JP3156127B2 - Artificial wood made of waste paper and styrene resin and method for producing the same - Google Patents

Artificial wood made of waste paper and styrene resin and method for producing the same

Info

Publication number
JP3156127B2
JP3156127B2 JP25895598A JP25895598A JP3156127B2 JP 3156127 B2 JP3156127 B2 JP 3156127B2 JP 25895598 A JP25895598 A JP 25895598A JP 25895598 A JP25895598 A JP 25895598A JP 3156127 B2 JP3156127 B2 JP 3156127B2
Authority
JP
Japan
Prior art keywords
waste paper
styrene resin
paper pulp
methylene chloride
organic solvent
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
JP25895598A
Other languages
Japanese (ja)
Other versions
JP2000084909A (en
Inventor
松 茂 富 小
Original Assignee
小松 茂富
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 小松 茂富 filed Critical 小松 茂富
Priority to JP25895598A priority Critical patent/JP3156127B2/en
Publication of JP2000084909A publication Critical patent/JP2000084909A/en
Application granted granted Critical
Publication of JP3156127B2 publication Critical patent/JP3156127B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Dry Formation Of Fiberboard And The Like (AREA)

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は古紙材を主成分とす
る人工木材に関し、詳しくは古紙材とスチロール樹脂か
らなる人工木材とその製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to artificial wood mainly composed of used paper, and more particularly to an artificial wood made of used paper and styrene resin, and a method for producing the same.

【0002】[0002]

【従来の技術】従来、古紙材を利用した人工木材として
は、先ず、古紙材を粉砕し、得られた粉体状の古紙材3
0に対して樹脂分70の割合にて混合し、この混合物を
加熱,溶融し、固化していた。このような従来の方法に
よって製造された人工木材は、古紙材に対する樹脂分の
割合が多いことから、樹脂としての性質が強く、従って
天然の木材よりも重量が重くなり、釘打ち,切断等その
加工性も木材に比べて著しく悪いという欠点があった。
2. Description of the Related Art Conventionally, as artificial wood using waste paper, first, waste paper is pulverized and the obtained powdery waste paper 3 is obtained.
The resin was mixed at a ratio of 70 to 0, and the mixture was heated, melted, and solidified. Artificial wood manufactured by such a conventional method has a high resin content due to a large proportion of resin to waste paper, and therefore has a higher resin property, and therefore is heavier than natural wood, and can be used for nailing, cutting, and the like. There was a drawback that workability was significantly worse than wood.

【0003】また、古紙材の混合割合が少ないことか
ら、古紙材のリサイクルという面においても十分でな
く、古紙材よりも価格的に高い樹脂分を多く使用するこ
とから、最終製品としての価格も高いものにならざるを
えなかった。
[0003] Further, since the mixing ratio of the used paper material is small, the recycling of the used paper material is not sufficient, and the price of the final product is low because a large amount of resin is used, which is more expensive than the used paper material. It had to be expensive.

【0004】[0004]

【発明が解決しようとする課題】本発明は前記問題点を
解決するために創案されたものであり、重量的には木材
よりも軽いにもかかわらず木材同様の剛性と加工性があ
り、価格的にも安価に製造可能であり、また、古紙材の
使用割合が高いので古紙材のリサイクルを促進すること
ができる古紙材とスチロール樹脂による人工木材及びそ
の製造方法の提供をその目的としている。
SUMMARY OF THE INVENTION The present invention has been made in order to solve the above problems, and has the same rigidity and workability as wood even though it is lighter in weight than wood. It is an object of the present invention to provide an artificial wood made of a recycled paper material and a styrene resin, which can be manufactured at a low cost and can promote the recycling of the recycled paper material because of a high use ratio of the recycled paper material, and a method for producing the same.

【0005】[0005]

【課題を解決するための手段】本発明は前記目的を達成
するために、古紙細断機に古紙材と水とを投入して攪拌
し、当該古紙材を細断して古紙パルプ材とし、発泡スチ
ロール又はスチロール樹脂を塩化メチレン系有機溶剤に
て溶解して溶液とし、当該溶液中に前記古紙パルプ材を
投入して攪拌し、この攪拌された古紙パルプ材を所定形
状の型に収納し、プレスして水分及び前記塩化メチレン
系有機溶剤分を取り除き、この水分及び塩化メチレン系
有機溶剤分等が取り除かれた古紙パルプ材とスチロール
樹脂との混合物を乾燥して形成したことを特徴とする古
紙材とスチロール樹脂からなる人工木材とするものであ
る。
According to the present invention, in order to achieve the above object, waste paper and water are charged into a waste paper shredder and stirred, and the waste paper is shredded into waste pulp. The styrene foam or styrene resin is dissolved in a methylene chloride-based organic solvent to form a solution, and the used paper pulp material is put into the solution and stirred, and the stirred used paper pulp material is stored in a mold having a predetermined shape, and pressed. A waste paper material formed by drying a mixture of waste paper pulp material and styrene resin from which the moisture and the methylene chloride organic solvent component and the like have been removed. And artificial wood made of styrene resin.

【0006】また、前記発泡スチロール又はスチロール
樹脂分と前記古紙パルプ材との混合割合(重量)は3
0:70から40:60の範囲であることを特徴とする
ものである。
The mixing ratio (weight) of the styrene foam or styrene resin component to the waste paper pulp material is 3%.
The range is from 0:70 to 40:60.

【0007】また、古紙細断機に古紙材と水とを投入し
て攪拌し、当該古紙材を細断して古紙パルプ材とし、発
泡スチロール又はスチロール樹脂を塩化メチレン系有機
溶剤にて溶解して得た溶液中に前記古紙パルプ材を投入
して攪拌し、攪拌された古紙パルプ材を所定形状の型に
収納し、プレスして水分及び前記塩化メチレン系有機溶
剤分を除去し、この水分及び塩化メチレン系有機溶剤分
等が除去された古紙パルプ材とスチロール樹脂との混合
物を乾燥して形成したことを特徴とする古紙材とスチロ
ール樹脂からなる人工木材の製造方法とするものであ
る。
Further, waste paper and water are put into a waste paper shredder and stirred, and the waste paper is shredded into waste pulp, and styrene foam or a styrene resin is dissolved in a methylene chloride-based organic solvent. The waste paper pulp material is put into the obtained solution and stirred, the stirred waste paper pulp material is stored in a mold having a predetermined shape, and pressed to remove moisture and the methylene chloride-based organic solvent component. A method for producing an artificial wood made of a used paper material and a styrene resin, wherein the mixture is formed by drying a mixture of a used paper pulp material from which a methylene chloride-based organic solvent and the like have been removed and a styrene resin.

【0008】また、前記発泡スチロール又はスチロール
樹脂分と前記古紙パルプ材との混合割合(重量)は、3
0:70から40:60の範囲であることを特徴とし、
前記塩化メチレン系有機溶剤と、発泡スチロール又はス
チロール樹脂との混合割合(重量)は70:30である
ことを特徴とするものである。
The mixing ratio (weight) of the styrene foam or styrene resin component to the waste paper pulp material is 3%.
0:70 to 40:60,
The mixing ratio (by weight) of the methylene chloride-based organic solvent and the styrene foam or styrene resin is 70:30.

【0009】また、前記塩化メチレン系有機溶剤にて溶
解された発泡スチロール又はスチロール樹脂液中に投入
される古紙パルプ材は、水分略35パーセントとなるよ
うに予め脱水されていることを特徴とし、前記塩化メチ
レン系有機溶剤による発泡スチロール又はスチロール樹
脂の溶解は、水をいれた槽体中にて行なわれることを特
徴とし、前記溶解液中に投入された古紙パルプ材を攪拌
する際には、予め所定容量の水が投入されることを特徴
とするものである。
[0009] Further, the waste paper pulp material put into the styrene foam or styrene resin solution dissolved in the methylene chloride-based organic solvent is dehydrated in advance so as to have a water content of about 35%. Dissolution of the foamed styrene or styrene resin with the methylene chloride-based organic solvent is characterized in that it is carried out in a tank body filled with water. It is characterized in that a volume of water is charged.

【0010】[0010]

【発明の実施の形態】本発明の一実施の形態を図面を参
照して説明する。図1は発泡スチロール又はスチロール
樹脂(以下単にスチロール樹脂と称する)を塩化メチレ
ン系有機溶剤にて溶解した溶液中に古紙パルプ3が投入
され、ミキサー4にて攪拌する状態を説明するための概
念図である。また、図2は、前記攪拌された古紙パルプ
を金型5に収納し、プレス機6にてプレスして古紙パル
プ材の水分及び塩化メチレン系有機溶剤分を絞り出す
(除去する)状態を説明するための概念図である。以
下、説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a conceptual diagram illustrating a state in which waste paper pulp 3 is put into a solution in which styrene foam or a styrene resin (hereinafter, simply referred to as a styrene resin) is dissolved in a methylene chloride-based organic solvent, and is stirred by a mixer 4. is there. FIG. 2 illustrates a state in which the agitated waste paper pulp is stored in a mold 5 and pressed by a press machine 6 to squeeze (remove) water and methylene chloride-based organic solvent components of the waste paper pulp material. FIG. This will be described below.

【0011】この発明に係る人工木材及びその製造方法
においては、従来例と異なり、古紙材を、先ず、水の入
った古紙細断機(通称パルパー:図示せず)に投入して
攪拌し、細断する。これにより、古紙材を綿状の古紙パ
ルプとする。
In the artificial wood and the method for producing the same according to the present invention, unlike the conventional example, first, the used paper material is put into a used paper shredder (commonly called pulper: not shown) containing water and stirred. Shred. In this way, the used paper material is made into cotton-like used paper pulp.

【0012】次いで、この綿状の古紙パルプを脱水機
(図示せず)にて水分含有量が35パーセント程度とな
るように脱水する。この脱水工程はかならずしも必要な
ものではなく、脱水せずに次工程に進んでもよい。
Next, the flocculent waste paper pulp is dewatered by a dehydrator (not shown) so that the water content becomes about 35%. This dehydration step is not always necessary, and the process may proceed to the next step without dehydration.

【0013】前記工程とは別に、スチロール樹脂の塩化
メチレン系有機溶剤による溶解を行なう。本発明におけ
る塩化メチレン系有機溶剤としては、塩化メチレン,ト
リクロロエチレン,クロロホルム,四塩化炭素,テトラ
クロロエチレン(バークロロエチレン)等、及びこれら
の混合物が使用される。それぞれ、比重が1.3〜1.
6、沸点が40°〜120°程度であり取り扱いが容易
である。
Separately from the above steps, the styrene resin is dissolved with a methylene chloride-based organic solvent. As the methylene chloride-based organic solvent in the present invention, methylene chloride, trichloroethylene, chloroform, carbon tetrachloride, tetrachloroethylene (verchloroethylene), and the like, and a mixture thereof are used. Each has a specific gravity of 1.3 to 1.
6. It has a boiling point of about 40 ° to 120 ° and is easy to handle.

【0014】これらの塩化メチレン系有機溶剤と、スチ
ロール樹脂を槽体1に投入し、さらに水を投入してミキ
サー4にて十分に攪拌し、スチロール樹脂の溶解を行な
う。塩化メチレン系有機溶剤とスチロール樹脂分との混
合割合(重量)は略70:30程度にする。また、投入
される水は、浄水に限らず井戸水や工業用水等を使用す
ることもできる。水の比重は略1であり、溶剤の比重は
前記のように1.3〜1.6程度であるから、図1に示
すように溶液2の上部に水層5が形成される。この水層
5が槽体1中で溶剤成分の表面を密封し、その大気中へ
の放散を防ぎ、この作用により、密閉容器や密閉された
建物等の設備を不要とすることができ、また、槽体1の
設置場所を選ばす、環境へ悪影響を及ぼすこともなく、
作業も安全に行なうことができる。
The methylene chloride-based organic solvent and the styrene resin are charged into the tank 1, water is further charged, and the mixture is sufficiently stirred by the mixer 4 to dissolve the styrene resin. The mixing ratio (weight) of the methylene chloride-based organic solvent and the styrene resin component is set to about 70:30. The water to be supplied is not limited to purified water, but well water or industrial water can also be used. Since the specific gravity of water is approximately 1 and the specific gravity of the solvent is about 1.3 to 1.6 as described above, an aqueous layer 5 is formed on the solution 2 as shown in FIG. This water layer 5 seals the surface of the solvent component in the tank body 1 and prevents its emission into the atmosphere. By this action, it is possible to eliminate the need for equipment such as a closed container or a closed building. , Choosing the location of the tank body 1, without adversely affecting the environment,
Work can be done safely.

【0015】次いで、前記ミキサー4にて攪拌された溶
液中に、脱水された古紙パルプ3を投入し、同じくミキ
サー4にて十分に攪拌する。この実施の形態において
は、溶剤による樹脂分の溶解を行なう槽体1にそのまま
古紙パルプ3を投入するが、樹脂の溶解を行なう槽体
と、溶解された溶液へ古紙パルプを投入する槽体とを別
にするようにしてもよいのはもちろんである。
Next, the dewatered waste paper pulp 3 is put into the solution stirred by the mixer 4 and sufficiently stirred by the mixer 4. In this embodiment, the waste paper pulp 3 is directly charged into the tank body 1 for dissolving the resin component by the solvent, and a tank body for dissolving the resin and a tank body for charging the waste paper pulp to the dissolved solution. Of course, it may be made to be different.

【0016】スチロール樹脂と古紙パルプとの混合割合
(重量)は30:70から40:60程度の範囲であ
る。スチロール樹脂の割合が30というのは略限界であ
って、30以下になると、樹脂が古紙パルプの各繊維を
つなぐバインダーとしての役割が弱くなり、剛性のある
製品とならない。逆に、古紙パルプに対する樹脂分が多
くなると、樹脂としての性質が強くなり、「木材」とし
ての性質が失われる。このような点を勘案すると、樹脂
と古紙パルプとの混合割合(重量)は前記30:70か
ら40:60程度の範囲となる。
The mixing ratio (weight) of the styrene resin and the waste paper pulp is in the range of about 30:70 to 40:60. The ratio of the styrene resin is about 30 which is almost the limit. When the ratio is 30 or less, the role of the resin as a binder for connecting the fibers of the waste paper pulp is weakened, and a rigid product is not obtained. Conversely, when the resin content in the wastepaper pulp increases, the properties as a resin become stronger and the properties as "wood" are lost. In consideration of such points, the mixing ratio (weight) of the resin and the wastepaper pulp is in the range of about 30:70 to 40:60.

【0017】以上のような割合の樹脂分と古紙パルプと
が槽体1内にて所定時間、十分に繰り返し攪拌される。
これにより、古紙パルプの各繊維質の微細な孔等に含む
水分が溶剤によって分離され、樹脂分と入れ代わる。樹
脂分は、各繊維質をつなぐバインダーとなり、各繊維質
は樹脂により接続されて一体化する。このように、塩化
メチレン系有機溶剤によって溶解されたスチロール樹脂
は、古紙パルプの各繊維質の中で繊維分子構造的に強く
融着し、木材化が行われる。
The resin content and the waste paper pulp having the above ratios are sufficiently and repeatedly stirred in the tank 1 for a predetermined time.
As a result, the water contained in the fine pores of each fibrous material of the used paper pulp is separated by the solvent and replaces the resin component. The resin serves as a binder connecting the fibers, and the fibers are connected and integrated by the resin. As described above, the styrene resin dissolved by the methylene chloride-based organic solvent is strongly fused in a fiber molecular structure in each fiber of the waste paper pulp, and is converted into wood.

【0018】なお、この実施の形態では、前記投入され
る古紙パルプは、予め水分含有量35パーセントとなる
ように脱水されているが、前記のように古紙パルプに含
まれる水分は溶剤により分離されることから、脱水せず
にそのまま投入するようにしてもよい。
In this embodiment, the used waste paper pulp is previously dehydrated so as to have a water content of 35%, but the water contained in the waste paper pulp is separated by the solvent as described above. For this reason, it may be supplied as it is without dewatering.

【0019】前記十分に攪拌されたスチロール樹脂と古
紙パルプの混練体6は、所定形状の金型7に収納され、
プレス機8にてプレス成形される。このプレスにより、
スチロール樹脂と古紙パルプから有機溶剤と水分とが絞
りだされ、槽体9に回収される。槽体9の符号10は回
収された有機溶剤であり、再度、溶剤として使用され
る。比重の軽い水分11は溶剤10の上層に貯留する。
The kneaded body 6 of the sufficiently stirred styrene resin and waste paper pulp is stored in a mold 7 having a predetermined shape.
It is press-formed by a press machine 8. With this press,
The organic solvent and moisture are squeezed out of the styrene resin and the waste paper pulp and collected in the tank 9. Reference numeral 10 of the tank 9 is a recovered organic solvent, which is used again as a solvent. Water 11 having a low specific gravity is stored in the upper layer of the solvent 10.

【0020】前記プレス,成形された混練体6は、図示
しない加熱炉にて加熱,乾燥され、残る有機溶剤や水分
が除かれ、人工木材が完成する。なお、前記金型7とプ
レス機8によるプレスを加熱炉内で行い、プレス,形成
の後、直接に加熱,乾燥するようにしてもよい。
The pressed and formed kneaded body 6 is heated and dried in a heating furnace (not shown) to remove the remaining organic solvent and moisture, thereby completing artificial wood. Pressing by the mold 7 and the press machine 8 may be performed in a heating furnace, and after pressing and forming, heating and drying may be performed directly.

【0021】以上のような工程を経て製品化された人工
木材は、剛性は本来の木材と同程度であるが、重量が三
分の一と軽く、その加工性も本来の木材と同様であり、
たとえば釘打ちやカンナがけ、のこぎり引き等も天然の
木材と同様に可能である。また、着色性も良いという優
れた特質を備えている。
The artificial wood commercialized through the above process has the same rigidity as the original wood, but has a light weight of one third and its workability is the same as that of the original wood. ,
For example, nailing, canning, sawing, etc. are possible as well as natural wood. In addition, it has an excellent characteristic that coloring properties are good.

【0022】なお、別な実施の形態として、前記樹脂成
分として、ポリスチレンを所定割合にて混合すると、完
成した人工木材に弾力性を持たせることができる。
As another embodiment, when polystyrene is mixed at a predetermined ratio as the resin component, the finished artificial wood can have elasticity.

【0023】[0023]

【発明の効果】以上説明したように、本発明に係る古紙
材とスチロール樹脂からなる人工木材及びその製造方法
によれば、古紙材の使用割合が高いことから古紙材のリ
サイクルを促進することができ、また、重量的には木材
よりも軽いにもかかわらず木材同様の剛性と加工性があ
り、価格的にも安価に製造可能である古紙材とスチロー
ル樹脂による人工木材及びその製造方法を提供すること
ができる。また、有機溶剤の揮発等によって環境に悪影
響を与えることがなく、特別の密閉容器や密閉建物等の
施設が不要であり、安全に作業を行うことができる等の
優れた効果を奏する。
As described above, according to the artificial wood made of waste paper and styrene resin and the method for producing the same according to the present invention, it is possible to promote the recycling of waste paper because the usage ratio of waste paper is high. Provided is an artificial wood made of waste paper and styrene resin, which has the same rigidity and processability as wood even though it is lighter in weight than wood, and can be manufactured at a low cost, and a method of manufacturing the same. can do. In addition, there is no adverse effect on the environment due to volatilization of the organic solvent, and special facilities such as a closed container and a closed building are not required, and excellent effects such as safe operation can be obtained.

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

【図1】発泡スチロール又はスチロール樹脂を塩化メチ
レン系有機溶剤にて溶解した溶液中に投入された古紙パ
ルプ3をミキサー4にて攪拌する状態を説明するための
概念図である。
FIG. 1 is a conceptual diagram illustrating a state in which a used paper pulp 3 put in a solution in which styrene foam or a styrene resin is dissolved in a methylene chloride-based organic solvent is stirred by a mixer 4.

【図2】攪拌された古紙パルプを金型7に収納し、プレ
ス機8にてプレスして古紙パルプの水分及び塩化メチレ
ン系有機溶剤分を絞り出す状態を説明するための概念図
である。
FIG. 2 is a conceptual view for explaining a state in which agitated used paper pulp is stored in a mold 7 and pressed by a press machine 8 to squeeze out water and methylene chloride-based organic solvent content of the used paper pulp.

【符号の説明】[Explanation of symbols]

1 槽体 2 溶解液 3 古紙パルプ 4 ミキサー 5 水層 6 混練体 7 金型 8 プレス機 9 槽体 10 溶剤 11 水層 DESCRIPTION OF SYMBOLS 1 Tank body 2 Dissolution liquid 3 Waste paper pulp 4 Mixer 5 Water layer 6 Kneaded body 7 Mold 8 Press machine 9 Tank body 10 Solvent 11 Water layer

Claims (8)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 古紙裁断機に古紙材と水とを投入して撹
拌し、当該古紙材を裁断して古紙パルプ材とし、 発泡スチロール又はスチロール樹脂を塩化メチレン系有
機溶剤にて溶解して溶液とし、当該溶液中に前記古紙パ
ルプ材を投入して撹拌し、 この撹拌された古紙パルプ材を所定形状の型に収納し、
プレスして水分及び前記塩化メチレン系有機溶剤分を取
り除き、 この水分及び塩化メチレン系有機溶剤分等が取り除かれ
た古紙パルプ材とスチロール樹脂との混合物を乾燥して
形成したことを特徴とする古紙材とスチロール樹脂から
なる人工木材。
A waste paper material and water are put into a waste paper cutting machine and agitated, and the waste paper material is cut into a waste paper pulp material. The waste paper pulp material is put into the solution and stirred, and the stirred waste paper pulp material is stored in a mold having a predetermined shape,
A waste paper formed by pressing to remove moisture and the methylene chloride-based organic solvent component, and drying a mixture of the waste paper pulp material and the styrene resin from which the moisture and the methylene chloride-based organic solvent component have been removed; Artificial wood made of wood and styrene resin.
【請求項2】 前記発泡スチロール又はスチロール樹脂
と前記古紙パルプ材との混合割合(重量)は、30:7
0から40:60の範囲であることを特徴とする請求項
1記載の古紙材とスチロール樹脂からなる人工木材。
2. The mixing ratio (weight) of the expanded polystyrene or styrene resin to the waste paper pulp material is 30: 7.
The artificial wood made of waste paper and styrene resin according to claim 1, wherein the ratio is in the range of 0 to 40:60.
【請求項3】 古紙裁断機に古紙材と水とを投入して撹
拌し、当該古紙材を裁断して古紙パルプ材とし、 発泡スチロール又はスチロール樹脂を塩化メチレン系有
機溶剤にて溶解して得た溶液中に前記古紙パルプ材を投
入して撹拌し、 この撹拌された古紙パルプ材を所定形状の型に収納し、
プレスして水分及び前記塩化メチレン系有機溶剤分を除
去し、 この水分及び塩化メチレン系有機溶剤分等が除去された
古紙パルプ材とスチロール樹脂との混合物を乾燥して形
成することを特徴とする古紙材とスチロール樹脂からな
る人工木材の製造方法。
3. A waste paper material and water are put into a waste paper cutting machine and stirred, and the waste paper material is cut into a waste paper pulp material, and styrene foam or a styrene resin is dissolved in a methylene chloride-based organic solvent. The waste paper pulp material is put into the solution and stirred, and the stirred waste paper pulp material is stored in a mold having a predetermined shape,
Pressing to remove water and the methylene chloride-based organic solvent component, and drying and forming a mixture of the waste paper pulp material and the styrene resin from which the moisture and the methylene chloride-based organic solvent component have been removed. A method for producing artificial wood made of waste paper and styrene resin.
【請求項4】 前記発泡スチロール又はスチロール樹脂
と前記古紙パルプ材との混合割合(重量)は、30:7
0から40:60の範囲であることを特徴とする請求項
3記載の古紙材とスチロール樹脂からなる人工木材の製
造方法。
4. The mixing ratio (weight) of the expanded polystyrene or styrene resin to the waste paper pulp material is 30: 7.
4. The method of claim 3, wherein the ratio is in the range of 0 to 40:60.
【請求項5】 前記塩化メチレン系有機溶剤と、発泡ス
チロール又はスチロール樹脂との混合割合(重量)は7
0:30であることを特徴とする請求項3記載の古紙材
とスチロール樹脂からなる人工木材の製造方法。
5. The mixing ratio (weight) of the methylene chloride-based organic solvent to styrene foam or styrene resin is 7%.
The method for producing an artificial wood made of waste paper and styrene resin according to claim 3, wherein the ratio is 0:30.
【請求項6】 前記発泡スチロール又はスチロール樹脂
を塩化メチレン系有 機溶剤にて溶解して得た溶液中に投
入する古紙パルプ材は、水分含有量略35パーセント
となるように予め脱水されていることを特徴とする請求
項3記載の古紙材とスチロール樹脂からなる人工木材の
製造方法。
6. The styrene foam or styrene resin
Waste paper pulp material to be introduced into the solution obtained by dissolving in methylene chloride-based organic solvents, according to claim 3, wherein the water content is preliminarily dehydrated so as to be substantially 35% A method for producing artificial wood made of waste paper and styrene resin.
【請求項7】 発泡スチロール又はスチロール樹脂の前
記塩化メチレン系有機溶剤による溶解は、水を保有する
槽体中にて行うことを特徴とする請求項3記載の古紙材
とスチロール樹脂からなる人工木材の製造方法。
7. The artificial wood made of waste paper and styrene resin according to claim 3, wherein the dissolving of the styrene foam or the styrene resin with the methylene chloride-based organic solvent is performed in a tank holding water. Production method.
【請求項8】 前記溶液中に投入された古紙パルプ材を
撹拌する際には、予め所定容量の水が投入されることを
特徴とする請求項3記載の古紙材とスチロール樹脂から
なる人工木材の製造方法。
8. The artificial wood made of waste paper and styrene resin according to claim 3, wherein a predetermined volume of water is introduced before stirring the waste paper pulp put into the solution. Manufacturing method.
JP25895598A 1998-09-11 1998-09-11 Artificial wood made of waste paper and styrene resin and method for producing the same Expired - Fee Related JP3156127B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25895598A JP3156127B2 (en) 1998-09-11 1998-09-11 Artificial wood made of waste paper and styrene resin and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25895598A JP3156127B2 (en) 1998-09-11 1998-09-11 Artificial wood made of waste paper and styrene resin and method for producing the same

Publications (2)

Publication Number Publication Date
JP2000084909A JP2000084909A (en) 2000-03-28
JP3156127B2 true JP3156127B2 (en) 2001-04-16

Family

ID=17327356

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25895598A Expired - Fee Related JP3156127B2 (en) 1998-09-11 1998-09-11 Artificial wood made of waste paper and styrene resin and method for producing the same

Country Status (1)

Country Link
JP (1) JP3156127B2 (en)

Also Published As

Publication number Publication date
JP2000084909A (en) 2000-03-28

Similar Documents

Publication Publication Date Title
CN103088695A (en) Device and method for producing cardboard paper by utilizing paper mill sludge and waste paper
DK93494A (en) Washing, cleaning, disinfecting and / or preservative-containing recycling containers
CA2058540A1 (en) Method for reprocessing thermoplast-coated packing materials and thermoplast material for further processing
JP2009274318A (en) Resin for injection molding and method for manufacturing resin for injection molding
JP3156127B2 (en) Artificial wood made of waste paper and styrene resin and method for producing the same
WO1994006854A1 (en) Method of and apparatus for regenerating waste polyvinyl chloride
CA2153981A1 (en) A method to separate the cellulose based fibers in straw from each other and a moulding composition for plastic forming of cellulose containing fiber products
JP4064327B2 (en) Foamed concrete and method for producing the same
KR950006534B1 (en) Method of producing paper-vessel
JPH0671647A (en) Method for recycling waste
CN109054316A (en) Ecological environment-friendly packaging material and preparation method thereof
CN113652096A (en) Manufacturing method of disposable tableware based on crop straws
GB2109023A (en) Recycling of paper and other materials
CN105860556A (en) Packaging material and forming method thereof, package and package forming mould and special package for oil filter
GB2395162A (en) A method of producing moulded products from waste paper`
JP3826180B2 (en) Non-combustible heating element artificial wood and method for producing the same
KR100917856B1 (en) Reproducing method of wast e.p.s
KR970070338A (en) Method of manufacturing sheet material using waste products
JPH11140800A (en) Production of molding product of reinforced pulp material
JP2001340839A (en) Method and apparatus for treating industrial waste
JPH06218732A (en) Insulation board for rush-mat floor/and its production
JP2002105468A (en) Solid fuel and its manufacturing method
JPS6023489A (en) Production of solid fuel composed mainly of waste substance generated in regeneration of waste paper
JP2006089862A (en) Method for producing paper plastic molded product of non-paper pulp plant fiber
KR101784966B1 (en) Method of processing waste paper to a cotton type

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090209

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090209

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100209

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees