in heat fluidityInfo
- Publication number
- JPH04156302A JPH04156302A JP28058590A JP28058590A JPH04156302A JP H04156302 A JPH04156302 A JP H04156302A JP 28058590 A JP28058590 A JP 28058590A JP 28058590 A JP28058590 A JP 28058590A JP H04156302 A JPH04156302 A JP H04156302A
- Authority
- JP
- Japan
- Prior art keywords
- wood
- monoepoxy compound
- composition
- based material
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002023 wood Substances 0.000 title claims abstract description 172
- 239000000463 material Substances 0.000 title claims abstract description 66
- 239000000203 mixture Substances 0.000 title claims abstract description 55
- 229920001169 thermoplastic Polymers 0.000 title claims description 38
- 239000004416 thermosoftening plastic Substances 0.000 title claims description 38
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 150000001875 compounds Chemical class 0.000 claims abstract description 48
- 150000008065 acid anhydrides Chemical class 0.000 claims abstract description 25
- 150000007519 polyprotic acids Polymers 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 15
- 239000002253 acid Substances 0.000 abstract description 14
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract description 11
- 239000000843 powder Substances 0.000 abstract description 10
- 239000010875 treated wood Substances 0.000 abstract description 10
- 238000001125 extrusion Methods 0.000 abstract description 6
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 abstract description 4
- 239000000835 fiber Substances 0.000 abstract description 3
- 238000001746 injection moulding Methods 0.000 abstract description 3
- 238000010025 steaming Methods 0.000 abstract description 3
- 238000005886 esterification reaction Methods 0.000 abstract description 2
- 229920006395 saturated elastomer Polymers 0.000 abstract description 2
- 239000002360 explosive Substances 0.000 abstract 5
- 125000001931 aliphatic group Chemical group 0.000 abstract 1
- 230000006837 decompression Effects 0.000 abstract 1
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 38
- 239000004593 Epoxy Substances 0.000 description 15
- 238000000944 Soxhlet extraction Methods 0.000 description 14
- 238000006266 etherification reaction Methods 0.000 description 12
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 12
- 238000005422 blasting Methods 0.000 description 11
- 239000003054 catalyst Substances 0.000 description 11
- 238000002156 mixing Methods 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 10
- 235000013312 flour Nutrition 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 description 7
- FQYUMYWMJTYZTK-UHFFFAOYSA-N Phenyl glycidyl ether Chemical compound C1OC1COC1=CC=CC=C1 FQYUMYWMJTYZTK-UHFFFAOYSA-N 0.000 description 7
- 150000008064 anhydrides Chemical group 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- 229940014800 succinic anhydride Drugs 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- YSUQLAYJZDEMOT-UHFFFAOYSA-N 2-(butoxymethyl)oxirane Chemical compound CCCCOCC1CO1 YSUQLAYJZDEMOT-UHFFFAOYSA-N 0.000 description 6
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 6
- 238000000465 moulding Methods 0.000 description 6
- 235000011056 potassium acetate Nutrition 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 241001618203 Melanoxylon Species 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 5
- 239000011260 aqueous acid Substances 0.000 description 4
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229920005610 lignin Polymers 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 239000001913 cellulose Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- 125000003700 epoxy group Chemical group 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 150000004665 fatty acids Chemical class 0.000 description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 238000004448 titration Methods 0.000 description 3
- OKIZCWYLBDKLSU-UHFFFAOYSA-M N,N,N-Trimethylmethanaminium chloride Chemical compound [Cl-].C[N+](C)(C)C OKIZCWYLBDKLSU-UHFFFAOYSA-M 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 description 2
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229920002522 Wood fibre Polymers 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 235000013325 dietary fiber Nutrition 0.000 description 2
- XXBDWLFCJWSEKW-UHFFFAOYSA-N dimethylbenzylamine Chemical compound CN(C)CC1=CC=CC=C1 XXBDWLFCJWSEKW-UHFFFAOYSA-N 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000002025 wood fiber Substances 0.000 description 2
- KMOUUZVZFBCRAM-OLQVQODUSA-N (3as,7ar)-3a,4,7,7a-tetrahydro-2-benzofuran-1,3-dione Chemical compound C1C=CC[C@@H]2C(=O)OC(=O)[C@@H]21 KMOUUZVZFBCRAM-OLQVQODUSA-N 0.000 description 1
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical group CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 1
- STMDPCBYJCIZOD-UHFFFAOYSA-N 2-(2,4-dinitroanilino)-4-methylpentanoic acid Chemical compound CC(C)CC(C(O)=O)NC1=CC=C([N+]([O-])=O)C=C1[N+]([O-])=O STMDPCBYJCIZOD-UHFFFAOYSA-N 0.000 description 1
- LKMJVFRMDSNFRT-UHFFFAOYSA-N 2-(methoxymethyl)oxirane Chemical compound COCC1CO1 LKMJVFRMDSNFRT-UHFFFAOYSA-N 0.000 description 1
- AGULWIQIYWWFBJ-UHFFFAOYSA-N 3,4-dichlorofuran-2,5-dione Chemical compound ClC1=C(Cl)C(=O)OC1=O AGULWIQIYWWFBJ-UHFFFAOYSA-N 0.000 description 1
- OFNISBHGPNMTMS-UHFFFAOYSA-N 3-methylideneoxolane-2,5-dione Chemical compound C=C1CC(=O)OC1=O OFNISBHGPNMTMS-UHFFFAOYSA-N 0.000 description 1
- 240000005020 Acaciella glauca Species 0.000 description 1
- 235000018782 Dacrydium cupressinum Nutrition 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- 235000013697 Pinus resinosa Nutrition 0.000 description 1
- 241000785681 Sander vitreus Species 0.000 description 1
- 239000003568 Sodium, potassium and calcium salts of fatty acids Substances 0.000 description 1
- QHWKHLYUUZGSCW-UHFFFAOYSA-N Tetrabromophthalic anhydride Chemical compound BrC1=C(Br)C(Br)=C2C(=O)OC(=O)C2=C1Br QHWKHLYUUZGSCW-UHFFFAOYSA-N 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N acetic acid Substances CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 1
- MNZMECMQTYGSOI-UHFFFAOYSA-N acetic acid;hydron;bromide Chemical compound Br.CC(O)=O MNZMECMQTYGSOI-UHFFFAOYSA-N 0.000 description 1
- 125000004018 acid anhydride group Chemical group 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- GYZLOYUZLJXAJU-UHFFFAOYSA-N diglycidyl ether Chemical compound C1OC1COCC1CO1 GYZLOYUZLJXAJU-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000011094 fiberboard Substances 0.000 description 1
- ANSXAPJVJOKRDJ-UHFFFAOYSA-N furo[3,4-f][2]benzofuran-1,3,5,7-tetrone Chemical compound C1=C2C(=O)OC(=O)C2=CC2=C1C(=O)OC2=O ANSXAPJVJOKRDJ-UHFFFAOYSA-N 0.000 description 1
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 239000010893 paper waste Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 235000013966 potassium salts of fatty acid Nutrition 0.000 description 1
- CASUWPDYGGAUQV-UHFFFAOYSA-M potassium;methanol;hydroxide Chemical compound [OH-].[K+].OC CASUWPDYGGAUQV-UHFFFAOYSA-M 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000007017 scission Effects 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
- SRPWOOOHEPICQU-UHFFFAOYSA-N trimellitic anhydride Chemical compound OC(=O)C1=CC=C2C(=O)OC(=O)C2=C1 SRPWOOOHEPICQU-UHFFFAOYSA-N 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、押出し成形用材料として使用可能な熱流動性
に優れた熱可塑性木質材組成物の製造方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing a thermoplastic wood composition having excellent thermal fluidity and usable as an extrusion molding material.
石油や石炭等の化石資源より得られる合成樹脂類は、安
価で且つ熱圧成形等の加工方法で容易に加工できるため
、工業用原料として大量に用いられているが、その埋蔵
量には限界があり、それら資源の枯渇が世界的な問題と
なっている。一方、木材を代表とする木質材料は、再生
産可能な資源として最近注目を集めている。しかしなが
ら、木材を粉砕しただけの木質材料は、熱圧成形ができ
ないため、任意の形状、特に任意の曲面に加工するのは
容易ではない。Synthetic resins obtained from fossil resources such as petroleum and coal are used in large quantities as industrial raw materials because they are inexpensive and can be easily processed using processing methods such as hot pressing, but there is a limit to their reserves. The depletion of these resources has become a global problem. On the other hand, wood materials such as wood have recently attracted attention as a renewable resource. However, since a wood material made by simply crushing wood cannot be hot-pressed, it is not easy to process it into any shape, especially any curved surface.
また、従来、木質材料は、その優れた特徴を生かして建
築材料を始め、その他種々の用途に使用されてきている
が、小径木や間伐材、或は木材工場から排出されるオガ
クズ等は、大部分が焼却等の方法で廃棄されており、有
効な利用方法の開発が望まれている。In addition, wood materials have traditionally been used for various purposes such as building materials due to their excellent characteristics, but small-diameter trees, thinned wood, and sawdust discharged from wood factories are Most of the waste is disposed of by methods such as incineration, and there is a desire to develop effective ways to use it.
これら木質材料を熱圧成形可能な材料とするため、本発
明者等は、先に、改質木材小片の製造方法(特開昭6O
−83806)を提案した。この改質木材小片は、木材
小片に二塩基酸無水物とモノエポキシ化合物とを付加エ
ステル化反応させたものであり、熱圧加工が可能で、耐
湿、耐水性に優れた表面の固いシートまたはボードとす
ることができるものである。In order to make these wood materials into materials that can be molded under heat and pressure, the present inventors first developed a method for producing modified wood pieces (Japanese Patent Laid-Open No.
-83806) was proposed. These modified wood chips are made by subjecting wood chips to an addition esterification reaction with a dibasic acid anhydride and a monoepoxy compound, and can be heat-press processed into hard sheets or sheets with excellent moisture and water resistance. It can be used as a board.
また、特開昭62−77903では、脂肪酸のカリウム
塩の存在下、木材小片とエポキシ化合物を常圧下かつ無
溶媒中で反応させ、来月にエーテル結合を介して有機基
を結合させた化学修飾木質材の製造方法を従業じた。In addition, in JP-A-62-77903, a chemical modification in which small pieces of wood and an epoxy compound are reacted under normal pressure and without a solvent in the presence of potassium salts of fatty acids, and organic groups are bonded through ether bonds. We have developed a method for manufacturing wood materials.
しかしながら、これら改質木材小片および化学修飾木質
材(以下、これらを総称して化学修飾木質+オと略記す
る)は、成形品とするのに、180〜200 ’C,3
00kg/ct以上と相当な高温高圧で熱圧成形する必
要があり、生産性およびエネルギー効率の点からも好ま
しくない。However, these modified wood pieces and chemically modified wood materials (hereinafter collectively abbreviated as "chemically modified wood + O") require a temperature of 180 to 200'C, 3
It is necessary to perform hot-press molding at a considerably high temperature and pressure of 00 kg/ct or more, which is not preferable from the viewpoint of productivity and energy efficiency.
上記の他にも、木質材を熱可塑性とすべく研究が進めら
れており、木質材に熱流動性を付与するには、木質材中
のセルロースの結晶構造を崩すことが重要であると言わ
れでいる。In addition to the above, research is underway to make wood materials thermoplastic, and it is said that in order to impart thermofluidity to wood materials, it is important to disrupt the crystal structure of cellulose in wood materials. It's me.
一方、爆砕処理した木材は、現在、家畜の粗飼料として
応用が検討され、従来の粗飼料と遜色ないことが確認さ
れている。また、爆砕処理による木材の構造変化につい
ての研究もなされており、爆砕処理により、木材中のセ
ルロースは結晶化度が上昇し、リグニンはアリルエーテ
ル結合が解裂して低分子化すると報告されている。On the other hand, blasted wood is currently being considered for use as roughage for livestock, and it has been confirmed that it is comparable to conventional roughage. Research has also been conducted on structural changes in wood due to blasting treatment, and it has been reported that blasting increases the crystallinity of cellulose in wood, and that lignin becomes lower molecular due to the cleavage of allyl ether bonds. There is.
本発明者等は、比較的高い木質材含量を有しながらも、
熱流動性が優れ、通常の押出し成形条件で成形可能な熱
可塑性木質+4組成物を得るべく検討を行った。The inventors have discovered that while having a relatively high wood content,
Studies were conducted to obtain a thermoplastic wood +4 composition that has excellent thermal fluidity and can be molded under normal extrusion conditions.
本発明者等は、」二記の問題点に鑑み鋭意研究を重ねた
結果、驚くべきことに、爆砕処理した木質材は、爆砕処
理により結晶化度が上昇するにも拘らず、該爆砕処理し
た木質材にモノエポキシ化合物、あるいは、モノエポキ
シ化合物および多塩基酸無水物を反応させて得られる木
質材組成物は、通常の木質材を用いた場合に比べて著し
く優れた熱流動性を有することを見出し、本発明を完成
するに至ったものである。The inventors of the present invention have conducted extensive research in view of the problems mentioned in section 2 above, and have surprisingly found that although the crystallinity of wood materials that have been subjected to blasting treatment increases due to the blasting treatment, The wood composition obtained by reacting a monoepoxy compound or a monoepoxy compound and a polybasic acid anhydride with a wood material has significantly superior thermal fluidity compared to the case where ordinary wood material is used. This discovery led to the completion of the present invention.
即ち、本発明は、爆砕処理した木質材100重= 3
=
置部と、モノエポキシ化合物50〜300重量部、ある
いは、該爆砕処理した木質材100重量部とモノエポキ
シ化合物および多塩基酸無水物を合計で50〜300重
量部とを反応させることを特徴とする熱流動性に優れた
熱可塑性木質材組成物の製造方法を提供するものである
。That is, in the present invention, 100 weights of blasted wood materials = 3
= A feature of reacting the okibe with 50 to 300 parts by weight of a monoepoxy compound, or 100 parts by weight of the blasted wood material and a total of 50 to 300 parts by weight of the monoepoxy compound and polybasic acid anhydride. The present invention provides a method for producing a thermoplastic wood composition having excellent thermal fluidity.
本発明の熱可塑性木質材組成物の製造方法は、木質材成
分として爆砕処理した木質材100重量部にモノエポキ
シ化合物50〜300重量部、あるいはモノエポキシ化
合物と多塩基酸無水物を合計で50〜300重量部とを
反応させるのであるが、例えば、爆砕処理した木質材の
水酸基に、触媒として脂肪酸のカリウム塩の存在下、エ
ーテル結合を介して爆砕処理した木質材の水酸基にモノ
エポキシ化合物を付加させる方法、木質材の水酸基に多
塩基酸無水物とモノエポキシ化合物を交互に付加エステ
ル化反応させる方法等が挙げられる。The method for producing a thermoplastic wood composition of the present invention includes adding 50 to 300 parts by weight of a monoepoxy compound to 100 parts by weight of blast-treated wood as a wood component, or adding 50 to 300 parts by weight of a monoepoxy compound and a polybasic acid anhydride in total. For example, a monoepoxy compound is reacted with the hydroxyl groups of the blasted wood through an ether bond in the presence of a potassium salt of a fatty acid as a catalyst. Examples include a method of adding a polybasic acid anhydride and a monoepoxy compound to the hydroxyl group of a wood material, and a method of alternately adding and esterifying a polybasic acid anhydride and a monoepoxy compound.
これらの方法において、爆砕処理した木質材100重量
部に対し、モノエポキシ化合物、あるいはモノエポキシ
化合物および多塩基酸無水物の合計が50重量部より少
ない場合は、得られた熱可塑性木質材組成物は熱流動性
が乏しく、例えば、熱流動性の一つの指標であるメルト
インデックス(Ml)の測定が不可能である。逆に、爆
砕処理した木質材100重量部に対し、モノエポキシ化
合物、あるいはモノエポキシ化合物および多塩基酸無水
物の合計が300重量部より多い場合は、熱流動性は優
れるものの、木質材含量が低くなりすぎ、本発明の目的
に反するばかりでな(、経済的にも好ましくない。In these methods, if the monoepoxy compound or the total amount of the monoepoxy compound and polybasic acid anhydride is less than 50 parts by weight based on 100 parts by weight of the blasted wood material, the resulting thermoplastic wood composition has poor thermal fluidity, and for example, it is impossible to measure the melt index (Ml), which is one index of thermal fluidity. On the other hand, if the monoepoxy compound or the total amount of monoepoxy compound and polybasic acid anhydride is more than 300 parts by weight per 100 parts by weight of the blasted wood, although the thermal fluidity is excellent, the wood content is This becomes too low, which not only goes against the purpose of the present invention (but is also economically unfavorable).
本発明の熱可塑性木質材組成物の製造に用いられる爆砕
処理した木質材成分としては、原木や樹種には特に制限
はなく、木粉、木材繊維、木材チップ等の木材、未利用
のまま大量に廃棄される麦ワラ、稲ワラ、モミガラ、故
紙、リンター、ハカス等の植物繊維、その他のセルロー
スやリグニンを主成分とするリグノセルロース材料を爆
砕処理後粉砕したものが挙げられる。さらに、水利を使
用する工業において工業廃棄物として副生ずる木材小片
、オガクズを爆砕処理後粉砕したもの、バ−ティクルボ
ード、ファイバーボード等の製造工程中に排出されるザ
ンダー粉等を爆砕処理したものも用いることができる。The blasted wood components used in the production of the thermoplastic wood composition of the present invention are not particularly limited to logs or tree species, and include wood such as wood flour, wood fibers, and wood chips, as well as large amounts of unused wood. Examples include plant fibers such as wheat straw, rice straw, rice husk, waste paper, linters, and lignocellulose materials whose main components are cellulose and lignin, which are discarded in the field, and are pulverized after being blasted. In addition, small pieces of wood and sawdust produced by-product as industrial waste in industries that use water conservancy are blasted and pulverized, and zander powder, etc. discharged during the manufacturing process of particle boards, fiberboards, etc., is blasted and treated. can also be used.
また逆に、上記の木質材成分を粉砕機、ヘンシェルミキ
ザー等によって木材チップ、木材繊維、微細化した木粉
等とした後に、爆砕処理して用いることもできる。爆砕
処理は、3〜50kg/c+品の飽和水藤気中で0.1
〜30分間蒸煮後、象、激に解圧することによって行う
ことができる。このようにして爆砕処理して得られた木
質材成分の含水率が高い場合は、熱風乾燥機や真空乾燥
機等により乾燥して水分を10%以下に除去して用いる
のが好ましい。木質材成分中に水分が多く残存すると、
この水分が多塩基酸無水物の無水酸基と反応して多価カ
ルボン酸を副生じたり、モノエポキシ化合物のエポキシ
基を開環させたりするので好ましくない。Conversely, the above-mentioned wood material components can be processed into wood chips, wood fibers, finely divided wood powder, etc. using a pulverizer, Henschel mixer, etc., and then used by being subjected to explosion treatment. The blasting process is carried out in 3-50 kg/c+ of saturated water with 0.1
This can be done by boiling for ~30 minutes and then vigorously decompressing. If the moisture content of the wood component obtained by blasting in this way is high, it is preferable to dry it with a hot air dryer, vacuum dryer, etc. to remove the moisture to 10% or less before use. If a large amount of moisture remains in the wood components,
This water is not preferable because it reacts with the anhydride group of the polybasic acid anhydride to produce a polyhydric carboxylic acid as a by-product or opens the epoxy group of the monoepoxy compound.
モノエポキシ化合物としては、分子中に1個のエポキシ
基を含む化合物であればよく、例えば、フェニルグリシ
ジルエーテル、アリルグリシジルエーテル、スチレンオ
キサイド、オクチレンオキサイド、メチルグリシジルエ
ーテル、ブチルグリシジルエーテル、タレジルグリシジ
ルエーテル、エピクロルヒドリン等があげられる。The monoepoxy compound may be any compound containing one epoxy group in the molecule, such as phenyl glycidyl ether, allyl glycidyl ether, styrene oxide, octylene oxide, methyl glycidyl ether, butyl glycidyl ether, talesyl glycidyl. Examples include ether and epichlorohydrin.
多塩基酸無水物としては、無水マレイン酸、無水コハク
酸、無水フタル酸、無水へキサヒドロフクル酸、無水テ
トラヒドロフタル酸、無水ジクロロマレイン酸、無水イ
タコン酸、無水テトラブロモフタル酸、無水ヘラ]・酸
、無水トリメリット酸、無水ピロメリット酸等が挙げら
れるが、特に工業的に有利で安価な無水マレイン酸、無
水コハク酸、無水フタル酸が好ましい。Examples of polybasic acid anhydrides include maleic anhydride, succinic anhydride, phthalic anhydride, hexahydrofucric anhydride, tetrahydrophthalic anhydride, dichloromaleic anhydride, itaconic anhydride, tetrabromophthalic anhydride, and hexahydrofuric anhydride. , trimellitic anhydride, pyromellitic anhydride, etc., but maleic anhydride, succinic anhydride, and phthalic anhydride are particularly preferred because they are industrially advantageous and inexpensive.
爆砕処理した木質材にモノエポキシ化合物および多塩基
酸無水物を反応させる場合のモノエポキシ化合物と多塩
基酸無水物との仕込み比は、モノエポキシ化合物のエポ
キシ基1当量に対し、多塩基酸無水物中の無水酸基1.
5当量以下が好ましい。When reacting a monoepoxy compound and a polybasic acid anhydride with blast-treated wood, the charging ratio of the monoepoxy compound and the polybasic acid anhydride is 1 equivalent of the epoxy group of the monoepoxy compound. Acid anhydride groups in substances 1.
It is preferably 5 equivalents or less.
これより多塩基酸無水物中の無水酸基が多い場合は、木
質材の水酸基に付加したカルボキシル基を末端に有する
多塩基酸無水物の半エステルが多くなり、得られた熱可
塑性木質材組成物の耐水性が一7=
低下するので好ましくない。If there are more anhydride groups in the polybasic acid anhydride than this, there will be more half esters of the polybasic acid anhydride which have carboxyl groups added to the hydroxyl groups of the wood material at the ends, and the resulting thermoplastic wood composition It is not preferable because the water resistance of 17% decreases.
爆砕処理した木質材にモノエポキシ化合物および多塩基
酸無水物を反応させる場合は、無触媒下でも充分に進行
するが、反応を促進させるために炭酸ナトリウム、ジメ
チルベンジルアミン、ピリジン、テトラメチルアンモニ
ウムクロライドあるいは脂肪酸のカリウム塩等の触媒を
用いてもよく、爆砕処理した木質材にモノエポキシ化合
物を付加エーテル化反応させる場合は、触媒として脂肪
酸のカリウム塩、ジメチルベンジルアミンあるいはテト
ラメチルアンモニウムクロライド等の触媒を用いるのが
好ましい。When reacting blasted wood with monoepoxy compounds and polybasic acid anhydrides, the reaction proceeds satisfactorily even without a catalyst, but sodium carbonate, dimethylbenzylamine, pyridine, and tetramethylammonium chloride are used to accelerate the reaction. Alternatively, a catalyst such as a potassium salt of a fatty acid may be used, and when a monoepoxy compound is subjected to an addition etherification reaction on blasted wood, a catalyst such as a potassium salt of a fatty acid, dimethylbenzylamine, or tetramethylammonium chloride may be used as a catalyst. It is preferable to use
上記の方法においては、反応に供したモノエポキシ化合
物、あるいは多塩基酸無水物とモノエポキシ化合物の合
計量のうち約10〜80重量%程度は各々が反応して木
質材成分に結合していないオリゴマーとして副生ずる。In the above method, about 10 to 80% by weight of the monoepoxy compound or the total amount of the polybasic acid anhydride and monoepoxy compound subjected to the reaction does not react and bind to the wood component. Produced as a by-product as oligomers.
本発明では、このオリゴマーも溶剤による抽出等により
除去することな(熱可塑性木質材組成物の一成分として
用いられる。In the present invention, this oligomer is also used as a component of the thermoplastic wood composition without being removed by extraction with a solvent or the like.
また、上記の爆砕処理した木質材とモノエポキシ化合物
、あるいはモノエポキシ化合物および多塩基酸無水物と
の反応においては、爆砕処理した木質材とモノエポキシ
化合物、あるいはモノエポキシ化合物および多塩基酸無
水物とが反応してアセトンに可溶となった木質材も一部
生成する。In addition, in the reaction between the blasted wood material and the monoepoxy compound, or the monoepoxy compound and the polybasic acid anhydride, the blasted wood material and the monoepoxy compound, or the monoepoxy compound and the polybasic acid anhydride. A part of the wood material that is soluble in acetone is also produced by the reaction.
さらに、本発明の製造方法においては、少量の未反応物
が残存する。その残存量は、モノエポキシ化合物と多塩
基酸無水物の仕込み比率、反応温度あるいは反応時間等
によっても変化させること 中ができるが、反応生
成物全体の20重量%以下にするのが好ましい。Furthermore, in the production method of the present invention, a small amount of unreacted substances remain. The residual amount can be varied depending on the charging ratio of monoepoxy compound and polybasic acid anhydride, reaction temperature, reaction time, etc., but it is preferably 20% by weight or less of the entire reaction product.
本発明の製造方法で製造された熱可塑性木質材組成物は
、その原料である爆砕処理した木質材の結晶化度が爆砕
処理していない木質材よりも高いので、熱流動性がかえ
って低下するのではないかと予想されるにも拘らず、優
れた熱流動性を有するのは予想外のことである。その原
因は明らかではないが、木質材中でバインダーとして作
用しているリグニンが、木質材を爆砕処理することによ
一1〇−
り分解し、その分解したリグニンとモノエポキシ化合物
、あるいはモノエポキシ化合物および多塩基酸無水物が
反応して生成した反応生成物や上記のオリゴマーが熱可
塑性木質材の可塑剤として作用するため、従来の熱可塑
性木質材よりも熱流動性が著しく向−トするものと考え
られる。In the thermoplastic wood composition produced by the production method of the present invention, the crystallinity of the blasted wood that is its raw material is higher than that of unexploded wood, so the thermal fluidity is actually reduced. It is unexpected that it has excellent thermal fluidity, even though it is expected that it will have good thermal fluidity. The cause is not clear, but lignin, which acts as a binder in wood, decomposes over 110-years by blasting the wood, and the decomposed lignin and monoepoxy compound or monoepoxy The reaction products produced by the reaction of the compound and polybasic acid anhydride and the above oligomers act as plasticizers for thermoplastic wood, resulting in significantly improved thermal fluidity compared to conventional thermoplastic wood. considered to be a thing.
以上の如く、本発明の製造方法で得られた熱可塑性木質
材組成物は、従来の化学修飾木質材に比べ熱流動性が著
しく向上しているばかりでなく、その製造時に副生ずる
オリゴマーおよび未反応物を溶剤による抽出等の操作に
よって除去する必要がないという利点も有している。さ
らに、小径木や間伐材、さらには木材工業より副生ずる
木材小片、木粉等も爆砕処理することにより用いること
ができ、これらの有効利用の面からも極めて有用である
。As described above, the thermoplastic wood material composition obtained by the production method of the present invention not only has significantly improved thermal fluidity compared to conventional chemically modified wood materials, but also has oligomers and unused materials by-produced during its production. Another advantage is that there is no need to remove reactants by extraction with a solvent or other operations. Furthermore, small-diameter trees, thinned wood, wood chips, wood powder, etc. produced as by-products of the wood industry can be used by blasting, and are extremely useful from the standpoint of their effective utilization.
本発明の製造方法で得られた熱可塑性木質材組成物を成
形品とするため成形加工する場合は、そのままプレス成
形は勿論、押出し成形、射出成形等により通常の熱可塑
性樹脂を成形加工する加工条件で成形加工することがで
きるが、その前にブレンター、ニーター、ミキシンクロ
ール、バンバリーミキサ−等の混練機を用いて均一に混
練後、上記の成形加工方法によって成形することができ
る。このようにして得られた成形品は、多くの分野にお
いて、工業部品材料、建築材料等として好適なものであ
る。When molding the thermoplastic wood composition obtained by the production method of the present invention to make a molded article, it can be press-molded as is, or it can be processed by molding ordinary thermoplastic resins by extrusion molding, injection molding, etc. The mixture can be molded under the following conditions, but before that, it can be uniformly kneaded using a kneader such as a blender, kneader, mixer roll, Banbury mixer, etc., and then molded by the above-mentioned molding method. The molded product thus obtained is suitable as an industrial part material, a building material, etc. in many fields.
[実施例]
以下、本発明を、実施例および比較例によって更に具体
的に説明するが、これらに使用される爆砕処理した木粉
は、それぞれ含水率を5%以下に乾燥したものである。[Examples] Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples. The blasted wood flour used in these examples was dried to a moisture content of 5% or less.
また、本発明はこれら実施例に制限されるものではない
。Furthermore, the present invention is not limited to these Examples.
尚、生成物の無水酸価は、水系酸価と非水系酸価との差
より求めた。The anhydrous acid value of the product was determined from the difference between the aqueous acid value and the non-aqueous acid value.
水系酸価は、精秤した試料約0.3gをアセトン30m
2およびイオン交換水10dの混合溶媒中に分散し、2
0分間室内に放置後、O,I N K OH−HzOで
滴定して得た値より求めた。For the aqueous acid value, add approximately 0.3 g of a precisely weighed sample to 30 m of acetone.
2 and 10 d of ion-exchanged water,
It was determined from the value obtained by titration with O, IN K OH-HzO after being left in the room for 0 minutes.
非水系酸価は、精秤した試料約0.3gをアセトン30
rrdlに分散後、0.IN KOH−メタノールで
滴定して得た値より求めた。The non-aqueous acid value is determined by adding approximately 0.3 g of a precisely weighed sample to acetone 30
After dispersing in rrdl, 0. It was determined from the value obtained by titration with IN KOH-methanol.
エポキシ価は、精秤した試料約0.3gに0.1NHB
r−酢酸溶液7 mRを加え20分間室内に放fffL
O,I N フェニルグリシジルニーテルルクロル
ベンゼン溶液10m1を加え、更に20分間室内に放置
した後、0.1NHBr−酢酸溶液で滴定して得た値よ
り求めた。The epoxy value is 0.1NHB per approximately 0.3g of accurately weighed sample.
Add 7 mR of r-acetic acid solution and leave in the room for 20 minutesfffL
After adding 10 ml of O,IN phenylglycidylniterulchlorobenzene solution and leaving it in the room for another 20 minutes, the value was determined by titration with 0.1N HBr-acetic acid solution.
アセトン可溶部は木質材成分に結合していないオリゴマ
ーおよびアセj・ンに可溶となった木質材を意味してお
り、試料の重量(X)、アセトンによるソックスレー抽
出で溶出した重量 (Y)および未反応のモノエポキシ
化合物および多塩基酸無水物の合計の重量(Z)より次
式によって求めた。The acetone-soluble portion refers to the oligomers that are not bonded to wood components and the wood that has become soluble in acetone.The weight of the sample (X) and the weight eluted by Soxhlet extraction with acetone (Y ) and the total weight (Z) of unreacted monoepoxy compound and polybasic acid anhydride using the following formula.
アセトン可溶部(重量%) = 100 (”1−Z)
/Xメルトインデックス(M I )は、JIS K
7210に従い、150°C1試験荷重10kg、あ
るいは190°C1試験荷重10kgで測定した値より
求めた。Acetone soluble part (weight%) = 100 ("1-Z)
/X melt index (MI) is JIS K
7210, it was determined from the value measured at 150°C1 test load of 10kg or 190°C1 test load of 10kg.
実施例 1゜
木質材として30kg/c+flで5分間蒸煮後爆砕処
−13=
理したメラノキシロンの乾燥木粉20. Og、無水コ
ハク酸6.52 gを500 mlの四ツロセバラブル
フラスコに仕込み、130°Cで2時間攪拌下に反応後
、スチレンオキサイド23.48gを加え】50°Cで
1時間、さらに、200°Cで4時間反応させた。その
後、エーテル化反応の触媒としての酢酸カリウム0.2
6 gを加え150 ’Cで3時間、200°Cで1時
間加熱して、残存している過剰のスチレンオキサイドを
木質材の水酸基にエーテル化反応で付加させて、本発明
の熱可塑性木質材組成物を得た。この熱可塑性木質材組
成物の無水酸価、エポキシ価、ソックスレー抽出による
アセトン可溶部の重量%およびミキシングロール後のM
lの値を表1に示す。Example 1゜Dry wood powder of melanoxylon treated as wood material by steaming at 30 kg/c+fl for 5 minutes and then blasting treatment -13=20. 0g, 6.52 g of succinic anhydride was placed in a 500 ml four-way adjustable flask, and after reacting with stirring at 130°C for 2 hours, 23.48 g of styrene oxide was added.] At 50°C for 1 hour, The reaction was carried out at 200°C for 4 hours. Then, 0.2 potassium acetate as a catalyst for the etherification reaction.
6 g was added and heated at 150'C for 3 hours and at 200°C for 1 hour to add the remaining excess styrene oxide to the hydroxyl groups of the wood material through an etherification reaction, thereby producing the thermoplastic wood material of the present invention. A composition was obtained. Anhydrous acid value, epoxy value, weight % of acetone soluble portion by Soxhlet extraction and M after mixing roll of this thermoplastic wood composition
The values of l are shown in Table 1.
実施例 2゜
木質材として20kg/cnlで6分間蒸煮後爆砕処理
したメラノキシロンの乾燥木粉を用いた以外は実施例■
と同様にして、本発明の熱可塑性木質材組成物を得た。Example 2゜Example 2 except that dried melanoxylon wood flour, which had been steamed at 20 kg/cnl for 6 minutes and then exploded, was used as the wood material.
In the same manner as above, a thermoplastic wood composition of the present invention was obtained.
この熱可塑性木質材組成物の無水酸価、エポキシ価、ソ
ックスレー抽出によるアセトン可溶部の重量%およびミ
キシングロール後のMlの値を表1に示す。Table 1 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and Ml value after mixing roll of this thermoplastic wood composition.
比較例 1゜
木質材として乾燥木粉(商品名: LIGNOCEL
5150 TR; J 、 Rettenmaier
& 5oehne 社製;繊維長: 30−60μ)
を用いた以外は実施例1と同様にして、木質材組成物を
得た。ごの木質材組成物の無水酸価、エポキシ価、ソッ
クスレー抽出によるアセトン可溶部の重量%およびミキ
シングロール後のMlの値を表1に示す。Comparative example 1゜Dry wood flour as wood material (product name: LIGNOCEL
5150 TR; J, Rettenmaier
&5oehne; fiber length: 30-60μ)
A wood composition was obtained in the same manner as in Example 1 except that the following was used. Table 1 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and Ml value after mixing roll of the wood composition.
比較例 2
木質材として乾燥木粉(商品名: LIGNOCEL
5150 TR; J 、 Rettenmaier
& 5oehne 社製; 120メツシュ全通)を
用いた以外は実施例1と同様にして、木質材組成物を得
た。この木質材組成物の無水酸価、エポキシ価、ソック
スレー抽出によるアセトン可溶部の重量%およびミキシ
ングロール後のMIの値を表1に示す。Comparative example 2 Dried wood flour (product name: LIGNOCEL) as wood material
5150 TR; J, Rettenmaier
A wood material composition was obtained in the same manner as in Example 1, except that a 120-mesh (manufactured by &5oehne) was used. Table 1 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and MI value after mixing roll of this wood composition.
比較例 3゜
木質材として蒸煮処理をした乾燥赤松木粉を用いた以外
は実施例1と同様にして、木質材組成物を得た。この木
質材組成物の無水酸価、エポキシ価、ソックスレー抽出
によるアセトン可溶部の重量%およびミキシングロール
後のMlの値を表1に示す。Comparative Example 3 A wood material composition was obtained in the same manner as in Example 1, except that dry red pine wood powder subjected to steaming treatment was used as the wood material. Table 1 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and Ml value after mixing roll of this wood composition.
実施例1および2は、爆砕処理した木質材を用い、木質
材成分100重量部に対しモノエポキシ化合物を含む反
応性物質を150重量部反応させているため、得られた
木質材組成物は熱流動性が優れていることがMIの測定
結果からも確認された。=方、比較例1ないし3は、木
質材成分1()0重量部に対しモノエポキシ化合物を含
む反応性物質を150重量部反応させているが、木質材
成分として爆砕処理した木質材を用いていないため、熱
流動性に乏しい。In Examples 1 and 2, blast-treated wood was used, and 150 parts by weight of a reactive substance containing a monoepoxy compound was reacted with 100 parts by weight of the wood components, so the resulting wood compositions were heat-resistant. It was also confirmed from the MI measurement results that the fluidity was excellent. = On the other hand, in Comparative Examples 1 to 3, 150 parts by weight of a reactive substance containing a monoepoxy compound was reacted with 0 parts by weight of wood component 1 (), but using blast-treated wood as the wood component. Because of this, it has poor thermal fluidity.
表1
実施例 3゜
木質材として30kg/cflで5分間蒸煮後爆砕処理
したメラノキシロンの乾燥木粉20. Og、無水コハ
ク酸11.71g、およびスチレンオキサイド1、8.
29 g ヲ500 mllのセパラブルフラスコに入
れ、120°Cで7時間反応させ、無水酸価Oeq/k
g、エポキシ価0.16 eq/kg、ソックスレー抽
出におけるアセトン可溶部67重量%、木質材含量40
重量%の熱可塑性木質材組成物を得た。この熱可塑性木
質材組成物のミキシングロール後のMlの値は、150
°C、荷重10kgの場合0.2、190°C、荷重1
.0kgの場合0.9であった。Table 1 Example 3゜Dry wood powder of melanoxylon which was steamed at 30 kg/cfl for 5 minutes and then exploded as a wood material 20. Og, 11.71 g of succinic anhydride, and styrene oxide 1,8.
Pour 29 g into a 500 ml separable flask, react at 120°C for 7 hours, and reduce the anhydrous acid value Oeq/k.
g, epoxy value 0.16 eq/kg, acetone soluble part in Soxhlet extraction 67% by weight, wood content 40
A thermoplastic wood composition of % by weight was obtained. The Ml value of this thermoplastic wood composition after mixing roll is 150
°C, load 10kg: 0.2, 190°C, load 1
.. In the case of 0 kg, it was 0.9.
実施例 4、
木質材として20kg/cJで6分間蒸煮後爆砕処理し
たメラノキシロンの乾燥木粉4 0. O gおよびフ
ェニルグリシジルエーテル49.10gを500mβの
四ツロセパラブルフラスコに仕込み、220°Cで4時
間攪拌下に加熱後、無水コハク酸10.90gを加え1
50°Cで4時間、さらに、未反応のフェニルグリシジ
ルエーテルをエーテル化反応で木質材の水酸基に付加さ
せるため、エーテル化反応の触媒である酢酸カリウム0
. 4 2 gを加え150°Cで5時間反応させて、
木質材台it40重量%の熱可塑性木質材組成物を得た
。この熱可塑性木質材&11成物の無水酸価、エポキシ
価、ソックスレー抽出によるアセトン可溶部の重量%お
よびミキシングロール後のMlの値を表2に示す。Example 4: Dry melanoxylon wood powder 4, which was steamed at 20 kg/cJ for 6 minutes and then exploded as a wood material. Og and 49.10 g of phenyl glycidyl ether were charged into a 500 mβ four-separable flask, heated at 220°C for 4 hours with stirring, and then 10.90 g of succinic anhydride was added.
At 50°C for 4 hours, in order to add unreacted phenyl glycidyl ether to the hydroxyl groups of the wood in an etherification reaction, potassium acetate, which is a catalyst for the etherification reaction, was added.
.. 42 g was added and reacted at 150°C for 5 hours,
A thermoplastic wood composition having a wood base of 40% by weight was obtained. Table 2 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and Ml value after mixing roll of this thermoplastic wood material &11 product.
比較例 4。Comparative example 4.
木質材として乾燥木粉(商品名: LIGNOCEL
5150 TR;J、Rettenmaier & 5
oehne社製;120メツシュ全通)を用いた以外は
実施例4と同様にして、木質材含量40重量%の木質材
組成物を得た。この木質材組成物の無水酸価、エポキシ
価、ソックスレー抽出によるアセトン可溶部の重量%お
よびミキシングロール後のMIの値を表2に示す。Dried wood flour as a wood material (product name: LIGNOCEL
5150 TR; J, Rettenmaier & 5
A wood material composition having a wood material content of 40% by weight was obtained in the same manner as in Example 4, except that 120 mesh (manufactured by Oehne) was used. Table 2 shows the anhydrous acid value, epoxy value, weight percent of acetone soluble portion by Soxhlet extraction, and MI value after mixing roll of this wood composition.
実施例4は、爆砕処理した木質材を用い、木質材成分1
00重量部に対しモノエポキシ化合物を含む反応性物質
を150重量部反応させているため、得られた木質材組
成物は熱流動性が優れている。一方、比較例4は、木質
材成分100重量部に対しモノエポキシ化合物を含む反
応性物質を150重量部反応゛させているが、木質材成
分として爆砕処理した木質材を用いていないため熱流動
性に乏しい。In Example 4, wood material subjected to blasting treatment was used, and wood material component 1
Since 150 parts by weight of a reactive substance containing a monoepoxy compound is reacted with 00 parts by weight, the obtained wood composition has excellent thermal fluidity. On the other hand, in Comparative Example 4, 150 parts by weight of a reactive substance containing a monoepoxy compound was reacted with 100 parts by weight of the wood component, but since the wood component did not use blasted wood, it lacking in sex.
表2
実施例 5゜
木質材として20kg/cfflで6分間蒸煮後爆砕処
理したメラノキシロンの乾燥木粉20. Ogおよびフ
ェニルグリシジルエーテル22.58gを500雁の四
ツロセバラブルフラスコに仕込み、220°Cで4時間
攪拌下に加熱後、無水フクル酸7.42gを加え150
°Cで4時間、さらに、未反応のフェニルグリシジルエ
ーテルを木質材の水酸基にエーテル化反応で付加させる
ため、エーテル化反応の触媒である酢酸カリウム0.2
0 gを加え150°Cで5時間反応させて、木質材含
量40重量%の熱可塑性木質材組成物を得た。分析の結
果、この熱可塑性木質材組成物は、無水酸価0.13
eq/kg、エポキシ価Oeq/kg、ソックスレー抽
出によるアセトン可溶部68重量%であった。この熱可
塑性木質材組成物のミキシングロール後のMlの値は、
150°C1荷重10kgの場合0.6.190°C1
荷重10kgの場合2.0であった。Table 2 Example 5゜Dry wood powder of melanoxylon which was steamed at 20 kg/cffl for 6 minutes and then exploded as a wood material 20. Charge Og and 22.58 g of phenylglycidyl ether into a 500-gear four-piece adjustable flask, and heat at 220°C for 4 hours with stirring, then add 7.42 g of fucuric anhydride to 150 g.
°C for 4 hours, and in order to add unreacted phenyl glycidyl ether to the hydroxyl groups of the wood material in an etherification reaction, 0.2% potassium acetate, which is a catalyst for the etherification reaction, was added.
0 g was added and reacted at 150°C for 5 hours to obtain a thermoplastic wood composition with a wood content of 40% by weight. As a result of analysis, this thermoplastic wood composition has an anhydrous acid value of 0.13.
eq/kg, epoxy value Oeq/kg, and acetone soluble portion by Soxhlet extraction of 68% by weight. The Ml value of this thermoplastic wood composition after mixing rolls is:
150°C1 load 10kg 0.6.190°C1
It was 2.0 when the load was 10 kg.
実施例 6゜
木質材として30 kg / aflで6分間蒸煮後爆
砕処理したラワンの乾燥木粉17.5 gおよびスチレ
ンオキサイド32.5 gを500 mflの四ツロセ
パラブルフラスコに仕込み、220°Cで4時間攪拌下
に加熱後、エーテル化反応の触媒である酢酸カリウム0
.49 gを加え150 ’Cで6時間反応させて、木
質材台N35重量%の熱可塑性木質材組成物を得た。分
析の結果、この熱可塑性木質材組成物は、エポキシ価0
.25 eq/kg、ソックスレー抽出によるアセトン
可溶部69重量%であった。この熱可塑性木質材組成物
のミキシングロール後のMlの値は、190“C1荷重
10kgの場合20であった。Example 6゜17.5 g of dried lauan wood flour, which had been steamed at 30 kg/afl for 6 minutes and then exploded as a wood material, and 32.5 g of styrene oxide were placed in a 500 mfl four-piece separable flask and heated at 220°C. After heating with stirring for 4 hours at
.. 49 g was added and reacted at 150'C for 6 hours to obtain a thermoplastic wood composition containing 35% by weight of wood base N. As a result of analysis, this thermoplastic wood composition has an epoxy value of 0.
.. 25 eq/kg, and the acetone soluble portion was 69% by weight by Soxhlet extraction. The Ml value of this thermoplastic wood composition after mixing roll was 190"C1 and 20 at a load of 10 kg.
実施例 7〜9゜
木質材として30kg/cイで5分間蒸煮後爆砕処理し
たラワンの乾燥木粉を用い、モノエポキシ化合物と共に
500dの四ツロセバラブルフラスコに仕込み、220
°Cで4時間攪拌下に加熱後、無水コハク酸を加え15
0°Cで4時間、さらに、未反応のモノエポキシ化合物
をエーテル化反応で木質材の水酸基に付加させるため、
エーテル化反応の触媒である酢酸カリウムを加え150
で5時間反応させて、本発明の熱可塑性木質材組成物を
得た。得られた熱可塑性木質材組成物の無水酸価、エポ
キシ価、ソックスレー抽出によるアセトン可溶部の重量
%およびMlの値を表3に示す。Examples 7-9゜ Dried lauan wood flour, which has been steamed at 30 kg/c for 5 minutes and then exploded, was used as the wood material, and charged into a 500 d four-piece collapsible flask with a monoepoxy compound.
After heating with stirring for 4 hours at °C, succinic anhydride was added to
At 0°C for 4 hours, in order to add the unreacted monoepoxy compound to the hydroxyl group of the wood material through an etherification reaction,
Add potassium acetate, which is a catalyst for the etherification reaction, and add 150
The mixture was reacted for 5 hours to obtain a thermoplastic wood composition of the present invention. Table 3 shows the anhydride acid value, epoxy value, weight % of acetone soluble portion determined by Soxhlet extraction, and Ml values of the obtained thermoplastic wood composition.
比較例 5゜
木質材として30kg/cfで5分間蒸煮後爆砕処理し
たラワンの乾燥木粉を用い、モノエポキシ化合物である
ブチルグリシジルエーテルと共に500雁の四ツロセパ
ラブルフラスコに仕込み、220°Cで4時間攪拌下に
加熱後、無水コハク酸を加え150°Cで4時間、さら
に、木質材の水酸基に未反応のブチルグリシジルエーテ
ルをエーテル化反応で付加させるため、エーテル化反応
の触媒として酢酸カリウムを加え150 ’Cで5時間
反応させて、木質材含量70重量%の木質材組成物を得
た。得られた木質材組成物の無水酸価、エポキシ価、ソ
ックスレー抽出によるアセトン可溶部の重量%およびM
Iの値を表3に併せて示す。Comparative Example 5゜ Dried lauan wood flour, which had been steamed at 30 kg/cf for 5 minutes and then exploded, was used as a 5° wood material. It was charged into a 500-gear Yotsuro separable flask with butyl glycidyl ether, a monoepoxy compound, and heated at 220°C. After heating with stirring for 4 hours, succinic anhydride was added and heated at 150°C for 4 hours. Potassium acetate was added as a catalyst for the etherification reaction to add unreacted butyl glycidyl ether to the hydroxyl groups of the wood. was added and reacted at 150'C for 5 hours to obtain a wood composition with a wood content of 70% by weight. Anhydrous acid value, epoxy value, weight % of acetone soluble portion by Soxhlet extraction and M of the obtained wood composition
The values of I are also shown in Table 3.
実施例7〜9の木質材組成物は、木質材として爆砕処理
した木質材を用いているためMlの測定においても優れ
た熱流動性を示したが、比較例5の木質材組成物は、爆
砕処理した木質材を用いたにも拘らず、木質材含量が多
過ぎるため、Mlの測定は不可能で熱流動性に乏しかっ
た。The wood compositions of Examples 7 to 9 used blast-treated wood as the wood material, so they showed excellent thermal fluidity in the measurement of Ml, but the wood composition of Comparative Example 5 Even though blast-treated wood was used, the wood content was too high, making it impossible to measure Ml and resulting in poor thermal fluidity.
表3 PGE :フェニルグリシジルエーテル。Table 3 PGE: Phenyl glycidyl ether.
BGE ニブチルグリシジルエーテル。BGE Nibutyl glycidyl ether.
SO:スチレンオキサイド。SO: Styrene oxide.
23 一
実施例 10゜
木質材として30kg/c+fで5分間蒸煮後爆砕処理
したラワンの乾燥木粉40gをブチルグリシジルエーテ
ル47.96 gと共に500mβの四ツロセパラブル
フラスコに仕込み、220°Cで4時間攪拌下に加熱後
、無水マレイン酸12.04 gを加え150°Cで4
時間、さらに、木質材の水酸基に未反応のブチルグリシ
ジルエーテルをエーテル化反応で付加させるため、エー
テル化反応の触媒として酢酸カリウム0.48 gを加
え150で5時間反応させて、本発明の木質材含量40
重量%の熱可塑性木質材組成物を得た。得られた熱可塑
性木質材組成物は、無水酸価0.03eq/kg、エポ
キシ価0.06eq/kg、ソックスレー抽出によるア
セトン可溶部58重量%であった。この熱可塑性木質材
組成物のミキシングロール後のMlO値は、150°C
1荷重10kgの場合、183であった。23 One Example 40g of dried lauan wood flour, which was steamed as a 10° wood material at 30kg/c+f for 5 minutes and then exploded, was charged into a 500mβ four-separable flask with 47.96g of butyl glycidyl ether, and heated at 220°C. After heating with stirring for an hour, 12.04 g of maleic anhydride was added and heated at 150°C for 4 hours.
Furthermore, in order to add unreacted butyl glycidyl ether to the hydroxyl groups of the wood material in an etherification reaction, 0.48 g of potassium acetate was added as a catalyst for the etherification reaction, and the reaction was carried out at 150° C. for 5 hours. Material content 40
A thermoplastic wood composition of % by weight was obtained. The obtained thermoplastic wood material composition had an anhydride acid value of 0.03 eq/kg, an epoxy value of 0.06 eq/kg, and an acetone soluble portion of 58% by weight as determined by Soxhlet extraction. The MlO value of this thermoplastic wood composition after mixing roll is 150°C
In the case of 1 load of 10 kg, it was 183.
以上の如く、本発明の製造方法で得られた熱可塑性木質
材組成物は、従来の化学修飾木質材に比−9へ −
−Z 4−
べ、熱流動性が著しく向上しているため、熱圧成形は勿
論、押出し成形、射出成形等の通常の成形方法で成形加
工できるため、産業上有用であるばかりでなく、小径木
や間伐材、さらには水利工業より副生ずる木材小片、木
粉等も爆砕処理することにより用いることができ、これ
らの有効利用の面からも極めて有用である。また、該熱
可塑性木質材組成物は、反応後、溶剤による抽出等の後
処理が不要で、そのまま押出成形等に用いることができ
るため、工業的に極めて有用である。As described above, the thermoplastic wood material composition obtained by the production method of the present invention has significantly improved thermal fluidity compared to conventional chemically modified wood materials. It is not only useful industrially because it can be molded by conventional molding methods such as extrusion molding and injection molding, as well as hot-press molding, but it is also useful for small diameter trees, thinned wood, and wood chips and wood powder that are by-products of the water conservancy industry. etc. can also be used by subjecting them to blasting treatment, and are extremely useful from the standpoint of their effective utilization. Further, the thermoplastic wood composition does not require post-treatment such as extraction with a solvent after the reaction, and can be used as it is for extrusion molding, etc., and is therefore extremely useful industrially.
Claims (1)
シ化合物50〜300重量部、あるいは、該爆砕処理し
た木質材100重量部とモノエポキシ化合物および多塩
基酸無水物を合計で50〜300重量部とを反応させる
ことを特徴とする熱流動性に優れた熱可塑性木質材組成
物の製造方法。(1) 100 parts by weight of the blasted wood material and 50 to 300 parts by weight of a monoepoxy compound, or 100 parts by weight of the blasted wood material, a monoepoxy compound, and a polybasic acid anhydride in a total of 50 to 300 parts by weight. 1. A method for producing a thermoplastic wood composition having excellent thermal fluidity, the method comprising reacting with a thermoplastic wood composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28058590A JP2636072B2 (en) | 1990-10-20 | 1990-10-20 | Method for producing thermoplastic wood material composition having excellent heat fluidity |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28058590A JP2636072B2 (en) | 1990-10-20 | 1990-10-20 | Method for producing thermoplastic wood material composition having excellent heat fluidity |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04156302A true JPH04156302A (en) | 1992-05-28 |
JP2636072B2 JP2636072B2 (en) | 1997-07-30 |
Family
ID=17627086
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28058590A Expired - Lifetime JP2636072B2 (en) | 1990-10-20 | 1990-10-20 | Method for producing thermoplastic wood material composition having excellent heat fluidity |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2636072B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995013907A1 (en) * | 1993-11-19 | 1995-05-26 | Japan Chemical Engineering & Machinery Co., Ltd. | Benzylated wooden material and process for producing the same |
FR2814107A1 (en) * | 2000-09-21 | 2002-03-22 | Commissariat Energie Atomique | Chemical treatment of substrate having reactive functions, e.g. for hydrophobizing wood, comprises contacting moist substrate with a gaseous organic reagent |
-
1990
- 1990-10-20 JP JP28058590A patent/JP2636072B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995013907A1 (en) * | 1993-11-19 | 1995-05-26 | Japan Chemical Engineering & Machinery Co., Ltd. | Benzylated wooden material and process for producing the same |
US5591832A (en) * | 1993-11-19 | 1997-01-07 | Japan Chemical Engineering & Machinery Co., Ltd. | Benzylated lignocellulosic substance and a producing method thereof |
FR2814107A1 (en) * | 2000-09-21 | 2002-03-22 | Commissariat Energie Atomique | Chemical treatment of substrate having reactive functions, e.g. for hydrophobizing wood, comprises contacting moist substrate with a gaseous organic reagent |
WO2002024420A1 (en) * | 2000-09-21 | 2002-03-28 | Atelier Regional De Conservation Arc-Nucleart | Method for chemical treatment of a surface |
Also Published As
Publication number | Publication date |
---|---|
JP2636072B2 (en) | 1997-07-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Matsuda | Preparation and utilization of esterified woods bearing carboxyl groups | |
JPH0436846B2 (en) | ||
Matsuda et al. | Preparation and crosslinking of oligoesterified woods based on maleic anhydride and allyl glycidyl ether | |
CN113881208B (en) | Functionalized modified straw/polylactic acid composite material and preparation method thereof | |
JPWO2006001076A1 (en) | Thermoplastic cellulosic composition, process for producing the same, and molded article thereof | |
JPH04156302A (en) | Manufacture of thermoplastic wood-based material composition excellent in heat fluidity | |
JPS6083806A (en) | Manufacture of modified wooden piece | |
US4888403A (en) | Process for producing plastic-like woody moldings from dibasic acid anhydrides and unsaturated monoglycidyl ethers | |
JP2661779B2 (en) | Thermoplastic wood-based molding composition and method for producing the same | |
JP2653903B2 (en) | Cellulose-based molding composition and method for producing the same | |
CN108456433A (en) | A kind of environment-friendly type plastic and preparation method thereof prepared using straw refuse | |
JP2657244B2 (en) | Manufacturing method of chemically modified wood | |
JPH0436845B2 (en) | ||
JP2640604B2 (en) | Manufacturing method of chemically modified wood | |
JP2646307B2 (en) | Method for producing chemically modified wood with excellent thermal fluidity | |
JP2021123717A (en) | Resin composition | |
JP3810888B2 (en) | WOODEN MATERIAL BASED MATERIAL AND ITS MANUFACTURING METHOD | |
JP3409092B2 (en) | Thermosetting chemically modified wood material composition | |
US20240166772A1 (en) | Composition comprising cellulose nanofiber and lignin or complex of these components, and method for producing lignocellulose-derived material | |
JPH04122744A (en) | Chemically modified cellulose material composition for molding | |
JPH0439001A (en) | Manufacture of cellulosic resin | |
JP2636068B2 (en) | Oligoesterified wood material composition | |
SU825564A1 (en) | Press-composition based on hydrolyzed lignine | |
JP2972115B2 (en) | Method for continuous production of thermoplastic wood-based molding composition | |
JPS61215675A (en) | Production of plasticized lignocellulose/epoxy resin adhesive |