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JPS6337683B2 - - Google Patents
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JPS6337683B2 - - Google Patents

Info

Publication number
JPS6337683B2
JPS6337683B2 JP59024909A JP2490984A JPS6337683B2 JP S6337683 B2 JPS6337683 B2 JP S6337683B2 JP 59024909 A JP59024909 A JP 59024909A JP 2490984 A JP2490984 A JP 2490984A JP S6337683 B2 JPS6337683 B2 JP S6337683B2
Authority
JP
Japan
Prior art keywords
thermoplastic resin
weight
parts
mixer
facing material
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
Application number
JP59024909A
Other languages
Japanese (ja)
Other versions
JPS60168611A (en
Inventor
Sadao Moryama
Yutaka Kanekawa
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.)
HAISHIITO KOGYO KK
IKEDA BUTSUSAN KK
Original Assignee
HAISHIITO KOGYO KK
IKEDA BUTSUSAN KK
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 HAISHIITO KOGYO KK, IKEDA BUTSUSAN KK filed Critical HAISHIITO KOGYO KK
Priority to JP59024909A priority Critical patent/JPS60168611A/en
Publication of JPS60168611A publication Critical patent/JPS60168611A/en
Publication of JPS6337683B2 publication Critical patent/JPS6337683B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/0026Recovery of plastics or other constituents of waste material containing plastics by agglomeration or compacting
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Paper (AREA)
  • Processing Of Solid Wastes (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は表装材及び段ボール基材からなる端破
材を用いた複合材組成物の製造方法に関し、更に
詳細に説明すると、車両用内装品として用いられ
る表装材と段ボール基材とからなる各種内装品を
製造する際に発生する端破材を複合材組成物の製
造方法に関する。 従来、車両用内装品を製造する場合には、多量
の端破材が発生し、これらを廃棄する場合には廃
棄処理費用が増大し製品コストを増大させる原因
となつている。また端破材を再生使用し、省資源
に役立てる事も行なわれているが、従来の段ボー
ル天井等にあつては表装材に塩化ビニル樹脂とウ
レタンフオーム等の積層品を用いるものが多く、
塩化ビニル樹脂が再生使用時に熱分解して解素ガ
スを発生させ、またウレタンフオームも熱分解に
よりガスを発生させるので、これらの塩素ガスを
始めとする分解ガスが成形機のシリンダー等を腐
蝕させると共に作業環境の悪化及び分解ガスが組
成物に混入して物性劣化を生じさせる虞れを有し
ていた。従つて段ボール天井等の内装品は表装材
と段ボール基材を分離して段ボール基材のみを再
生利用しており、端破材の分離は大巾な工数増加
となりコストメリツトを損ない廃棄処理しなけれ
ばならず、省資源化に逆行するものであつた。 本発明の目的は表装材と段ボール基材からなる
端破材を表装材と段ボール基材に予じめ分離させ
る事なく、同時に再生使用する事が出来、この際
有害な塩素ガスを始めとする各種の分解ガスが成
形機等を腐蝕させたり、作業環境を悪化させる事
がなく、物性においても優れ、また添加する熱可
塑性樹脂の使用量を減少させる事の出来る著しく
経済性に優れた表装材及び段ボール基材からなる
端破材を用いた複合材組成物の製造方法を提供す
るものである。 以下本発明に係る製造方法の一実施例を詳述す
る。 本発明に用いられる表装材はポリプロピレン樹
脂PP、またはポリエチレン樹脂PE等の熱可塑性
樹脂とオレフイン系エラストマー及び発泡PPま
たは発泡PEフオームの積層品からなり、特に塩
化ビニル樹脂、塩ビ酢酸ビニル樹脂の如き塩素系
ビニル樹脂を含まないものである。 表装材が積層される段ボール基材は通常の段ボ
ール基材の他熱可塑性樹脂によりコーテイングし
たものであつてもよい。 前記構成の表装材と段ボール基材からなる端破
材を粉砕して粗砕片を形成する。この粗砕片に熱
可塑性樹脂と水とを添加し、加熱ミキサーに収納
し、密閉状態で撹拌し、前記粗砕片の段ボール成
分を蒸気圧と撹拌により解繊し、熱可塑性樹脂成
分を可塑化する。次いで加熱ミキサー内の水蒸気
を含む発生ガスをミキサーより徐々に排出し、更
に撹拌を継続して温度を上昇させ熱可塑性樹脂成
分を溶融し、解繊されたパルプ繊維に熱可塑性樹
脂を均一に含浸させ溶融混合物を形成する。次に
溶融混合物を常温のミキサー内に移して熱可塑性
樹脂量の調整を行ない均一な造粒物を形成し、こ
の造粒物を成形加工して複合材組成物を製造す
る。 実施例 表装材35重量%、段ボール基材65重量%程度の
端破材を1〜8mmに粉砕して粗砕片を形成する。
前記表装材はPP樹脂とオレフイン系エラストマ
ーから形成されている。この粗砕片100重量部に
対して30〜50重量部の熱可塑性樹脂と、3〜10重
量部の水を添加して加熱ミキサーに収納する。前
記添加する熱可塑性樹脂は塩素系ビニル樹脂を含
まない。また加熱ミキサーは発生ガスの除去のた
めのブロアー装置を備えている。 加熱ミキサーに粗砕片、熱可塑性樹脂及び水を
収納し、密閉状態で加熱ミキサーを回転駆動させ
る。加熱ミキサーを500〜800rpmで回転駆動させ
ると、原材料が高速撹拌され、原材料が摩擦熱に
より温度上昇し、ミキサー内部の温度が120〜150
℃に上昇する。この温度範囲で12〜18分間維持す
ると、あらかじめ原材料として添加した水が水蒸
気となり、かつ密閉状態でミキサーが回転駆動し
ているので粗砕片の段ボール成分が蒸気圧(2〜
3Kg/cm2)と撹拌による叩解により解繊し、パル
プ繊維となる。またパルプ繊維中のリグニンが溶
出すると共に、表装材成分、即ち熱可塑性樹脂及
び添加した熱可塑性樹脂が可塑化する。 次いで付属のブロアー装置を作動させて徐々に
水蒸気及び発生ガスを外部に除去する。水蒸気等
の発生ガスが除去されるに従い、ミキサー内部の
温度は摩擦熱により上昇し、3〜5分間で150〜
200℃に上昇する。ミキサー内部の温度が150℃以
上になるとPP樹脂は溶融を始め叩解により解繊
したパルプ繊維に熱可塑性樹脂が均一にとりかこ
む状態、一般的に樹脂にぬれる状態となる。完全
に発生ガスを除去するとミキサー内部の温度は
200〜205℃となつている。従つてパルプ繊維と溶
融した熱可塑性樹脂とからなる溶融混合物が得ら
れる。 次に溶融混合物を加熱ミキサーから取出し、常
温のミキサーに収納し、熱可塑性樹脂量の調整を
行なう。熱可塑性樹脂が少ない場合には適宜量、
例えば15〜30重量部のPP樹脂またはPE樹脂をミ
キサーに添加し、200〜500rpmで撹拌しながら均
一な造粒物を形成する。 得られた造粒物を好ましくはガス抜き装置を備
えた押出機またはインジエクシヨンマシンで成形
加工して複合材組成物を製造する。 前述せる複合材組成物の製造方法により製造し
た再生圧縮ボードの物性試験結果を従来の再生圧
縮ボードと比較して表―1に示す。
The present invention relates to a method for producing a composite composition using scrap materials consisting of a facing material and a corrugated cardboard base material, and more specifically, the present invention relates to a method for manufacturing a composite material composition using scrap materials consisting of a facing material and a corrugated cardboard base material, and more specifically, it relates to a method for manufacturing a composite material composition using a scrap material made of a facing material and a corrugated cardboard base material. The present invention relates to a method for producing a composite material composition using scraps generated during the production of products. Conventionally, when manufacturing vehicle interior parts, a large amount of scrap materials are generated, and when these scraps are disposed of, the disposal costs increase, causing an increase in product costs. In addition, waste materials are recycled and used to help conserve resources, but in the case of conventional corrugated ceilings, many of the covering materials are made of laminated products such as vinyl chloride resin and urethane foam.
Vinyl chloride resin thermally decomposes during recycling and generates decomposed gas, and urethane foam also generates gas through thermal decomposition, so these decomposed gases including chlorine gas corrode the cylinders of molding machines, etc. At the same time, there was a risk that the working environment would deteriorate and decomposition gas would mix into the composition, causing deterioration of physical properties. Therefore, for interior products such as corrugated ceilings, the facing material and the corrugated base material are separated and only the corrugated base material is recycled. Separating the scraps greatly increases the number of man-hours, which impairs cost benefits and must be disposed of. Naturally, this went against the grain of resource conservation. The object of the present invention is to be able to simultaneously recycle and reuse waste material consisting of a facing material and a corrugated board base material without having to separate them into the facing material and the corrugated board base material in advance. A surface material that is extremely economical because various decomposed gases do not corrode molding machines, etc. or worsen the working environment, and it has excellent physical properties and can reduce the amount of added thermoplastic resin used. The present invention also provides a method for producing a composite composition using scrap material made of a corrugated cardboard base material. An embodiment of the manufacturing method according to the present invention will be described in detail below. The facing material used in the present invention is composed of a laminate of a thermoplastic resin such as polypropylene resin PP or polyethylene resin PE, an olefin elastomer, and foamed PP or foamed PE foam. It does not contain vinyl resin. The corrugated board base material on which the facing material is laminated may be a normal corrugated board base material or one coated with a thermoplastic resin. The scrap material consisting of the facing material and the corrugated cardboard base material having the above structure is crushed to form coarse pieces. A thermoplastic resin and water are added to the coarsely crushed pieces, and the mixture is placed in a heating mixer and stirred in a closed state.The cardboard component of the coarsely crushed pieces is defibrated by steam pressure and stirring, and the thermoplastic resin component is plasticized. . Next, the generated gas containing water vapor in the heating mixer is gradually discharged from the mixer, and stirring is continued to raise the temperature to melt the thermoplastic resin component and uniformly impregnate the defibrated pulp fibers with the thermoplastic resin. to form a molten mixture. Next, the molten mixture is transferred into a mixer at room temperature to adjust the amount of thermoplastic resin to form uniform granules, and the granules are molded to produce a composite composition. Example A scrap material containing approximately 35% by weight of the facing material and 65% by weight of the corrugated board base material is crushed into pieces of 1 to 8 mm to form coarse pieces.
The covering material is made of PP resin and olefin elastomer. 30 to 50 parts by weight of thermoplastic resin and 3 to 10 parts by weight of water are added to 100 parts by weight of the crushed pieces, and the mixture is stored in a heating mixer. The thermoplastic resin added does not contain chlorinated vinyl resin. The heating mixer is also equipped with a blower device for removing generated gas. The crushed pieces, thermoplastic resin, and water are placed in a heating mixer, and the heating mixer is rotated in a closed state. When the heating mixer is driven to rotate at 500 to 800 rpm, the raw materials are stirred at high speed, the temperature of the raw materials increases due to frictional heat, and the temperature inside the mixer increases to 120 to 150 rpm.
rises to ℃. When maintained in this temperature range for 12 to 18 minutes, the water added in advance as a raw material turns into steam, and since the mixer is rotating in a closed state, the cardboard components of the coarse pieces are heated to a vapor pressure of 2 to 18 minutes.
3Kg/cm 2 ) and is defibrated by beating with stirring to become pulp fibers. Further, as the lignin in the pulp fibers is eluted, the facing material components, that is, the thermoplastic resin and the added thermoplastic resin are plasticized. Next, the attached blower device is operated to gradually remove water vapor and generated gas to the outside. As generated gases such as water vapor are removed, the temperature inside the mixer rises due to frictional heat, and the temperature rises to 150 - 150 in 3 to 5 minutes.
The temperature rises to 200℃. When the temperature inside the mixer reaches 150°C or higher, the PP resin begins to melt and the thermoplastic resin uniformly surrounds the pulp fibers defibrated by beating, generally becoming wet with the resin. When the generated gas is completely removed, the temperature inside the mixer will be
The temperature is 200-205℃. A molten mixture of pulp fibers and molten thermoplastic resin is thus obtained. Next, the molten mixture is taken out from the heating mixer and placed in a mixer at room temperature, and the amount of thermoplastic resin is adjusted. If the amount of thermoplastic resin is small, add an appropriate amount.
For example, add 15 to 30 parts by weight of PP resin or PE resin to a mixer and form uniform granules while stirring at 200 to 500 rpm. The resulting granules are preferably molded using an extruder or injection machine equipped with a degassing device to produce a composite composition. Table 1 shows the physical property test results of the recycled compressed board manufactured by the method for manufacturing the composite composition described above, in comparison with the conventional recycled compressed board.

【表】 表―1中、比較例1は実施例1と同様の粗砕片
を用いて従来方法により製造した再生圧縮ボード
であり、比較例2は表装材成分に塩化ビニル樹脂
を含むものであり、比較例3は市販の一般的な再
生圧縮ボードである。 上記物性の耐衝撃性、成形ボードの樹脂のねば
り等の物性の良さは明らかであり、物性向上の要
因は水を添加して一定時間に発生する蒸気による
段ボールの叩解、解繊が十分に促進され、かつ樹
脂中に均一に分散配置されている事がわかる。 端破材の再生利用の状態を比較例と共に表―2
に示す。
[Table] In Table 1, Comparative Example 1 is a recycled compressed board manufactured by a conventional method using the same crushed pieces as in Example 1, and Comparative Example 2 is a board that contains vinyl chloride resin as a facing material component. , Comparative Example 3 is a commercially available general recycled compression board. It is clear that the physical properties mentioned above are good, such as the impact resistance and the stickiness of the resin of the molded board, and the reason for the improvement in physical properties is that the beating and defibration of the cardboard is sufficiently promoted by the steam generated over a certain period of time when water is added. It can be seen that the particles are dispersed uniformly in the resin. Table 2 shows the state of recycling of scrap materials along with comparative examples.
Shown below.

【表】 表―2に示す如く、本発明方法によれば、樹脂
添加量が30〜40部と最も少なく、原材料費が大巾
に削減出来経済性に優れている。
[Table] As shown in Table 2, according to the method of the present invention, the amount of resin added is the smallest at 30 to 40 parts, and the cost of raw materials can be greatly reduced, resulting in excellent economic efficiency.

Claims (1)

【特許請求の範囲】[Claims] 1 塩素系ビニル樹脂を含まない熱可塑性樹脂か
らなる表装材と、該表装材に接合された段ボール
基材とからなる端破材を粉砕して粗砕片を形成
し、ブロアー装置を備える加熱ミキサーに前記粗
砕片と、前記粗砕片100重量部に対して、30〜50
重量部の熱可塑性樹脂と、3〜10重量部の水を添
加し、密閉状態で120〜150℃の温度範囲で撹拌
し、粗砕片の段ボール成分を前記添加した水によ
る蒸気圧と撹拌により解繊し、表装材成分を可塑
化し、次いで前記ブロアー装置を作動させて水蒸
気を含む発生ガスをミキサーより徐々に排出し、
撹拌を継続して熱可塑性樹脂成分を溶融し、解繊
されたパルプ繊維に熱可塑性樹脂を均一に含浸さ
せた溶融混合物を形成し、次いで、溶融混合物を
常温のミキサー内に移して熱可塑性樹脂量の調整
のなされた均一な造粒物を形成し、該造粒物を成
形加工して複合材組成物を製造する事を特徴とす
る表装材及び段ボール基材からなる端破材を用い
た複合材組成物の製造方法。
1. Crushed scraps consisting of a facing material made of a thermoplastic resin that does not contain chlorinated vinyl resin and a corrugated cardboard base material joined to the facing material are crushed to form coarse pieces, and then put into a heating mixer equipped with a blower device. 30 to 50 parts by weight of the coarsely crushed pieces and 100 parts by weight of the coarsely crushed pieces
Parts by weight of thermoplastic resin and 3 to 10 parts by weight of water are added and stirred in a sealed state at a temperature range of 120 to 150°C, and the cardboard components of the coarsely crushed pieces are dissolved by the steam pressure and stirring caused by the added water. fiber, plasticize the facing material components, and then operate the blower device to gradually discharge the generated gas containing water vapor from the mixer,
Continue stirring to melt the thermoplastic resin component to form a molten mixture in which the defibrated pulp fibers are uniformly impregnated with the thermoplastic resin, and then transfer the molten mixture into a mixer at room temperature to melt the thermoplastic resin. Using scrap material consisting of a facing material and a corrugated cardboard base material, which is characterized by forming uniform granules with controlled amounts and molding the granules to produce a composite composition. Method of manufacturing a composite composition.
JP59024909A 1984-02-13 1984-02-13 Manufacture of composition of composite material making use of scrap material consisting of binding material and card board base material Granted JPS60168611A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59024909A JPS60168611A (en) 1984-02-13 1984-02-13 Manufacture of composition of composite material making use of scrap material consisting of binding material and card board base material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59024909A JPS60168611A (en) 1984-02-13 1984-02-13 Manufacture of composition of composite material making use of scrap material consisting of binding material and card board base material

Publications (2)

Publication Number Publication Date
JPS60168611A JPS60168611A (en) 1985-09-02
JPS6337683B2 true JPS6337683B2 (en) 1988-07-26

Family

ID=12151300

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59024909A Granted JPS60168611A (en) 1984-02-13 1984-02-13 Manufacture of composition of composite material making use of scrap material consisting of binding material and card board base material

Country Status (1)

Country Link
JP (1) JPS60168611A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0633109A1 (en) * 1993-07-08 1995-01-11 Kampffmeyer, Gerhard Moulded part and its manufacturing process
US5973035A (en) * 1997-10-31 1999-10-26 Xyleco, Inc. Cellulosic fiber composites
EP1762145B1 (en) * 1999-06-22 2007-09-12 Xyleco, Inc. Texturized cellulosic and lignocellulosic materials and compositions and composites made therefrom

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5621577A (en) * 1979-07-31 1981-02-28 Kosaku Taga Paste product stuffed with rice cake or boiled rice and its production

Also Published As

Publication number Publication date
JPS60168611A (en) 1985-09-02

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