TWI628227B - Cross-linking composite high-performance ABS/PLA environmentally friendly green material preparation method - Google Patents

Cross-linking composite high-performance ABS/PLA environmentally friendly green material preparation method Download PDF

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TWI628227B
TWI628227B TW104118837A TW104118837A TWI628227B TW I628227 B TWI628227 B TW I628227B TW 104118837 A TW104118837 A TW 104118837A TW 104118837 A TW104118837 A TW 104118837A TW I628227 B TWI628227 B TW I628227B
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pla
abs
twin
chain extender
molecular weight
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TW201643220A (en
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巫昇炎
張志仁
鍾曜竹
張燮永
陳建明
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喬福泡綿股份有限公司
財團法人工業技術研究院
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Abstract

一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,係包含有:高分子量PLA30%或50%,ABS40或60%,增韌劑8%,擴鏈劑1%,ABS回收塑料1%,高分子量PLA裂解,擴鏈反應,耐水解設計,製程中確實除水,利用PLA之COOH-OH末端,以MAH、GMA等官能化添加劑進行封端改質,因ABS加工溫度200~230℃,MI 200℃ 5kg:2g/10min,PLA加工溫度170~200℃,MI 190℃ 2.16kg:8g/10min,再將製程以雙螺桿組態之方式,進行適當混煉,並利用具有流變控制與相容劑作用的擴鏈劑,改變高分子量PLA之流變質,溫度與剪切,使其得進行形態控制,增韌劑可有效提升物性,得進行增韌改質。 A cross-linking composite high-performance ABS/PLA green raw green material preparation method comprises: high molecular weight PLA 30% or 50%, ABS 40 or 60%, toughener 8%, chain extender 1%, ABS recycled plastic 1%, high molecular weight PLA cracking, chain extension reaction, hydrolysis resistance design, water removal in the process, using COOH-OH end of PLA, with MAH, GMA and other functional additives for end-end modification, due to ABS processing temperature 200~ 230°C, MI 200°C 5kg: 2g/10min, PLA processing temperature 170~200°C, MI 190°C 2.16kg: 8g/10min, and then the process is mixed in a twin-screw configuration, and the flow is utilized. The chain extender controlled by the variable control and the compatibilizer can change the flow deterioration of the high molecular weight PLA, the temperature and the shear, so that the shape control can be performed, and the toughening agent can effectively improve the physical properties, and the toughening and upgrading can be performed.

Description

交聯複合型高性能ABS/PLA環保生質綠材製備方法 Cross-linking composite high-performance ABS/PLA environmentally friendly green material preparation method

本發明提供一種ABS/PLA合金之技術領域,尤指其技術上提供一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,其ABS高膠粉與PLA樹脂通過共混擠出,製備了ABS高膠粉/PLA共混合金之高分子合金技術。 The invention provides a technical field of ABS/PLA alloy, in particular to a method for preparing a cross-linked composite high-performance ABS/PLA environment-friendly green material, wherein ABS high-poly powder and PLA resin are blended and extruded. A polymer alloy technology of ABS high rubber powder/PLA blend alloy was prepared.

PLA(聚乳酸)習知特性:市場上電子產品所使用之塑料主要為石化系HIPS、ABS、PC/ABS及PC樹脂等生質來源的產品。若要取代上述石化塑料,往往有許多問題需克服,以市面上產量最大的主流生質塑膠PLA為例,應用於耐久性電子產品材料主要的挑戰點有:(1)未結晶PLA的耐熱性僅在60℃左右,不僅無法通過電子產品的環境測試,甚至達海運的最低耐熱條件都無法達到;(2)經過結晶處理的PLA雖然耐熱性可達100℃以上,但目前仍有射出成型週期(Cycle Time)過長,造成生產效率低的問題,另外還有尺寸安定性不佳、成型收縮等問題仍需克服;(3)PLA為剪切敏感材料,熔融強度不佳導致加工點度過稀的問題時常發生,分子量的快速下降也是回收不易的主因;(4)與 PC、ABS等常用電子產品外殼用材料相比,PLA的韌性或耐衝撃強度不佳,僅舆壓克力相近,純PLA製品通常較容易損壞,並不適合用於高價電子產品;(5)由於生物分解/易水解的特性,使用壽命受到限制;(6)成本問題(如表一所示),目前PLA的售價仍較高,但石化原料不斷地飆漲與合成技術的持續改良,此消彼長之下,預估PLA的原料售價將在未來十年趨近於ABS、PS、PP等石化塑膠,而價格更低廉的TPS應用技術也持續發展。 PLA (polylactic acid) conventional characteristics: The plastics used in electronic products on the market are mainly petrochemical products such as HIPS, ABS, PC/ABS and PC resins. To replace the above-mentioned petrochemical plastics, there are often many problems to be overcome. Take the largest mainstream plastic PLA on the market as an example. The main challenges for durable electronic products are: (1) Heat resistance of uncrystallized PLA Only at about 60 °C, not only can not pass the environmental test of electronic products, even the lowest heat-resistant conditions of shipping can not be achieved; (2) PLA has been heat-treated up to 100 °C, but there is still injection molding cycle (Cycle Time) is too long, resulting in low production efficiency, in addition to poor dimensional stability, molding shrinkage and other issues still need to be overcome; (3) PLA is a shear sensitive material, the melting strength is poor, the processing point is spent Dilute problems often occur, and the rapid decline of molecular weight is also the main cause of recovery; (4) and Compared with PC, ABS and other common electronic products, PLA's toughness or impact strength is not good, only the pressure is similar, pure PLA products are usually more susceptible to damage, not suitable for high-priced electronic products; (5) because Biodegradation/easy hydrolysis characteristics, limited service life; (6) Cost problem (as shown in Table 1), the current price of PLA is still high, but petrochemical raw materials continue to soar and synthetic technology continues to improve, this Under the circumstance, it is estimated that the price of PLA raw materials will approach petrochemical plastics such as ABS, PS and PP in the next decade, and the cheaper TPS application technology will continue to develop.

生質合膠技術:高分子合膠即兩種或兩種以上的高分子直接以熔融加工的方式混摻成均勻的單一材料,宛如合金一般,因此也稱之為高分子合金。高分子奈米複合材料領域中,奈米合膠與有機-無機奈米複合材料之最大不同點在於,奈米合膠會因為所選擇的系統、組成、添加 劑及加工條件的不同而產生獨特的相行為,如兩相高分子產生的共連續相結構,不僅能使複材同時具有兩種高分子的特性,有時更能產生協同作用(Synergistic Effect),其性能比其中任一相更佳,雖然純嵌段共聚合物(Block Copolymer)也能夠有以上特性,但通常合膠的經濟效益遠大於合成新的高分子。 Biomass compounding technology: polymer glue, that is, two or more kinds of polymers are directly mixed into a uniform single material by melt processing, which is like an alloy. Therefore, it is also called a polymer alloy. In the field of polymer nanocomposites, the biggest difference between nano-gels and organic-inorganic nanocomposites is that nano-gels are selected because of the system, composition, and addition. Different phase behaviors due to different agents and processing conditions, such as the co-continuous phase structure produced by the two-phase polymer, can not only make the composite material have the characteristics of two polymers at the same time, but sometimes produce synergistic effects (Synergistic Effect). The performance is better than any of the phases. Although the block copolymer can also have the above characteristics, the economic benefit of the gel is generally greater than that of the new polymer.

透過混煉加工將生質塑膠高性能化的主要方法有:(1)與植物纖維混煉;(2)與各種添加劑混煉;(3)與石油系塑膠混煉成生質合膠等方法。生質合膠的設計以石油樹膠為主要基材,形成海綿狀的網狀結構,使易水解、分解之生質材料得以受到包覆,並提供主要的機械強度,因此生質合膠之耐久性與現有材料無異,目前市面上有許多產品也能通過電子產品所要求的環境測試。 The main methods for improving the quality of raw plastics through mixing and processing are: (1) mixing with plant fibers; (2) mixing with various additives; (3) mixing with petroleum-based plastics into raw rubber and other methods. . The design of the raw rubber is based on petroleum gum as the main substrate, forming a sponge-like network structure, which allows the easily hydrolyzed and decomposed raw materials to be coated and provides the main mechanical strength, so the endurance of the raw rubber is durable. Sex is no different from existing materials. There are many products on the market that can pass the environmental tests required by electronic products.

聚乳酸(PLA)具有良好的強度和剛性,但柔軟性和抗衝擊性能較差,常溫下是一種硬而脆的材料,如要實現如聚丙烯(PP)、聚苯乙烯(PS)和聚對笨二甲酸乙二醇酯(PET)等材料在薄膜、片材、瓶子及各種熱成型品和注塑品上的廣泛應用,必須對PLA進行增韌改性丙烯腈-丁二烯-苯乙烯共聚物(ABS)具有耐衝擊、表面硬度高、耐化學藥品及電性能良好、易於加工成形等優點。但PLA和通用ABS樹脂為不相容體系,兩者共混體系的可加工性、物理機械性能很差。目前,國內外關於ABS/PLA共混的研究報導較 少。ABS高膠粉為高橡膠相(PB橡膠粒子)含量的韌性材料,具有比ABS更好的韌性,並於多種聚合物有較好的相容效果,如果能夠將PLA與ABS高膠粉很好的混合,得到相容性較好的共混體系,即能得到高韌性的PLA複合材料,又可以簡化工藝路線,降低成本。 Polylactic acid (PLA) has good strength and rigidity, but has poor flexibility and impact resistance. It is a hard and brittle material at room temperature, such as polypropylene (PP), polystyrene (PS) and poly. For the wide application of materials such as polyethylene glycol diester (PET) in films, sheets, bottles and various thermoformed and injection molded products, it is necessary to toughen and modify acrylonitrile-butadiene-styrene copolymerization of PLA. The material (ABS) has the advantages of impact resistance, high surface hardness, good chemical and electrical resistance, and easy processing. However, PLA and general-purpose ABS resins are incompatible systems, and the processability and physical and mechanical properties of the blend systems are poor. At present, the research reports on ABS/PLA blending at home and abroad are more less. ABS high rubber powder is a tough material with high rubber phase (PB rubber particle) content. It has better toughness than ABS and has good compatibility with various polymers. If it can be used, PLA and ABS high rubber powder are very good. The mixing method can obtain a blending system with better compatibility, that is, a high toughness PLA composite material can be obtained, and the process route can be simplified and the cost can be reduced.

習知技術如中國專利申請號第201310310723.7號「一種製造ABS/PLA合金材料用的大分子相容劑的製備方法」,其提及所述的相容劑是由苯乙烯類物質5-40、環氧類0.5-10、引發劑類0.1-5通過本體聚合,溶液聚合或懸浮聚合得到的共聚物。該共聚物與短鏈PLA熔融共混,其中短鏈PLA質量分數為1-95,得到大分子相容劑,該相容劑基於梳型大分子的結構,利用主鏈的聚苯乙烯結構提高了與ABS的相容性,而支鏈的聚乳酸鏈段又提高了與聚乳酸相的相容性,對ABS與PLA兩相的增容起到很好的作用,能大幅提高共混物的力學性能,熔體穩定性和加工性能,其中短鏈PLA可以使用工業PLA回料代替,降低了生產,提高材料利用率,節約能源。 A conventional technique such as Chinese Patent Application No. 201310310723.7 "Manufacturing Method of Macromolecular Compatibilizer for ABS/PLA Alloy Material", which mentions that the compatibilizer is composed of styrene substances 5-40, A copolymer obtained by bulk polymerization, solution polymerization or suspension polymerization of epoxy type 0.5-10, initiator type 0.1-5. The copolymer is melt-blended with short-chain PLA, wherein the short-chain PLA mass fraction is 1-95, and a macromolecular compatibilizer is obtained, which is based on the structure of the comb-type macromolecule and is improved by the polystyrene structure of the main chain. The compatibility with ABS, and the branched polylactic acid segment improves the compatibility with the polylactic acid phase, and plays a good role in the compatibilization of the two phases of ABS and PLA, which can greatly improve the blend. The mechanical properties, melt stability and processing properties, of which short-chain PLA can be replaced by industrial PLA, reduce production, improve material utilization and save energy.

是以,針對上述習知結構所存在之問題點,如何開發一種更具理想實用性之創新結構,實消費者所殷切企盼,亦係相關業者須努力研發突破之目標及方向。 Therefore, in view of the problems existing in the above-mentioned conventional structure, how to develop an innovative structure that is more ideal and practical, the consumers are eagerly awaiting, and the relevant industry must strive to develop the goal and direction of breakthrough.

有鑑於此,發明人本於多年從事相關產品之製造開發與設計經驗,針對上述之目標,詳加設計與審慎評 估後,終得一確具實用性之本發明。 In view of this, the inventor has been engaged in the manufacturing development and design experience of related products for many years, and has designed and carefully evaluated the above objectives. After the evaluation, the invention is finally practical.

本發明之主要目的在於提供一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,其ABS高膠粉與PLA樹脂通過共混擠出,製備了ABS高膠粉/PLA共混合金。 The main object of the present invention is to provide a cross-linking composite high-performance ABS/PLA environmentally-friendly green material preparation method, wherein ABS high-adhesive powder/PLA blend alloy is prepared by blending and extruding ABS high-adhesive powder and PLA resin. .

為達上述目的,本發明提供一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,係包含有:高分子量PLA30或50%,ABS40或60%,增韌劑8%,擴鏈劑1%,ABS回收塑料1%,高分子量PLA裂解,擴鏈反應,耐水解設計,製程中確實除水,利用PLA之COOH-OH末端,以MAH、GMA等官能化添加劑進行封端改質,因ABS加工溫度200~230℃,MI 200℃ 5kg:2g/10min,PLA加工溫度170~200℃,MI 190℃ 2.16kg:8g/10min,再將製程以雙螺桿組態之方式,進行適當混煉,並利用具有流變控制與相容劑作用的擴鏈劑,改變高分子量PLA之流變質,溫度與剪切,使其得進行形態控制,增韌劑可有效提升物性,得進行增韌改質。 In order to achieve the above object, the present invention provides a method for preparing a cross-linked composite high-performance ABS/PLA environmentally friendly green material, which comprises: high molecular weight PLA 30 or 50%, ABS 40 or 60%, toughener 8%, chain extension 1%, ABS recycled plastic 1%, high molecular weight PLA cracking, chain extension reaction, hydrolysis resistance design, water removal in the process, using COOH-OH end of PLA, with MAH, GMA and other functional additives for end-end modification , because ABS processing temperature is 200~230°C, MI 200°C 5kg: 2g/10min, PLA processing temperature is 170~200°C, MI 190°C 2.16kg: 8g/10min, and then the process is carried out in a twin-screw configuration. Mixing, and using the chain extender with rheology control and compatibilizer to change the flow deterioration of high molecular weight PLA, temperature and shear, so that it can be controlled by morphology, and the toughening agent can effectively improve the physical properties. Toughness modification.

有關本發明所採用之技術、手段及其功效,茲舉一較佳實施例並配合圖式詳細說明於後,相信本發明上述之目的、構造及特徵,當可由之得一深入而具體的瞭解。 The above-mentioned objects, structures and features of the present invention will be described in detail with reference to the preferred embodiments of the present invention. .

10‧‧‧混煉加工範圍 10‧‧‧Knife processing range

CE-1‧‧‧PLA+擴鏈劑-1 CE-1‧‧‧PLA+ chain extender-1

CE-2‧‧‧PLA+擴鏈劑-2 CE-2‧‧‧PLA+ Chain Extender-2

CE-3‧‧‧PLA+擴鏈劑-3 CE-3‧‧‧PLA+ chain extender-3

CE-4‧‧‧PLA+擴鏈劑-4 CE-4‧‧‧PLA+ chain extender-4

AP-107‧‧‧合金代號 AP-107‧‧‧ alloy code

AP-113‧‧‧合金代號 AP-113‧‧‧ alloy code

AP-114‧‧‧合金代號 AP-114‧‧‧ alloy code

AP-140‧‧‧合金代號 AP-140‧‧‧ alloy code

AP-146‧‧‧合金代號 AP-146‧‧‧ alloy code

AP-150‧‧‧合金代號 AP-150‧‧‧ alloy code

第一圖係為MBS樹脂結構示意圖。 The first figure is a schematic diagram of the structure of the MBS resin.

第二圖係PLA之COOH-OH末端以官能化添加劑進行封端改質之示意圖。 The second figure is a schematic diagram of the end-capping modification of the COOH-OH end of PLA with a functionalized additive.

第三圖係擴鏈劑對PLA增黏性能比較示意圖。 The third figure is a schematic diagram comparing the viscosity-increasing properties of the chain extender on PLA.

第四圖係四種擴鏈劑之形態變化示意圖。 The fourth figure is a schematic diagram of the morphological changes of four chain extenders.

第五圖係ABS/PLA合金配方圖。 The fifth figure is the ABS/PLA alloy formula.

第六圖係ABS/PLA合金成品顯微照片示意圖。 The sixth picture is a schematic photomicrograph of the finished ABS/PLA alloy.

第七圖係為螺桿組態圖。 The seventh picture is the screw configuration diagram.

本發明係提供一種交聯複合型高性能ABS/PLA環保生質綠材製備方法之設計者。 The invention provides a designer of a cross-linking composite high-performance ABS/PLA environment-friendly green material preparation method.

為使 貴審查委員對本發明之目的、特徵及功效能夠有更進一步之瞭解與認識,茲配合實施方式及圖式詳述如後:熱熔融指數(MI):熔融指數是一種表示塑膠材料加工時流動性的指標。MI值越大表示此塑膠材料之加工流動性越好,反之,則越差。最常見之測試標準為ASTMD1238。MI值可作為判斷塑膠分子量高低的參考。物性和加工性的取捨。在設定的壓力和溫度下,將樣品置入一固定直徑和長度的模頭,測量單位時間內流出的重量(g/10min)表示材料的流動性。MI(g/10min)=收集樣品重(g)/ 收集時間(sec)×600sec。 In order to enable your review committee to have a better understanding and understanding of the purpose, features and effects of the present invention, the implementation method and the drawings are detailed as follows: Thermal Melt Index (MI): The melt index is a representation of the processing of plastic materials. Indicator of liquidity. The larger the MI value, the better the processing fluidity of the plastic material, and vice versa. The most common test standard is ASTM D1238. The MI value can be used as a reference for judging the molecular weight of the plastic. Material and processing trade-offs. The sample was placed in a fixed diameter and length die at a set pressure and temperature, and the weight (g/10 min) flowing out per unit time was measured to indicate the fluidity of the material. MI (g/10min) = collected sample weight (g) / Collection time (sec) × 600 sec.

MMA:甲基丙烯酸甲酯(methyl methacrylate,MMA)是一種有機物,分子式為CH2=C(CH3)COOCH3,無色液體,是將甲基丙烯酸(MAA)與甲醇經酯化形成的,它是生產透明塑料聚甲基丙烯酸甲酯(PMMA)的單體。 MMA: methyl methacrylate (MMA) is an organic compound with the formula CH2=C(CH3)COOCH3, a colorless liquid formed by esterification of methacrylic acid (MAA) with methanol. A monomer of plastic polymethyl methacrylate (PMMA).

MAA:甲基丙烯酸(MAA),結構式H2C=C(CH3)COOH,甲基丙烯酸在常溫下為無色透明液體。易溶於熱水、乙醇和大多數有機溶劑。易聚合。其蒸氣可與空氣形成爆炸性混合物。具中等毒性,對皮膚和粘膜有較強的刺激性,但未見致癌現象。 MAA: methacrylic acid (MAA), structural formula H2C=C(CH3)COOH, methacrylic acid is a colorless transparent liquid at normal temperature. Soluble in hot water, ethanol and most organic solvents. Easy to aggregate. Its vapor can form an explosive mixture with air. It is moderately toxic and has strong irritation to skin and mucous membranes, but no carcinogenicity.

ST:苯乙烯(styrol,ST)。 ST: Styrene (ST).

GMA:甲基丙烯酸縮水甘油酯,與PLA上的酸基(-COOH)及氫氧基(-OH)官能基產生化學反應,進行封端改質。 GMA: glycidyl methacrylate, which chemically reacts with the acid group (-COOH) and hydroxyl (-OH) functional groups on PLA to carry out end-capping modification.

EMA:甲基丙烯酸乙酯。 EMA: Ethyl methacrylate.

擴鏈劑為MMA-MAA-St-GMA-EMA copolymer。 The chain extender is MMA-MAA-St-GMA-EMA copolymer.

ABS:丙烯腈-丁二烯-苯乙烯共聚物(Acrylonitrile Butadiene Styrene,ABS),耐衝擊強度高、韌性佳。 ABS: Acrylonitrile Butadiene Styrene (ABS), high impact strength and good toughness.

PLA:聚乳酸(Polylactic acid,PLA),熱塑性材料,具生物可分解性,可分解為水與二氧化碳。 PLA: Polylactic acid (PLA), a thermoplastic material that is biodegradable and decomposes into water and carbon dioxide.

MI:熔融指數,英文名稱為melt index,將塑 膠材料置於一鐵管,並依一定溫度(℃)與荷重(1200g、2160g、5000g)下,於10分鐘內所流出之塑膠材料重量,是ASTM(悟性檢測規範)D1238所訂測試標準。 MI: Melt index, English name is melt index, will be plastic The weight of the plastic material flowing out in an iron pipe at a certain temperature (°C) and load (1200g, 2160g, 5000g) within 10 minutes is the test standard set by ASTM (Perspective Test Specification) D1238.

MAH:馬來酸酐官能基,與PLA上的酸基(-COOH)及氫氧基(-OH)官能基產生化學反應,進行封端改質。 MAH: A maleic anhydride functional group that undergoes a chemical reaction with an acid group (-COOH) and a hydroxyl (-OH) functional group on PLA to carry out end-capping modification.

由於PLA屬於水性,ABS屬於油性,需加入能將兩者結合的官能基,這就是官能化,而擴鏈劑就是一種含有官能基的媒介,這種反應,就如同肥皂一樣,由擴鏈劑將水相及油相結合,用來解決PLA的加工溫度,耐水解及耐剪切力。 Since PLA is water-based, ABS is oily, and it is necessary to add a functional group that can combine the two. This is functionalization, and the chain extender is a medium containing a functional group. This reaction is like a soap. The water phase and the oil phase are combined to solve the processing temperature of the PLA, hydrolysis resistance and shear resistance.

生質材料PLA反應改質技術,本發明將會從聚酯系融熔加工時產生的熱分解、水解及材料本身的分子量等導致材料黏度過稀的三方面來著手。 The raw material PLA reaction modification technology, the present invention will start from the three aspects of thermal decomposition, hydrolysis, and the molecular weight of the material itself caused by the melt melting of the polyester system.

(1)PLA裂解與水解問題:酯類生質塑膠PLA之末端酸基為造成加工過程中分子量下降的主因,由於高分子斷鏈將產生更多的末端酸基,使得裂解反應更加速進行。因此為了減少末端酸基,除了製程中需確實除水外,在一開始就使用高分子量的PLA可以有效改善裂解情形,最終在本發明也會導入耐水解配方,增加終端產品應用的壽命。 (1) PLA cracking and hydrolysis problem: The terminal acid group of the ester-based plastic PLA is the main cause of the molecular weight drop during processing. The polymer chain scission will generate more terminal acid groups, which makes the cracking reaction more accelerated. Therefore, in order to reduce the terminal acid group, in addition to the need to reliably remove water in the process, the use of high molecular weight PLA can effectively improve the cracking situation at the beginning, and finally the hydrolysis-resistant formulation is also introduced in the present invention to increase the service life of the terminal product.

(2)加工視窗差異:ABS與PLA之加工視窗差異 如下,ABS加工溫度200~230℃,MI 200℃ 5kg:2g/10min為ABS之MI值,指受壓重5kg情況下,10分鐘內所流出之塑膠材料重量2g,ABS需在200~230℃加工,其熔融黏度高,PLA加工溫度170~200℃,MI 190℃ 2.16kg:8g/10min為PLA之MI值,指受壓重2.16kg情況下,10分鐘內所流出之塑膠材料重量8g,而PLA加工溫度為170~200℃,並且加工黏度與melt strength(熔體強度)皆較低,若不改善會使複合材料的domain size(相區尺寸)過大,造成物性快速下降。為了克服此問題:除了需使用合適的螺桿組態、溫度、剪切力進行熔融混煉外,PLA的分子量需要再進一步的提高,以提升熔融黏度。ABS將使用流變改質配方,進一步拉近兩相高分子的黏度與加工視窗差異,改善混煉品質。 (2) Processing window difference: difference between processing window of ABS and PLA As follows, ABS processing temperature is 200~230°C, MI 200°C 5kg: 2g/10min is the MI value of ABS, which means that the weight of plastic material flowing out within 10 minutes under the pressure of 5kg is 2g, and the ABS needs to be 200~230°C. Processing, its melt viscosity is high, PLA processing temperature is 170~200°C, MI 190°C 2.16kg: 8g/10min is the MI value of PLA, which means that the weight of plastic material flowing out within 10 minutes is 8g under the pressure of 2.16kg. The processing temperature of PLA is 170~200°C, and the processing viscosity and melt strength are both low. If it is not improved, the domain size of the composite will be too large, which will cause the physical property to drop rapidly. In order to overcome this problem: in addition to the need to use the appropriate screw configuration, temperature, shear force for melt mixing, the molecular weight of PLA needs to be further improved to improve the melt viscosity. ABS will use a rheological modification formula to further narrow the viscosity of the two-phase polymer and the processing window to improve the mixing quality.

(3)兩相相容問題:ABS為親油性高分子,而PLA相較之下為親水,排斥的兩相將會大幅降低整體韌性。已知PLA與PMMA之相容性良好,若能使用如第一圖之MBS樹脂,或是利用PLA之末端反應之多官能反應型添加劑,這兩種添加劑之結構與ABS相近,若能利用該類添加劑對PLA進行改質,將有效提升ABS與PLA兩相的相容性,並進一步提升物性。 (3) Two-phase compatibility problem: ABS is a lipophilic polymer, while PLA is hydrophilic, and the two phases of rejection will greatly reduce the overall toughness. It is known that the compatibility between PLA and PMMA is good. If the MBS resin as shown in the first figure or the polyfunctional reaction type additive using the terminal reaction of PLA is used, the structure of the two additives is similar to that of ABS. The modification of PLA by the additive will effectively improve the compatibility of the two phases of ABS and PLA, and further enhance the physical properties.

本發明將使用反應押出的方式,同時克服水解問題,並增加兩相相容性,其技術內容如上圖所示,PLA具有較高的酸價/醇價,末端官能基容易提供活性H+,引發 高分子水解斷鏈,本發明將使用德國添加劑技術,利用一種具多環氧官能基的反應型相容劑,與高分子末端羧基進行End-capping(封端),除了增加分子量以外,也可作為水解穩定劑,並增進兩相間的相容性。當PLA進行熔融加工,尤其是與加工溫度較高之工程塑膠ABS相混製備成生質複材時,其末端酸基會攻擊主鏈,進而產生更多的末端酸基,這時若使用可與酸基反應之添加劑,除了可防止PLA之分子量快速下降以外,更可以進一步產生擴鏈作用,增加分子量、加工黏度與相容性。此類添加劑之大量的Glycidyl methacrylate(甲基丙烯酸縮水甘油酯)官能基能夠與混煉過程中斷鏈的PLA進行反應,進而達到黏度調控的目的。在混煉研究中,將設計適當流變性之PLA與正確規格之ABS加以配對,模擬並評估兩相高分子之最佳加工窗口為剪切分散或是拉伸流動分散,利用TSE/SSE(雙螺桿擠出機/單螺桿擠出機)搭配EFM(拉伸流動攪拌機)製造出強度足夠之ABS/PLA合金材料。 The present invention will use the reaction ejecting method while overcoming the hydrolysis problem and increasing the compatibility of the two phases. The technical content thereof is as shown in the above figure, PLA has a higher acid value/alcohol value, and the terminal functional group easily provides active H+, which is triggered. Polymer hydrolysis chain scission, the present invention will use German additive technology, using a reactive compatibilizer with multiple epoxy functional groups, and End-capping with the terminal carboxyl group of the polymer, in addition to increasing the molecular weight, As a hydrolysis stabilizer, and improve the compatibility between the two phases. When PLA is melt processed, especially when mixed with engineering plastic ABS with high processing temperature to prepare a composite material, the terminal acid group will attack the main chain, which will generate more terminal acid groups. The acid-based reaction additive can further prevent the molecular weight of the PLA from rapidly decreasing, and further increase the molecular weight, processing viscosity and compatibility. A large amount of Glycidyl methacrylate (glycidyl methacrylate) functional group of such additives can react with the PLA in the chain of the mixing process to achieve viscosity control. In the mixing study, the appropriate rheological PLA is paired with the correct specification of ABS to simulate and evaluate the optimal processing window of the two-phase polymer for shear dispersion or tensile flow dispersion, using TSE/SSE (double Screw Extruder / Single Screw Extruder) EFM (Stretched Flow Mixer) is used to produce ABS/PLA alloy materials of sufficient strength.

本發明提供一種交聯複合型高性能PLA-ABS環保生質綠材製備方法,係包含有:PLA裂解,PLA裂解減少末端酸基,使用高分子量PLA,擴鏈反應,耐水解設計,製程中確實除水,利用PLA之COOH-OH末端以MAH或GMA等官能化添加劑進行封端改質(如第二圖所示)。製程上採用雙螺桿組態設計,適 當混煉溫度與剪切,並使用高分子量PLA,流變改質配方,其中其一螺桿中ABS加工溫度為200~230℃,熔融指數(MI)200℃,5kg:2g/10min,另一螺桿中PLA加工溫度為170~200℃,熔融指數(MI)190℃,2.16kg:8g/10min。 The invention provides a cross-linking composite high-performance PLA-ABS environmentally-friendly green material preparation method, which comprises: PLA cracking, PLA cracking to reduce terminal acid groups, using high molecular weight PLA, chain extension reaction, hydrolysis resistance design, and process Indeed, in addition to water, the COOH-OH end of the PLA is end-capped with a functional additive such as MAH or GMA (as shown in the second figure). The process adopts twin-screw configuration design, suitable When the mixing temperature and shearing, and the use of high molecular weight PLA, rheology modification formula, in which a screw processing ABS processing temperature is 200 ~ 230 ° C, melt index (MI) 200 ° C, 5kg: 2g/10min, another The processing temperature of the PLA in the screw is 170-200 ° C, the melt index (MI) is 190 ° C, 2.16 kg: 8 g/10 min.

參閱第三圖所示,係擴鏈劑對PLA增黏性能比較,圖中X軸為剪切速率(shear rate)(1/s),Y軸為黏度(viscousity)(pa.S),PLA+擴鏈劑-1為(CE-1),PLA+擴鏈劑-2為(CE-2),PLA+擴鏈劑-3為(CE-3),PLA+擴鏈劑-4為(CE-4),標號之方塊範圍為混煉加工範圍10,由圖示可知,擴鏈劑-1具有流動較佳。擴鏈劑-2其合金耐剪力較佳。而擴鏈劑-3,擴鏈劑-4之擴鏈效果不佳,可能是含有較高酸基所致。 Referring to the third figure, the chain extender is compared to the viscosity-increasing performance of PLA. The X-axis is the shear rate (1/s) and the Y-axis is the viscousity (pa.S). PLA+ Chain extender-1 is (CE-1), PLA+ chain extender-2 is (CE-2), PLA+ chain extender-3 is (CE-3), and PLA+ chain extender-4 is (CE-4). The square of the label is in the kneading processing range of 10. As can be seen from the figure, the chain extender-1 has a better flow. Chain extender-2 has better shear resistance. However, chain extender-3, chain extender-4 has a poor chain extension effect, which may be caused by a higher acid group.

參閱第四圖所示,四種擴鏈劑之形態變化,以電子顯微鏡(SEM)觀察,代號AP-107(擴鏈劑-1),代號AP-113(擴鏈劑-2),代號AP-114(擴鏈劑-3),AP-140(擴鏈劑-4),其中代號AP-114(擴鏈劑-3),AP-140(擴鏈劑-4)有較明顯之相分離界面,而代號AP-113(擴鏈劑-2)相容性較好,選擇物性最佳的代號AP-107,代號AP-113的合金進行電子顯微鏡(TEM)觀察,觀察代號AP-113(擴鏈劑-2)之晶塊尺寸(domain size)較小,相容性較佳,相厚度界於0.5~1μm。 Referring to the fourth figure, the morphological changes of the four chain extenders were observed by electron microscopy (SEM), code AP-107 (chain extender-1), code AP-113 (chain extender-2), code AP -114 (chain extender-3), AP-140 (chain extender-4), wherein the code AP-114 (chain extender-3), AP-140 (chain extender-4) has obvious phase separation The interface, code AP-113 (chain extender-2) has good compatibility, the best physical property code AP-107, the alloy coded AP-113 is observed by electron microscopy (TEM), and the code AP-113 is observed. The chain extender-2) has a smaller domain size and better compatibility, and the phase thickness is 0.5 to 1 μm.

參閱第五、第六圖所示,交聯複合型高性能ABS/PLA環保生質綠材製備方法,其中,參照組為ABS-2 原料100%,其物性為艾佐德沖擊強度(izod impact stength)24.5(kg-cm/cm),彎曲強度(flexural modulus)20000(kg/cm2),抗拉強度(tensile stength)400(kg/cm2),熱變形溫度(HDT℃,66psi)87℃,熔融指數(MI)5(g/10min,200℃,5kg),生質含量0%。合金1的代號為AP-146,配方為ABS-2為60%,PLA-1為30%,增韌劑-2為8%,擴鏈劑-2為1%,ABS回收塑料1%,其物性為艾佐德沖擊強度(izod impact stength)44.6(kg-cm/cm),彎曲強度(flexural modulus)21957(kg/cm2),抗拉強度(tensile stength)421(kg/cm2),熱變形溫度(HDT℃,66psi)88.2℃,熔融指數(MI)7.04(g/10min,200℃,5kg),生質含量30%。合金2的代號為AP-150,配方為ABS-2為40%,PLA-1為50%,增韌劑-2為8%,擴鏈劑-2為1%,ABS回收塑料1%,其物性為艾佐德沖擊強度(izod impact stength)35.3(kg-cm/cm),彎曲強度(flexural modulus)28233(kg/cm2),抗拉強度(tensile stength)457(kg/cm2),熱變形溫度(HDT℃,66psi)80.8℃,熔融指數(MI)9.34(g/10min,200℃,5kg),生質含量50%。其中,擴鏈劑-2具有較流變控制與相容劑的作用,晶塊尺寸(domain size)較小,相容性較佳,相厚度界於0.5~1μm。搭配一定組成的增韌劑,可有效提升物性,PLA含量為30%時,其艾佐德沖擊強度(izod impact stength)44.6(kg-cm/cm)。 Referring to the fifth and sixth figures, the cross-linked composite high-performance ABS/PLA environmentally-friendly green material preparation method, wherein the reference group is 100% of ABS-2 raw material, and its physical property is Izod impact strength (izod impact) Stength) 24.5 (kg-cm/cm), flexural modulus 20000 (kg/cm 2 ), tensile strength (tensile stength) 400 (kg/cm 2 ), heat distortion temperature (HDT ° C, 66 psi) 87 °C, melt index (MI) 5 (g/10 min, 200 ° C, 5 kg), biomass content 0%. Alloy 1 is coded AP-146, formula is 60% for ABS-2, 30% for PLA-1, 8% for toughener-2, 1% for chain extender-2, and 1% for ABS recycled plastic. The physical properties are izod impact stength 44.6 (kg-cm/cm), flexural modulus 21957 (kg/cm 2 ), tensile strength (tensile stength) 421 (kg/cm 2 ), The heat distortion temperature (HDT ° C, 66 psi) was 88.2 ° C, the melt index (MI) was 7.04 (g/10 min, 200 ° C, 5 kg), and the biomass content was 30%. Alloy 2 is coded AP-150, formula is 40% for ABS-2, 50% for PLA-1, 8% for toughener-2, 1% for chain extender-2, and 1% for ABS recycled plastic. The physical properties are izod impact stength 35.3 (kg-cm/cm), flexural modulus 28233 (kg/cm 2 ), tensile strength (tensile stength) 457 (kg/cm 2 ), The heat distortion temperature (HDT ° C, 66 psi) was 80.8 ° C, the melt index (MI) was 9.34 (g/10 min, 200 ° C, 5 kg), and the biomass content was 50%. Among them, chain extender-2 has the function of rheology control and compatibilizer, the domain size is small, the compatibility is better, and the phase thickness is 0.5~1μm. With a certain composition of toughening agent, physical properties can be effectively improved. When the PLA content is 30%, the izod impact stength is 44.6 (kg-cm/cm).

本發明合金的熱熔融指數(MI),MI值為大於 15g/10min。傳統PLA在製作產品外殼或固定PIN腳的最小尺寸是在1~1.2mm,本發明ABS/PLA合金可達到05~0.9mm。PLA在常溫之缺角耐衝擊系數為2,本發明ABS/PLA合金可達到低溫-40度時,缺角耐衝擊系數為40。本發明ABS/PLA合金有符合EPEAT環保規範。EPEAT環保規範:2006年7月,由美國環保署公佈的一項評量電子產品是否具有良好環境績效的工具『電子產品環境評估工具』(The Electronic Product Environmental Assessment Tool,EPEAT)可幫助政府機關與私人企業在採買綠色電子產品時做為參考指標。 The hot melt index (MI) of the alloy of the present invention has a MI value greater than 15g/10min. The minimum size of the conventional PLA in the production of the product casing or the fixed PIN pin is 1 to 1.2 mm, and the ABS/PLA alloy of the present invention can reach 05 to 0.9 mm. The impact resistance coefficient of the PLA at normal temperature is 2, and the ABS/PLA alloy of the present invention can reach a low temperature of -40 degrees, and the notched impact resistance coefficient is 40. The ABS/PLA alloy of the present invention is in compliance with the EPEAT environmental protection specification. EPEAT Environmental Code: In July 2006, the Electronic Product Environmental Assessment Tool (EPEAT), published by the US Environmental Protection Agency to assess whether electronic products have good environmental performance, can help government agencies and Private companies are used as reference indicators when buying green electronics.

參閱第七圖所示,係螺桿組態圖,本發明合金材料係由複數雙螺桿系統,作一各雙螺桿位置之調配組合,形成數個素料及混煉段,以達到本合金材料最好的耐剪切,流動性,強度及黏度。 Referring to the seventh figure, the screw configuration diagram, the alloy material of the invention is composed of a plurality of twin-screw systems, and a combination of two screw positions is formed to form a plurality of materials and mixing sections to achieve the best alloy material. Resistance to shear, flow, strength and viscosity.

螺桿加工溫度200~230是ABS加工的工作溫度,170~200是PLA加工的工作溫度,本發明合金主要是要克服兩材料各自加工溫度之結合,使PLA在高於200度時,物性不會被破壞而ABS在低於200度時,流變不會變小,造成融溶不完全。所以將兩材料混煉,使用擴鏈劑,使兩材料結晶融合,產生擴鏈反應,以提高兩材質在170~230之間,物性不會產生過多變化,以達到混煉合金之目的。所以擴鏈劑係為兩材質之相容劑,增加彼此黏度,中和兩材料的加工問度差異。本發明合金係增加兩材料之擴鏈反 應,MI質提升,耐水解,強化彼此物性結晶鏈結。使其增加成型成品時之流動性,並可在冷模(模具本身溫度)40~50度時作出大面積、小尺寸之產品,比如記憶卡外殼,電視螢幕外殼、電子事務機外殼,使3C產品更具有耐衝擊,使用擴鏈劑2的耐衝擊與抗拉都比原本PLA好,又兼具環保。 The screw processing temperature is 200~230, which is the working temperature of ABS processing, and 170~200 is the working temperature of PLA processing. The alloy of the present invention mainly needs to overcome the combination of the processing temperatures of the two materials, so that the physical properties of PLA are higher than 200 degrees. When the ABS is below 200 degrees, the rheology will not become small, resulting in incomplete melting. Therefore, the two materials are kneaded, and the chain extender is used to fuse the two materials to form a chain extension reaction, so as to improve the two materials between 170 and 230, and the physical properties do not change too much, so as to achieve the purpose of mixing the alloy. Therefore, the chain extender is a compatibilizer of two materials, which increases the mutual viscosity and neutralizes the processing difference between the two materials. The alloy of the invention increases the chain extension of the two materials Should be, the quality of MI is improved, hydrolysis resistance, and strengthening physical and crystalline chains. It can increase the fluidity of the finished product, and can make large-area and small-sized products in the cold mold (temperature of the mold itself) 40~50 degrees, such as memory card casing, TV screen casing, electronic transaction machine casing, making 3C The product is more resistant to impact, and the impact resistance and tensile resistance of the chain extender 2 are better than the original PLA, and it is also environmentally friendly.

前文係針對本發明之較佳實施例為本發明之技術特徵進行具體之說明;惟,熟悉此項技術之人士當可在不脫離本發明之精神與原則下對本發明進行變更與修改,而該等變更與修改,皆應涵蓋於如下申請專利範圍所界定之範疇中。 The present invention has been described with reference to the preferred embodiments of the present invention. However, those skilled in the art can change and modify the present invention without departing from the spirit and scope of the invention. Such changes and modifications shall be covered in the scope defined by the following patent application.

綜上所述,本發明係提供一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,其確已達到本發明之所有目的,另其組合結構之空間型態未見於同類產品,亦未曾公開於申請前,已符合專利法之規定,爰依法提出申請。 In summary, the present invention provides a method for preparing a cross-linked composite high-performance ABS/PLA environmentally-friendly green material, which has indeed achieved all the objects of the present invention, and the spatial pattern of the combined structure is not found in the same product. It has not been disclosed before the application, has complied with the provisions of the Patent Law, and has applied for it according to law.

Claims (6)

一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,包括:ABS為60%,PLA為30%,增韌劑為8%,擴鏈劑為1%,ABS回收塑料1%,擴鏈劑為MMA-MAA-St-GMA-EMA copolymer,PLA使用高分子量PLA,PLA之COOH-OH末端以官能化添加劑進行封端改質,以雙螺桿組態設計製作ABS/PLA合金,因ABS加工溫度200~230℃,熱熔融指數(MI)200℃ 5kg:2g/10min,為ABS之MI值,指受壓重5kg情況下,10分鐘內所流出之塑膠材料重量2g,PLA加工溫度170~200℃,熱熔融指數(MI)190℃ 2.16kg:8g/10min,為PLA之MI值,指受壓重2.16kg情況下,10分鐘內所流出之塑膠材料重量8g,再將製程以雙螺桿組態之方式,進行適當混煉,並利用具有流變控制與相容劑作用的擴鏈劑,改變高分子量PLA之流變質,溫度與剪切,使其得進行形態控制,增韌劑可有效提升物性,得進行增韌改質,雙螺桿係由複數雙螺桿系統,作一各雙螺桿位置之調配組合,形成數個素料及混煉段,以達到本發明ABS/PLA合金材料最好的耐剪切,流動性,強度及黏度。 A cross-linking composite high-performance ABS/PLA environmentally-friendly green material preparation method comprises: ABS is 60%, PLA is 30%, toughener is 8%, chain extender is 1%, ABS recycled plastic is 1%, The chain extender is MMA-MAA-St-GMA-EMA copolymer, the PLA uses high molecular weight PLA, the COOH-OH end of PLA is end-capped with functionalized additives, and the ABS/PLA alloy is designed and manufactured in a twin-screw configuration. ABS processing temperature 200~230 °C, hot melt index (MI) 200 °C 5kg: 2g/10min, is the MI value of ABS, refers to the weight of plastic material flowing out within 10 minutes under the pressure of 5kg, PLA processing temperature 170~200°C, hot melt index (MI) 190°C 2.16kg: 8g/10min, which is the MI value of PLA, which means that the weight of the plastic material flowing out within 10 minutes is 8g under the pressure of 2.16kg, and then the process is The twin-screw configuration method, suitable mixing, and using the chain extender with rheology control and compatibilizer to change the metamorphism of high molecular weight PLA, temperature and shear, so that it can be controlled by morphology and toughened. The agent can effectively improve the physical properties, and the toughening and upgrading is carried out. The twin-screw system is composed of a plurality of twin-screw systems, and the position of each twin-screw position is adjusted. Combined to form a plurality of prime materials kneading section, the present invention is to achieve the ABS / PLA alloy material best shear resistance, flowability, strength and viscosity. 如申請專利範圍第1項所述之交聯複合型高性能ABS/PLA環保生質綠材製備方法,其中前述官能化添加劑為MAH、GMA等官能化添加劑其中之一。 The method for preparing a cross-linked composite high-performance ABS/PLA environmentally-friendly green material according to the first aspect of the invention, wherein the functionalized additive is one of functional additives such as MAH and GMA. 如申請專利範圍第1項所述之交聯複合型高性能ABS/PLA環保生質綠材製備方法,其中前述ABS/PLA合金材料的熱熔融指數(MI)值為大於15g/10min。 The method for preparing a crosslinked composite high-performance ABS/PLA environmentally friendly green material according to claim 1, wherein the ABS/PLA alloy material has a heat melt index (MI) value of more than 15 g/10 min. 一種交聯複合型高性能ABS/PLA環保生質綠材製備方法,包括:ABS為40%,PLA為50%,增韌劑為8%,擴鏈劑為1%,ABS回收塑料1%,擴鏈劑為MMA-MAA-St-GMA-EMA copolymer,PLA使用高分子量PLA,PLA之COOH-OH末端以官能化添加劑進行封端改質,以雙螺桿組態設計製作ABS/PLA合金,因ABS加工溫度200~230℃,熱熔融指數(MI)200℃ 5kg:2g/10min,為ABS之MI值,指受壓重5kg情況下,10分鐘內所流出之塑膠材料重量2g,PLA加工溫度170~200℃,熱熔融指數(MI)190℃ 2.16kg:8g/10min,為PLA之MI值,指受壓重2.16kg情況下,10分鐘內所流出之塑膠材料重量8g,再將製程以雙螺桿組態之方式,進行適當混煉,並利用具有流變控制與相容劑作用的擴鏈劑,改變高分子量PLA之流變質,溫度與剪切,使其得進行形態控制,增韌劑可有效提升物性,得進行增韌改質,雙螺桿係由複數雙螺桿系統,作一各雙螺桿位置之調配組合,形成數個素料及混煉段,以達到本發明合金材料最好的耐剪切,流動性,強度及黏度。 A cross-linking composite high-performance ABS/PLA environmentally-friendly green material preparation method comprises: ABS 40%, PLA 50%, toughener 8%, chain extender 1%, ABS recycled plastic 1%, The chain extender is MMA-MAA-St-GMA-EMA copolymer, the PLA uses high molecular weight PLA, the COOH-OH end of PLA is end-capped with functionalized additives, and the ABS/PLA alloy is designed and manufactured in a twin-screw configuration. ABS processing temperature 200~230 °C, hot melt index (MI) 200 °C 5kg: 2g/10min, is the MI value of ABS, refers to the weight of plastic material flowing out within 10 minutes under the pressure of 5kg, PLA processing temperature 170~200°C, hot melt index (MI) 190°C 2.16kg: 8g/10min, which is the MI value of PLA, which means that the weight of the plastic material flowing out within 10 minutes is 8g under the pressure of 2.16kg, and then the process is The twin-screw configuration method, suitable mixing, and using the chain extender with rheology control and compatibilizer to change the metamorphism of high molecular weight PLA, temperature and shear, so that it can be controlled by morphology and toughened. The agent can effectively improve the physical properties, and the toughening and upgrading is carried out. The twin-screw system is composed of a plurality of twin-screw systems, and the position of each twin-screw position is adjusted. Combined to form a plurality of prime materials kneading segments, to achieve the best alloy material of the present invention, shear resistance, flowability, strength and viscosity. 如申請專利範圍第4項所述之交聯複合型高性能 ABS/PLA環保生質綠材製備方法,其中前述官能化添加劑為MAH、GMA等官能化添加劑其中之一。 Cross-linked composite high performance as described in claim 4 ABS/PLA environmentally friendly green material preparation method, wherein the aforementioned functionalization additive is one of functional additives such as MAH and GMA. 如申請專利範圍第4項所述之交聯複合型高性能ABS/PLA環保生質綠材製備方法,其中前述ABS/PLA合金材料的熱熔融指數(MI)值為大於15g/10min。 The method for preparing a crosslinked composite high-performance ABS/PLA environmentally friendly green material according to claim 4, wherein the ABS/PLA alloy material has a heat melt index (MI) value of more than 15 g/10 min.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102844336A (en) * 2009-07-21 2012-12-26 巴斯夫公司 Process for the production of condensation polymers via in-reactor chain extension and products thereof
CN103073861A (en) * 2012-12-24 2013-05-01 深圳市亚塑科技有限公司 PLA/ABS/silica composition and preparation method and application thereof
CN103384704A (en) * 2011-04-18 2013-11-06 乐金华奥斯有限公司 Biodegradable polymer composite material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102844336A (en) * 2009-07-21 2012-12-26 巴斯夫公司 Process for the production of condensation polymers via in-reactor chain extension and products thereof
CN103384704A (en) * 2011-04-18 2013-11-06 乐金华奥斯有限公司 Biodegradable polymer composite material
CN103073861A (en) * 2012-12-24 2013-05-01 深圳市亚塑科技有限公司 PLA/ABS/silica composition and preparation method and application thereof

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