JP3322518B2 - Artificial wood and method for producing the same - Google Patents

Artificial wood and method for producing the same

Info

Publication number
JP3322518B2
JP3322518B2 JP09876395A JP9876395A JP3322518B2 JP 3322518 B2 JP3322518 B2 JP 3322518B2 JP 09876395 A JP09876395 A JP 09876395A JP 9876395 A JP9876395 A JP 9876395A JP 3322518 B2 JP3322518 B2 JP 3322518B2
Authority
JP
Japan
Prior art keywords
wood
powder
particle size
fine
waste
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.)
Expired - Fee Related
Application number
JP09876395A
Other languages
Japanese (ja)
Other versions
JPH08290410A (en
Inventor
博久 吉田
慎治 松本
賢二 西沢
英雄 角田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP09876395A priority Critical patent/JP3322518B2/en
Publication of JPH08290410A publication Critical patent/JPH08290410A/en
Application granted granted Critical
Publication of JP3322518B2 publication Critical patent/JP3322518B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は産業上不可欠ではあるが
世界的に枯褐傾向にある遅成長性の松、ヤカールなどの
高強度木材の代替材となる廉価な高強度人工木材および
その製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an inexpensive high-strength artificial wood which can be used as a substitute for high-strength wood, such as pine and yakar, which are indispensable in industry but tend to be browned worldwide, and their production. About the method.

【0002】[0002]

【従来の技術】人工木材としては切削木片を主原料とし
たパーティクルボード、解織パルプを主原料としたファ
イバーボードなどが市販されている。しかしこれらは強
度的に弱く、特に吸水強度が著しく低い為に造船工場で
使用される盤木や重量荷物の底に敷くパレットなど屋外
使用の高強度木材の代替材としては使用できない。
2. Description of the Related Art As artificial wood, a particle board made mainly of cut wood chips and a fiber board made mainly of unwoven pulp are commercially available. However, these materials are weak in strength, and in particular, have extremely low water absorption strength, so that they cannot be used as substitutes for high-strength wood for outdoor use, such as planks used in shipyards and pallets laid on the bottom of heavy loads.

【0003】[0003]

【発明が解決しようとする課題】[Problems to be solved by the invention]

1)強度、特に吸水強度の向上 従来の人工木材は、家屋の内壁材や家具調度品用として
使用されることが多く、高強度はこれ程要求されず、ま
た屋内使用の為に吸水強度も問題になっていなかった。
実際に市販品で強度的に優れるファイバーボードを購入
し、強度テストを行った結果、乾燥曲げ強度は300〜
500kg/cm2 あったが、吸水後は手で壊れる「ボ
ロボロ」の状態で吸水強度測定不能であった。 2)コスト低減と量産化 前述の船台用盤木等に使用される松、ヤカールはかなり
高価で、かつ北米等の輸入先では自然保護の観点から伐
採禁止傾向が強く、入手も困難になりつつある。
1) Improvement of strength, especially water absorption strength Conventional artificial wood is often used for interior wall materials of houses and furniture furniture, so high strength is not so required, and water absorption strength is also a problem for indoor use. Was not turned on.
As a result of actually purchasing a commercially available fiberboard with excellent strength and conducting a strength test, the dry bending strength is 300 ~
Although the water absorption was 500 kg / cm 2 , the water absorption strength could not be measured because the water was broken by hand after water absorption. 2) Cost reduction and mass production The pine and yakar used for the above-mentioned sideboards are quite expensive, and the import destinations in North America and the like have a strong tendency to prohibit logging from the viewpoint of nature protection, and it is becoming difficult to obtain them. is there.

【0004】3)強度の方向性偏差低減 天然木材は年輪の方向、すなわち正目と板目方向で強度
が大きく異なる。その為に廃材発生も多くなり、また現
場作業者も大変気をつかっている。本発明は、上記の問
題点を解消し、強度、特に吸水強度に優れた人工木材並
びにそれを低減されたコストで製造することのできる製
造方法を提供することを目的とする。
[0004] 3) Reduction of Directional Deviation of Strength [0004] Natural wood greatly differs in strength in the direction of annual rings, that is, the grain direction and the grain direction. As a result, waste materials are increasing, and on-site workers are also very careful. An object of the present invention is to solve the above-mentioned problems and to provide an artificial wood having excellent strength, particularly excellent water absorption strength, and a manufacturing method capable of manufacturing the same at a reduced cost.

【0005】[0005]

【課題を解決するための手段】上記の目的は、バインダ
ーを加えた木粉を圧縮成形して人工木材を製造する方法
において、木粉原料を平均粒度分布が100〜500μ
mの粗粒木粉と平均粒度分布が10〜50μmの微粒木
粉であって、かつ前記粗粒木粉の平均粒径の1/3〜1
/10の平均粒径を有する微粒木粉とに粉砕分級し、粗
粒木粉100重量部に対して10〜60重量部の微粒木
粉を加えて木材粉相互の最密充填を促進することを特徴
とする高強度人工木材の製造方法及びバインダーを加え
た木粉を圧縮成形してなる人工木材において、該木粉が
平均粒度分布が100〜500μmの粗粒木粉と該粗粒
木粉100重量部に対して、平均粒度分布が10〜50
μmの微粒木粉であって、かつ前記粗粒木粉の平均粒径
の1/3〜1/10の平均粒径を有する微粒木粉を10
〜60重量部加えて木材粉の相互最密充填を促進してな
る高強度人工木材によって達成することができる。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing artificial wood by compression-molding wood powder to which a binder has been added, wherein the wood powder raw material has an average particle size distribution of 100 to 500 μm.
m coarse-grained wood flour and fine-grained wood with an average particle size distribution of 10 to 50 μm
Flour and 1/3 to 1 of the average particle size of the coarse wood flour
Crushing and classifying into fine wood powder having an average particle size of / 10, and adding 10 to 60 parts by weight of fine wood powder to 100 parts by weight of coarse wood powder to promote close packing between wood powders. A method for producing a high-strength artificial wood characterized by the fact that synthetic wood obtained by compression-molding wood flour to which a binder has been added is characterized in that the wood flour is
The average particle size distribution is 10 to 50 with respect to coarse wood powder having an average particle size distribution of 100 to 500 μm and 100 parts by weight of the coarse wood powder.
10 μm fine wood flour having a mean particle size of 1/3 to 1/10 of the mean grain size of the coarse wood flour.
It can be achieved by a high-strength artificial wood which promotes mutual close packing of wood powder in addition to 〜60 parts by weight.

【0006】ここで用いられる木粉の原料となる木材と
しては、特に種類を選ばず、天然木、また解体家屋や製
材所から発生する廃木材、風倒木、立ち枯れ木等のま
つ、杉、ラワン等が用いられ、必要に応じて加えられる
熱硬化性樹脂としてはエポキシ系、ポリエステル系の廃
FRP等が挙げられる。又、木粉のうち、粗粒木粉と微
粒木粉の平均粒度分布は夫々100〜500μm、10
〜50μmのものを用いるのが好ましく、特に微粒木粉
の平均粒径は粗粒木粉の1/3〜1/10とすることが
必要である。熱硬化性樹脂の平均粒径は3〜30μmの
範囲とするのが好ましく、又、その配合量は木材粉合計
量100重量部に対して30〜70重量部とするのが好
ましい。
The wood used as a raw material for the wood flour used herein is not particularly limited, and may be natural wood, waste wood generated from demolition houses or sawmills, wind-down trees, dead wood, etc., cedar, lauan. And the like, and as the thermosetting resin added as needed, epoxy-based, polyester-based waste FRP and the like can be mentioned. Further, among the wood flours, the average grain size distribution of the coarse wood flour and the fine wood flour is 100 to 500 μm,
It is preferable to use one having a particle size of from 50 μm to 50 μm. In particular, it is necessary that the average particle size of the fine wood powder is 1/3 to 1/10 of that of the coarse wood powder. The average particle size of the thermosetting resin is preferably in the range of 3 to 30 μm, and the compounding amount is preferably 30 to 70 parts by weight based on 100 parts by weight of the total amount of wood powder.

【0007】さらに、本発明においては、粉砕粗粒木
粉、粉砕微粒木粉、粉砕熱硬化性樹脂微粒を一つの粉砕
機でワンパス湿式連続粉砕することにより製造すること
ができる。このような粉砕処理は、例えば図4に示すよ
うな装置(三菱ウルトラファインミル−以下UFミルと
いう−)を用いて行う。UFミルとは、攪拌翼を装着し
た内筒・外筒を有し、その間隙に粉砕ボールを充填し、
内筒・外筒をそれぞれ単独、もしくは同時に回転させ、
供給された粉体、もしくは粉体スラリを連続粉砕・連続
排出させる横型超微粒ミルのことである。
Further, in the present invention, it can be produced by one-pass wet continuous pulverization of pulverized coarse wood powder, pulverized fine wood powder, and pulverized thermosetting resin fine particles with one pulverizer. Such a pulverizing process is performed using, for example, an apparatus as shown in FIG. 4 (Mitsubishi Ultra Fine Mill-hereinafter referred to as UF mill-). The UF mill has an inner cylinder and an outer cylinder equipped with stirring blades, and fills the gap with crushed balls,
Rotate the inner cylinder and outer cylinder individually or simultaneously,
This is a horizontal ultrafine mill that continuously pulverizes and continuously discharges the supplied powder or powder slurry.

【0008】図4はUFミルの内筒を単独で回転させ湿
式連続粉砕させる運用方式を図示している。被砕物は原
料ホッパー1から供給機2により、またスラリー媒液
(本発明の場合は水)はタンク3から供給ポンプ4によ
りUFミルに連続供給される。UFミル外筒5と回転す
るUFミル内筒6との間隙に充填された粉砕ボール7に
より粉砕された微粒スラリーは、ミル端部同心円周方向
に設けられた排出スリット8により粉砕ボールと分離さ
れ、粉砕粉のみが連続排出され製品タンク9に回収され
る。この方法によると、粗粉砕木粉、微粉砕木粉、微粉
砕熱硬化性樹脂を、それぞれ別々の粉砕機にて連続粉砕
し、後工程にて均一混合分散する場合により、製造設備
等に要するコストを低減することができる。
FIG. 4 shows an operation system in which the inner cylinder of the UF mill is independently rotated to perform wet continuous pulverization. The crushed material is continuously supplied from a raw material hopper 1 to a UF mill by a feeder 2, and the slurry medium (water in the present invention) is continuously supplied from a tank 3 to a UF mill by a supply pump 4. The fine slurry crushed by the crushing balls 7 filled in the gap between the UF mill outer cylinder 5 and the rotating UF mill inner cylinder 6 is separated from the crushing balls by a discharge slit 8 provided concentrically around the end of the mill. Only the pulverized powder is continuously discharged and collected in the product tank 9. According to this method, coarsely pulverized wood powder, finely pulverized wood powder, and finely pulverized thermosetting resin are each continuously pulverized by a separate pulverizer and uniformly mixed and dispersed in a later step, which is necessary for manufacturing equipment and the like. Cost can be reduced.

【0009】更に本発明の好ましい実施態様において
は、UFミルの操業に当って、原料木粉及びFRPの供
給口10を図5における砕料の流れの、上流側から下流
側へのその配置を変えることにより、ミル内部への滞留
時間を決め粉砕粒径を調整することで、2種類の原料
(木粉、FRP)、3粒径(木粉2種、FRP1種)の
粉砕スラリを、ミル1台にて連続製造可能とすることが
できる。またUFミルの内筒、外筒攪拌翼および粉砕ボ
ールによるランダムな攪拌効果により3粒径粉砕粉の均
一混合分散をも、ミル1台にて連続処理可能となる。
Further, in a preferred embodiment of the present invention, in the operation of the UF mill, the supply port 10 for the raw wood flour and the FRP is arranged in the flow of the crushing material in FIG. 5 from the upstream side to the downstream side. By changing the residence time in the mill and adjusting the pulverized particle size, the pulverized slurry of two types of raw materials (wood flour, FRP) and three particle sizes (two types of wood flour, one FRP) can be milled. Continuous production can be performed by one unit. Further, the uniform mixing and dispersion of the three-particle-size pulverized powder can be continuously processed by one mill by the random stirring effect of the inner and outer cylinder stirring blades and the grinding balls of the UF mill.

【0010】[0010]

【作用】以下本発明を更に詳細に説明する。 (1)強度、特に吸水強度の向上 粗粒木粉と微粒木粉とを混合することにより、粗粒木
粉の空隙に微粒木粉が入り込む、いわゆる木材粉相互に
「最密充填構造」を形成させることにより、緻密さが大
きく向上し、これにより全体強度を向上させる。 更に微粒木粉よりも細い熱硬化性樹脂を加えることに
より、微粒木粉空隙に樹脂粉が入り込み最密充填構造が
一層促進させると同時に、圧縮成形時の熱により樹脂粉
が硬化するので全体の強度、剛性が向上できる。 木粉同士を接着するバインダーとして撥水性の強いイ
ソシアネート系バインダーを使用する。このバインダー
の撥水性と最密充填構造による緻密さから、最終製品の
吸水率が大幅に低減でき、吸水強度が向上する。
The present invention will be described in more detail below. (1) Improvement of strength, especially water absorption strength By mixing coarse wood flour and fine wood flour, fine wood flour enters gaps of coarse wood flour, so-called “close-packed structure” between wood flours. By forming, the denseness is greatly improved, thereby improving the overall strength. Further, by adding a thermosetting resin finer than the fine-grained wood powder, the resin powder enters the voids of the fine-grained wood powder to further promote the close-packed structure, and at the same time, the resin powder is hardened by the heat at the time of compression molding. Strength and rigidity can be improved. An isocyanate-based binder having strong water repellency is used as a binder for bonding wood powders. Due to the water repellency of the binder and the denseness due to the close-packed structure, the water absorption of the final product can be greatly reduced, and the water absorption strength is improved.

【0011】(2)コスト低減と量産化 最近、台風による風倒木や廃ガス(SO3 等)による大
都市周辺の立枯木が増加し、2次災害防止の点からも有
効利用が急がれている。また、熱硬化性樹脂の代表であ
るFRP製品である廃FRP船とか、廃浴槽の処理が大
きな社会問題となっている。本発明はこれらの多量に発
生し有効処理が待たれている廃木材と廃FRPを主原料
として用いることができるので人工木材である為に廉価
であり、かつ量産も可能であり、また廃棄物の再資源化
という意味からも社会的意義は大きい。 (3)強度の方向性偏差低減 本発明は粗粒木粉、微粒木粉、FRP粉による均一最密
充填構造を基本としているので、年輪の方向に大きく左
右されることがなく、強度の方向性偏差が大幅に低減で
きる。
(2) Cost reduction and mass production Recently, typhoon-induced fallen trees and dead trees around large cities due to waste gas (such as SO 3 ) have increased, and effective use has been urgently required in terms of preventing secondary disasters. ing. Also, treatment of waste FRP ships, which are FRP products that are representative of thermosetting resins, and waste tubs has become a major social problem. The present invention can use waste wood and waste FRP, which are generated in a large amount and are waiting for effective treatment, as main raw materials. Therefore, the artificial wood is inexpensive, and mass production is possible. It has great social significance from the viewpoint of resource recycling. (3) Reduction of Directional Deviation of Strength The present invention is based on a uniform close-packed structure made of coarse wood powder, fine wood powder and FRP powder, so that it is not largely influenced by the direction of the annual rings, Sex deviation can be greatly reduced.

【0012】〈最密充填構造形成の為の最適粒径比と最
適配合比〉最密充填の為の最適粒径比は真球の場合は理
論的検討は可能であるが、繊維状の木材粉の場合は理論
的検討は難しく実験検討を行った。図2の曲線[I] は微
粒木材の平均粒径(D50S と粗粒木材の平均粒径(D
50B との比α〔=(D50S /(D50B 〕と試作人
工木材の圧縮強度比との関係を示したものである。尚、
微粒木材の混合比β(微粒木材/粗粒木材)、バインダ
ー添加量、成形条件等はすべて一定とした。曲線[II]は
FRP粉の平均粒径(D50F と(D50S との比を示
したものである。図2から明らかな様にαの低下に従い
強度は顕著に増加し、粗粒木材の空隙に微粒木材が入り
込む最密充填構造が形成された効果によるものである。
またFRP粉を混入した場合は、その熱硬化性効果によ
り約40%強度が向上した。更にαの適正値は強度面か
ら1/3以下、粉砕動力の増加防止から1/10以上、
すなわちα=1/3〜1/10が適正と判断された。
<Optimal particle size ratio and optimum compounding ratio for forming a close-packed structure> The optimum particle size ratio for a close-packed structure can be theoretically examined in the case of a true sphere. In the case of powder, it was difficult to conduct a theoretical study and an experimental study was conducted. Curve in Figure 2 [I] average particle diameter (D 50) of fine wood average particle size of the S and coarse wood (D
Shows the relationship between the 50) the ratio α [= (D 50) S / ( D 50) B ] and B and prototype compressive strength ratio of the artificial timber. still,
The mixing ratio β of fine wood (fine wood / coarse wood), the amount of binder added, and molding conditions were all constant. Curve [II] shows the ratio between the average particle size (D 50 ) F and (D 50 ) S of the FRP powder. As is apparent from FIG. 2, the strength increases remarkably as α decreases, and this is due to the effect of forming a close-packed structure in which fine-grained wood enters pores of coarse-grained wood.
When the FRP powder was mixed, the strength was improved by about 40% due to the thermosetting effect. Further, the appropriate value of α is 1/3 or less from the viewpoint of strength, and 1/10 or more from prevention of increase in grinding power.
That is, α = 1/3 to 1/10 was determined to be appropriate.

【0013】図3はα=1/6一定として、混合比βの
影響をテストしたものである。FRP粉を混入しない曲
線[III] ではβ=0.1〜0.6が適正と判断された。
真球充填時の空隙率は20〜40%であるが、木材粉が
繊維状であり、また圧縮成形する為に適正範囲が拡がっ
たものと推定される。FRP粉混入の曲線[IV]の場合
は、FRP粉混入率の増加と共に強度は向上するが、F
RP粉の粉砕動力はかなり大きい為に、60重量%以上
の混入はコスト高を招くので、β=0.2〜0.5が適
正である。
FIG. 3 shows a test of the effect of the mixture ratio β with α = 1/6 constant. In the curve [III] in which the FRP powder was not mixed, β = 0.1 to 0.6 was determined to be appropriate.
Although the porosity at the time of filling a true sphere is 20 to 40%, it is presumed that the wood powder is fibrous and the appropriate range has been expanded for compression molding. In the case of the curve [IV] of FRP powder mixing, although the strength increases with an increase in the FRP powder mixing ratio,
Since the pulverizing power of the RP powder is considerably large, the mixing of 60% by weight or more causes an increase in cost, so that β = 0.2 to 0.5 is appropriate.

【0014】[0014]

【実施例】以下本発明を実施例により更に詳細に説明す
る。 (実施例1)図1は本発明の方法を模式的に示したフロ
ーシートである。廃木材としては家屋解体時に発生した
ラワン材を原料とし、粉砕して平均粒径150μmの粗
粒木粉と25μmの微粒木粉をとした。廃FRPとして
は家庭から粗大ゴミとして排出された廃浴槽を原料と
し、粉砕した5μmFRP粉をとした。バインダーは撥
水性のあるイソシアネート系のもの(大鹿振興社製)を
使用した。混合比は粗粒木粉100に対して微粒木粉3
0、FRP粉30、バインダー5(いずれも重量%)と
した。これら4種類の素材を均一に混合攪拌した後に加
熱圧縮成形機(圧力15kg/cm2 、温度150℃)
にて成形、人工木材とした。得られた人工木材の特性を
表1に示した。表1には、天然松材と市販人工木材の特
性値も併記した。
The present invention will be described in more detail with reference to the following examples. (Embodiment 1) FIG. 1 is a flow sheet schematically showing the method of the present invention. As the waste wood, raw wood generated at the time of house dismantling was used as a raw material, and pulverized into coarse wood powder having an average particle size of 150 μm and fine wood powder having a average particle size of 25 μm. As the waste FRP, a 5 μm FRP powder obtained by pulverizing a waste bath tub discharged as oversized garbage from a household was used. The binder used was a water-repellent isocyanate-based binder (manufactured by Oshika Shinko Co., Ltd.). The mixing ratio is 100 for coarse wood powder and 3 for fine wood powder.
0, FRP powder 30, and binder 5 (all by weight). After uniformly mixing and stirring these four materials, a heat compression molding machine (pressure 15 kg / cm 2 , temperature 150 ° C.)
And made into artificial wood. Table 1 shows the properties of the obtained artificial wood. Table 1 also shows characteristic values of natural pine wood and commercially available artificial wood.

【0015】[0015]

【表1】 [Table 1]

【0016】(実施例2)図5のUFミルを用い、原料
ホッパー11,12,13にそれぞれ、FRP粉砕原
料、木粉原料(微粒粉用)、木粉原料(粗粒粉用)を充
填した。図5に示すように、各種原料粉の供給口位置
を、砕料の流れ方向に対して排出口からの距離をLP
WS、LWBとなるよう設置した。より細かく粉砕するに
はミル内滞留時間を多くする必要があるため、供給口の
位置をLP >LWS>LWBと排出口から離して配置してあ
る。図6に木粉及びFRP粉をUFミルバッチ(回分
式)粉砕試験で同等の運転条件(ミル回転数、ボール量
(率)等)にて粉砕したときの各粉砕特性の模式図を示
す。バッチ粉砕時は、図のように粉砕時間が長いほどよ
り細かい粉体が得られる。人工木材製造に要求される、
粗粒木粉粒径をDWB、所要粉砕時間をtWB、微粒木粉粒
径をDWS、所要粉砕時間をtWS、FRP粉粒径をDP
所要粉砕時間をtP としたとき所要粉砕時間は、tWB
WS:tP =1:4:8であった。これらの結果を図5
の様な連続粉砕の条件に反映させるには、所要粉砕時間
分、ミル内の滞留時間を調整すれば所要の粉砕粒径が得
られるから、供給口−排出口間の距離の比率を、所要バ
ッチ粉砕時間の比率にしてやれば良い。そこで、下記表
2に示される原料粉の粒径と配合割合とするため、UF
ミルの3種粉砕原料の供給口の位置をLWB:LWS:LP
=1:4:8の位置に配置することにより、1段粉砕で
目的とする人口木材の乾燥と成形前スラリを連続的に製
造した。
(Embodiment 2) Using the UF mill of FIG. 5, the raw material hoppers 11, 12, and 13 are filled with a raw material for FRP, a raw material for wood powder (for fine powder), and a raw material for wood powder (for coarse powder), respectively. did. As shown in FIG. 5, the positions of the supply ports for the various raw material powders are L P ,
LWS and LWB were installed. Since it is necessary to increase the residence time in the mill for finer pulverization, the position of the supply port is set to be L P > L WS > L WB and away from the discharge port. FIG. 6 is a schematic diagram of each pulverizing characteristic when wood powder and FRP powder are pulverized in a UF mill batch (batch type) pulverization test under the same operating conditions (mill rotation speed, ball amount (rate), etc.). At the time of batch pulverization, finer powder is obtained as the pulverization time is longer as shown in the figure. Required for artificial wood production,
The coarse wood powder particle size is D WB , the required grinding time is t WB , the fine wood powder particle size is D WS , the required grinding time is t WS , and the FRP powder particle size is D P ,
When the required grinding time is t P , the required grinding time is t WB :
t WS : t P = 1: 4: 8. These results are shown in FIG.
If the required grinding particle size is adjusted by adjusting the required grinding time and the residence time in the mill, the ratio of the distance between the supply port and the discharge port is required to be reflected in the continuous grinding conditions such as What is necessary is just to make it the ratio of batch grinding time. Therefore, in order to obtain the particle size and mixing ratio of the raw material powder shown in Table 2 below, UF
L WB : L WS : L P
By arranging them at the position of = 1: 4: 8, drying of the target artificial wood and slurry before molding were continuously produced by single-stage pulverization.

【0017】[0017]

【表2】 [Table 2]

【0018】[0018]

【発明の効果】これより本発明の方法により得られる人
工木材は下記の優れた特性を有する: (1)従来の市販人工木材に比較して、強度、特に吸水
強度が格段に優れる、 (2)天然松材とほぼ同等の強度を有し、強度の方向性
が小さく、最弱強度では天然松材よりもむしろ優れる、 (3)風倒木や立枯木などの廃木材と処理が厄介で社会
問題となっている廃FRP製品(廃FRP船、廃浴槽)
を主原料として使用するので、低コストで製造でき、か
つ廃棄物の再資源化の面から社会的意義も大きい。 (4)特にUFミルを用いて行うときは、製造コストを
著しく低減することができる(ほぼ従来法の半分)。
Thus, the artificial wood obtained by the method of the present invention has the following excellent properties: (1) Compared with the conventional commercial artificial wood, the strength, particularly the water absorption strength, is remarkably excellent. ) It has almost the same strength as natural pine wood, the directionality of the strength is small, and the weakest strength is better than natural pine wood. (3) Waste wood such as wind-down trees and dead trees are difficult to treat and society Waste FRP products in question (waste FRP ships, waste tubs)
Since it is used as a main raw material, it can be manufactured at low cost and has great social significance in terms of recycling of waste. (4) Especially when using a UF mill, the manufacturing cost can be significantly reduced (almost half of the conventional method).

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1は、本発明の方法に係る製造プロセスの一
例を示すフローシート図、
FIG. 1 is a flow sheet diagram showing an example of a manufacturing process according to the method of the present invention,

【図2】図2は、本発明の方法により得られた人工木材
について、原料の平均粒径比と強度比との関係を示すグ
ラフ
FIG. 2 is a graph showing the relationship between the average particle size ratio of raw materials and the strength ratio for artificial wood obtained by the method of the present invention.

【図3】図3は、本発明の方法により得られた人工木材
について原料の混合比と強度比との関係を示すグラフ、
FIG. 3 is a graph showing the relationship between the mixing ratio of raw materials and the strength ratio for artificial wood obtained by the method of the present invention;

【図4】図4は、UFミルを用いたワンパス湿式連続粉
砕装置を示す概念図、
FIG. 4 is a conceptual diagram showing a one-pass wet continuous pulverizer using a UF mill,

【図5】図5は、原料供給口の配置を変えることにより
粉砕粒径を調整する手段を説明する模式図、
FIG. 5 is a schematic diagram illustrating a means for adjusting the particle size by changing the arrangement of the raw material supply ports;

【図6】図6は、木粉及びFRP粉をUFミルバッチ粉
砕試験で粉砕したときの夫々の粉砕特性を示すグラフで
ある。
FIG. 6 is a graph showing the respective pulverization characteristics when wood powder and FRP powder are pulverized by a UF mill batch pulverization test.

【符号の説明】[Explanation of symbols]

1:原料ホッパ 2:供給機 3:タンク 4:供給ポンプ 5:UFみル外筒 6:UFミル内筒 7:粉砕ボール 8:排出スリット 9:製品タンク 1: Material hopper 2: Feeder 3: Tank 4: Supply pump 5: UF mill outer cylinder 6: UF mill inner cylinder 7: Grinding ball 8: Discharge slit 9: Product tank

───────────────────────────────────────────────────── フロントページの続き (72)発明者 角田 英雄 長崎県長崎市深堀町五丁目717番1号 三菱重工業株式会社長崎研究所内 (56)参考文献 特開 昭53−13681(JP,A) 特開 平7−9467(JP,A) (58)調査した分野(Int.Cl.7,DB名) B27N 1/00 - 5/00 B27L 11/00 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Hideo Tsunoda 5-717-1 Fukahori-cho, Nagasaki-shi, Nagasaki Mitsubishi Heavy Industries, Ltd. Nagasaki Research Laboratory (56) References JP-A-53-13681 (JP, A) Kaihei 7-9467 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B27N 1/00-5/00 B27L 11/00

Claims (9)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 バインダーを加えた木粉を圧縮成形して
人工木材を製造する方法において、木粉原料を平均粒度
分布が100〜500μmの粗粒木粉と平均粒度分布が
10〜50μmの微粒木粉であって、かつ前記粗粒木粉
の平均粒径の1/3〜1/10の平均粒径を有する微粒
木粉とに粉砕分級し、粗粒木粉100重量部に対して1
0〜60重量部の微粒木粉を加えて木材粉相互の最密充
填を促進することを特徴とする高強度人工木材の製造方
法。
1. A method for producing artificial wood by compression-molding wood powder to which a binder has been added, wherein the wood powder raw material has an average particle size.
Coarse wood flour with distribution of 100-500μm and average particle size distribution
Fine-grained wood flour having a particle size of 10 to 50 μm and having an average particle size of 1/3 to 1/10 of the average grain size of the coarse-grained wood flour is crushed and classified. 1 for part
A method for producing high-strength artificial wood, characterized in that 0 to 60 parts by weight of fine wood powder is added to promote close packing between wood powders.
【請求項2】 微粒木粉平均粒径の1/3〜1/10の
平均粒径を有する熱硬化性樹脂粉を加えて剛性を大きく
する請求項1に記載の高強度人工木材の製造方法。
2. The method for producing a high-strength artificial wood according to claim 1, wherein the rigidity is increased by adding a thermosetting resin powder having an average particle size of 1/3 to 1/10 of the average particle size of the fine wood powder. .
【請求項3】 風倒木、立枯木又は家屋解体材木などの
廃木材を木粉原料とし、廃船や廃浴槽から多量に発生す
る廃FRPを熱硬化性樹脂原料とする請求項1又は請求
項2に記載の高強度人工木材の製造方法。
3. The method according to claim 1, wherein waste wood such as wind-down wood, standing wood or house dismantled wood is used as wood flour raw material, and waste FRP generated in large quantities from waste boats and waste bath tubs is used as thermosetting resin raw material. 3. The method for producing a high-strength artificial wood according to 2.
【請求項4】 木粉原料を、湿式粉砕処理により、粗粒
木粉と粗粒木粉平均粒子径の1/10〜1/3の平均子
粒径を有する微粒木粉とに粉砕分級し、粗粒木粉100
重量部に対して10〜60重量部の微粒木粉を加えて木
粉相互の最密充填を促進し、また微粒木粉平均粒子径の
1/10〜1/3の平均粒子径を有する熱硬化性樹脂粉
を加え剛性を大きくすることからなる人工木材の製造方
法において、粉砕粗粒木粉・微粒木粉、粉砕熱硬化性樹
脂微粒を一つの粉砕機にて1パス連続湿式製造すること
を特徴とする高強度人工木材の製造方法。
4. A wood flour raw material is pulverized and classified by wet pulverization into coarse wood flour and fine wood flour having an average particle size of 1/10 to 1/3 of the average grain size of the coarse wood flour. , Coarse wood flour 100
10 to 60 parts by weight of fine wood flour is added to the parts by weight to promote the close packing of the wood flour, and heat having an average particle size of 1/10 to 1/3 of the average particle size of fine wood flour In a method for producing artificial wood, which comprises adding curable resin powder to increase rigidity, one-pass continuous wet production of pulverized coarse wood powder, fine wood powder, and pulverized thermosetting resin fine particles with one pulverizer. A method for producing high-strength artificial wood, characterized by the following.
【請求項5】 粉砕機への粉砕原料供給箇所を、上流側
から下流側へと任意の箇所に設置することで粉砕機内部
の滞留時間を調整し、FRP粉、微粉木材、粗粉木材を
均一混合・分散したスラリーを一つの粉砕機にて1パス
連続湿式製造する請求項4に記載の高強度人工木材の製
造方法。
5. A pulverizing raw material supply point to a pulverizer is installed at an arbitrary point from an upstream side to a downstream side to adjust a residence time inside the pulverizer, thereby reducing FRP powder, fine powder wood, and coarse powder wood. The method for producing a high-strength artificial wood according to claim 4, wherein the uniformly mixed and dispersed slurry is subjected to one-pass continuous wet production with one pulverizer.
【請求項6】 風倒木、立枯木又は家屋解体材木などの
廃木材を木粉原料とし、廃船や廃浴槽から多量に発生す
る廃FRPを熱硬化性樹脂原料とする請求項4又は5に
記載の高強度人工木材の製造方法。
6. The method according to claim 4 or 5, wherein waste wood such as wind-down trees, dead wood or house demolition wood is used as a raw material for wood flour, and waste FRP generated in large quantities from waste ships and waste tubs is used as a raw material for thermosetting resin. The method for producing a high-strength artificial wood according to the above.
【請求項7】 バインダーを加えた木粉を圧縮成形して
なる人工木材において、該木粉が平均粒度分布が100
〜500μmの粗粒木粉と該粗粒木粉100重量部に対
して、平均粒度分布が10〜50μmの微粒木粉であっ
て、かつ前記粗粒木粉の平均粒径の1/3〜1/10の
平均粒径を有する微粒木粉を10〜60重量部加えて木
材粉の相互最密充填を促進してなる高強度人工木材。
7. An artificial wood obtained by compression-molding wood powder to which a binder has been added, wherein the wood powder has an average particle size distribution of 100.
With respect to coarse wood flour of ~ 500 µm and 100 parts by weight of the coarse wood flour , fine wood flour having an average particle size distribution of 10 ~ 50 µm
And 10 to 60 parts by weight of fine wood flour having an average grain size of 1/3 to 1/10 of the average grain size of the coarse wood flour is added to promote mutual close packing of wood flour. Strength artificial wood.
【請求項8】 微粒木粉平均粒径の1/3〜1/10の
平均粒径を有する熱硬化性樹脂粉を更に加えてなる請求
項7に記載の高強度人工木材。
8. The high-strength artificial wood according to claim 7, further comprising a thermosetting resin powder having an average particle size of 1/3 to 1/10 of the average particle size of the fine wood powder.
【請求項9】 風倒木、立枯木又は家屋解体材木などの
廃木材を木粉原料とし、廃船又は廃浴槽から多量に発生
する廃FRPをバインダー用の熱硬化性樹脂原料として
用いてなる請求項7又は8に記載の高強度人工木材。
9. A method in which waste wood such as wind-down wood, dead wood or house demolition wood is used as wood flour raw material, and waste FRP generated in large quantities from a waste ship or waste tub is used as a thermosetting resin raw material for a binder. Item 7. High-strength artificial wood according to item 7 or 8.
JP09876395A 1995-04-24 1995-04-24 Artificial wood and method for producing the same Expired - Fee Related JP3322518B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09876395A JP3322518B2 (en) 1995-04-24 1995-04-24 Artificial wood and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09876395A JP3322518B2 (en) 1995-04-24 1995-04-24 Artificial wood and method for producing the same

Publications (2)

Publication Number Publication Date
JPH08290410A JPH08290410A (en) 1996-11-05
JP3322518B2 true JP3322518B2 (en) 2002-09-09

Family

ID=14228451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP09876395A Expired - Fee Related JP3322518B2 (en) 1995-04-24 1995-04-24 Artificial wood and method for producing the same

Country Status (1)

Country Link
JP (1) JP3322518B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005238502A (en) * 2004-02-24 2005-09-08 Sekisui Chem Co Ltd Woody chip formed product
JP5261693B2 (en) * 2006-12-26 2013-08-14 西日本技術開発有限会社 Method for producing cereal by-product-biofiber composite regenerated molding and rice husk-molding base material for greening medium
JP2012111063A (en) * 2010-11-22 2012-06-14 Eidai Co Ltd Method of manufacturing wood fiberboard, and wood fiberboard
CN108858632B (en) * 2018-06-01 2021-07-02 中山市时兴装饰有限公司 Cold pressing and siloxane modified cold pressing wood grain process and pure-color veneer-free open paint wooden door

Also Published As

Publication number Publication date
JPH08290410A (en) 1996-11-05

Similar Documents

Publication Publication Date Title
EP0655310B1 (en) Method of manufacturing wood-like product and the product
US5665425A (en) Wood meal and method of manufacturing the same
CN113019648A (en) High-efficient preparation system of abandonment concrete regeneration sand powder
JP3322518B2 (en) Artificial wood and method for producing the same
CN105540591B (en) The preparation method of multi items boron carbide micro powder
CN104446071A (en) Dry sand making process
WO2013085478A1 (en) Grinding work member and centrifugal disintegrator based thereon
JP4379263B2 (en) Woody fuel production method
DE3544798C2 (en) Device for comminution and grinding and drying (grinding drying) of moist material
JP3581736B2 (en) Method and apparatus for crushing and drying cellulosic crushed material
CN115124368B (en) Foamed ceramic powder and preparation method and application thereof
WO1988001906A1 (en) Method and equipment for the production of particularly finely divided dry powders
AU2020444462B2 (en) System for controlling powder particle component and particle size and control method of the system
CN211246814U (en) Thermoplastic resin rubbing crusher
CN219898444U (en) Superfine steel slag micro powder production system
AU654587B2 (en) Wood meal and method of manufacturing the same
CA1297673C (en) Water slurry of carbonized substances, and process of manufacturing the same
CN211755904U (en) A smash and mix integrated device for producing mix powder
JPS588341Y2 (en) Crusher
RU33123U1 (en) Cone mill
Mihailichenko et al. Milling equipment modernization: a unit for utilizing fibrous waste of woodworking production
CN207521125U (en) A kind of air-flow crushing stirring integratedization reaction kettle
JP2673918B2 (en) Composite powder and method for producing composite powder
JPH05177610A (en) Wood meal and production thereof
JPH03217251A (en) Vertical type grinder

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20020521

LAPS Cancellation because of no payment of annual fees