JPH04224902A - Method for forming wood flour and wood flour and wood flour paint - Google Patents
Method for forming wood flour and wood flour and wood flour paintInfo
- Publication number
- JPH04224902A JPH04224902A JP2414370A JP41437090A JPH04224902A JP H04224902 A JPH04224902 A JP H04224902A JP 2414370 A JP2414370 A JP 2414370A JP 41437090 A JP41437090 A JP 41437090A JP H04224902 A JPH04224902 A JP H04224902A
- Authority
- JP
- Japan
- Prior art keywords
- wood flour
- wood
- wood powder
- raw material
- less
- 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 169
- 235000013312 flour Nutrition 0.000 title claims abstract description 58
- 239000003973 paint Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims description 22
- 239000002994 raw material Substances 0.000 claims abstract description 46
- 239000002245 particle Substances 0.000 claims abstract description 38
- 238000000576 coating method Methods 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 18
- 238000010025 steaming Methods 0.000 claims abstract description 18
- 239000011248 coating agent Substances 0.000 claims abstract description 16
- 239000000843 powder Substances 0.000 claims description 104
- 238000009835 boiling Methods 0.000 claims description 10
- 239000007787 solid Substances 0.000 claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000000227 grinding Methods 0.000 claims description 8
- 230000008569 process Effects 0.000 claims description 8
- 238000009837 dry grinding Methods 0.000 claims 1
- 238000010298 pulverizing process Methods 0.000 abstract description 10
- 238000010411 cooking Methods 0.000 abstract 1
- 229920005989 resin Polymers 0.000 description 27
- 239000011347 resin Substances 0.000 description 27
- 238000000465 moulding Methods 0.000 description 13
- 238000002156 mixing Methods 0.000 description 10
- 235000013339 cereals Nutrition 0.000 description 8
- 238000005498 polishing Methods 0.000 description 8
- 229920005610 lignin Polymers 0.000 description 7
- 239000000203 mixture Substances 0.000 description 6
- 239000001913 cellulose Substances 0.000 description 5
- 229920002678 cellulose Polymers 0.000 description 5
- 239000000049 pigment Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- 235000007173 Abies balsamea Nutrition 0.000 description 3
- 239000004606 Fillers/Extenders Substances 0.000 description 3
- 241000218685 Tsuga Species 0.000 description 3
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 210000004081 cilia Anatomy 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000002360 explosive Substances 0.000 description 3
- 230000001965 increasing effect Effects 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 229920002488 Hemicellulose Polymers 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 239000007844 bleaching agent Substances 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000011802 pulverized particle Substances 0.000 description 2
- 239000000565 sealant Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 229920001864 tannin Polymers 0.000 description 2
- 239000001648 tannin Substances 0.000 description 2
- 235000018553 tannin Nutrition 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000001886 ciliary effect Effects 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- GRWZHXKQBITJKP-UHFFFAOYSA-L dithionite(2-) Chemical compound [O-]S(=O)S([O-])=O GRWZHXKQBITJKP-UHFFFAOYSA-L 0.000 description 1
- 238000009503 electrostatic coating Methods 0.000 description 1
- ZINJLDJMHCUBIP-UHFFFAOYSA-N ethametsulfuron-methyl Chemical compound CCOC1=NC(NC)=NC(NC(=O)NS(=O)(=O)C=2C(=CC=CC=2)C(=O)OC)=N1 ZINJLDJMHCUBIP-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000002649 leather substitute Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 229920005906 polyester polyol Polymers 0.000 description 1
- 229920001228 polyisocyanate Polymers 0.000 description 1
- 239000005056 polyisocyanate Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- PFUVRDFDKPNGAV-UHFFFAOYSA-N sodium peroxide Chemical compound [Na+].[Na+].[O-][O-] PFUVRDFDKPNGAV-UHFFFAOYSA-N 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
Landscapes
- Debarking, Splitting, And Disintegration Of Timber (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
- Paints Or Removers (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は木材微粉を得る方法及
び粒径が16μm以下に取り揃えられた樹脂成形用骨材
としての木粉と、木材微粉を含む塗料の提供に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for obtaining fine wood powder, wood powder as aggregate for resin molding whose particle size is 16 μm or less, and a paint containing fine wood powder.
【0002】0002
【従来の技術】微粉状に粉砕した木粉を成形樹脂中に含
ませることで成形時に生ずる歪みを無くすと共に、成形
樹脂に硬さをもたらしたり、成形樹脂に吸湿性をもたら
すことが試みられてきた。かゝる従来の樹脂成形用の骨
材としての木粉は、樹脂に対する配合時の分散性を良く
する意図、及び樹脂成形時に成形機内に木酸ガスが生じ
ないように改良されたものが多く、その典型的な木粉と
しては尿素樹脂で硬化処理の施されたパーティクルボー
ドの表面研磨粉を用いていた。かゝるパーティクルボー
ドの表面研磨粉を用いる主たる理由は、パーティクルボ
ードの表面研磨粉が微細であり、しかも繊毛部分の少な
い“粒”の形状をなしていることにあった。即ち、この
種のパーティクルボードの表面研磨の方法によって微細
な粉末を容易に得ることができると共に、滑性の良い粉
末とされ、粉粒状の樹脂原料に対する良好な分散配合性
のある木粉とされていた。[Prior Art] Attempts have been made to eliminate distortion that occurs during molding by incorporating finely ground wood flour into molding resin, as well as to provide hardness and hygroscopicity to molding resin. Ta. Most of the wood flour used as aggregate for conventional resin molding has been improved to improve its dispersibility when blending into the resin, and to prevent wood acid gas from being generated in the molding machine during resin molding. The typical wood powder used was particle board surface polishing powder that had been hardened with urea resin. The main reason for using such particle board surface polishing powder is that the particle board surface polishing powder is fine and has a "grain" shape with few cilia. That is, by this type of surface polishing method of particle board, fine powder can be easily obtained, and the powder has good slipperiness, and the wood powder has good dispersion and blending properties for powder-like resin raw materials. was.
【0003】これに対し、木材を直接微粉状に粉砕する
方法は、乾式粉砕機を用いて粉砕する場合でも、湿式粉
砕機を用いて粉砕する場合であっても粉砕効率が悪く、
長時間の粉砕処理にも拘らず粉砕粉中に粒径の大きい木
粉が多量に残る不都合を有していた。又、得られた粉砕
木粉が“粒”状をなさず、その多くが繊維状とされてお
り、短径側で計測した粒径が数ミクロンであっても長径
側が繊毛状に長くなっている不都合を有していた。この
ような従来の木粉では、樹脂に配合して用いた際に木粉
相互が絡み有って凝集状態を作り出すことが多く、樹脂
材料に対し均一に分散されない不都合を有していた。
又、粉砕木粉の粒径が極端にバラついていることから成
形された樹脂製品に成形歪み等をもたらし易く、しかも
機械的な強度が部分的に異なる等の不都合を有していた
。又、このような粒の不揃えと、繊毛状の形状特性から
塗料あるいはフィルム等の薄い樹脂皮膜の形成骨材とし
ては不向きであった。On the other hand, the method of directly pulverizing wood into fine powder has poor pulverization efficiency, regardless of whether it is pulverized using a dry pulverizer or a wet pulverizer.
Despite the long pulverization process, a large amount of wood flour with a large particle size remains in the pulverized powder, which is disadvantageous. In addition, the obtained crushed wood powder does not have a "granular" shape, and most of it is fibrous, and even if the particle size measured on the short diameter side is several microns, the long diameter side becomes long like cilia. It had some inconveniences. When such conventional wood flour is blended with resin and used, the wood flour often becomes entangled with each other and creates an agglomerated state, which has the disadvantage that it is not uniformly dispersed in the resin material. Furthermore, since the particle size of the pulverized wood powder varies greatly, molded resin products tend to suffer from molding distortions, and the mechanical strength of the product tends to vary depending on the part. Furthermore, due to the irregularity of the grains and the cilia-like shape characteristics, it was not suitable as an aggregate for forming thin resin coatings such as paints or films.
【0004】0004
【発明が解決しようとする課題】かゝる点から開発され
てきている前記のパーティクルボードの表面研磨粉の活
用は、この表面研磨粉が繊毛状より粒状に近く樹脂材料
に分散配合し易い利点を有している。しかしながら、パ
ーティクルボードの表面研磨粉は、研磨対象であるパー
ティクルボードの素材的特性並びに切削手段、例えば使
用サンドペーパーのメッシュ等によって粒径にバラつき
が多く、しかも均一の木材特性を有していない不都合が
あった。又、この種のパーティクルボードの表面研磨粉
は主として尿素系の樹脂の硬化部分を有しており、木粉
特有の吸放湿性並びに肌触り感が極端に悪化されている
不都合を有していた。[Problems to be Solved by the Invention] Utilization of the above-mentioned particle board surface polishing powder, which has been developed from this point of view, has the advantage that this surface polishing powder has a granular shape rather than a ciliated shape, and is easier to disperse and blend into resin materials. have. However, the particle size of particle board surface polishing powder varies depending on the material characteristics of the particle board to be polished and the cutting method, such as the mesh of the sandpaper used, and furthermore, it has the disadvantage that it does not have uniform wood characteristics. was there. Furthermore, the surface polishing powder of this type of particle board mainly has a hardened portion of urea-based resin, and has the disadvantage that the moisture absorption and desorption properties and texture peculiar to wood powder are extremely deteriorated.
【0005】かゝる点から天然の木材の性質を残し、し
かも微細に粉砕されている木粉と、かゝる特長を有する
木粉の収率の良い粉砕方法、及び、かゝる特長を有する
木粉を含む塗料の提供を本発明は目的としてなされてい
る。[0005] From this point of view, we have developed a finely ground wood powder that retains the properties of natural wood, a method for grinding wood powder with a high yield that has such features, and a method for producing wood powder that has such features. An object of the present invention is to provide a paint containing wood powder having the following properties.
【0006】[0006]
【課題を解決するための手段】本発明は、かゝる目的を
達成するべく、請求項1の発明に係る木粉の成形方法は
、ツガあるいはラワン等の原料木を粉砕して得た粗粉砕
原料木材粉に煮沸又は蒸煮の処理を施す工程と、この煮
沸又は蒸煮の処理が施されてニグニン、タンニン質ある
いは樹脂等がセルロースと可分的な状態とされている原
料木材粉を、その含有水分が10wt%以下となるまで
強制的に乾燥する乾燥処理工程と、この乾燥処理の施さ
れた原料木材粉を乾式粉砕手段によって粉砕、分級し、
粒径が16μm以下の木材微粉とする粉砕工程とで構成
してある。[Means for Solving the Problems] In order to achieve the above object, the present invention provides a method for forming wood flour according to the invention of claim 1, in which a coarse wood powder obtained by crushing raw material wood such as hemlock or lauan is used. A process of boiling or steaming the pulverized raw material wood powder, and processing the raw material wood flour, which has been subjected to this boiling or steaming treatment so that nignin, tannins, resins, etc. can be separated from cellulose. A drying process in which the moisture content is forcibly dried until it becomes 10 wt% or less, and the raw material wood powder subjected to this drying process is crushed and classified by dry crushing means,
It consists of a pulverization step to produce fine wood powder with a particle size of 16 μm or less.
【0007】次いで、請求項2の発明に係る木粉は、粒
径が16μm以下に取り揃えられ、しかも含有水分が5
wt%以下となるように調整して構成してあり、特に、
樹脂に配合して用いるのに適する木粉の構成としてある
。更に、請求項3の発明に係る塗料は、粒径が16μm
以下であり、しかも含有水分が5wt%以下である木粉
を含めた構成としてある。次いで、請求項4の発明に係
る木粉塗料は、ビヒクルの固形分に対し、粒径が16μ
m以下で、含有水分が5wt%以下の木粉を150wt
%〜300wt %の範囲で配合した構成としてある
。更に、請求項5の発明に係る木粉塗料は、ビヒクルの
固形分に対し、粒径が16μm以下で、含有水分が5w
t%以下の木粉を15wt%〜25wt%の範囲で配合
した構成としてある。[0007] Next, the wood flour according to the invention of claim 2 has a particle size of 16 μm or less, and has a water content of 5 μm or less.
It is adjusted and configured so that it is less than wt%, and in particular,
The composition of wood powder is suitable for use in combination with resin. Furthermore, the paint according to the invention of claim 3 has a particle size of 16 μm.
In addition, the composition includes wood flour having a moisture content of 5 wt% or less. Next, the wood powder paint according to the invention of claim 4 has a particle size of 16 μm based on the solid content of the vehicle.
150wt of wood flour with a moisture content of 5wt% or less
% to 300 wt %. Furthermore, the wood powder paint according to the invention of claim 5 has a particle size of 16 μm or less and a water content of 5 w based on the solid content of the vehicle.
It has a composition in which less than t% of wood flour is blended in a range of 15wt% to 25wt%.
【0008】[0008]
【作用】粗粉砕されている原料木材粉は、その粉砕処理
前に煮沸又は蒸煮処理と、これに続く強制的な乾燥処理
とが施されており、木材微粉とする時点での含有水分が
10wt%まで引き下げられていることから、原料木材
粉は組織的に脆く、粉砕処理時の破断性が良好となる。
塗料に含まれている木粉の粒径が16μm以下であり、
含有水分が5wt%以下であることから塗料としての展
延性が阻害されず、形成皮膜にクラック、ピンホール等
を生じないように機能する。[Effect] The coarsely ground raw material wood powder is boiled or steamed before the grinding process, followed by a forced drying process, and the moisture content at the time it is made into fine wood powder is 10w. %, the raw material wood powder is structurally brittle and has good breakability during pulverization. The particle size of the wood powder contained in the paint is 16 μm or less,
Since the water content is 5 wt% or less, the spreadability as a paint is not inhibited, and the film functions to prevent cracks, pinholes, etc. from occurring in the formed film.
【0009】[0009]
【実施例】以下本発明の典型的な一実施例について詳細
に説明する。こゝで粉砕対象として用いられる原料木材
粉はツガ、ラワン等の針葉樹及びかつ葉樹のいずれの種
類のものであっても良い。これらの樹木又は、チップを
機械的に粉砕し150 メッシュよりも細かい粒径の粉
砕粉、特に120 メッシュ以下の粒径に粉砕した原料
木材粉を用意する。かゝる原料木材粉に対しては必要な
前処理を施す。この原料木材粉の前処理は、通例リグニ
ン、タンニン質あるいは色素、樹脂等を有している原料
木材粉に対し、漂白あるいは不要物質の除去として施さ
れる。
漂白の典型例としては、塩素を用いてリグニンを可溶性
の塩化リグニンとし、アルカリにて溶解除去すると共に
サラシ粉を用いて色素及び残留リグニンの漂白をなす。
又、極力リグニンを残した状態で白色度を高める必要の
ある場合には、可酸化水素、過酸化ナトリウム、次亜塩
素酸塩、亜ニチオン酸塩等を用いて単段漂白を施す。[Embodiment] A typical embodiment of the present invention will be described in detail below. The raw material wood powder used as the object to be crushed may be any type of coniferous wood or leaf wood such as hemlock or lauan. Raw material wood powder is prepared by mechanically crushing these trees or chips to have a particle size finer than 150 mesh, particularly to a particle size of 120 mesh or less. Necessary pretreatment is applied to such raw material wood powder. This pretreatment of the raw material wood powder, which usually contains lignin, tannins, pigments, resins, etc., is carried out to bleach or remove unnecessary substances. A typical example of bleaching is to convert lignin into soluble chlorinated lignin using chlorine, dissolve and remove it with alkali, and bleach the pigment and residual lignin using salsa flour. If it is necessary to increase the whiteness while leaving as much lignin as possible, single-stage bleaching is performed using hydrogen oxide, sodium peroxide, hypochlorite, dithionite, or the like.
【0010】このようにして用意された原料木材粉を回
転筒内に投入する。この回転筒には、筒の周面を覆うよ
うにジャケットが取付けられていると共に蓋を閉じた際
に密閉された処理空間となる原料木材粉の投入処理室が
ある。この回転筒の処理室内に原料木材粉の投入をなす
と共に蓋を閉じ、密閉処理空間とした状態で、この密閉
処理空間に30分間連続して蒸気を供給し、密閉処理空
間の内部圧が1.9kg /cm2 、120 ℃を維
持するようになす。この際に回転筒の密閉処理室を取り
囲んでいるジャケット内に蒸気を供給して、この密閉処
理室を外部から加熱することによって、前記の密閉処理
室での処理条件の維持をなすようにするのが好ましい。
又、この密閉処理室での原料木材粉の蒸煮処理は、回転
筒の回転によって該密閉処理室内の原料木材粉が回転撹
拌状態でなされるのが好ましい。[0010] The raw wood powder prepared in this way is put into a rotating cylinder. This rotary cylinder has a jacket attached to cover the circumferential surface of the cylinder, and a processing chamber for feeding raw wood powder, which becomes a sealed processing space when the lid is closed. Raw material wood powder is introduced into the processing chamber of this rotary cylinder, and the lid is closed to create a sealed processing space. Steam is continuously supplied to this sealed processing space for 30 minutes, and the internal pressure of the sealed processing space is reduced to 1. .9kg/cm2 and maintain a temperature of 120°C. At this time, the processing conditions in the sealed processing chamber are maintained by supplying steam into the jacket surrounding the sealed processing chamber of the rotating cylinder and heating this sealed processing chamber from the outside. is preferable. Further, it is preferable that the steaming treatment of the raw material wood powder in the sealed processing chamber is performed while the raw material wood powder in the sealed processing chamber is rotated and agitated by the rotation of a rotary cylinder.
【0011】こゝで施される蒸煮処理の処理条件は投入
原料木材粉の樹種によってもたらされる性状の差異、投
入量によって異なると共に、処理室内の室圧及び処理温
度と処理時間とが相関的な関係におかれている。又、一
般に前記の処理条件を高めた場合、追って説明する粉砕
性が処理条件の加重に見合って良好とされ、特に10μ
mアンダーの微細粉砕粉の時間当りの収率が良好となる
ことが認められた。この蒸煮工程ではリグニンその他の
繊維結合物質とセルロース、ヘミセルロース間の結合が
緩められると共に、セルロースの構成が緩められフイブ
リルの緩かな結合状態になるものと仮定される。[0011] The processing conditions of the steaming treatment carried out here vary depending on the properties of the input wood powder caused by the species of wood and the input amount, and the processing time is correlated with the chamber pressure and processing temperature in the processing chamber. placed in a relationship. Generally, when the above-mentioned processing conditions are increased, the crushability, which will be explained later, is said to be good commensurate with the increased processing conditions.
It was found that the yield per hour of finely pulverized powder under m was good. It is assumed that this steaming step loosens the bonds between lignin and other fiber-binding substances, cellulose, and hemicellulose, and loosens the structure of cellulose to form loosely bonded fibrils.
【0012】特に、回転筒の外周のジャケットを用いて
密閉処理室内にある原料木材粉を処理室内と外部とから
加熱する方式では、処理室内で加熱された部分にある原
料木材粉の含む水分が膨張し、その組織を急激に膨張さ
せると共に、この加熱された部分にある原料木材粉が回
転撹拌によって非加熱部分に移動され、この木材粉の加
熱表面に急激に結露を生じ、木材粉の含む水分の冷却収
縮を誘起する作用が連続して生じ、これによって、リグ
ニンその他の繊維結合物質とセルロース、ヘミセルロー
ス間の結合を緩めると共に、セルロース構成自体が緩か
なフイブリルの結合状態に移行される。[0012] In particular, in a method in which the raw material wood powder in the sealed processing chamber is heated from inside the processing chamber and the outside using a jacket around the outer periphery of the rotating cylinder, the moisture contained in the raw material wood powder in the heated part of the processing chamber is heated. At the same time, the raw wood powder in the heated part is moved to the non-heated part by rotational agitation, rapidly condensing on the heated surface of the wood powder, and the wood powder contains The action of inducing cooling contraction of moisture occurs continuously, which loosens the bonds between lignin and other fiber-binding substances, cellulose, and hemicellulose, and shifts the cellulose structure itself to a state of loose fibrillar bonding.
【0013】かゝる蒸煮処理を施すことなく原料木材粉
を加圧釜内に投入して煮沸処理を施しても良い。この場
合でも釜内温度が120 ℃前後となるように釜内気圧
を設定し、30分以上煮沸処理を施すのが好ましい。尚
、この煮沸処理においても、原料木材粉を投入したゲー
ジを加圧釜内に入れて充分に煮沸した後、これを釜外に
取り出し、急速に冷却させる処理を反復して施すことに
よっても原料木材粉の破砕時の収率が良好とされる。[0013] The raw material wood powder may be put into a pressure cooker and subjected to a boiling treatment without such a steaming treatment. Even in this case, it is preferable to set the pressure inside the pot so that the temperature inside the pot is around 120° C., and to perform the boiling treatment for 30 minutes or more. In addition, in this boiling process, the gauge containing the raw material wood powder is placed in the pressure cooker and boiled sufficiently, then taken out of the pot and rapidly cooled. The yield when crushing the powder is said to be good.
【0014】このようにして蒸煮又は煮沸処理の施され
た原料木材粉に水切り処理を施す。この水切り処理は脱
絞の方法、あるいは遠心分離の方法で強制的に施しても
良く、次工程の乾燥処理の処理時間を短縮できると共に
原料木材粉の破砕時の収率に良い影響をもたらす。原料
木材粉の乾燥は含有水分が10wt%以内、一般的には
8wt%以内となるまで強制乾燥の方法で施す。この原
料木材粉に対する乾燥処理は、この原料木材粉の有する
含有水分が低くなるまで施すのが良く、好ましくは5w
t%以下、更に好ましくは3wt%以下となるまで乾燥
処理を施す。この乾燥方法の一つとしては、先に原料木
材粉の蒸煮処理に用いた回転筒の密閉処理室に対する蒸
気の供給を中止し、ジャケット部分にのみ蒸気を供給し
ながら回転筒を回転させると共に、密閉処理室内に生ず
る過湿エヤーを抜気する構成とし、前記の蒸煮処理に連
続した乾燥処理とすることができる。又、加圧釜内から
取り出したゲージ内の原料木材粉に対し、このゲージ内
に熱風を吹き入れることによって原料木材粉に含まれて
いる水分を除去することによって先の加圧釜による煮沸
処理と連続した乾燥処理とすることができる。[0014] The raw material wood flour that has been subjected to the steaming or boiling treatment in this manner is subjected to a draining treatment. This draining treatment may be forcibly performed by a de-squeezing method or a centrifugal separation method, which can shorten the processing time of the next step of drying treatment and has a positive effect on the yield of the raw material wood powder when it is crushed. The raw wood powder is dried by forced drying until the moisture content is within 10 wt%, generally within 8 wt%. The drying treatment for this raw material wood powder is preferably carried out until the moisture content of this raw material wood powder becomes low, preferably 5w.
The drying treatment is performed until the concentration is t% or less, more preferably 3wt% or less. One of the drying methods is to stop the supply of steam to the sealed processing chamber of the rotary cylinder used for steaming the raw material wood powder, and to rotate the rotary cylinder while supplying steam only to the jacket part. The structure is such that the overhumidified air generated in the sealed processing chamber is vented, and the drying processing can be performed in succession to the steaming processing described above. In addition, hot air is blown into the gauge of the raw material wood powder taken out from the pressure cooker to remove the water contained in the raw wood powder, which is continuous with the boiling process in the pressure cooker. It can be a drying process.
【0015】乾燥され、しかも80〜150 メッシュ
、好ましくは120 メッシュ以下の粒径に取り揃えら
れた原料木材粉の粉砕をする。この原料木材粉の粉砕で
は、粉砕粒径が16μm以下、含有水分が5wt%以下
となるように粉砕する。この粉砕粒径は、粉砕粉の短径
側で測定した粒径で示してあり好ましくは10μm以下
、更に好ましくは5μm以下に粒径が取り揃えられてい
る粉砕粉であることが好ましい。又、粉砕木粉は、粉砕
効率及び粉砕後における樹脂との混合使用の点から、そ
の含有水分が5wt%以下、好ましくは3wt%以下と
するのが良く、含水率が極力0に近づくように粉砕する
のが好ましい。[0015] The dried raw material wood powder is pulverized to a particle size of 80 to 150 mesh, preferably 120 mesh or less. The raw material wood powder is pulverized so that the pulverized particle size is 16 μm or less and the moisture content is 5 wt % or less. The pulverized particle size is indicated by the particle size measured on the minor axis side of the pulverized powder, and the pulverized powder preferably has a uniform particle size of 10 μm or less, more preferably 5 μm or less. In addition, from the viewpoint of crushing efficiency and mixing use with resin after crushing, it is preferable that the moisture content of the crushed wood flour is 5 wt% or less, preferably 3 wt% or less, and the moisture content should be as close to 0 as possible. Preferably, it is ground.
【0016】かゝる点から原料木材粉の粉砕は磨り潰し
を主体とする乾式ボールミルを用いて粉砕するのが好ま
しい一粉砕方法である。この乾式ボールミルによる粉砕
では、ミル内の湿度が高まらないようになすと共に、特
にミル内温度が上昇しないように注意する。かゝる乾式
ボールミルによる原料木材粉の粉砕では、粉砕に伴って
粉砕機内の温度が急激に上昇し、暴爆を生ずる危険があ
ることから図1に示されるようにミル本体1の周面に冷
却ジャケット2を設け、この冷却ジャケット2に常時冷
却水を供給し、ミル内温度が80℃以下、好ましくは7
0℃以下となるようにして粉砕運転をする。ミル内にあ
る原料木材粉は、ミル内のボール3相互あるいはボール
3と原料木材粉との間の摩擦熱によって急速に加熱され
、原料木材粉の有していた水分が取り除かれ、粉砕の継
続によって5wt%以下、更には3wt%以下まで含有
水分が引き下げられる。こゝで示されるボールミルはミ
ル本体1の上部にロータ4のモータ5を有し、錐形下部
にバルブ6で開閉される取出し口7を有する上面開口の
バッチタイプのものであって、粉砕時に生ずる暴爆の危
険を大気解放によって避ける構成としてある。又、8は
ジャケット2に対する冷却水の供給パイプを、9はその
排水パイプを示してあり、ミル内温度が暴爆温域にいた
らぬように常時冷却する構成としてある。さらに、こゝ
で用いられているボール3は3mm〜5mm径のセラミ
ックスボールとし、暴爆を生ずる虞れのあるスレンレス
製のボールの使用を避けている。From this point of view, it is preferable to use a dry ball mill, which mainly performs grinding, to grind the raw material wood powder. When pulverizing with this dry ball mill, care must be taken not to increase the humidity inside the mill, and especially to prevent the temperature inside the mill from increasing. When the raw material wood powder is crushed by such a dry ball mill, the temperature inside the crusher rises rapidly during the crushing process, and there is a risk of an explosive explosion. A cooling jacket 2 is provided, and cooling water is constantly supplied to the cooling jacket 2, so that the temperature inside the mill is 80°C or less, preferably 70°C.
The grinding operation is carried out so that the temperature is below 0°C. The raw material wood powder in the mill is rapidly heated by the heat of friction between the balls 3 in the mill or between the balls 3 and the raw material wood powder, and the water contained in the raw material wood powder is removed, allowing continued pulverization. The moisture content is reduced to 5 wt% or less, further to 3 wt% or less. The ball mill shown here has a motor 5 with a rotor 4 in the upper part of the mill body 1, and is a batch type with an opening at the top and has an outlet 7 opened and closed by a valve 6 in the conical lower part. The structure is designed to avoid the risk of a violent explosion by releasing the atmosphere. Further, reference numeral 8 indicates a cooling water supply pipe to the jacket 2, and reference numeral 9 indicates a drain pipe thereof, which are designed to be constantly cooled so that the temperature inside the mill does not reach the explosive temperature range. Furthermore, the ball 3 used here is a ceramic ball with a diameter of 3 mm to 5 mm, avoiding the use of stainless steel balls that may cause explosive explosions.
【0017】かゝる大気解放型のボールミルに対し密閉
型のボールミルを用いて原料木材粉の粉砕をなしても良
い。この密閉タイプのボールミルによる原料木材粉の粉
砕では、ミル内の酸素濃度を15%以内とし、ミル内温
度を80℃以下に設定することが好ましい。図2のボー
ルミルは、その一例を示したものであって、前記の図1
のボールミルに蓋10を取りつけ、粉砕室を大気から遮
断すると共にパイプ11からボールミル内のエアーを抜
き出し、パイプ12からチッ素ガスを該ミル内に封入し
、ミル内を不活性の密閉された雰囲気として用いる。更
に、他の方法としてはボールミル内に連続してチッ素ガ
スを供給することでミル内の酸素濃度を15%以下に維
持しながら原料木材粉の粉砕をなしても良い。[0017] Instead of such an air-open type ball mill, a closed type ball mill may be used to pulverize the raw material wood powder. When grinding raw material wood powder using this closed type ball mill, it is preferable to set the oxygen concentration in the mill to 15% or less and the temperature in the mill to 80° C. or less. The ball mill shown in FIG. 2 is an example of the ball mill shown in FIG.
A lid 10 is attached to the ball mill, the crushing chamber is isolated from the atmosphere, and the air inside the ball mill is extracted from the pipe 11. Nitrogen gas is sealed into the mill from the pipe 12 to create an inert, sealed atmosphere inside the mill. used as Furthermore, as another method, the raw material wood powder may be pulverized while maintaining the oxygen concentration in the mill at 15% or less by continuously supplying nitrogen gas into the ball mill.
【0018】このようにして粉砕された木粉を分級して
必要とする粒径に取り揃えられた使用木粉を得る。図3
の分級機は比重分級によるものであって、矢印Yから投
入した未分級木粉をロータ13の回転により遠心分離状
態とし、分級木粉を矢印Wからバキュームして取り出す
と共に分級条件を満たさない粗粉を矢印Xから取り出す
。
尚、この風量分級においても、分級機内で微小木材粉が
暴爆する虞れがあり、矢印Nからチッ素ガスを分級機内
に連続して供給し、分級機内の酸素濃度を15%以内と
して分級する。図3の分級機では、0.4KW のモー
タ14を用いてロータ13を800 〜1000R.P
.M で回転させると共に矢印Nから200 リッター
/分のチッ素ガスを供給しながら分級し次の表1で示さ
れる分級木粉を得た。The wood flour thus pulverized is classified to obtain wood flour to be used having the required particle size. Figure 3
The classifier is based on gravity classification, in which unclassified wood flour input from arrow Y is centrifuged by the rotation of rotor 13, classified wood flour is vacuumed out from arrow W, and coarse wood flour that does not meet the classification conditions is removed. Take out the powder from the arrow X. In addition, even in this air volume classification, there is a risk of explosion of minute wood powder inside the classifier, so nitrogen gas is continuously supplied into the classifier from arrow N, and the oxygen concentration inside the classifier is kept within 15% for classification. do. In the classifier shown in FIG. 3, a 0.4KW motor 14 is used to drive the rotor 13 at a speed of 800 to 1000R. P
.. The wood powder was classified while being rotated by M and nitrogen gas was supplied at 200 liters/minute from the arrow N to obtain the classified wood flour shown in Table 1 below.
【0019】[0019]
【表1】[Table 1]
【0020】尚、前記の図1で示されるボールミルを5
.4 リッター容量とし、このボールミル内に3mm系
のジルコニア径のセラミックスボールを2.4 リッタ
ー装填したボールミルを用いて前記の蒸煮処理並びに乾
燥処理を施した原料木材粉の粉砕を2時間続行した後、
前記図3で示される分級機を用いて分級点の粒径が5μ
mとなるように分級したところ、粉砕木粉全量の90w
t%〜100wt %が5μmアンダーとなった。これ
に対し、蒸煮処理又は煮沸処理の施されていない乾燥木
粉を同一の条件で粉砕、分級したところ、粉砕木粉全量
の60wt%以上が5μmオーバーの粗い木粉として残
り、粉砕収率が極端に悪かった。又、前記の蒸煮処理を
施した原料木材粉を、含有水分を12wt%の状態で前
記と同一の条件で粉砕、分級したところ、粉砕木粉全量
の50wt%以上が5μmオーバーの粗い木粉として残
り、粉砕収率の面で難が認められた。It should be noted that the ball mill shown in FIG.
.. Using a ball mill with a capacity of 4 liters and 2.4 liters of 3 mm zirconia diameter ceramic balls loaded into the ball mill, the raw material wood powder that had been subjected to the steaming and drying treatment was continued to be pulverized for 2 hours.
Using the classifier shown in Figure 3 above, the particle size at the classification point is 5μ.
When classified into m, the total amount of crushed wood powder was 90w.
t% to 100wt% was under 5 μm. On the other hand, when dry wood flour that has not been subjected to steaming or boiling treatment is crushed and classified under the same conditions, more than 60 wt% of the total amount of crushed wood flour remains as coarse wood flour with a diameter exceeding 5 μm, and the crushing yield is low. It was extremely bad. In addition, when the raw material wood flour subjected to the above-mentioned steaming treatment was crushed and classified under the same conditions as above with a water content of 12 wt%, 50 wt% or more of the total amount of crushed wood flour was found to be coarse wood flour exceeding 5 μm. However, difficulties were observed in terms of pulverization yield.
【0021】尚、前記の原料木材粉の蒸煮処理に際して
、ケイ酸ナトリウムの5%水溶液を原料木材粉に含浸し
て処理することによって効率の良い蒸煮処理と脱色処理
とができる。[0021] In the steaming treatment of the raw material wood powder, efficient steaming treatment and decolorization treatment can be achieved by impregnating the raw material wood flour with a 5% aqueous solution of sodium silicate.
【0022】上記の方法で得られた木粉は、繊毛部分が
従来の木粉に比べて極端に少なく樹脂に配合して用いる
のに適しており、これを電子顕微鏡写真を用いて観察し
たところ、ツガの木粉では針状の微細粒子形状をなして
おり、ラワン材では楕円状の微細粒子形状のものが多く
見受けられた。従って、塩化ビニル等の各種の樹脂に配
合し、各種の成形方法によって、各種の樹脂成形物を得
ることができる。例えば上記で得られた16μmアンダ
ーの木粉25wt%をABS樹脂に配合して押し出し成
形によりテーブルの組付け脚を得た。このテーブルの組
付け脚は硬く、肌触り感が天然木に近く、削ることがで
きた。
又、上記で得られた5μmアンダーの木粉を塩化ビニル
樹脂に15wt%配合して2mm厚の軟質の塩ビシート
を押し出し成形により得た。得られたシートは手触り感
が柔かく、べたつき感がなく、しかも気泡等の発生が認
められなかった。更に、上記で得られた8μmアンダー
の木粉を6ナイロン樹脂に対し30wt%配合して湾曲
したアームグリップを射出成形により得た。得られたア
ームグリップは柔かい手触り感の割に硬く、成形歪みも
なかった。
又、射出時の樹脂の流動性が従来の木粉の混入時と異な
り良好であって、射出圧を低く設定することができた。[0022] The wood flour obtained by the above method has an extremely small number of ciliary parts compared to conventional wood flour, and is suitable for use in blending with resin. In hemlock wood powder, fine particles were found in the form of needles, while in lauan wood, fine particles in the form of ellipsoids were often observed. Therefore, various resin molded products can be obtained by blending with various resins such as vinyl chloride and using various molding methods. For example, 25 wt % of the wood powder with a diameter under 16 μm obtained above was blended with an ABS resin and extrusion molded to obtain a table assembly leg. The legs of this table are hard and feel close to natural wood, and could be carved. In addition, 15 wt % of the wood powder with a diameter under 5 μm obtained above was blended with vinyl chloride resin to obtain a soft vinyl chloride sheet with a thickness of 2 mm by extrusion molding. The obtained sheet was soft to the touch, had no sticky feeling, and no air bubbles were observed. Furthermore, a curved arm grip was obtained by injection molding by blending 30 wt % of the wood powder with a diameter under 8 μm obtained above in 6 nylon resin. The obtained arm grip was soft to the touch but hard, and there was no molding distortion. Furthermore, the fluidity of the resin during injection was good, unlike when conventional wood flour was mixed in, and the injection pressure could be set low.
【0023】次いで上記の木粉を塗料に配合して用いる
ことで木質様の表面特性を各種の物品にもたらすことが
できる。こゝで塗装対象とされる物品としては樹脂製の
成形物、金属製の成形物と共に木材成形物、更には合成
皮革等の全ての物品の表面に塗布形成して用いることが
できる。こゝで用いられる木粉は粒径が細かいほど良い
塗膜面の形成に適している。又、嵩比重が高く、繊毛状
でない木粉を用いるのが好ましい。更に又、塗膜面にピ
ンホール等が生じないように充分に乾燥されている木粉
を用いるのが良い。かゝる点から塗料に用いられる木粉
は、少なくとも粒径が16μmアンダーであり、含有水
分が5wt%以下であることを要する。尚、混入率は塗
料の性状、塗布目的等によって各別に設定される必要が
ある。[0023] Next, by blending the above-mentioned wood flour into a paint and using it, wood-like surface characteristics can be imparted to various articles. The objects to be coated here include resin moldings, metal moldings, wood moldings, and synthetic leather, all of which can be coated and used. The finer the particle size of the wood powder used here, the more suitable it is for forming a good coating surface. Further, it is preferable to use wood flour that has a high bulk specific gravity and is not ciliated. Furthermore, it is preferable to use wood flour that has been sufficiently dried to prevent pinholes from forming on the coating surface. From this point of view, wood flour used in paints must have a particle size of at least 16 μm or less and a water content of 5 wt% or less. Incidentally, the mixing rate needs to be set individually depending on the properties of the paint, the purpose of application, etc.
【0024】上記で得られた木粉を用いて下塗り塗料及
び上塗り用の塗料を得た。この塗料に配合した木粉は粒
径が細かいほど手の感触が柔かく、13μmと8.2
μmの粒径の木粉を配合して得られた塗膜表面の光沢、
吸湿性、着色性には差が無かった。下塗りとしての目止
剤として用いられる塗料はビヒクルの固形分に対し15
0wt %〜300wt %の木粉を混入して用いる。
こゝで目止剤のビヒクルに配合される木粉をビヒクルの
固形分に対し300wt %以上とした場合、目止め面
がモロモロの状態となり上塗り処理に難を生ずると共に
木材面の木理がボケる不都合を生ずる。又、ビヒクルの
固形分に対し150 wt%以下の配合率では目止め効
果が少なく、次工程の塗料との間での層間付着性が劣る
ことゝなり、本実施例ではビヒクルの固形分に対し20
0 wt%の木粉を配合して下塗り塗料として用いた。[0024] Using the wood powder obtained above, an undercoat paint and a topcoat paint were obtained. The finer the particle size of the wood powder mixed in this paint, the softer it feels on the hand;
The gloss of the coating surface obtained by blending wood powder with a particle size of μm,
There was no difference in hygroscopicity or colorability. The paint used as a sealant as an undercoat has a content of 15% based on the solid content of the vehicle.
0 wt % to 300 wt % wood flour is used. If the wood powder blended into the sealant vehicle is 300 wt % or more based on the solid content of the vehicle, the sealing surface will become crumbly, making topcoating difficult, and the grain of the wood surface will become blurred. This will cause some inconvenience. In addition, if the blending ratio is less than 150 wt% based on the solid content of the vehicle, the sealing effect will be small and the interlayer adhesion with the paint in the next process will be poor. 20
0 wt% wood flour was blended and used as an undercoat.
【0025】次いで上塗り塗料としては、ビヒクルの固
形分に対し上記の木粉を15wt%〜25wt%の範囲
で配合して用いるのが良い。このビヒクルの固形分に対
する木粉の配合量を25wt%以上とした場合、形成塗
膜が白濁状態となり、透明感が喪なわれる不都合があり
、又、ビヒクルの固形分に対し木粉の配合量を15wt
%以下とした場合、形成塗膜にテカリを生じ完全無反射
状の艶消し塗膜を得ることができない。かゝる点から本
実施例ではビヒクルの固形分に対し上記の木粉を20w
t%配合して上塗り塗料とした。[0025] Next, as a top coat, the above-mentioned wood flour is preferably blended in an amount of 15 wt% to 25 wt% based on the solid content of the vehicle. If the amount of wood flour added to the solid content of the vehicle is 25 wt% or more, the formed coating film becomes cloudy and loses its transparency. 15wt
% or less, the formed coating film becomes shiny and a completely non-reflective matte coating film cannot be obtained. From this point of view, in this example, 20w of the above wood flour was added to the solid content of the vehicle.
t% was mixed to make a top coat.
【0026】かゝる塗料を天然木材の面に塗布して用い
た。先ず前記の下塗り塗料を刷毛等で木材面に塗布し、
塗布後たゞちに拭き取って木材面にある導管等の穴部分
のみを埋めると共に木理部に付着している塗料を取り除
く。次いで、前記の上塗り塗料を、この下塗り塗料で目
止め処理の施された面に塗布形成する。かゝる木粉を有
する塗料は、下塗り時の拭き取りに際しても木材面の導
管あるいは細胞の空間部分に強く付着すると共に木理部
で容易に拭き取られる特長を有しており、シリカ等の無
機系の体質顔料を含む下塗り塗料に比較して木材面の導
管あるいは細胞の空間部分に対する付着性が特に良好で
あることから、木材面に対する塗布後の拭き取りによっ
ても木理部を除く面が下塗り塗料で覆われている特長を
有している。又、かゝる木粉を有する塗料は、塗布塗膜
間の層間付着性が良好であって、シリカ等の無機系の体
質顔料を含む塗料に比較して剥離等の不都合を生ずるこ
とがない。[0026] Such a paint was used by applying it to the surface of natural wood. First, apply the undercoat paint to the wood surface with a brush, etc.
Immediately after application, wipe it off to fill in only the holes for conduits etc. on the wood surface and remove any paint adhering to the wood grain. Next, the top coat is applied to the surface that has been sealed with the undercoat. Paints containing such wood powder have the characteristics that they strongly adhere to the conduits or cell spaces on the wood surface when wiped off during undercoating, and are easily wiped off by the wood grain. Compared to undercoat paints containing extender pigments, the adhesion to conduits or cell spaces on wood surfaces is particularly good. It has the characteristics of being covered with. In addition, paints containing such wood powder have good interlayer adhesion between applied coatings, and do not cause problems such as peeling compared to paints containing inorganic extender pigments such as silica. .
【0027】又、上記の上塗り塗料は塗膜表面の光沢が
均一に無くなり、良好な無反射塗膜を形成する。又、前
記の木材面に塗布した場合、どの角度からも木理が鮮明
にあらわれる。これに対し、シリカ系の体質顔料を含む
艶消し塗料を用いたところ塗面が白濁し、木理がボケた
感じとなり、天然木材の有する木目の風合いが無くなっ
た。[0027] Furthermore, the above-mentioned top coating paint uniformly eliminates gloss on the surface of the coating film, forming a good non-reflective coating film. Furthermore, when applied to the wood surface, the wood grains are clearly visible from any angle. On the other hand, when a matte paint containing a silica-based extender pigment was used, the painted surface became cloudy, the wood grains seemed blurred, and the grain texture of natural wood was lost.
【0028】尚、前記の上塗り塗料も、下塗り塗料も塗
布方法に制約は無く、刷毛塗り、吹付け塗装、静電塗装
、フローコーター塗装等いずれの塗装方法にも適してい
る。尚、上塗り塗装を吹付けの方法で処理する場合、木
粉を配合した塗料を200 メッシュの金網を通しなが
ら行なうのが良く、木粉の凝集を避けることができる。[0028] There are no restrictions on the coating method for the above-mentioned top coat and undercoat, and any coating method such as brush coating, spray coating, electrostatic coating, flow coater coating, etc. is suitable. When the top coat is applied by spraying, it is best to pass the paint containing wood powder through a 200-mesh wire gauze to avoid agglomeration of the wood powder.
【0029】尚、木材面に対する上記木粉配合の塗料の
典型例としては、前記の下塗り塗料のビヒクルをアルキ
ド樹脂とし、木粉の配合率を200 wt%として構成
し、又、上塗り塗料のビヒクルをポリエステルポリオー
ル樹脂とHMDI系ポリイソシアネート樹脂からなる二
液タイプのウレタン樹脂とし、ビヒクルに対し20wt
%の木粉を配合して構成する。この上塗り塗料の典型的
な配合例を表2に示す。この表2の配合例は上記粉砕木
粉を10.70 wt%含む塗料1と、7.20wt%
含む塗料2とからなっており、いずれも層間付着性が良
く、透明感を有しながらも完全に無反射の艶消し塗膜を
形成することができた。[0029] Typical examples of the wood powder-containing paint for wood surfaces include an alkyd resin as the vehicle for the undercoat and a wood flour content of 200 wt%; is a two-component type urethane resin consisting of polyester polyol resin and HMDI polyisocyanate resin, and the weight is 20wt relative to the vehicle.
% of wood flour. Typical formulation examples of this top coating are shown in Table 2. The formulation example in Table 2 is Paint 1 containing 10.70 wt% of the above-mentioned crushed wood flour and 7.20 wt% of the above-mentioned crushed wood powder.
All of them had good interlayer adhesion and were able to form a completely non-reflective matte coating film with a transparent feel.
【0030】[0030]
【表2】[Table 2]
【0031】[0031]
【発明の効果】本発明に係る木粉の成形方法では、粉砕
対象物を粗粉砕して用意すると共に、この粗粉砕の原料
木材粉に煮沸又は蒸煮の処理を施した後、充分な乾燥条
件のもとで粉砕していることから粉砕の収率が良好であ
り、特に16μmアンダーの微粉状の木粉の効率の良い
粉砕を可能とした。又、粉砕して得られた木粉には繊毛
部分が少なく針状又は楕円状の粒となっており、互に凝
集することがなく樹脂等に配合して用いる際の分散性が
良好である。更に16μmアンダーの木粉を含む塗料で
は層間の付着性が良好であり、下塗り塗料として用いた
場合の目止め効果に優れていると共に、上塗り塗料とし
て用いた場合には透明感のある完全無反射状の艶消し面
を形成できる特長を有している。[Effects of the Invention] In the method for forming wood flour according to the present invention, the object to be crushed is prepared by coarsely crushing it, and after the coarsely crushed raw material wood flour is subjected to boiling or steaming treatment, sufficient drying conditions are applied. Since the grinding is carried out under the same conditions as above, the grinding yield is good, and in particular, it is possible to efficiently grind fine wood flour under 16 μm in size. In addition, the wood powder obtained by pulverization has fewer cilia and has acicular or elliptical particles, which do not aggregate with each other and have good dispersibility when used in resins, etc. . Furthermore, paints containing wood powder under 16 μm have good adhesion between layers, and have excellent sealing effects when used as an undercoat, and are transparent and completely non-reflective when used as a topcoat. It has the feature of being able to form a matte surface.
【図1】解放型のボールミルの要部破断正面図。FIG. 1 is a cutaway front view of essential parts of an open-type ball mill.
【図2】密閉型のボールミルの要部破断正面図。FIG. 2 is a cutaway front view of essential parts of a closed ball mill.
【図3】分級機の要部破断正面図。FIG. 3 is a cutaway front view of the main parts of the classifier.
1 ミル本体 2 ジャケット 3 ボール 4 ロータ 5 モータ 6 バルブ 7 取り出し口 8 供給パイプ 9 排水パイプ 10 蓋 11 パイプ 12 パイプ 13 ロータ 14 モータ 1 Mill body 2. Jacket 3 Ball 4 Rotor 5 Motor 6 Valve 7 Ejection port 8 Supply pipe 9 Drain pipe 10 Lid 11 Pipe 12 Pipe 13 Rotor 14 Motor
Claims (5)
は蒸煮処理を施す工程と、この煮沸処理又は蒸煮処理の
施された原料木材粉を、その含有水分が10wt%以下
となるまで強制乾燥する乾燥処理工程と、この乾燥原料
木材粉を乾式粉砕により粉砕分級して粒径が16μm以
下の木材微粉とする粉砕工程とからなることを特徴とす
る木粉の成形方法。Claim 1: Boiling or steaming coarsely crushed raw material wood powder, and forced drying of the boiled or steamed raw material wood powder until its moisture content is 10 wt% or less. A method for forming wood powder, comprising: a drying process, and a grinding process, in which the dried raw material wood powder is pulverized and classified by dry grinding to obtain fine wood powder having a particle size of 16 μm or less.
水分が5wt%以下であることを特徴とする木粉。2. Wood flour characterized by having a particle size of 16 μm or less and a moisture content of 5 wt% or less.
水分が5wt%以下である木粉が含まれていることを特
徴とする木粉塗料。3. A wood powder paint characterized by containing wood powder having a particle size of 16 μm or less and a water content of 5 wt % or less.
水分が5wt%以下である木粉が、ビヒクルの固形分に
対し150wt %〜300wt %含まれていること
を特徴とする木粉塗料。4. A wood powder paint comprising 150 wt % to 300 wt % of wood flour having a particle size of 16 μm or less and a moisture content of 5 wt % or less based on the solid content of the vehicle.
水分が5wt%以下である木粉が、ビヒクルの固形分に
対し15wt%〜25wt%含まれていることを特徴と
する木粉塗料。5. A wood powder coating comprising 15 wt % to 25 wt % of wood flour having a particle size of 16 μm or less and a water content of 5 wt % or less based on the solid content of the vehicle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2414370A JP2965711B2 (en) | 1990-12-26 | 1990-12-26 | Wood flour molding method and wood flour paint |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2414370A JP2965711B2 (en) | 1990-12-26 | 1990-12-26 | Wood flour molding method and wood flour paint |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04224902A true JPH04224902A (en) | 1992-08-14 |
| JP2965711B2 JP2965711B2 (en) | 1999-10-18 |
Family
ID=18522858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2414370A Expired - Fee Related JP2965711B2 (en) | 1990-12-26 | 1990-12-26 | Wood flour molding method and wood flour paint |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2965711B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009209237A (en) * | 2008-03-03 | 2009-09-17 | Otani Toryo Kk | Coating material for woodwork |
| JP2016215419A (en) * | 2015-05-15 | 2016-12-22 | トヨタ紡織株式会社 | Wood board and manufacturing method thereof |
| CN110615150A (en) * | 2019-10-28 | 2019-12-27 | 徐州金河木业有限公司 | Waste treatment device for wood processing |
-
1990
- 1990-12-26 JP JP2414370A patent/JP2965711B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009209237A (en) * | 2008-03-03 | 2009-09-17 | Otani Toryo Kk | Coating material for woodwork |
| JP2016215419A (en) * | 2015-05-15 | 2016-12-22 | トヨタ紡織株式会社 | Wood board and manufacturing method thereof |
| CN110615150A (en) * | 2019-10-28 | 2019-12-27 | 徐州金河木业有限公司 | Waste treatment device for wood processing |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2965711B2 (en) | 1999-10-18 |
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