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JPH0347286B2 - - Google Patents
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JPH0347286B2 - - Google Patents

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Publication number
JPH0347286B2
JPH0347286B2 JP17693985A JP17693985A JPH0347286B2 JP H0347286 B2 JPH0347286 B2 JP H0347286B2 JP 17693985 A JP17693985 A JP 17693985A JP 17693985 A JP17693985 A JP 17693985A JP H0347286 B2 JPH0347286 B2 JP H0347286B2
Authority
JP
Japan
Prior art keywords
rgp
cellulose
modified
weight
unsaturated carboxylic
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
JP17693985A
Other languages
Japanese (ja)
Other versions
JPS6239656A (en
Inventor
Nobuo Shiraishi
Hideo Ookawa
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.)
Calp Kogyo KK
Original Assignee
Calp Kogyo 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 Calp Kogyo KK filed Critical Calp Kogyo KK
Priority to JP17693985A priority Critical patent/JPS6239656A/en
Publication of JPS6239656A publication Critical patent/JPS6239656A/en
Publication of JPH0347286B2 publication Critical patent/JPH0347286B2/ja
Granted legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Other Resins Obtained By Reactions Not Involving Carbon-To-Carbon Unsaturated Bonds (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

〔産業䞊の利甚分野〕 本発明は新芏グラフト䜓の補造方法に関し、詳
しくはセルロヌス系材料ず倉性ポリオレフむンず
からなる暹脂成圢品の機械的匷床、衚面平滑性、
衚面光沢性を向䞊させるずずもに暹脂成圢品に透
明性を付䞎する新芏グラフト䜓の補造方法に関す
る。 〔埓来技術及び発明が解決しようずする問題点〕 朚材、パルプ等のセルロヌス系材料は熱可塑化
が困難であり、それのみではボヌド、シヌトなど
ぞの熱圧成圢を行なうこずが困難であ぀た。埓぀
お、朚材粉末等は蟲業資材、充填材などの付加䟡
倀の䜎い分野での利甚に限られ、はなはだしくは
党く利甚されるこずなく焌华されおいるのが珟状
である。 そこで、このようなセルロヌス系材料の高床利
甚に぀いお皮々の怜蚎が進められおいる。䟋えば
熱可塑性暹脂ず朚粉を溶融混緎した成圢材料が知
えられおいるが、分散性、盞溶性、接着性が十分
でない。埓぀お、機械的匷床、衚面平滑性、衚面
光沢性の点で十分なものが埗られおいなか぀た。 本発明は以䞊の問題点を解消し、さらに暹脂成
圢品に優れた透明性を付䞎する新芏グラフト䜓の
補造方法を提䟛するものである。 〔問題点を解決するための手段〕 すなわち本発明は、少なくずもセルロヌスを含
むセルロヌス系材料(A)成分に、䞍飜和カルボ
ン酞たたはその誘導䜓で倉性した倉性ポリオレフ
むン(B)成分をグラフトさせるこずを特城ずす
る新芏グラフト䜓の補造方法を提䟛するものであ
る。 本発明においお少なくずもセルロヌスを含む、
セルロヌス系材料にはセルロヌスのみからなる有
機繊維やセルロヌスの他に他の成分を含有する有
機繊維が含たれる。䟋えばセルロヌス系繊維、リ
グノセルロヌス系繊維などがあり、具䜓的には朚
材パルプ、リフアむナヌ、グランド・パルプ
RGP、補玙パルプ、故玙、粉砕凊理した朚片、
朚粉、果実穀粉、各皮セルロヌスを䟋瀺するこず
ができる。このように本発明におけるセルロヌス
系材料の圢状は特に限定はなく、繊維状、粒状、
粉状等のセルロヌス系材料を䜿甚するこずができ
る。たた、必芁に応じお朚材パルプ、故玙等を粉
砕したものを䜿甚するこずもできる。 ここで朚粉ずしおは束、モミ、ポプラ、゚ゟ束
等の粉砕品や鋞屑、カンナ屑があり、果実穀粉ず
しおはクルミ、ピヌナツツ、ダシ等の果実の粉砕
品がある。たた、各皮セルロヌスずしお朚材パル
プをアルカリ凊理し、機械的に现断したアルフア
繊維フロツクや綿実から埗られるコツトンリンタ
ヌ、コツトンフロツク、人絹を现断した人絹フロ
ツク等がある。これらの䞭でも特にRGPや朚粉
を甚いるこずが奜たしい。なお、朚粉を甚いる堎
合にはできるだけ埮粉化しお繊維同士のからみ合
いをなくしたものが奜たしいが、䜜業の煩雑さ、
経枈性等を考慮するず、通垞20〜400メツシナ皋
床のものが甚いられる。たた、RGPを甚いる堎
合にも脱むオン氎で撹拌凊理しお繊維同士のから
みをほぐしたものを甚いるこずが奜たしい。 なお、本発明においおはセルロヌスは郚分的に
化孊倉性されたものであ぀おもよく、たずえばア
セチル化、ラりロむル化等の䜎玚たたは高玚脂肪
酞による゚ステル化゚チル化、プロピル化、ア
リル化、ベンゞル化、カルボキシル化、ヒドロキ
シル゚チル化等の゚ヌテル化クロル化、ブロム
化のようなハロゲン化等の方法で倉性されたもの
であ぀おもよい。 次に、本発明においおは(B)成分ずしお、ポリオ
レフむンを䞍飜和カルボン酞たたはその誘導䜓で
倉性した倉性ポリオレフむンを甚いる。 倉性ポリオレフむンずしおは、たずえば、 (a)ポリオレフむンず暹脂ず䞍飜和カルボン酞た
たはその誘導䜓ず、ラゞカル発生剀ずを溶媒の存
圚䞋たたは䞍存圚䞋に加熱混合するこずにより埗
られるもの、(b)ポリオレフむン暹脂に䞍飜和カル
ボン酞たたはその誘導䜓ず゚ラストマヌずラゞカ
ル発生剀ずを溶媒の存圚䞋たたは䞍存圚䞋で加熱
混合しお埗たもの等を挙げるこずができる。この
発明においおは、前蚘各皮の倉性ポリオレフむン
のいずれにおいおも䞍飜和カルボン酞たたはその
誘導䜓の付加量は0.1〜14重量、特に0.5〜10重
量が奜たしい。 前蚘倉性ポリオレフむンの原料ずなるポリオレ
フむン暹脂ずしおは劂䜕なるものであ぀おも良
く、たずえば䜎密床ポリ゚チレン、䞭密床ポリ゚
チレン、高密床ポリ゚チレン、ポリプロピレン、
ポリブテン、ポリ−−メチルペンテン−等の
モノオレフむンポリマヌあるいぱチレン−プロ
ピレンコポリマヌたたはこれらのポリマヌ混合物
等が奜適に挙げられる。 前蚘゚ラストマヌはゞ゚ンモノマヌを䞻成分ず
する数平均分子量500〜10000の重合䜓で、宀枩で
流動性を瀺すものが奜たしい。このような䟋ずし
お、たずえば分子内にカルボキシル基、氎酞基、
メルカプト基、ハロゲン原子、アミノ基、アゞリ
ゞノ基、゚ポキシ基等の官胜基を有する−
ポリブタゞ゚ン、−ポリブタゞ゚ン、ポリ
む゜プレン、ポリクロロプレン、−ポリペ
ンタゞ゚ン、スチレン−ブタゞ゚ンコポリマヌ、
アクリロニトリル−ブタゞ゚ンコポリマヌ、ブタ
ゞ゚ン−む゜プレンコポリマヌ、プタゞ゚ン−ペ
ンタゞ゚ンコポリマヌのような゚ラストマヌや末
端ヒドロキシル化−ポリブタゞ゚ン、
−ポリブタゞ゚ン等の䞍飜和カルボン酞半゚ス
テル化物あるいは官胜基を有しない数平均分子量
500〜10000の−ポリブタゞ゚ン、−
ポリブタゞ゚ン、スチレン−ブタゞ゚ンコポリマ
ヌ、アクリロニトリル−ブタゞ゚ンコポリマヌ等
たたは熱分解ゎム、オゟン分解ゎム等、さらには
以䞊に挙げた゚ラストマヌの混合物等が挙げられ
る。 前蚘䞍飜和カルボン酞たたはその誘導䜓ずしお
は、たずえばマレむン酞、無氎ナゞツク酞、むタ
コン酞、シトラコン酞、クロトン酞、む゜クロト
ン酞、メサコン酞、アンゲリカ酞、゜ルビン酞、
アクリル酞、無氎マレむン酞、無氎むタコン酞、
無氎シトラコン酞等が奜たしく、特に無氎マレむ
ン酞が奜たしい。たた、前蚘䞍飜和カルボン酞の
誘導䜓ずしおは、前蚘䞍飜和カルボン酞の金属
塩、アミド、むミド、゚ステル等を䜿甚するこず
ができる。なお、この倉性ポリオレフむンに䜿甚
する前蚘䞍飜和カルボン酞およびその誘導䜓には
前蚘したものの䞭の皮あるいは皮以䞊を䜿甚
するこずができる。 前蚘ラゞカル発生剀は、ポリオレフむン暹脂ず
必芁に応じお配合された゚ラストマヌず䞍飜和カ
ルボン酞たたはその誘導䜓ずの反応を促進するも
のであれば良く、たずえば、ベンゟむルパヌオキ
シド、ラりリルパヌオキシド、アゟビスむ゜ブチ
ロニトリル、クメンパヌオキシド、αα′−ビス
−ブチルパヌオキシゞむ゜プロピルベンれ
ン、ゞ−−ブチルパヌオキシド、−ゞ
−ブチルパヌオキシヘキサン等を奜適に䜿
甚するこずができる。 このような各皮の倉性ポリオレフむンの䞭で
も、特にメルトむンデツクス以䞋、MIず略す
る。が0.5〜20010分のポリ゚チレンおよ
びたたはポリプロピレンず無氎マレむン酞ず末
端ヒドロキシル化ポリブタゞ゚ンずをキシレン、
トル゚ン、ヘプタン、モノクロルベンれン等の溶
媒䞭でベンゟむルパヌオキシド等のラゞカル発生
剀を䜿甚しお反応するこずにより埗られるずころ
の、無氎マレむン酞を0.5〜10重量付加した暹
脂が奜適である。 䞊蚘(A)成分ず(B)成分の配合割合は(A)成分10〜95
重量、奜たしくは15〜90重量に察しお(B)成分
〜90重量、奜たしくは10〜85重量である。
ここで(A)成分が95重量を超えるず剛性が䜎䞋す
るので奜たしくない。たた、(A)成分が10重量未
満であるず匷床、透明性、光沢性が䜎䞋するので
奜たしくない。 本発明で目的ずする新芏グラフト䜓は䞊述の成
分を混緎し、グラフトさせお埗られるものであ
る。すなわち、䞊述の成分を混緎するこずによ
り、セルロヌスの氎酞基ず倉性ポリオレフむン暹
脂のカルボキシル基ずの゚ステル結合によるグラ
フト化反応を生ぜしめる。ここで混緎は埓来公知
の方法、䟋えばバンバリミキサヌ、ヘンシ゚ルミ
キサヌ等の混合機やニヌダヌ、各皮抌出機などを
甚いお行なえばよい。たた、混緎は溶媒䞭で行な
぀おもよい。いずれにしおも適床の加熱䞋におい
お行なうこずが奜たしい。なお、混緎は䟋えばニ
ヌダヌ、バンバリヌミキサヌの堎合140〜200℃、
奜たしくは150〜190℃の枩床にお10〜30分間、奜
たしくは15〜20分間行なう。たた、この際のニヌ
ダヌ等の回転数は通垞50〜200rpm、奜たしくは
70〜150rpmである。混緎する際、必芁に応じお
該グラフト化反応を増進させる觊媒を添加するこ
ずができる。該觊媒ずしおはたずえばアルカリ金
属たたはアルカリ土類金属の炭酞塩、酞化物、氎
酞化物、カルボン酞塩あるいは−ゞメチル
ベンゞルアミン、トリ゚チルアミン等のアミン系
化合物、ピリゞン、ゞメチルアニリン等を觊媒ず
しお加えるこずができる。 本発明で目的ずする新芏グラフト䜓は、このよ
うに少なくずもセルロヌスを含むセルロヌス系材
料に䞍飜和カルボン酞たたはその誘導䜓で倉性し
た倉性ポルオレフむンをグラフトさせおなるもの
であり、この倉性ポリオレフむンをグラフトさせ
る割合は特に制限はないが、通垞重量以䞊、
奜たしくは重量以䞊である。 グラフトさせる割合が䜎いずセルロヌス系材料
の熱可塑性および熱可塑性暹脂ずの分散性、盞溶
性が䞍十分ずなり奜たしくない。 このようにしお埗られた新芏グラフト䜓を含む
暹脂組成物を加圧成圢、フむルム成圢、抌出成
圢、射出成圢等の手段によ぀お適宜圢状に成圢し
お各皮成圢品を補造するこずができる。 〔発明の効果〕 本発明の方法により埗られる新芏グラフト䜓を
含む暹脂組生物の成圢品は機械的匷床が著しく優
れたものであり、さらに優れた透明性、平滑性、
光沢性を有しおいる。 したが぀お、本発明の方法により埗られる新芏
グラフト䜓を含む成圢品はフむルムやシヌト材
料、家具、建材衚面仕䞊げ材、構造材、自動
車、家電のハりゞング、内装材、音響郚材等の玠
材ずしお有効に甚いられる。 〔実斜䟋〕 以䞋、本発明を実斜䟋等により詳现に説明す
る。 調補䟋  RGPの調補 ニナヌゞヌランド産ラゞアヌタパむンず脱氎む
オン氎を家電ミキサヌ䞭で分間撹拌凊理し、繊
維のからみをほぐした埌、濟集しおメタノヌル、
次いで゚ヌテルで掗浄し、也燥させるこずにより
RGPを埗た。 調補䟋  アセチル化RGPの調補 調補䟋にお埗られたRGPを酢酞テトラリン
液で前凊理し、アセチル化剀ずしお無氎酢酞、觊
媒ずしお酢酞カリ、溶剀ずしおテトラリンを甚い
お140℃で24時間反応を行な぀おアセチル化RGP
を埗た。 調補䟋  アセチル化朚粉の調補 調補䟋においお、RGPの代りに200メツシナ
の朚粉を甚いたこず以倖は調補䟋ず同様の方法
におアセチル化朚粉を埗た。 調補䟋  ベンゞル化RGPの調補 RGP50を氎酞化ナトリりム氎溶液氎酞化
ナトリりム50、氎500mlにお調補䞭で100〜
102℃にお時間反応させた埌、真空濟過した。
この濟過品に塩化ベンゞル20ml氎0.5を
添加し、102℃で時間反応させた埌、真空濟過
を行ない、次いで80℃で時間也燥させおベンゞ
ル化RGPを埗た。 実斜䟋〜13及び比范䟋〜 160℃に調枩されたニヌダヌ東掋粟機補ラボ
プラストミルに(A)成分ずしお第衚に瀺す所定
割合のセルロヌス系材料を導入し、回転数90r・
・・で玄10分間緎぀たのち、(B)成分ずしお所
定量の無氎マレむン酞倉性ポリプロピレン以
䞋、MAH倉性PPず略称たたは未倉性ポリプ
ロピレン以䞋、未倉性PPず略称を加え30分
間混緎した。なお、䞊蚘(A)成分ず(B)成分の合蚈重
量は装眮のミキシング郚分の容量に合せ24ずし
た。 埗られた混緎物を170℃で加圧成圢しお0.3mm厚
のフむルムを補造した。このフむルムより80mm×
mmの短冊圢詊片を䜜り、䞋蚘の方法により物性
の評䟡を行な぀た。評䟡結果を第衚に瀺す。 評䟡方法  匕匵匷さ、匕匵砎断䌞びおよび匕匵匟性率詊
鹓 暙点間距離40mm、匕匵速床10mmminの条件
にお枬定した。  透明性 スガ詊隓機(æ ª)補、カラヌコンピナヌタヌ
HGM−20を甚いお党光線透過率を枬定した。  平滑性 詊片の衚面を目芖しお評䟡した。 ○ 極めお平滑 △ 郚分的に荒い × 荒い  光沢性 詊片の衚面を目芖しお評䟡した。 ○ 極めお良奜 △ 若干くもりがある × 䞍良 比范䟋  実斜䟋においお(A)成分ず(B)成分の配合比を第
衚に瀺す所定量にし、混緎時間を分間に倉え
たこず以倖は実斜䟋ず同様に行な぀た。結果を
第衚に瀺す。 次に、埗られたフむルムに぀いお重量枛少率を
枬定したずころ比范䟋で埗られたフむルムは
48.7、比范䟋で埗られたフむルムは28.1で
あ぀た。これらのフむルムはいずれも䞍透明でセ
ルロヌス系材料の分散は䞍良であ぀た。
[Industrial Application Field] The present invention relates to a method for producing a new graft body, and more specifically, to improve the mechanical strength, surface smoothness, and
The present invention relates to a method for producing a new graft body that improves surface gloss and imparts transparency to resin molded products. [Prior art and problems to be solved by the invention] Cellulose-based materials such as wood and pulp are difficult to thermoplasticize, and it has been difficult to thermo-press them into boards, sheets, etc. . Therefore, the use of wood powder and the like is limited to fields with low added value such as agricultural materials and fillers, and the current situation is that wood powder is not used at all and is incinerated. Therefore, various studies are underway regarding the advanced utilization of such cellulose-based materials. For example, a molding material made by melting and kneading a thermoplastic resin and wood flour is known, but its dispersibility, compatibility, and adhesiveness are insufficient. Therefore, sufficient mechanical strength, surface smoothness, and surface gloss have not been obtained. The present invention solves the above-mentioned problems and also provides a method for producing a new graft body that imparts excellent transparency to resin molded products. [Means for solving the problem] That is, the present invention grafts a modified polyolefin modified with an unsaturated carboxylic acid or a derivative thereof (component (B)) to a cellulose-based material containing at least cellulose (component (A)). The present invention provides a method for producing a novel graft body characterized by the following. In the present invention, it contains at least cellulose,
Cellulose-based materials include organic fibers consisting only of cellulose and organic fibers containing other components in addition to cellulose. For example, there are cellulose fibers, lignocellulose fibers, etc., specifically wood pulp, refiner, ground pulp (RGP), paper pulp, waste paper, pulverized wood chips,
Examples include wood flour, fruit flour, and various celluloses. As described above, the shape of the cellulose material in the present invention is not particularly limited, and may be fibrous, granular,
Cellulose-based materials such as powder can be used. Moreover, pulverized wood pulp, waste paper, etc. can also be used if necessary. Wood flour includes crushed products such as pine, fir, poplar, and Scots pine, sawdust, and canna shavings, and fruit flour includes crushed products of fruits such as walnuts, peanuts, and coconut. In addition, various types of cellulose include alpha fiber flock obtained by treating wood pulp with alkali and mechanically shredding it, cotton linters and cotton flock obtained from cotton seeds, and human silk flock obtained by shredding human silk. Among these, it is particularly preferable to use RGP and wood flour. In addition, when using wood flour, it is preferable to make it as fine as possible to eliminate entanglement between fibers, but it is difficult to work with,
Considering economic efficiency, etc., one having a capacity of about 20 to 400 meshes is usually used. Furthermore, even when RGP is used, it is preferable to use one that has been stirred with deionized water to loosen the entanglements between the fibers. In the present invention, cellulose may be partially chemically modified, such as esterification with lower or higher fatty acids such as acetylation and lauroylation; ethylation, propylation, allylation, benzylation, It may be modified by etherification such as carboxylation and hydroxylethylation; halogenation such as chlorination and bromination. Next, in the present invention, a modified polyolefin obtained by modifying a polyolefin with an unsaturated carboxylic acid or a derivative thereof is used as the component (B). Examples of modified polyolefins include (a) polyolefins obtained by heating and mixing polyolefins, resins, unsaturated carboxylic acids or derivatives thereof, and radical generators in the presence or absence of a solvent; (b) polyolefins Examples include those obtained by heating and mixing a resin, an unsaturated carboxylic acid or a derivative thereof, an elastomer, and a radical generator in the presence or absence of a solvent. In this invention, the amount of unsaturated carboxylic acid or its derivative added in any of the various modified polyolefins is preferably 0.1 to 14% by weight, particularly 0.5 to 10% by weight. The polyolefin resin that serves as the raw material for the modified polyolefin may be of any type, such as low density polyethylene, medium density polyethylene, high density polyethylene, polypropylene,
Preferred examples include monoolefin polymers such as polybutene and poly-4-methylpentene-1, ethylene-propylene copolymers, and mixtures of these polymers. The elastomer is preferably a polymer containing a diene monomer as a main component and having a number average molecular weight of 500 to 10,000, and exhibits fluidity at room temperature. Examples of this include carboxyl groups, hydroxyl groups,
1,2- containing functional groups such as mercapto groups, halogen atoms, amino groups, aziridino groups, and epoxy groups
Polybutadiene, 1,4-polybutadiene, polyisoprene, polychloroprene, 1,2-polypentadiene, styrene-butadiene copolymer,
Elastomers such as acrylonitrile-butadiene copolymer, butadiene-isoprene copolymer, butadiene-pentadiene copolymer and terminally hydroxylated 1,2-polybutadiene, 1,
Unsaturated carboxylic acid half esters such as 4-polybutadiene or number average molecular weight without functional groups
500-10000 1,2-polybutadiene, 1,4-
Examples include polybutadiene, styrene-butadiene copolymer, acrylonitrile-butadiene copolymer, pyrolyzed rubber, ozonolyzed rubber, and mixtures of the above-mentioned elastomers. Examples of the unsaturated carboxylic acids or derivatives thereof include maleic acid, nadic anhydride, itaconic acid, citraconic acid, crotonic acid, isocrotonic acid, mesaconic acid, angelic acid, sorbic acid,
Acrylic acid, maleic anhydride, itaconic anhydride,
Citraconic anhydride and the like are preferred, and maleic anhydride is particularly preferred. Further, as the derivative of the unsaturated carboxylic acid, metal salts, amides, imides, esters, etc. of the unsaturated carboxylic acid can be used. Incidentally, as the unsaturated carboxylic acid and its derivatives used in this modified polyolefin, one or more of the above-mentioned ones can be used. The radical generator may be one that promotes the reaction between the polyolefin resin, an elastomer blended as necessary, and an unsaturated carboxylic acid or a derivative thereof, such as benzoyl peroxide, lauryl peroxide, azobisisomer, etc. Butyronitrile, cumene peroxide, α,α'-bis(t-butylperoxydiisopropyl)benzene, di-t-butylperoxide, 2,5-di(t-butylperoxy)hexane, etc. are preferably used. can do. Among these various modified polyolefins, in particular, polyethylene and/or polypropylene with a melt index (hereinafter abbreviated as MI) of 0.5 to 200 g/10 minutes, maleic anhydride, and terminal hydroxylated polybutadiene are combined with xylene,
Preferred is a resin to which 0.5 to 10% by weight of maleic anhydride is added, which is obtained by reaction using a radical generator such as benzoyl peroxide in a solvent such as toluene, heptane, or monochlorobenzene. The blending ratio of the above (A) component and (B) component is (A) component 10 to 95
The amount of component (B) is 5 to 90% by weight, preferably 10 to 85% by weight relative to the weight of component (B), preferably 15 to 90% by weight.
Here, if the content of component (A) exceeds 95% by weight, the rigidity decreases, which is not preferable. In addition, if the amount of component (A) is less than 10% by weight, strength, transparency, and glossiness decrease, which is not preferable. The novel graft body targeted by the present invention is obtained by kneading and grafting the above-mentioned components. That is, by kneading the above-mentioned components, a grafting reaction is caused by ester bonds between the hydroxyl groups of cellulose and the carboxyl groups of the modified polyolefin resin. The kneading may be carried out using a conventionally known method, such as a mixer such as a Banbury mixer or a Henschel mixer, a kneader, or various extruders. Further, the kneading may be performed in a solvent. In any case, it is preferable to conduct the heating under moderate heating. In addition, kneading is carried out at 140 to 200℃ using a kneader or Banbury mixer, for example.
It is preferably carried out at a temperature of 150 to 190°C for 10 to 30 minutes, preferably 15 to 20 minutes. In addition, the rotation speed of the kneader etc. at this time is usually 50 to 200 rpm, preferably
70~150rpm. During kneading, a catalyst that enhances the grafting reaction can be added if necessary. Examples of the catalyst include carbonates, oxides, hydroxides, carboxylates of alkali metals or alkaline earth metals, amine compounds such as N,N-dimethylbenzylamine and triethylamine, pyridine, dimethylaniline, etc. can be added. The novel graft material targeted by the present invention is obtained by grafting a modified polyolefin modified with an unsaturated carboxylic acid or a derivative thereof onto a cellulose-based material containing at least cellulose. There is no particular restriction on the proportion, but it is usually 3% by weight or more,
Preferably it is 4% by weight or more. If the grafting ratio is low, the thermoplasticity of the cellulose material and the dispersibility and compatibility with the thermoplastic resin will be insufficient, which is not preferable. Various molded products can be produced by molding the resin composition containing the novel graft body obtained in this way into an appropriate shape by means such as pressure molding, film molding, extrusion molding, and injection molding. [Effects of the Invention] The molded article of the resin assembly containing the new graft body obtained by the method of the present invention has extremely excellent mechanical strength, and also has excellent transparency, smoothness, and
It has luster. Therefore, molded products containing the novel graft body obtained by the method of the present invention can be used as materials for film and sheet materials, furniture, building materials (surface finishing materials, structural materials), automobiles, housings for home appliances, interior materials, acoustic materials, etc. It is effectively used as [Example] Hereinafter, the present invention will be explained in detail with reference to Examples. Preparation Example 1 Preparation of RGP New Zealand radiata pine and dehydrated ionized water were stirred in a home appliance mixer for 1 minute to loosen the fibers, and then collected by filtration and mixed with methanol,
By then washing with ether and drying
Got RGP. Preparation Example 2 Preparation of acetylated RGP RGP obtained in Preparation Example 1 was pretreated with tetralin acetate solution, and reacted at 140°C for 24 hours using acetic anhydride as an acetylating agent, potassium acetate as a catalyst, and tetralin as a solvent. Acetylated RGP by
I got it. Preparation Example 3 Preparation of Acetylated Wood Flour Acetylated wood flour was obtained in the same manner as in Preparation Example 2, except that 200 mesh wood flour was used instead of RGP. Preparation Example 4 Preparation of benzylated RGP 50g of RGP was dissolved in a sodium hydroxide aqueous solution (prepared with 50g of sodium hydroxide and 500ml of water) at 100~
After reacting at 102°C for 3 hours, the mixture was vacuum filtered.
Benzyl chloride (20 ml/water 0.5) was added to this filtered product and reacted at 102°C for 5 hours, followed by vacuum filtration and then dried at 80°C for 8 hours to obtain benzylated RGP. Examples 1 to 13 and Comparative Examples 1 to 6 A cellulose-based material in a predetermined proportion shown in Table 1 as component (A) was introduced into a kneader (Laboplast Mill manufactured by Toyo Seiki Co., Ltd.) whose temperature was controlled at 160°C, and the rotation speed was 90r・
After kneading for about 10 minutes at pm, add a predetermined amount of maleic anhydride-modified polypropylene (hereinafter abbreviated as MAH-modified PP) or unmodified polypropylene (hereinafter abbreviated as unmodified PP) as component (B). Kneaded for a minute. The total weight of the components (A) and (B) was 24 g, which corresponded to the capacity of the mixing section of the device. The obtained kneaded product was pressure-molded at 170°C to produce a film with a thickness of 0.3 mm. 80mm× from this film
A 5 mm rectangular specimen was prepared and its physical properties were evaluated using the following method. The evaluation results are shown in Table 1. Evaluation method 1 Tensile strength, tensile elongation at break, and tensile modulus test Measured under the conditions of a gauge distance of 40 mm and a tensile speed of 10 mm/min. 2 Transparency Color computer manufactured by Suga Test Instruments Co., Ltd.
Total light transmittance was measured using HGM-20. 3 Smoothness The surface of the specimen was visually observed and evaluated. ○...Extremely smooth △...Partially rough ×...Rough 4 Glossiness The surface of the specimen was visually observed and evaluated. ○...Extremely good △...Slightly cloudy ×...Poor comparative example 7, 8 In Example 1, the blending ratio of component (A) and (B) component was set to the specified amount shown in Table 1, and the kneading time was set to 3 minutes. The same procedure as in Example 1 was carried out except for the changes. The results are shown in Table 1. Next, the weight loss rate of the obtained film was measured, and the film obtained in Comparative Example 7 was
48.7%, and the film obtained in Comparative Example 8 had 28.1%. All of these films were opaque and had poor dispersion of cellulosic material.

【衚】【table】

【衚】 参考䟋 実斜䟋及び比范䟋で甚いたず同じ未倉性PPた
たはMAH倉性PPずRGRを第衚に瀺す所定重
量比で所定条件で混緎しお埗られた組成物に぀い
おRGPにグラフトしおいないポリプロピレン区
分をキシレンで48時間゜ツクスレヌ抜出した。キ
シレン抜出による重量枛少率を第衚に瀺す。 なお、重量枛少率は次匏により求めた。 −×100 ただし、はPPたたはMAH倉性PPずRGPの
合蚈重量を瀺し、は混緎品をキシレンで抜出し
た抜出残枣の重量を瀺す。
[Table] Reference Example A composition obtained by kneading the same unmodified PP or MAH-modified PP and RGR as used in the Examples and Comparative Examples at the predetermined weight ratio shown in Table 2 under the predetermined conditions was grafted onto RGP. The polypropylene sections without were Soxhlet extracted with xylene for 48 hours. Table 2 shows the weight loss rate due to xylene extraction. In addition, the weight reduction rate was calculated|required by the following formula. M-N/M×100 (However, M indicates the total weight of PP or MAH-modified PP and RGP, and N indicates the weight of the extraction residue obtained by extracting the kneaded product with xylene.)

【衚】 第衚より明らかなように、RGPずPPの混緎
物からはPPがキシレン抜出で完党に取陀かれる
のに察し、RGPずMAH倉性PPではMAH倉性
PPの䞀郚が抜出されずに残枣䞭に残぀おいる。 次に、該抜出残枣のIR分析を行な぀た。その
結果、RGPずPPの混緎物からの残枣のIRスペク
トルにはPP由来の吞収ピヌクは認められなか぀
たのに察し、RGPずMAH倉性PPの混緎物から
の残枣のスペクトルには1820cm-1、1890cm-1など
にPP由来の吞収ピヌクが認められた。 次に、RGPずPPの混緎物、RGPずMAH倉性
PPの混緎物のそれぞれを0.2mm厚に加圧成圢しお
埗られたフむルムをサフラニン染色し、光孊顕埮
鏡にお芳察した。その結果、RGPずPPの混緎物
から成圢されたフむルムはPPの連続盞に粗いサ
フラニン染色されたRGPが存圚しおいるのに察
し、RGPずMAH倉性PPの混緎物から成圢され
たフむルムはRGPが现かく分散しおいた。 以䞊の結果より、RGPずMAH倉性PPの混緎
物は郚分的にグラフトが生起しおいるこずが確認
された。
[Table] As is clear from Table 2, PP is completely removed from the kneaded mixture of RGP and PP by xylene extraction, whereas in RGP and MAH-modified PP, PP is completely removed by xylene extraction.
A portion of PP remains in the residue without being extracted. Next, the extracted residue was subjected to IR analysis. As a result, no absorption peak derived from PP was observed in the IR spectrum of the residue from the mixture of RGP and PP, whereas the spectrum of the residue from the mixture of RGP and MAH-modified PP had 1820 cm -1 , Absorption peaks derived from PP were observed at 1890 cm -1 etc. Next, mix RGP and PP, RGP and MAH modified
The films obtained by pressure molding each of the PP kneaded products to a thickness of 0.2 mm were stained with safranin and observed using an optical microscope. As a result, the film formed from the mixture of RGP and PP has rough safranin-dyed RGP in the continuous phase of PP, whereas the film formed from the mixture of RGP and MAH-modified PP has RGP. were finely dispersed. From the above results, it was confirmed that grafting occurred partially in the kneaded product of RGP and MAH-modified PP.

Claims (1)

【特蚱請求の範囲】  少なくずもセルロヌスを含むセルロヌス系材
料に、䞍飜和カルボン酞たたはその誘導䜓で倉性
した倉性ポリオレフむンをグラフトさせるこずを
特城ずする新芏グラフト䜓の補造方法。  セルロヌスが郚分的に化孊倉性されたもので
ある特蚱請求の範囲第項蚘茉の補造方法。  化孊倉性が゚ステル化、゚ヌテル化たたはハ
ロゲン化である特蚱請求の範囲第項蚘茉の補造
方法。  倉性ポリオレフむンを重量以䞊グラフト
させた特蚱請求の範囲第〜項のいずれかに蚘
茉の補造方法。
[Claims] 1. A method for producing a novel graft material, which comprises grafting a modified polyolefin modified with an unsaturated carboxylic acid or a derivative thereof onto a cellulose-based material containing at least cellulose. 2. The manufacturing method according to claim 1, wherein the cellulose is partially chemically modified. 3. The manufacturing method according to claim 2, wherein the chemical modification is esterification, etherification, or halogenation. 4. The manufacturing method according to any one of claims 1 to 3, wherein 3% by weight or more of modified polyolefin is grafted.
JP17693985A 1985-08-13 1985-08-13 Novel grafted material Granted JPS6239656A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17693985A JPS6239656A (en) 1985-08-13 1985-08-13 Novel grafted material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17693985A JPS6239656A (en) 1985-08-13 1985-08-13 Novel grafted material

Publications (2)

Publication Number Publication Date
JPS6239656A JPS6239656A (en) 1987-02-20
JPH0347286B2 true JPH0347286B2 (en) 1991-07-18

Family

ID=16022379

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17693985A Granted JPS6239656A (en) 1985-08-13 1985-08-13 Novel grafted material

Country Status (1)

Country Link
JP (1) JPS6239656A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2886211B2 (en) * 1989-10-20 1999-04-26 株匏䌚瀟東芝 Combined cycle power plant
WO2024058246A1 (en) * 2022-09-16 2024-03-21 囜立倧孊法人京郜倧孊 Composition

Also Published As

Publication number Publication date
JPS6239656A (en) 1987-02-20

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