TW201221579A - Polylatic acid and polyolefin-based composition - Google Patents

Polylatic acid and polyolefin-based composition Download PDF

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TW201221579A
TW201221579A TW100140142A TW100140142A TW201221579A TW 201221579 A TW201221579 A TW 201221579A TW 100140142 A TW100140142 A TW 100140142A TW 100140142 A TW100140142 A TW 100140142A TW 201221579 A TW201221579 A TW 201221579A
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Taiwan
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resin
polyalkenyl
polylactic acid
film
mass
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TW100140142A
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Chinese (zh)
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TWI510547B (en
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Yoshihiro Maekawa
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Chukoh Chem Ind
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Abstract

The present invention relates to a composition of poly lactic acid and poly allyl series, characterized in that the total amount is 100 wt %, and 4.5 to 30 wt % of poly lactic acid resin, 25 to 93.0 wt % of poly allyl resin and 2.5 to 45 wt % of a modified poly allyl compound; and the content of the modified poly allyl compound is 0.25-fold higher and 1.5-fold less than that of the poly lactic acid resin.

Description

201221579 六、發明說明: 【發明所屬之技術領域】 [0001]本發明係關於一種尤其是在製造膠膜等塑膠製品時所使 用的聚乳酸及聚烯基系組成物。 【先前技術] [00〇2]近年來,在日常生活中使用數量胤大的各種塑膠製品。 其結果,從自然環境保護的觀念來看,發生包含該等塑 膠製品使用後之處理等在内的問題。例如在超級市場等 0 使用之包裝用托盤、購物袋、瀝水網、樹苗用盆等係藉 由擠出成形法而形成。該等拋棄式塑膠材料日常係作為 垃圾,從家庭或商業設施排放出龐大的數量。在現狀下 ,該等大多數係藉由焚化來廢棄。然而,該等大多數係 使用來自石化資源之通用塑膠’主要使用聚烯基系樹脂 又,自以往,該等塑膠材料之燃燒卡路里甚高,具有損 傷焚化爐的問題。同時近來’當該等歸材料完全焚化 〇 二物質中的碳素會作為c〇2而—口氣釋出,從而作為地 暖化的主因而構成問題。 解決該問題的手段,近十幾年來採用將數十%之碳酸 手機物’添加於聚烯基系樹脂中以令發熱量減低之 =°然而’所添加的無機物殘留作為灰懷,反而與掩 有關聯而被視為問題。又’就產生CO方面來看, 仍處於絲毫未解決之狀況。 對策係要求可減少燃燒時之發熱量,而且作為燃 :刀不會殘留大量殘渣的材料。其中-種材料係提案 10014014#單編號_,基㈣系成形用組成物,其含有:由不飽和叛酸或 UU14Ui 第3頁/共23頁 1013006142-0 201221579 其衍生物所改質後之聚稀基樹脂、由不飽和叛酸或其衍 生物所改質後之聚烯基樹脂與未改質聚烯基樹脂之混合 物、及澱粉系材料(專利文獻1)。該聚烯基-澱粉系成形 用組成物之特徵在於加工性、熱流動性及光分解性良好 ,具有在實用上足夠之機械性強度。 又,聚烯基-澱粉系成形用組成物以外之對策係提案聚乳 酸-改質聚烯基系樹脂組成物,係於聚乳酸樹脂含有由不 飽和羧酸或其衍生物所改質後之聚烯基樹脂(專利文獻2 、3)。該等聚乳酸-改質聚烯基系樹脂組成物之特徵在於 強度、耐衝擊性良好,且具有生物分解性。 然而,將如上述之聚烯基-澱粉系組成物使用於一般性膠 膜用途時,由於在組成物中含有殿粉系,因此作為垃圾 予以廢棄並進行焚化處理時,燃燒時之卡路里降低,解 決灰分殘渣的問題,但卻具有如下問題。 (1) 因組成中含有澱粉系的影響,成形時為「臭氣」、「 氣體產生」等之主因,須注意成形時之溫度控制。 (2) 因組成中含有澱粉系的影響,即使注意成形時之溫度 控制,澱粉系組成仍受到成形時之熱影響而引起變色, 無法獲得透明膠膜。 (3) 適合作為家庭或商業設施所產生垃圾之回收袋。然而 ,由於組成中含有澱粉系組成,因此不適合直接與口接 觸之食品之捆包膠膜。 為了解決上述問題點,本案申請人先提案一種於聚烯基 系樹脂,添加數10%之聚乳酸之聚乳酸及聚烯基系組成物 之成形品(專利文獻4)。若依據專利文獻4之聚乳酸及聚 烯基系組成物之成形品,可同時具備與以往的聚烯基系 雨議1#單編號A0101 第4頁/共23頁 1013006142-0 201221579 樹脂製成形品同等之機械特性與品質特性,而且還可抑 制廢棄處理時之(:〇2產生量。 該類聚乳酸及聚烯基系組成物係由於聚乳酸含有率高, 因此可於自然環境中完全分解。因此,於使用後作為垃 圾廢棄時,可有別與以往的焚化廢棄而有利地利用掩埋 廢棄。然而,其具有以下問題。 (4) 樹脂成分為聚乳酸、改質聚烯基兩種成分,各個之樹 脂價格高達烯基系樹脂價格之2. 5〜10倍。因此,就廢棄 處理的觀點來看雖有效,但蘊含製品價格之成本升高主 因。 (5) 於成形時,須以暫且由雙軸擠出混合攪拌機混合攪拌 各個樹脂,並予以溶融擠出而受到薄片化、顆粒化之物 作為主原料,因此蘊含主原料進一步成本升高之主因。 [先行技術文獻] [專利文獻] [專利文獻1 ]曰本特開平6-340771號公報 [專利文獻2]日本特開2001-1230 55號公報 [專利文獻3]日本特開平9-316310號公報 [專利文獻4]日本特開20 07-30 8638號公報 【發明内容】 [0003] 本發明之目的在於提供一種低成本之聚乳酸及聚烯基系 組成物,其係克服以聚烯基及澱粉系組成物進行成形時 之上述問題點(1)〜(3)、以聚乳酸及改質聚烯基系樹脂 組成物進行成形時之上述問題點(4)、(5),活用聚乳酸 之特徵即剛性,且耐衝擊性良好,具有成形性及高機械 性強度。 1001401#料號删1 第5頁/共23頁 1013006142-0 201221579 本發明之聚乳酸及聚烯基系組成物之特徵為:總量成為 10D質量%而含有聚乳酸樹脂4. 5〜30質量%、聚烯基樹脂 25〜93. 0質量%及改質聚稀基化合物2. 5〜45質量% ;前 述改質聚烯基化合物係相對於前述聚乳酸樹脂含有〇. 25 倍以上、小於1. 5倍。 若依據本發明,可獲得活用聚乳酸之特徵即剛性,且耐 衝擊性良好,具有成形性及高機械性強度之低成本之聚 乳酸及聚稀基系組成物。 【實施方式】 [0004] 以下進一步詳細說明有關本發明。 於本發明中,聚乳酸樹脂係玉米、馬鈴薯、地瓜等之植 物殿粉經乳酸化及聚合之樹脂,其指僅由來自^乳酸、 D-乳酸、L-乳酸及D-乳酸之單體單位所構成的聚合物。 藉由將聚乳酸樹脂製成植物澱粉經乳酸化及聚合而獲得 之樹脂,可將c〇2之產生量抑制在丨5〜1〇%之比率。 聚乳酸樹脂可採習知之任意聚合方法來製造。最具代表 性的方法係將乳酸之奸環狀2量體之乳酸交醋,予以開環 聚合之方法(乳酸交醋法),但將乳酸直接予以縮合聚合 亦無妨。 聚乳酸樹脂由來自L-乳酸樹脂或D一乳酸樹脂、或者卜乳 酸樹脂及D-乳賴脂之單體單位所組朗,聚合體為結 晶性,具有高溶點。又,藉由使來自L-乳酸樹脂、D-乳 酸樹脂之單體單位之比率(以下稱為l/d)變化,可自由調 整結晶性•溶點。該等聚乳酸樹脂市售者有例如:三井 化學股份有限公司製、商品名稱:LACEA及Nature201221579 VI. Description of the Invention: [Technical Field of the Invention] [0001] The present invention relates to a polylactic acid and a polyalkenyl-based composition which are used especially in the production of a plastic article such as a film. [Prior Art] [00〇2] In recent years, a large number of various plastic products have been used in daily life. As a result, from the viewpoint of natural environmental protection, problems such as handling after use of the plastic products are generated. For example, packaging trays, shopping bags, draining nets, and seedling pots used in supermarkets and the like are formed by extrusion molding. These disposable plastic materials are used daily as garbage and emit large quantities from household or commercial facilities. In the current situation, most of these are discarded by incineration. However, most of these use general-purpose plastics from petrochemical resources, which mainly use polyalkenyl-based resins. Since the past, these plastic materials have a high calorie burning degree, which has a problem of injuring the incinerator. At the same time, recently, when these materials are completely incinerated, the carbon in the two substances will act as c〇2, and the breath will be released, thus posing as the main cause of geothermalization. The means to solve this problem, in the past decade or so, the use of tens of% of carbonic acid mobile phones 'added to the polyalkenyl resin to reduce the calorific value = ° However, the added inorganic residue as a gray, but instead Being associated is considered a problem. In terms of the production of CO, it is still in an unresolved situation. The countermeasures are required to reduce the amount of heat generated during combustion, and as a material that does not leave a large amount of residue. Among them, the material is proposed 10014014# single number _, base (four) is a forming composition, which contains: modified by unsaturated taurine or UU14Ui page 3 / 23 pages 1013041242-0 201221579 A dilute base resin, a mixture of a polyalkenyl resin modified with an unsaturated tarenic acid or a derivative thereof, an unmodified polyalkenyl resin, and a starch-based material (Patent Document 1). The polyalkenyl-starch-forming composition is characterized by good workability, thermal fluidity, and photodegradability, and has practically sufficient mechanical strength. In addition, a polylactic acid-modified polyalkenyl resin composition is proposed in addition to the polyalkenyl-starch molding composition, and the polylactic acid resin is modified by an unsaturated carboxylic acid or a derivative thereof. Polyalkenyl resin (Patent Documents 2 and 3). These polylactic acid-modified polyalkenyl resin compositions are characterized by good strength and impact resistance and biodegradability. However, when the polyalkenyl-starch-based composition as described above is used for general film use, since the composition contains a temple powder system, when it is disposed of as garbage and incinerated, the calories during burning are lowered. Solve the problem of ash residue, but it has the following problems. (1) Due to the influence of the starch system in the composition, the main cause of "odor" and "gas generation" during molding is to pay attention to the temperature control during molding. (2) Due to the influence of the starch system in the composition, even if the temperature control at the time of molding is taken care of, the starch composition is still affected by the heat during molding, and discoloration is caused, and a transparent film cannot be obtained. (3) Suitable as a recycling bag for garbage generated by household or commercial facilities. However, since the composition contains a starch-based composition, it is not suitable for a plastic film which is directly in contact with the mouth. In order to solve the problem, the applicant of the present invention has proposed a molded article of a polylactic acid and a polyalkenyl-based composition in which polyacrylic acid is added in an amount of 10% to a polyalkenyl resin (Patent Document 4). According to the molded article of the polylactic acid and the polyalkenyl-based composition of Patent Document 4, it can be formed with a resin of the conventional polyalkenyl group, a single-numbered A0101, a fourth page, a total of 23 pages, 1010306142-0, 201221579 resin. The product has the same mechanical properties and quality characteristics, and it can also suppress the amount of 〇2 produced during disposal. This type of polylactic acid and polyalkenyl-based compounds have a high polylactic acid content and can be completely decomposed in the natural environment. Therefore, when it is disposed of as waste after use, it can be advantageously disposed of by landfill with conventional incineration waste. However, it has the following problems. (4) The resin component is polylactic acid and modified polyalkenyl. The price of each resin is as high as 2. 5 to 10 times the price of the alkenyl resin. Therefore, although it is effective from the viewpoint of disposal, the cost of the product price increases. (5) At the time of forming, it is necessary to For the time being, the respective resins are mixed and stirred by a twin-screw extrusion mixer, and are melt-extruded and subjected to exfoliation and granulation as a main raw material, thereby implying a further increase in the cost of the main raw material. [Patent Document 1] [Patent Document 1] Japanese Patent Laid-Open Publication No. Hei 9-316310 (Patent Document 2) [Patent Document 4] Japanese Patent Laid-Open Publication No. 20 07-30 8638 [Description of the Invention] [0003] It is an object of the present invention to provide a low-cost polylactic acid and polyalkenyl-based composition which overcomes polyalkenyl groups and The above problems (1) to (3) in the case of molding the starch-based composition, and the above problems (4) and (5) in the formation of the polylactic acid and the modified polyalkenyl resin composition, the polylactic acid is used. It is characterized by rigidity, good impact resistance, and good formability and high mechanical strength. 1001401#Item No.1 Page 5 of 231013006142-0 201221579 Polylactic acid and polyalkenyl composition of the present invention 5〜45质量百分比; The above modification is as follows: the total amount is 10D% by mass, and the polylactic acid resin is contained in an amount of 5. 5~30% by mass, polyalkenyl resin 25~93. 0% by mass and modified polybasic compound 2. 5~45% by mass; The polyalkenyl compound is contained in an amount of more than 25 times the amount of the polylactic acid resin. According to the present invention, it is possible to obtain a low-cost polylactic acid and a poly-based base composition which are characterized by the use of polylactic acid, that is, rigidity, and excellent in impact resistance, and having moldability and high mechanical strength. Embodiments [0004] Hereinafter, the present invention will be described in further detail. In the present invention, the polylactic acid resin is a resin which is lactic acidated and polymerized by a plant powder of corn, potato, sweet potato, etc., which means only from lactic acid, D - a polymer composed of a monomer unit of lactic acid, L-lactic acid, and D-lactic acid. By producing a resin obtained by lactic acidating and polymerizing a polylactic acid resin, the amount of c〇2 can be suppressed.丨5~1〇% ratio. The polylactic acid resin can be produced by any conventional polymerization method. The most representative method is to transfer the lactic acid to the lactic acid, and to carry out the ring-opening polymerization method (lactic acid vinegar method), but it is also possible to directly condense the lactic acid. The polylactic acid resin is composed of a monomer unit derived from an L-lactic acid resin or a D-lactic acid resin, or a lactic acid resin and a D-milk lysate, and the polymer is crystalline and has a high melting point. Further, by changing the ratio of the monomer unit derived from the L-lactic acid resin and the D-lactic acid resin (hereinafter referred to as l/d), the crystallinity and melting point can be freely adjusted. Such polylactic acid resin commercials are, for example, manufactured by Mitsui Chemicals Co., Ltd., trade names: LACEA and Nature.

Works ; 10014014卢單編號 A0101 豐田汽車股份有限公司製、商品名稱:Ec〇 第6頁/共23頁 1013006142-0 201221579Works ; 10014014 Lu single number A0101 Toyota Motor Co., Ltd., trade name: Ec〇 Page 6 of 23 1013006142-0 201221579

Plastics u’ z;及浙江海生生物材料股份有限公司製 、商品名稱:REV00E ;於本發明,使用任一種樹脂均可 〇Plastics u' z; and Zhejiang Haisheng Biomaterials Co., Ltd., trade name: REV00E; in the present invention, any resin can be used 〇

前述聚乳酸樹脂之添加量為4. 5〜30質量%,但更宜為10 〜20質量%,因於使用時,機械特性良好,且有益於CO 2 刪減效果。在此,聚乳酸樹脂之添加量小於4. 5質量%時 ’由於烯系樹脂之含有量多,因此可獲得充分保持機械 特性’透氧率高的效果。然而,無法賦予微生物崩解性 ’亦未確認到燃燒卡路里之減低效果。又,c〇2刪減效果 亦少至1. 0%以下,故不適宜。另,當聚乳酸樹脂之添加 莖超過30質量%時,雖有益於微生物崩解性.,但獲得質地 硬脆之膠膜,導致透氧率降低。又,由於膠膜質感硬, 因此成形時產生皺摺等,發生無法安定成形的問題。 於本發明,作為聚烯基樹脂可使用各種材料,適宜舉出 例如聚丙烯、高密度聚乙烯(下文稱為HDPE)、中密度聚 乙烯(下文稱為LLDPE)、低密度聚乙烯(下文稱為LDpE) 〇 、聚-4-曱基戊締等單稀基聚合物,或者乙婦_丙烤共聚 4勿、乙烯-氣化乙烯基共聚物、丙烯_氣化乙烯基共聚物 或該等聚合物之混合物。 前述聚烯基樹脂之添加量為25〜93· 〇質量%,但更宜為 50〜75質量%,因可活用聚乳酸之特徵,同時有益於⑶ 刪減效果及燃燒卡路里之減低效果。在此 2 脂之添加量小於25質量%時,聚乳酸之特徵強烈,土c〇刪 減效果明顯增大’可獲得生物分解性•崩解性之效果2或 透明性良好之膠膜。“,由於聚乳酸之特徵強烈影響 ’因此獲得f地硬跪之膠膜,於耐衝擊性試驗中,在1〇 10014014#單編號A〇101 第7頁/共23頁 1013006142-0 201221579 次以下即破損,發生不適於膠膜用途的問題。另,當聚 烯基樹脂之添加量超過93.0質量%時,因含有許多聚烯基 樹脂的影響,熱風強度亦顯示出甚高數值。又,就耐衝 擊{•生而&,即使給予3〇次以上之衝擊,仍難以引起底部 脫落或本體裂開,可獲得機械特性良好之膠膜。然而, 無法獲得燃燒卡路里之減低效果。 ⑴述聚烯基系樹脂不僅止於一種,混合使用兩種以上亦 可例如以聚烯基系樹脂之一種之聚乙烯樹脂為例來說 聚乙稀樹脂之種類分為HDPE、LLDPE、LDPE三種。若 依據JIS規格:K6922-U塑膠聚乙烯(pe)成形用及擠出 用材料)’依密度及熔融比等品質項目而分類為三種16類 ’比重〇. 942以上分類為HDPE,比重〇. 91以上、小於 93分類為LDPE。 LLDpE係屬於令乙烯與若干量之^ -烯基共聚後之熱塑性 樹知之合成樹脂,於JISK6899-1 : 2000,定義為密度 .91〇以上、小於〇. 925之直鏈狀聚乙烯共聚物^ LLDP係 稱呼為別名直鏈狀低密度聚乙烯之樹脂。又,LLDP之耐 ’、、、〖生亦高(約125。(:)’相當於HDPE與LDPE之中間之樹脂 般而言’家庭中經常使用的垃圾袋係以HDPE、LLDP 為基質而形成’超市等使用的購物袋係以HDPE為基質而 。然而’若在成形或機械特性方面不構成問題,則 乂佐意比率添加HDPE、LLDPE、LDPE,進行適合於用途 之成形均可。 ;本發明’聚烯基樹脂為聚乙烯樹脂,該聚乙烯樹脂宜 相對於聚乳酸樹脂,含有0. 91倍以上、20. 7倍以下。在 此 > *如 l〇〇l4〇u夢單编號A_1右聚乙烯樹脂小於0. 91倍,則聚烯基樹脂之添加量 1013006142-0 第8頁/共23頁 201221579 會增加’樹脂彼此之相溶化性改善,但由於改質聚歸基 之添加量増加,因此成本升高。又,若超過2〇 7倍,聚 乙稀樹脂之添加量變多’聚稀基樹脂之添加量變少,因 此樹脂彼此之相溶性變差,於膠膜表面產生不均等,無 法獲得均勻的夥膜。 於本發明,關於聚乙稀樹脂宜相對於耐£1〇〇質量部,添 加5〜15質量部之LL則。該情況下之LLDp可獲得所韻 金屬之組成之相溶性亦佳,機械特性亦良好之物。在此 〇 ,LLDPE小於5質量部時,主要基質(HDPE)之特性變強, 拉伸強度或衝擊強度良好,但p、能獲得接近錢明之勝 膜》又,LLDP超過15質量部時,喪失_Ε之特徵。因此 二宜以適於機械特性及用途之比率來添加LLDP。再者, 茂金屬聚乙婦係指利用茂金屬觸媒(Kaminsky觸媒)聚合 後之聚口物’其為LLDPE之一種。在此,茂金屬觸媒係組 。-氣化錄與甲基氧化銘,具有對於乙稀顯示出高度聚 合活性,並且活性點平均之特徵。 〇 又茂金屬聚乙歸若與-般所謂ffDPE或LDPE、LLDPE之 組成相比較,其成本高,若添加量變多,則成本偏高 ㈣相對於主基質(組成比高的成分)之刪質 量部,宜為5〜15質量部。 :本發月作為改質聚稀基系化合物可舉出以下⑴〜 (6)之共聚物。 ⑴對“—稀基與丙稀酸醋之共聚物,使(甲基)丙稀酸醋 或笨乙稀接枝聚合而成之共聚物。 ⑴對α-稀基與醋酸乙稀基共聚物,使(曱基)丙稀酸酿 或笨乙烯接枝聚合而成之共聚物。 腦侧夢單魏 1013006142-0 201221579 (3) α -稀基與具有乙烯性不飽和結合之縮水甘油基含有 單體之共聚物。 (4) 使稀基、乙烯與丙烯酸酯及酸酐接枝聚合而成之 共聚物。 (5) 對α-烯基與乙烯-丙烯共聚物,使順丁烯二酸接枝聚 合而成之共聚物。 (6) 使乙烯與乙烯以外之α-烯基所組成的乙烯系共聚物 不飽和羧酸或其衍生物接枝聚合而成之共聚物。 上述聚合物之α-烯基可舉出乙稀、丙稀、丁婦-1、己稀 -1、4-甲基丁烯-1、4-曱基丁烯-1,但宜為乙烯、丙烯 〇 上述具有乙烯性不飽和結合之縮水甘油基含有單體可舉 出例如丙烯酸二縮水甘油基、甲基丙稀酸二縮水甘油基 、衣康酸單縮水甘油酯、丁烯三羧酸二縮水甘油酯、丁 烯三羧酸單縮水甘油酯、丁烯三羧酸三縮水甘油酯等縮 水甘油S旨類、或乙稀基縮水甘油S旨、丙稀基縮水甘油醋 、縮水甘油基乙氧醚類。(甲基)丙烯酸酯可舉出例如丙 烯酸甲基、曱基丙烯酸乙基、丙烯酸乙基、曱基丙烯酸 乙基,但作為耐衝擊改質劑尤其宜為甲基丙烯酸曱基。 前述改質烯基化合物可舉出以下(1)〜(7)。 (1) (乙烯+順丁烯二酸酐)接枝共聚物(商品名稱: ADMER、三井化學股份有限公司製) (2) α -烯基-丙烯共聚物(商品名稱:TAFUMER、三井化 學股份有限公司製) (3) 乙烯-縮水甘油基甲基丙烯酸酯共聚物接枝化ΡΜΜΑ( 商品名稱:M0DIPER Α4200、日本油脂股份有限公司製) 1001401#^ Α〇101 第10頁/共23頁 1013006142-0 201221579 (4) 乙烯-乙基丙烯酸酯共聚物接枝化pMMA(商品名稱: MODIPER A5200、日本油脂股份有限公司製) (5) 乙烯-醋酸乙烯基共聚物接枝化PMMA(商品名稱: MODIPER A6200、日本油脂股份有限公司製) (6) 乙烯-乙基丙烯酸酯-順丁烯二酸酐共聚物化pMMA(商 品名稱:MODIPER A8200、日本油脂股份有限公司製) (7) 乙烯-縮水甘油基甲基丙烯酸酯(E_GMA)共聚物及三 元聚合物(商品名稱:B0NDFAST、住友化學股份有限公 司製) 別述改質聚烯基系化合物之添加為2· 5〜45質量%,但從 膝膜表面之樹脂不均或有益於光澤性的觀點考量,更宜 為5〜20質量%。在此,改質聚稀基系化合物之添加量小 於2. 5貝量%時’未確認到因添加所帶來的物性提升及相 溶性效果》 另’田改質聚稀基系化合物之添加量超過45質量%時,可 確認到聚乳酸樹脂與聚稀基系樹脂之相溶效果。然而, 〇 *體而。聚稀基系化合物之含有率增加,無法發揮將 生物體利用作為能量m原料之來自植物的效果。 又,右與聚稀基系樹脂相比較,改質聚稀基系化合物之 原料價格间達2. 5倍以上,因此若添加改質聚稀基系化合 物之添加率,則發生成形品之成本升高的問題。 ;本發月文質聚婦基化合物係相對於聚乳酸樹脂含有 0·25倍以上、小於1 q拉 .D倍。在此,若改質聚烯基化合物小 ; 倍w利用則述化合物製造膠膜等塑膠成形品時 ,於膠膜表面產生椒 樹知不均°又,發生部分觀察到層間 剝離,於膠膜表面觀察不到光澤性等問題。進而言之, 1001401#單編號 A0101 第 11 頁 / 共 23 w ' ^ 1013006142-0 201221579 C〇2刪減率(%)為0.25倍以下,無法符合在本發明所發現 的c〇2刪減率(%)。另,改質聚烯基化合物相對於聚乳酸 樹脂為1. 5倍以上時,於膠膜表面未觀察到樹脂不均,就 相溶性的觀點來看雖適宜,但於部分產生皺褶。 於本發明,雖未特別限定,但於成形時若有開口性或底 膜光滑性等問題,則因應需要而添加可塑劑亦無妨。 可塑劑係從對於聚乳酸或改質聚烯基化合物等整體之相 溶性及可塑化能力的觀點來考量,宜由選自脂肪族二鹼 基酸酯系、苯二甲酸酯系、己二酸酯系、羥基多價羧酸 酯系、二醇酸衍生物、醚酯衍生物、纖維素衍生物、烷 基磷酸酯系、二烷基酯系、二酯系、三羧酸酯系、聚酯 系、環氧系、磺酸醯系、醚酯系、苯曱酸鹽系、聚二醇 二醋、烧基烧基醚二醋、脂肪酸醋、烧基_單S旨、擰檬 酸酯可塑劑所組成群組之至少一種以上來組成。 於本發明,可因應需要,以任意比率來添加顏料、氧化 防止劑、可塑劑、帶電防止劑、去光澤劑、劣化防止劑 、螢光增白劑、紫外線吸收劑、紫外線安定劑、滑劑、 結晶核劑、金屬粉、無機填充劑、碳黑、增黏劑、黏土 安定劑等。 獲得本發明之聚乳酸及聚烯基系組成物可舉出一般的膠 膜成形法之吹氣法、T形模法、雙軸延伸膠膜成形體之代 表性成形法之射出成形法、吹脹成形法或可見於瀝水網 之擠出網之成形法等成形方法,以下根據一般的膠膜成 形法來進行說明。 於本發明,聚乳酸樹脂、聚烯基系樹脂、改質聚烯基系 化合物等之混合方法或混合裝置並未特別限定,可連續 1013006142-0 第12頁/共23頁 201221579 處理者在工業上有利,較為適宜。例如包括如下方法(i) 、(2) 〇 (1) 以特定比率混合兩種以上之粒狀物,直接於吹氣法、 T形模法、雙軸延伸膠膜等之擠出成形機之漏斗内放入樹 脂,使其熔融而立即成形之方法。 (2) 以雙軸擠出機之成形機,熔融混合各個樹脂後,暫且 予以粒狀化,將該粒狀物放入吹氣法、T形模法、雙軸延 伸膠膜等之擠出機之漏斗内,使其熔融而成形之方法。 前述(1)之混合方法可減少樹脂之熱劣化,在製程上亦可 f) 一次集中進行成形,因此亦幾乎未有成形之成本升高。 前述(2)之混合方法係於進行膠膜等之成形前,暫且以熔 融擠出進行粒狀化,因此須實質防止聚合物劣化、變質 ,進而在獲得成形品時,與粒狀物成形品在製程上須分 為兩製程。因此,導致成形之成本升高。 以下舉出實施例,進一步具體說明本發明,本發明不限 定於該等實施例。 (比較例1) 以乾式混合法熔融混合聚乳酸PLA(商品名:LACEA-4 00 、三井化學股份有限公司製)10質量%、作為聚烯基系樹 脂之高密度聚乙烯HDPE(商品名稱:NOVATEC HF-730、 曰本聚乙烯股份有限公司製)90質量%,利用吹氣成形機 ,將吹脹比2. 5倍、厚度25//Π1之膠膜予以製膜。此時之 成形溫度為150〜200°C,室内溫度為25°C,保持在一定 (比較例2) 以乾式混合法熔融混合聚乳酸PLA(商品名:LACEA-400 1013006142-0 10014014^單編號A〇101 第13頁/共23頁 201221579 、三井化學股份有限公司製)2. 5質量%、作為聚烯基系樹 脂之HDPE(商品名稱:NOVATEC HF-730、日本聚乙烯股 份有限公司製)95. 0質量%、作為改質聚烯基之E-GMA (商 品名稱:B0NDFAST、住友化學股份有限公司製)2.5質量 %,利用吹氣成形機,將吹脹比2. 5倍、厚度25/zm之膠膜 予以製膜。此時之成形溫度為1 5 0〜2 0 0 °C,室内溫度為 25°C,保持在一定。 (實施例1) 以乾式混合法熔融混合聚乳酸PLA(商品名:LACEA-400 、三井化學股份有限公司製)4. 5質量%、作為聚烯基系樹 脂之HDPE(商品名稱:NOVATEC HF-730、日本聚乙烯股 份有限公司製)93. 0質量%、作為改質聚烯基之E-GMA(商 品名稱:B0NDFAST、住友化學股份有限公司製)2. 5質量 %,利用吹氣成形機,將吹脹比2. 5倍、厚度25//m之膠膜 予以製膜。此時之成形溫度為150〜200 °C,室内溫度為 2 5 °C,保持在一定。 (比較例3) 除了使用聚乳酸(PLA)2. 5質量%、聚烯基系樹脂 (HDPE)97. 0質量%、改質聚烯基(E-GMA)O. 5質量%以外 ,均與實施例1同樣地將膠膜予以製膜。 (實施例2) 除了使用聚乳酸(PLA)10質量%、聚烯基系樹脂 (HDPE)85質量%、改質聚烯基(E-GMA)5質量%以外,均 與實施例1同樣地將膠膜予以製膜。 (實施例3) 除了使用聚乳酸(PLA)30. 0質量%、聚烯基系樹脂 丽綱#科號舰01 1013006142-0 第14頁/共23頁 201221579 (HDPE)27. 5質量%、改質聚烯基(E-GMA)42. 5質量%以外 ,均與實施例1同樣地將膠膜予以製膜。 (實施例4) 以乾式混合法熔融混合聚乳酸PLA(商品名:LACEA-400 '三井化學股份有限公司製)1〇質量%、作為聚烯基系樹 脂之HDPE(商品名稱:NOVATEC HF-730、日本聚乙烯股 份有限公司製)80質量%、作為烯基系樹脂之茂金屬中密 度聚乙烯(茂金屬LLDPE)(商品名稱:EVOLUE SP2520、 曰本乙烯股份有限公司製)5質量%、及作為改質聚烯基之 Θ E-GMA(商品名稱:B0NDFAST、住友化學股份有限公司製 )5質量%,利用吹氣成形機,將吹脹比2. 5倍、厚度25// m之膠膜予以製膜。此時之成形溫度為150〜20(TC,室内 溫度為25°C,保持在一定。 (比較例4) 除了使用聚乳酸(PLA)2. 5質量%、聚烯基系樹脂 (HDPE)97. 0質量%、改質聚烯基(e-GMA)52. 5質量%以外 ,均與比較例2同樣地將膠膜予以製膜。 (比較例5) 作為聚烯基系樹脂為HDPE(商品名稱:NOVATEC UF421 、曰本聚乙烯股份有限公司製)1〇〇質量!%,利用吹氣成形 機,將吹脹比2. 5倍、厚度25 之膠膜予以製膜。 以後述之評估項目及評估方法,分別比較評估前述實施 例1〜4、比較例1〜5的材料。於下述表1、表2表示其結 1013006142-0 lOOMOH#單編號A〇m 第I5頁/共23頁 201221579 (表1 ) imm tt««2 實豪W 窗廉節 霄康例3 m/mE njmmm mmmmi vm i輒_ imm.5 酿扁 m/m 改窗雜靴_ rnmmmi 1. 0 0* 5 6 0. 2 0. S 聚罐薹 聚 9 38 20. 7 38. 8 8· S 吹臟_ 2, 5 2, 5 2. 5 2. 5 2-5 讎性 mmmm mmmm 本1 *1 mmm m 晡出安纖 t«ll 好 紐 a好 m &好 m m m m 凍賴麵 mmm m m m mmmn 賊紐 m m m a好 mu^rn *2 m m 幸3 瞎 0, &6 0. 98 〇. se 0* 93 o. sa mmt) 172 172 172 172 1?2 mmmmi MD 43 4§ 41 40 43 TD SI 32 30 30 30 mwmmm m MD 542 500 S10 §00 §35 TD 624 605 815 S95 630 mmm MD 109 105 107 1X0 IDi TD 5i 63 60 62 61 熱14» (WlSmssd 13. 5 14, 5 14. 0 14, 0 5以下 mxt «h 舰下 MUt 讎德里卿 4S. 3 4S. 3 44. 8 is. 3 43. 3 €0¾¾¾ 2. 90 2. 98 2. 96 2. 98 2. 90 002*»^*) 3. 3 0. f 1. 3 (K 7 3. 3 * 1未觀察到膠膜表面之樹脂不均,相溶性良好。 *2膠膜表面之樹脂不均狀態嚴重。 *3部分觀察到層間剝離,亦未觀察到膠膜表面之光澤性 麵·#單编號刪1 第16頁/共23頁 1013006142-0 201221579 [0005] ( m ) 實麄娜 mmm &較_ 比校阕$ 観成 mmpi/B- fumm/ ilt驕 UWB/MIk mmmm 歷 鐵成比《質最如 me®,雜 s mmm 3&祕 5/&S m 改質聚麵聽_ _满讎_ 1, 42 0. 5 1· 3 一 聚乙職鼢 聚乳醯窗甑鶴 0, 9 2 8. 5 0. 36 一 吹繼娜 2· S 2. 5 2. 5 2. 5 娜牲 瞎 *4 孝4 m 噴誠安定性 m 酶 i好 鸛翳安定性 a好 a好 a好 m mmwm. m- s好 稱不安定 m m m 杨不織 a好 娜 m m m 1. 02 0. 98 1. 04 0, 03 as 172 172 172 130 wmmm (MPa) MD 43 Bd 4§ 47 TD 34 32 37 43 mwmmm m MD 370 530 340 S10 TD β?δ 600 600 S60 mmm 〇3/ααώ MD 128 110 130 110 TD 66 58 08 ΙΟδ mmt 10. 0 Ϊ4. 0 δ. ο >15, 0 immm (Kj/g) 3T. 9 43. a 30* β 4 6* 0 002 数 1: 2. 70 2. 9 0 2. 65 a. oo rawtaw* ⑽ 10. 0 3, 3 11. 7 ο. bThe amount of the polylactic acid resin added is 4.5 to 30% by mass, but more preferably 10 to 20% by mass, because of good mechanical properties during use, and is advantageous for the CO 2 reduction effect. When the amount of the polylactic acid resin added is less than 4.5% by mass, the amount of the olefinic resin is large, so that the effect of sufficiently maintaining the mechanical properties and having a high oxygen permeability can be obtained. However, it was not possible to impart microbial disintegration ‘ and the calorie-reducing effect was not confirmed. Moreover, the c〇2 reduction effect is also less than 1.0%, so it is not suitable. Further, when the added stem of the polylactic acid resin exceeds 30% by mass, it is advantageous for microbial disintegration, but a hard and brittle film is obtained, resulting in a decrease in oxygen permeability. Further, since the texture of the film is hard, wrinkles and the like are formed during molding, and there is a problem that the molding cannot be stably formed. In the present invention, various materials can be used as the polyalkenyl resin, and suitable are, for example, polypropylene, high density polyethylene (hereinafter referred to as HDPE), medium density polyethylene (hereinafter referred to as LLDPE), and low density polyethylene (hereinafter referred to as a single-dilute polymer such as LDpE), poly-4-mercapto pentylene or the like, or a propylene-propylene copolymer 4, an ethylene-gasified vinyl copolymer, a propylene-gasified vinyl copolymer or the like a mixture of polymers. The polyalkenyl resin is added in an amount of 25 to 93 % by mass, but more preferably 50 to 75% by mass, because it can utilize the characteristics of polylactic acid, and is beneficial to (3) the effect of reduction and the reduction of calories burned. When the amount of the addition of the lipid is less than 25% by mass, the characteristic of the polylactic acid is strong, and the effect of removing the soil is significantly increased. The effect of biodegradability/disintegration 2 or a film having good transparency can be obtained. "Because of the strong influence of the characteristics of polylactic acid, the film of hard 跪 is obtained, in the impact resistance test, at 1〇10014014#单号A〇101 Page 7 / 23 pages 1013041242-0 201221579 times In other words, when the amount of the polyalkenyl resin added exceeds 93.0% by mass, the hot air strength also shows a very high value due to the influence of many polyalkenyl resins. Impact resistance {•生和和;, even if it is given more than 3 times of impact, it is still difficult to cause the bottom to fall off or the body to crack, and the film with good mechanical properties can be obtained. However, the calorific effect of burning calories cannot be obtained. The alkenyl resin is not limited to one type, and two or more types of polyethylene resins can be used in combination, for example, a polyethylene resin such as a polyalkenyl resin. The types of the polyethylene resin are classified into HDPE, LLDPE, and LDPE. JIS specification: K6922-U plastic polyethylene (pe) forming and extrusion materials) is classified into three types of 16 types of specific gravity according to quality items such as density and melting ratio. 942 or more is classified as HDPE, and specific gravity is 〇. LDE is classified as upper and lower than 93. LLDpE is a synthetic resin known as a thermoplastic resin obtained by copolymerizing ethylene with a certain amount of a-alkenyl group, and is defined as a density of more than 91 〇 and less than 〇. 925 in JIS K6899-1:2000. Linear polyethylene copolymer LLDP is a resin of the name linear low-density polyethylene. Moreover, the resistance of LLDP is ', ', and high (about 125. (:)' is equivalent to HDPE and LDPE. In the middle of the resin, the garbage bags that are often used in the home are formed by HDPE and LLDP. The shopping bags used in supermarkets and the like are based on HDPE. However, if there is no problem in terms of forming or mechanical properties,倍倍。 The polyethylene resin is preferably a polyethylene resin, the polyethylene resin is preferably 0.10 times the polylactic acid resin. The above, 20. 7 times or less. Here, > *, such as l〇〇l4〇u dream list number A_1 right polyethylene resin is less than 0.11 times, the amount of polyalkenyl resin added 101016014-2-0 page 8 / A total of 23 pages 201221579 will increase 'resin mutual compatibility The improvement is improved, but the cost is increased because the addition amount of the modified poly-base is increased. Further, if it exceeds 2〇7 times, the addition amount of the polyethylene resin becomes larger, and the addition amount of the poly-based resin becomes less, so the resins are mutually added. The compatibility is deteriorated, and unevenness is generated on the surface of the film, and a uniform film cannot be obtained. In the present invention, it is preferable to add LL of 5 to 15 parts by mass with respect to the mass portion of the polyethylene resin. In this case, LLDp can obtain a good compatibility of the composition of the metal of the rhyme, and the mechanical properties are also good. Here, when the LLDPE is less than 5 parts by mass, the characteristics of the main matrix (HDPE) become strong, and the tensile strength or impact strength is good, but p, which can obtain a film close to Qian Ming, and LLDP exceeds 15 mass parts, and is lost. _ Ε characteristics. Therefore, it is preferable to add LLDP at a ratio suitable for mechanical properties and use. Further, the metallocene polyethylene refers to a polymer which is polymerized by a metallocene catalyst (Kaminsky catalyst), which is one of LLDPE. Here, the metallocene catalyst system group. - Gasification and methylation, which have a high degree of polymerization activity for ethylene and an average of active sites. Compared with the composition of the so-called ffDPE or LDPE and LLDPE, the cost is high. If the amount of addition is increased, the cost is high. (4) The quality of the main matrix (component with high composition ratio) is deleted. Department, should be 5 to 15 quality departments. In the present invention, the copolymer of the following (1) to (6) is exemplified as the modified polybasic compound. (1) A copolymer obtained by graft-polymerizing (meth)acrylic acid vinegar or stupid ethylene copolymer with a copolymer of dilute base and acrylic acid vinegar. (1) Copolymer of α-thinyl group and vinyl acetate a copolymer obtained by grafting or polymerizing a vinyl acrylate or a stupid ethylene. Brain side dream single Wei 1013001412-0 201221579 (3) α-dilute group and glycidyl group containing ethylenic unsaturated bond a copolymer of a monomer. (4) A copolymer obtained by graft-polymerizing a dilute base with ethylene and an acrylate and an acid anhydride. (5) A copolymer of α-alkenyl and ethylene-propylene to which maleic acid is attached A copolymer obtained by polymerizing a branch. (6) A copolymer obtained by graft-polymerizing an ethylene-based copolymer unsaturated carboxylic acid or a derivative thereof composed of an α-alkenyl group other than ethylene. The alkenyl group may, for example, be ethylene, propylene, dibutyl-1, dilute-1, 4-methylbutene-1 or 4-mercaptobutene-1, but is preferably ethylene or propylene. The glycidyl group-containing monomer to which the unsaturated group is bonded may, for example, be diglycidyl acrylate, methacrylic acid diglycidyl group or itaconic acid monocondensed water. Oil ester, butylene tricarboxylic acid diglycidyl ester, butylene tricarboxylic acid monoglycidyl ester, butylene tricarboxylic acid triglycidyl ester, etc., or glycidyl glycidyl S, propylene A glycidyl vinegar or a glycidyl ethoxy ether. The (meth) acrylate may, for example, be a methyl acrylate, an ethyl methacrylate, an ethyl acrylate or an ethyl methacrylate, but as an impact modifier. In particular, the methacrylic acid methacrylate group is preferably the following (1) to (7). (1) (ethylene + maleic anhydride) graft copolymer (trade name: ADMER, Mitsui) (2) Alpha-alkenyl-propylene copolymer (trade name: TAFUMER, manufactured by Mitsui Chemicals, Inc.) (3) Ethylene-glycidyl methacrylate copolymer grafted oxime (commodity) Name: M0DIPER Α4200, manufactured by Nippon Oil & Fat Co., Ltd.) 1001401#^ Α〇101 Page 10 of 231013006142-0 201221579 (4) Ethylene-ethyl acrylate copolymer grafted pMMA (trade name: MODIPER A5200 Japan Oil and Fat Co., Ltd. (5) Ethylene-vinyl acetate copolymer grafted PMMA (trade name: MODIPER A6200, manufactured by Nippon Oil & Fat Co., Ltd.) (6) Ethylene-ethyl acrylate-maleic anhydride copolymerized pMMA (commodity) Name: MODIPER A8200, manufactured by Nippon Oil & Fat Co., Ltd.) (7) Ethylene-glycidyl methacrylate (E_GMA) copolymer and terpolymer (trade name: B0NDFAST, Sumitomo Chemical Co., Ltd.) The addition of the polyalkenyl compound is from 2 to 5 to 45% by mass, but it is preferably from 5 to 20% by mass from the viewpoint of unevenness of the resin on the surface of the knee membrane or benefit from glossiness. Here, when the addition amount of the modified poly-based compound is less than 2.5% by volume, 'the physical property improvement and the compatibility effect by the addition are not confirmed.>> The addition amount of the "Tian modified poly-based compound" When it exceeds 45 mass%, the compatibility effect of a polylactic acid resin and a poly-base resin can be confirmed. However, 〇 * body. The content of the poly-dense-based compound is increased, and the effect of using the organism as a raw material of the energy m cannot be exhibited. Further, the ratio of the raw material of the modified poly-based compound is 2.5 times or more as compared with the poly-based resin. Therefore, if the addition ratio of the modified poly-based compound is added, the cost of the molded product occurs. Raised question. The present invention has a polymorphic compound which is more than 0. 25 times and less than 1 q pull. D times. Here, if the modified polyalkenyl compound is small; when the compound is used to produce a plastic molded article such as a film, the pepper is not uniformly formed on the surface of the film, and partial peeling is observed in the film. No problems such as glossiness were observed on the surface. In other words, 1001401# single number A0101 page 11 / total 23 w ' ^ 1013006142-0 201221579 C〇2 cut-off rate (%) is 0.25 times or less, can not meet the c〇2 cut-off rate found in the present invention (%). Further, when the modified polyalkenyl compound was 1.5 times or more with respect to the polylactic acid resin, no resin unevenness was observed on the surface of the film, and it was suitable from the viewpoint of compatibility, but wrinkles were partially formed. In the present invention, although it is not particularly limited, if there is a problem such as opening property or smoothness of the base film during molding, it may be added as needed to add a plasticizer. The plasticizer is considered from the viewpoint of the overall compatibility and plasticizing ability for polylactic acid or a modified polyalkenyl compound, and is preferably selected from an aliphatic dibasic acid ester system, a phthalic acid ester system, and a phthalic acid ester. An acid ester type, a hydroxy polyvalent carboxylic acid ester type, a glycolic acid derivative, an ether ester derivative, a cellulose derivative, an alkyl phosphate type, a dialkyl ester type, a diester type, a tricarboxylic acid ester type, Polyester, epoxy, sulfonium sulfonate, ether ester, benzoate, polyglycol diacetate, alkyl ketone, fatty acid vinegar, alkyl ketone At least one or more of the group consisting of ester plasticizers is composed. In the present invention, a pigment, an oxidation preventive agent, a plasticizer, a charge preventive agent, a delustering agent, a deterioration preventive agent, a fluorescent whitening agent, an ultraviolet absorber, an ultraviolet stabilizer, a slip agent may be added at an arbitrary ratio as needed. , crystal nucleating agent, metal powder, inorganic filler, carbon black, tackifier, clay stabilizer, etc. The polylactic acid and the polyalkenyl-based composition of the present invention can be obtained by a general air film forming method, an air blowing method, a T-die method, a biaxially stretched film forming body, and a typical molding method. A molding method such as an expansion molding method or a molding method which can be found in an extrusion net of a draining net will be described below based on a general film forming method. In the present invention, a mixing method or a mixing device of a polylactic acid resin, a polyalkenyl resin, a modified polyalkenyl compound, or the like is not particularly limited, and may be continuously 10,103, 614, 00, 0, 12, 23, and 21, 21,921, processors in the industry. It is advantageous and suitable. For example, the following methods (i) and (2) 〇(1) are used to mix two or more kinds of granules at a specific ratio, and are directly used in an extrusion molding machine such as a blowing method, a T-die method, or a biaxially stretched film. A method in which a resin is placed in a funnel to melt it and form it immediately. (2) After the respective resins are melt-mixed in a molding machine of a twin-screw extruder, they are temporarily granulated, and the granules are placed in an extrusion method such as a blowing method, a T-die method, or a biaxially stretched film. The method of melting and forming the inside of the funnel of the machine. The mixing method of the above (1) can reduce the thermal deterioration of the resin, and can also be f-concentrated once in the process, so that the cost of forming is hardly increased. The mixing method of the above (2) is to granulate by melt extrusion before the molding of the film or the like is performed. Therefore, it is necessary to substantially prevent deterioration and deterioration of the polymer, and further, when the molded article is obtained, the molded article is formed. There must be two processes in the process. Therefore, the cost of forming is increased. The invention is further illustrated by the following examples, which are not intended to be limited to the examples. (Comparative Example 1) 10% by mass of a polylactic acid PLA (trade name: LACEA-4 00, manufactured by Mitsui Chemicals, Inc.) and a high-density polyethylene HDPE as a polyalkenyl resin (product name: 90% by mass of NOVATEC HF-730, manufactured by Sakamoto Polyethylene Co., Ltd., and a film having a blow ratio of 2.5 times and a thickness of 25//Π1 was formed by a blow molding machine. The molding temperature at this time was 150 to 200 ° C, and the indoor temperature was 25 ° C, which was kept constant (Comparative Example 2). The polylactic acid PLA was melt-mixed by dry mixing method (trade name: LACEA-400 1013006142-0 10014014^ single number A〇101 Page 13 of 23201221579, manufactured by Mitsui Chemicals Co., Ltd.) 2.5% by mass of HDPE as a polyalkenyl resin (trade name: NOVATEC HF-730, manufactured by Nippon Polyethylene Co., Ltd.) 5倍的厚度25 The thickness of the blower is 2. 5 times, the thickness is 25 by the blow molding machine. /zm film is used to form a film. At this time, the forming temperature was 150 to 200 ° C, and the room temperature was 25 ° C, which was kept constant. (Example 1) In a dry mixing method, a polylactic acid PLA (trade name: LACEA-400, manufactured by Mitsui Chemicals, Inc.) was added in an amount of 4.5% by mass, and HDPE was used as a polyalkenyl resin (trade name: NOVATEC HF- 730, 5% by mass, E-GMA (trade name: B0NDFAST, manufactured by Sumitomo Chemical Co., Ltd.) of modified polyalkenyl group, 2.5% by mass, using a blow molding machine The film was blown to a film having a ratio of 2.5 times and a thickness of 25/m. The forming temperature at this time is 150 to 200 ° C, and the indoor temperature is 2 5 ° C, which is kept constant. (Comparative Example 3), except that the polylactic acid (PLA) was used in an amount of 2.5% by mass, the polyalkenyl resin (HDPE) was 97.0% by mass, and the modified polyalkenyl group (E-GMA) was 0.5% by mass. The film was formed into a film in the same manner as in Example 1. (Example 2) The same as Example 1 except that 10% by mass of polylactic acid (PLA), 85% by mass of polyalkenyl resin (HDPE), and 5% by mass of modified polyalkenyl group (E-GMA) were used. The film is formed into a film. 5质量%, In addition to the use of polylactic acid (PLA) 30.0% by mass, polyalkenyl resin Li Gang #科号舰 01 1013006142-0 page 14 / 23 pages 201221579 (HDPE) 27. 5 mass%, The film was formed into a film in the same manner as in Example 1 except that the modified polyalkenyl group (E-GMA) was 42.5% by mass. (Example 4) In a dry mixing method, polylactic acid PLA (trade name: LACEA-400 'Mitsui Chemical Co., Ltd.), 1% by mass, and HDPE as a polyalkenyl resin (product name: NOVATEC HF-730) were melt-mixed. 80% by mass of a metallocene medium density polyethylene (metallocene LLDPE) (product name: EVOLUE SP2520, manufactured by Sakamoto Ethylene Co., Ltd.) as an alkenyl resin, and 5% by mass, and 5倍的厚度, 25//米的胶胶, using a blow molding machine, a blower ratio of 2. 5 times, a thickness of 25 / / m, as a modified polyalkenyl group, E-GMA (trade name: B0NDFAST, manufactured by Sumitomo Chemical Co., Ltd.) The film is formed into a film. 5质量%的聚烯基树脂树脂 (HDPE) 97 In addition to the use of polylactic acid (PLA) 2. 5 mass%, polyalkenyl resin (HDPE) 97, the molding temperature is 150 to 20 (TC, the room temperature is 25 ° C, and is kept constant. The film was formed into a film in the same manner as in Comparative Example 2 except that the modified polyalkenyl group (e-GMA) was 52.5% by mass. (Comparative Example 5) The polyalkenyl resin was HDPE ( Product name: NOVATEC UF421, manufactured by Sakamoto Polyethylene Co., Ltd.) 1 〇〇 mass %%, using a blow molding machine, a film having a blow ratio of 2.5 times and a thickness of 25 is formed. The items and the evaluation methods were compared and evaluated for the materials of the above-mentioned Examples 1 to 4 and Comparative Examples 1 to 5. The following Tables 1 and 2 show the knots 1010016142-0OOOOHH#Single number A〇m Page I5/Total 23 Page 201221579 (Table 1) imm tt««2 实豪 W window 霄 霄 3 3 3 3 3 m/mE njmmm mmmmi vm i辄_ imm.5 stuffed flat m / m change window shoes _ rnmmmi 1. 0 0* 5 6 0. 2 0. S Poly tank concentrating 9 38 20. 7 38. 8 8· S Blowing dirty _ 2, 5 2, 5 2. 5 2. 5 2-5 雠mmmm mmmm mm 1 1*1 mmm m晡出安纤t«ll good new a good m & good mmmm Frozen surface mmm mmm mmmn thief new mmma good mu^rn *2 mm fortunately 3 瞎0, &6 0. 98 〇. se 0* 93 o. sa mmt) 172 172 172 172 1?2 mmmmi MD 43 4§ 41 40 43 TD SI 32 30 30 30 mwmmm m MD 542 500 S10 §00 §35 TD 624 605 815 S95 630 mmm MD 109 105 107 1X0 IDi TD 5i 63 60 62 61 Heat 14» (WlSmssd 13. 5 14, 5 14 0 14, 0 5以下mxt «h Submarine MUt 雠德里卿 4S. 3 4S. 3 44. 8 is. 3 43. 3 €03⁄43⁄43⁄4 2. 90 2. 98 2. 96 2. 98 2. 90 002* »^*) 3. 3 0. f 1. 3 (K 7 3. 3 * 1 No resin unevenness was observed on the surface of the film, and the compatibility was good. *2 The resin unevenness on the surface of the film is severe. *3 part of the inter-layer peeling was observed, and the glossy surface of the film surface was not observed. #单编号删1 Page 16 of 23 1013006142-0 201221579 [0005] (m) Really mmm & _ 比校阕$ 観成mmpi/B- fumm/ ilt arrogant UWB/MIk mmmm 历铁成比“Quality as me®, miscellaneous s mmm 3& secret 5/&S m雠_ 1, 42 0. 5 1· 3 A 聚 职 鼢 鼢 醯 0 0 0 0, 9 2 8. 5 0. 36 一吹继娜2· S 2. 5 2. 5 2. 5瞎*4 filial piety 4 m squirting stability m enzyme i good 鹳翳 stability a good a good a good m mmwm. m- s good name is not stable mmm Yang woven a good mmm 1. 02 0. 98 1. 04 0, 03 as 172 172 172 130 wmmm (MPa) MD 43 Bd 4§ 47 TD 34 32 37 43 mwmmm m MD 370 530 340 S10 TD β?δ 600 600 S60 mmm 〇3/ααώ MD 128 110 130 110 TD 66 58 08 ΙΟδ mmt 10. 0 Ϊ4. 0 δ. ο >15, 0 immm (Kj/g) 3T. 9 43. a 30* β 4 6* 0 002 Number 1: 2. 70 2. 9 0 2. 65 a. oo rawtaw* (10) 10. 0 3, 3 11. 7 ο. b

[0006] *4未觀察到膠膜表面之樹脂不均,相溶性良好。 (評估項目及評估方法) (1) 加工性 加工性係根據實施例進行成形。採目視確認相溶性、連 續成形之喷出量安定性、製膜安定性、凍線安定性、捲 取安定性、以及膠膜開口性、皺褶或透明性之成形品狀 態。 (2) 比重 比重係遵循JIS-K-7112所記載的塑膠密度及比重之側定 方法來進行測定。 (3) 熔點 丽40^單編號鹿01 第17頁/共23頁 1013006142-0 201221579 熔點係遵循JIS-K-7121所記載的熱分析測定法之示差熱 分析裝置(島津製作所股份有限公司製之DSC_5〇型)來進 行測定。 (4) 拉伸破斷強度及拉伸破斷伸度 拉伸破斷強度及拉伸破斷伸度係遵循门^卜17〇2所記載 的拉伸試驗法來進行測定。試片係利用jis_k_7127所記 載的4號形試片。 (5) 撕裂強度 撕裂強度係遵循JIS-K-7128(直角形撕裂法)所記載的撕 裂試驗法來進行測定。 (6) 熱封強度 熱封強度係遵循JIS-K-1 711所記載的熱封強度測定法來 進行測定。再者,測定試片係測定以—般的製袋機在 射出數50片/rain的條件下進行製袋加工之袋體之密封部 。前述熱封強度係與前述拉伸破斷強度'拉伸破斷伸度 、撕裂強度一同成為用以確認機械性強度的指標。 (7 )耐衝擊性 予以製袋加工成任意大小之袋狀後,放入全容積量之1/2 容量的水,上下激烈振動,確認底部脫落或袋本體裂開 等之狀態。再者,實施例3之耐衝擊性為15次以上,可充 分耐受使用。 (8)燃燒卡路里 從使用於檢討之原材料之燃燒卡路里,即聚乳酸19KJ/g 、聚乙烯46KJ/g、改質聚烯基46KJ/g,藉由下式理論性 地算出。 燃燒卡路里(Kj/g):= 19χΧ + 46χΥ + 46χΖ/1()() 1001401#^'^ 0101 第18頁/共23頁 1013006142-0 201221579 其中, X .聚乳酸樹脂之質量部、γ :稀基系樹脂之質量部 ζ:改質聚烯基化合物之質量部 (9)燃燒時之C0產生量 C* 燃燒時之C〇2產生量係算出實施例、比較例所成形的膠膜 每lkg之C〇2產生量。算出方法係從rHealth Digest. 14( 1 ). 1 ( 1 999、小原仁時著)」,根據「塑膠 氧化分解時所產生的(:〇2量(來自化學構造的部分)」所記 載的c〇2產生量計算法而算出。計算法如下。 C〇2產生量(kg-C〇2/kg-Resin) =(來自石化資源之成分量)x3kg/c〇 +(來自生物質能*4 No resin unevenness on the surface of the film was observed, and the compatibility was good. (Evaluation item and evaluation method) (1) Processability Processability was formed according to the examples. The compatibility of the discharge, the stability of the discharge of the continuous molding, the film stability, the stability of the strand, the stability of the coil, and the shape of the film opening, wrinkles or transparency of the molded article were visually observed. (2) Specific gravity The specific gravity is measured by the side method of the plastic density and specific gravity described in JIS-K-7112. (3) Melting point 40^ Single number deer 01 Page 17 of 231013006142-0 201221579 The melting point is a differential thermal analysis device according to the thermal analysis method described in JIS-K-7121 (made by Shimadzu Corporation) DSC_5 type) for measurement. (4) Tensile breaking strength and tensile breaking elongation The tensile breaking strength and the tensile breaking elongation were measured in accordance with the tensile test method described in J.B. The test piece used the No. 4 test piece recorded by jis_k_7127. (5) Tear strength The tear strength was measured in accordance with the tear test method described in JIS-K-7128 (right angle tear method). (6) Heat seal strength The heat seal strength was measured in accordance with the heat seal strength measurement method described in JIS-K-1 711. Further, the test piece was subjected to measurement of a sealed portion of a bag body which was subjected to bagging processing under the condition that the number of shots was 50 pieces/rain. The heat seal strength is an index for confirming the mechanical strength together with the tensile breaking strength 'stretch breaking elongation and tear strength. (7) Impact resistance After the bag is processed into a bag of any size, water of 1/2 capacity of the full volume is placed, and the upper and lower sides vibrate vigorously, and the bottom is peeled off or the bag body is cracked. Further, the impact resistance of Example 3 was 15 or more, and it was sufficiently tolerated. (8) Burning calories The calories burned from the raw materials used for review, namely, polylactic acid 19 KJ/g, polyethylene 46 KJ/g, modified polyalkenyl 46 KJ/g, were theoretically calculated by the following formula. Burning calories (Kj/g): = 19χΧ + 46χΥ + 46χΖ/1()() 1001401#^'^ 0101 Page 18 of 23 1013006142-0 201221579 where X is the mass of polylactic acid resin, γ: The mass portion of the dilute base resin ζ: the mass portion of the modified polyalkenyl compound (9) The amount of C0 generated during combustion C* The amount of C〇2 produced during combustion is calculated for each of the films formed in the examples and comparative examples. The amount of C〇2 produced by lkg. The calculation method is based on rHealth Digest. 14( 1 ). 1 (1 999, Ohara Haruko), according to the "(2) (from the chemical structure). Calculated by the 〇2 production amount calculation method. The calculation method is as follows. C〇2 production amount (kg-C〇2/kg-Resin) = (component quantity from petrochemical resources) x3kg/c〇+ (from biomass energy

LL

之成分量)x2kg/CO L» 進而言之,若依據「Health Digest. 14(1). 1 (1999、 小原仁時著)」之「塑膠氧化分解時所產生的c〇量(來自 化學構造的部分)」,LLDPE、LDPE、HDPE等聚乙烯在燃 燒時之0〇2產生量係對於每ikg為3. Okg,因此從以下計 算式算出實施例1〜4、比較例1〜5所獲得之成形品之每 lkg之C〇2產生刪減率(%)。 c〇2產生刪減率(%) = 100-((實施例、比較例組成之c〇產生/3 〇kg/c〇 )χThe amount of the component) x2kg/CO L» In other words, according to "Health Digest. 14(1). 1 (1999, Ohara Hara)" "The amount of c〇 produced by plastic oxidative decomposition (from chemical structure) In the case of the LLDPE, the LDPE, the HDPE, and the like, the amount of the generated amount of the polyethylene is 3. Okg per ikg. Therefore, the examples 1 to 4 and the comparative examples 1 to 5 are obtained from the following calculation formula. The C 〇 2 per lkg of the molded article produced a cut-off rate (%). C〇2 produces a cut-off rate (%) = 100-((Example, comparative example, c〇 generation / 3 〇kg/c〇)χ

^ L 100} 上述實施例1〜4包含實施本發明所必需條件,即聚乳酸 樹脂、聚烯基系樹脂、改質聚烯基系化合物之組合之三 成分’聚乳酸樹脂為4. 5〜30質量!,聚烯基樹脂為25〜 93. 0質量% ’改質聚烯基系化合物為2. 5〜45質量%,相 對於聚乳酸樹脂’改質聚烯基系化合物含〇. 25倍以上、 1013006142-0 10014014#單編號A〇1〇l 第19頁/共23頁 201221579 小於1. 5倍,且按照以總量100%製膜之條件而製作。 依據表1、2之結果,上述實施例1〜4係除了含來自植物 之樹脂成分之生物質能型膠膜之成形安定以外,顯然機 械性強度、耐衝擊性亦良好,亦可達成c〇2刪減。 另,相對於聚乳酸樹脂,改質聚烯基系化合物含小於 0. 2 5倍之比較例1,其喷出安定量或製膜安定性雖為較良 好的狀況,但於成形所獲得的膠膜表面,觀察到樹脂不 均,外觀上亦不適宜,耐衝擊性為5次以下,發生破損。 比較例2的情況雖未觀察到膠膜表面之樹脂不均,相溶性 良好,但C〇2刪減效果不足。比較例3的情況係於膠膜層 間觀察到層間剝離現象,並且亦未觀察到膠膜表面之光 澤性,不具備本發明之作為來自植物之樹脂成分之生物 質能型膠膜之特性。又,於比較例3,耐衝擊性在10次以 下發生破損,c〇2刪減效果亦不足。 比較例4之C〇2刪減效果雖大,但於成形時觀察到傾向在 部分產生皺褶,隨著聚乳酸樹脂成分增加,改質聚烯基 化合物成分的比率亦傾向增加,因此原料成本增加,相 對於聚烯基樹脂價格為2. 5倍以上。又,於比較例4,耐 衝擊性在10次以下發生破損。比較例5的情況完全未獲得 c〇2刪減效果。 再者,本發明並未直接限定於上述實施形態,於實施階 段,可於不脫離其要旨的範圍内,將構成要素予以變形 而具體化。又,可藉由適當組合上述實施形態所揭示的 複數個構成要素,來形成各種發明。例如實施形態之聚 乳酸及聚烯基系組成物係藉由吹氣法而成形的情況,但 不限定於此。進而言之,亦可適當組合不同實施形態間 1001401#^^^ A〇101 第20頁/共23頁 1013006142-0 201221579 之構成要素。 【圖式簡單說明】 [0007] 無。 【主要元件符號說明】 [0008] 無。5〜 The poly- lactic acid resin of the combination of the polylactic acid resin, the polyalkenyl resin, and the modified polyalkenyl compound is 4. 5~ The quality of the modified polyalkenyl compound is 2. 5~45 mass%, relative to the polylactic acid resin, the modified polyalkenyl compound contains 〇. 25 More than 10 times, 1013006142-0 10014014# Single number A〇1〇l Page 19 of 23201221579 Less than 1.5 times, and made according to the conditions of 100% of the total film formation. According to the results of Tables 1 and 2, the above Examples 1 to 4 are excellent in mechanical strength and impact resistance in addition to the formation stability of the biomass-type adhesive film containing the resin component derived from the plant, and can also be achieved. 2 cuts. Further, with respect to the polylactic acid resin, the modified polyalkenyl compound contains less than 0.25 times Comparative Example 1, although the discharge safety amount or film stability is relatively good, but obtained by molding. On the surface of the film, unevenness in resin was observed, and the appearance was also unsuitable, and the impact resistance was 5 or less, and breakage occurred. In the case of Comparative Example 2, the resin unevenness on the surface of the film was not observed, and the compatibility was good, but the C〇2 reduction effect was insufficient. In the case of Comparative Example 3, the interlayer peeling phenomenon was observed between the film layers, and the glossiness of the surface of the film was not observed, and the properties of the bioenergy film which is a resin component derived from plants of the present invention were not provided. Further, in Comparative Example 3, the impact resistance was broken 10 times or less, and the c〇2 reduction effect was also insufficient. In Comparative Example 4, the C〇2 reduction effect was large, but it was observed that wrinkles were partially formed during molding, and as the polylactic acid resin component increased, the ratio of the modified polyalkenyl compound component also tends to increase, so the raw material cost 5倍以上。 The price is more than 2.5 times. Further, in Comparative Example 4, the impact resistance was broken 10 times or less. In the case of Comparative Example 5, the c〇2 deletion effect was not obtained at all. Further, the present invention is not limited to the above-described embodiments, and constituent elements may be modified and embodied in the scope of the invention without departing from the spirit and scope of the invention. Further, various inventions can be formed by appropriately combining a plurality of constituent elements disclosed in the above embodiments. For example, the polylactic acid and the polyalkenyl-based composition of the embodiment are formed by a blowing method, but are not limited thereto. In other words, it is also possible to appropriately combine the components of different embodiments between 1001401#^^^ A〇101 page 20/23 pages 1013006142-0 201221579. [Simple description of the schema] [0007] None. [Main component symbol description] [0008] None.

1Q()14()14f單編號A0101 第21頁/共23頁 1013006142-01Q()14()14f单单A0101 Page 21 of 23 1013006142-0

Claims (1)

201221579 七、申請專利範圍: 1 . 一種聚乳酸及聚烯基系組成物,其特徵為:總量成為100 質量%而含有聚乳酸樹脂4. 5〜30質量%、聚烯基樹脂25〜 93. 0質量%及改質聚烯基化合物2. 5〜45質量%;前述改 質聚烯基化合物係相對於前述聚乳酸樹脂含有0. 25倍以 上、小於1. 5倍。 2 .如申請專利範圍第1項之聚乳酸及聚烯基系組成物,其中 前述聚烯基樹脂為聚乙烯樹脂;該聚乙烯樹脂係相對於前 述聚乳酸樹脂含有0. 91倍以上、20. 7倍以下。 3 .如申請專利範圍第1或2項之聚乳酸及聚烯基系組成物,其 中前述聚乳酸樹脂係將植物澱粉予以乳酸化或聚合而獲得 之樹脂。 10014014^^'^^° A〇101 第22頁/共23頁 1013006142-05〜30质量%的聚烯树脂25〜93 The polylactic acid resin is contained in an amount of 100% by mass and contains polylactic acid resin 4. 5~30% by mass, polyalkenyl resin 25~93倍倍。 The 5% or more, less than 1.5 times the amount of the polylactic acid resin. 2倍以上的20。 The poly lactic acid resin is 0. 91 times or more, 20 . 7 times or less. 3. The polylactic acid and polyalkenyl composition according to claim 1 or 2, wherein the polylactic acid resin is a resin obtained by lactating or polymerizing plant starch. 10014014^^'^^° A〇101 Page 22 of 23 1013006142-0
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