TW211542B - Flexible multiply towpreg, products therefrom and methods of production therefor - Google Patents

Flexible multiply towpreg, products therefrom and methods of production therefor Download PDF

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Publication number
TW211542B
TW211542B TW081105390A TW81105390A TW211542B TW 211542 B TW211542 B TW 211542B TW 081105390 A TW081105390 A TW 081105390A TW 81105390 A TW81105390 A TW 81105390A TW 211542 B TW211542 B TW 211542B
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Taiwan
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prepreg
yarn
fiber
item
patent application
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TW081105390A
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Chinese (zh)
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John D Muzzy
Babu Varughese
Jonathan S Colton
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Georgia Tech Res Inst
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • Y02P70/62Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear

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Abstract

This invention relates to an improved flexible multiply towpreg, products therefrom, and methods of production therefor. The improved flexible towpreg comprises a plurality of towpreg plies which comprise reinforcing filaments and matrix forming material; the reinforcing filaments being substantially wetout by the matrix forming material such that the towpreg plies are substantially void-free composite articles, and the towpreg plies having an average thickness less than about 100 microns. The method of production for the improved flexible towpreg comprises the steps of spreading the reinforcing filaments to expose individually substantially all of the reinforcing filaments; coating the reinforcing filaments with the matrix forming material in a manner causing interfacial adhesion of the matrix forming material to the reinforcing filaments; forming the towpreg plies by heating the matrix forming material contacting the reinforcing filaments until the matrix forming material liquefies and coats the reinforcing filaments; and cooling the towpreg plies in a manner such that substantial cohesion between neighboring towpreg plies is prevented until the matrix forming material solidifies. Products include an improved flexible towpreg tape of a known geometry formed from the towpreg by forming the towpreg tape under pressure and elevated temperature in a means for creating a known tape geometry; a non-woven towpreg fabric fabricated from a plurality of the flexible, multiply towpregs by overlapping a plurality of the towpreg plies, and joining the towpreg plies together to form the fabric and, additionally, multidimensional fabrics, preforms and composite articles; and an improved flexible towpreg article in which the matrix forming material is recycled plastics.

Description

211542 Λ 6 Β 6 經濟部屮央標準,Λν員工消#合作社印製 五、發明説明(i ) 1. 發明的領域和範圍 本發明涉及的範圍包括柔韌的多股預浸漬纱,用其製 作的産品,以及製備方法。更具體一些,本發明涉及到一 種非常柔韌的多股預浸漬纱,該纱適合于紡織、编織及類 似的生産加工。由這種纱生産的産品以及製備這種纱的方 法均在本發明範圍之内。這種柔韌的多股預浸漬纱可加工 成一種柔靱的形狀和尺寸準確均勻的多股預浸漬纱帶,用 于長絲缠繞、擠拉及類似的生産工蓊。這種多股預浸漬纱 也可加工成一種非織造預浸漬料的織物,再進一步加工成 多維織物,預成型製品和覆合材料結構。這種預浸漬料還 可由連缠纖維和含有部分回收塑料的基體樹脂所組成。 2. 以發明生産工藝 由纖維和基體樹脂結合在一起做成的預浸漬纱,工藝 上鮮為人知,通常稱做''預浸漬料〃。預浸漬纱是預浸漬 料中的一種。通常的預浸漬料是由數百根或數千根纖維被 夾裹在連缠的樹脂基體中而做成。通常使用的增強纖維均 有市售,一般是由連績長線並成股,稱之為、、纱〃。毎股 纱中單絲數量多種不等。基體樹脂也有很多種類,但目前 主要有兩種樹脂為主,卽熱塑性高分子和部分固化的熱固 性高分子。 熱塑性高分子在預浸漬料和其它覆合材料製品中已廣 泛使用,並也將可獨立航空領域和其它高等覆合材料中使 用。比較起熱固性高分子材料,熱塑性高分子在破裂韌性 (請先閱讀背面之注意事項再填寫本頁)211542 Λ 6 Β 6 Standard issued by the Ministry of Economic Affairs, printed by the Λν Staff Consumer # Cooperative V. Description of the invention (i) 1. Field and scope of the invention The scope of the invention includes flexible multi-strand prepreg yarns made with Products, and preparation methods. More specifically, the present invention relates to a very flexible multi-strand prepreg yarn that is suitable for weaving, weaving and similar production processes. Products produced from such yarns and methods of making such yarns are within the scope of the present invention. This flexible multi-strand prepreg yarn can be processed into a flexible multi-strand prepreg tape with accurate and uniform shape and size for filament winding, pultrusion and similar production processes. This multi-strand prepreg yarn can also be processed into a non-woven prepreg fabric, which is further processed into multi-dimensional fabrics, pre-formed products and laminated material structures. This prepreg can also be composed of entangled fibers and a matrix resin containing partially recycled plastic. 2. Invented production process The prepreg yarn made by combining fiber and matrix resin is little known in the process, and is usually called prepreg. Prepreg yarn is one of prepregs. The usual prepreg is made of hundreds or thousands of fibers sandwiched in a tangled resin matrix. The commonly used reinforcing fibers are all commercially available, and are generally made up of long-term continuous strands and are called strands and yarns. The number of monofilaments in each yarn varies. There are many types of matrix resins, but currently there are two main types of resins, thermoplastic polymers and partially cured thermosetting polymers. Thermoplastic polymers have been widely used in prepregs and other laminate materials, and will also be used in the independent aerospace field and other advanced laminate materials. Compared with thermosetting polymer materials, thermoplastic polymers are in the fracture toughness (please read the notes on the back before filling this page)

本紙張尺度逍用中國國家標準(CNS)甲4規格(210X297公釐) -4 - V. 211542 Λ 6 Β 6 經濟部屮央標準局员工消費合作社印製 五、發明説明(2) ,沖擊強度以及耐腐蝕等方面更具優越性。熱塑性高分子 做成的預浸漬料可以有無限長的儲存期,保證後加工的質 量,並解決了熱固性高分子預浸漬料的儲存和冷凍的問題 。熱塑性高分子預浸漬料比多數熱固性高分子的剛性高聯 網絡更加堅韌。很少熱固性高分子能夠滿足使用在航空領 域中的覆合材料所要求的耐破壞性和濕熱壓縮強度。熱塑 性高分子在用作覆合材料基體樹脂時,由于其熔體粘度很 高,很難均勻地塗覆在纖維表面。一般情況下,熱塑性高 分子預浸漬料都很硬挺,不大適合于纺織、编織或舖製成 預成型製品,用它所做成的織物非常僵硬。同樣,在採用 這種硬挺的熱塑性高分子的預浸漬料進行長絲缠繞或製備 形狀覆染的製品時也很困難。在舖製過程中,必須在接觸 點上集中加熱才能使預浸漬料與模具相服貼。 熱固性高分子也用作預浸漬料的基體樹脂。使用熱固 性高分子預聚體做成的預浸漬料儘管也比較柔軟,但通常 都很粘,需使用一層保護性防粘劑。這層防粘在預浸漬料 使用之前一定要除去。盡管熱固性高分子預浸漬料可在某 些場合中使用,比如長絲纏繞,但由于它發粘,要使用保 護性防粘劑,因此不能用于紡織,编號,也不能用于散狀 或片狀模塑料中心斷切纖維的原料。 預浸漬纱還有其它兩種類型,一是金屬基體的預浸漬 纱,它同熱塑性預浸漬纱相似;一是部分固化的陶瓷預浸 漬纱,它同熱固性預浸漬纱相似。由于金屬和陶瓷覆合材 料的使用市場有限,這兩種預浸漬纱一般無貨供應,並且 本紙張尺度逍用中困困家樣準(CNS)甲4規格(210X297公货) (請先閱讀背面之注意事項再塡寫本頁) 裝- 訂· 線· -5 - 經濟部屮央標準局员工消費合作社印製 2ii642 λ 6 __B_6 五、發明説明(3) 在生産技術研發中也未受到重視。金屬和陶瓷預浸漬料可 以用類似于熱塑性和熱固性預浸漬料的加工方式進行生産 Ο 連缠纖維的預浸漬料可用多種浸漬方法生産,包括熱 溶融法,溶液法,乳液法,懸浮液法,表面聚合法,纖維 交混法,薄膜交織法,電鍍法和固醱粉末法。 熱熔融工藝是將纖維和樹脂在高剪切率下強行通過一 個高溫模具來達到浸漬。由于溫度很高,熱塑性高分子有 可能會降解。這値工藝方法的其它缺點是纖維纱受到的應 力很大,另外浸漬熱塑性塑料很困難。 溶液塗覆法是將樹脂基體材料溶解在溶劑中,然後該 纖維纱通過此溶液,再乾燥除去溶劑。這値工藝有兩個缺 點,一是熱塑性高分子的溶解度有限,多數工程塑料在室 溫下不溶于低沸點的溶劑。另外,同熱熔融法遇到的問題 一樣,很高的溶液粘度使得浸漬很困難。這個工藝的另一 問題是難以除去溶劑,預浸漬料中殘餘的溶劑會導致覆合 材料中所不希望的汽泡。 乳液法採用表面活性劑,將樹脂製備成一種水乳液, 從而把顆粒度很小的粉末狀基體材料塗覆到纖維表面。這 個工藝的缺點是很難將表面活性劑從最後的預浸漬纱中除 去。 懸浮液塗覆法,也叫做濕粉末法。這個方法不用溶劑 ,旨在解決多數熱塑性高分子在室溫下不溶解的問題。在 此方法中,粉末樹脂懸浮液在液體媒介中,通常是水。樹 (請先閱讀背面之注意事項再填寫本頁) 裝· 線· 本紙張尺度逍用中國國家標準(CNS)甲4規格(210x297公犮) -6 _ 經濟部屮央標準局貝工消#合作社印製 Λ 6益4^以_«6_ 五、發明説明(4) 脂在液體媒介中並没有溶介。纖維通過此懸浮液中。粒狀 的基體樹脂懸浮體並不會浸潤纖維表面,要用較高的壓力 才能使樹脂和纖維固結,製成覆合材料。這種預浸漬料一 般都很粘,所以不合適紡織或编織。這個工藝的另一缺點 是必須要除去液體媒介,和在製備高分子/液體膠體時所 使用的易揮發物質,懸浮劑或表面活性劑。另外,懸浮液 如果攪拌不良,則可能引起顆粒凝結,在加工過程中會出 現高分子粒子下況。 在乳液或懸浮液塗覆工藝中,懸浮體或乳膠體的粒子 尺寸要比纖維直經小才能達到緊密混合。對于很多無法用 乳液聚合或懸浮聚合製備的熱塑性高分子要做成如此小的 粒子是非常困難的。粒子的尺寸增加,則混合的質量降低 ,從而造成在固結後的覆合材料中,基體樹脂分散不好, 覆合材料性能低劣。 在表面聚合法中,高分子基體材料在纖維表面上聚合 而塗覆上去。這値工蕤的缺點是需要除去溶劑,阻聚劑或 聚合反應付産物等物質。表面聚合只能採用一些特殊的技 術來實現,例如電化學聚合。很多具有商業價值的高分子 材料不能採用此法生産。 在纖維交混法工藝中,高分子基體材料做成纖維狀, 然後與增強纖維在乾燥的情況下混编在一起。直到覆合材 料固結時,這些高分子基體纖維才通過某種方法,比如熔 融而浸潤到增強纖維表面。浸潤的效果取決于整値製品當 中樹脂與纖維的交混程度。由于這種交混物中樹脂基體没 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國鼷家標準(CNS)甲4規格(210x297公龙) Λ 6 13 6 211542 五、發明説明(5 ) (請先閱讀背面之注意事項再填寫本頁) 有浸潤增強纖維,在相同的加工時間和溫度下,這種纱需 要比完全潤濕的預浸漬纱更高的壓力才能固結成覆合材料 Ο 薄膜澆_的方法可解決熱塑性高分子在熱融法中所遇 到的一些問題。這種方法是將用熱熔法或溶液法鐃鏵而成 的基體材料的薄膜舖放在纖維上面。纖維被夾在兩層薄膜 當中,然後加熱、壓研,從而將樹脂壓入到缕維中去。 美國塞南米德(氰胺)公司(American Cyanamid)採 用電鍍法製備出一種柔勒的金屬基體預浸漬纱。該纱中每 根纖維均被金屬基欐充分浸潤,均勻塗覆。這種預浸漬纱 具備紡織、编織、長絲纏繞、以及製成散狀或片狀模塑料 所要求的各種性能。另外,這種預浸漬纱不用高壓狀可固 結。可是電鍍方法的缺點是可用來進行電鍍的原料種類有 限。多數具有商業價值的陶瓷或高分子材料均不能電鍍在 增強纖維表面。另外,由于纖雒本身在此方法中用作電報 之一,它必須能導電,因此玻璃纖維或有機纖維就無法進 行電鍍。 經濟部屮央標準局貝工消費合作社印製 固體粉末塗覆法是生産預浸漬料的一種最新方法。此 法的主要優點是不用任何溶劑,在加工過程中也不要引入 很大的應力。在多數採用此方法的合中,最終目的都是要 有效地形成一層很薄的,厚度均勻的高質量塗層。形成粉 末狀的樹脂在環境(溫度)或較高的儲存溫度下必須能夠 維持固體狀,當加熱時,能夠熔融成低粘度流體,滲透到 非織造織物纱束當中去。乾燥粉末塗覆法有很多優越性。 本紙張尺度逍用中國困家標準(CNS)甲4規格(210x297公龙) -8 - Λ 6 13 6 經濟部屮央標準局Α工消贽合作社印製 五、發明説明(6) 它不用溶劑或水,不潮濕,從而有助于覆合材料的回收使 用。這一點在經濟上很有好處,使得粉末有可能達到 1 0 ◦%的利用率。另外此法不用昂貴的溶劑,減少了溶 劑的揮發和浪費。正是主要由于這些優越性,粉末塗覆法 得到了研發和進一步的發展。 另一種粉末樹脂基體塗覆纖維的方法是奧托凱姆公司 (Atochem)發明的,即首先用乾燥的熱塑性高分子粉末塗 覆纖維表面,然後再將其用熱塑性材料包裹起來。但在這 個過程中,由于樹脂基體没有熔融,只有部分同包皮直接 接觸的纖維被樹脂浸潤。同被樹脂完全浸潤的預浸漬纱來 相比,在其它相同的加工條件下,這種預浸漬纱要採用更 高的壓力才能結實。另外,類似于懸浮液塗覆,這値工藝 需要使用粒度很小的粉末,一般小于2◦微米。要將熱塑 性高分子加工成如此細微的粉末,成本很高。 預浸漬纱中的樹脂基體的體積含量一般要超過2 5% 才可能固結,形成不含汽泡的覆合材料結構。如果樹脂含 量低于2 5%,則在固結過程中還要另外再加入樹脂。預 浸漬纱是一維線狀的,但通過紡織,编纖,長絲缠繞和其 它一些加工方法,可能變成二維和三維結構的産品。另外 ,預浸漬纱還可通過切割或其它方式製成不連缠的纖維增 加的,用于模塑工藝的原材料。 本發明的簡單概括 本發明中的基本預浸漬纱的最小彎曲半經不超過1 5 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度边用中Η國家標準(CNS)甲4規格(210X297公®) -9 - 經濟部屮央橾準局貝工消t合作社印製 . Λ 6-Li 五、發明説明(7) mm,每股纱的平均厚度不超過10〇wm,因而適合于 紡織,编織,長絲繾繞,以及深度加工成各種有用的形狀 和結構。紡織和编織工藝,要求每股纱的厚度不超過上述 限制。但如果組成預浸漬纱的各股纱之間不相互牽制,那 麼預浸漬纱的尺寸就不必受到約束。預浸漬纱中的各股是 整體預浸漬纱中的一個分割的單元,它遠比預浸漬纱整體 固結得多。股與股之間分開的距離至少是各股厚度的30 倍。它們既不發粘,又相互分開,因而可在很大程度上獨 立地進行柔性變形。 本發明中的多股柔韌預浸漬纱通過以下三個步驟製備 而成:(1)增強纖維纱向側面分散開,該所有單纖維均 暴露在周圍環境之中,(2)樹脂基體與分散開的纖維接 觸,産生界面粘結,(3)在樹脂基體凝固成不粘手狀態 之前;預浸漬纱中以各股纱保持相互分開,從而阻止股與 股之間有明顯的粘并。如此形成的基本預浸漬纱可再進一 步加工成各種有用的製品。 本發明中的多股柔韌預浸漬纱帶通過以下三個步驟製 備而成:(1)增強纖維纱向側面分散開,該所有單纖維 均暴露在周圍環境之中,(2)樹脂基體與分散開的纖維 接觸,産生界面粘結,(3)塗覆過的纖維纱在外力作用 下形成一定的形狀,從而製成一定尺寸的柔韌的帶子。 本發明中的多股柔勒的預浸漬纱非織造布是通過以下 四個步驟製備而成:(1)增強纖維纱向側面分散開,該 所有單纖維均暴露在周圍環境之中,(2)樹脂基體與分 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國B家糅準(CNS) V4規格(2丨0X297公釐) -10 - 21 Λ 6 B 6 經濟部屮央標準局貝工消t合作社印製 五、發明説明(8) 散開的纖維接觸,産生界面粘結,(3)在樹脂基體凝固 成不粘手狀態之前,預浸漬纱中的各股纱保持相互分開, 從而阻止股與股之間有明顯的粘并。如此形成了預浸漬抄 織物的基布,(4)採用叠加,點連接或針剌與連接方式 將預浸漬纱基布製成非織造布。 本發明中由回收塑料組成的樹脂基體所做成的柔韌預 浸漬纱採用以下三個步驟製備:(1)增強纖維向側面分 散開,該所有單纖維均暴露在周圍環境之中,(2)由回 收塑料組成的纖維基體與分散開的纖維接觸,産生界面粘 結,(3)在由回收塑料組成的樹脂基體凝固成不粘手狀 態之前,相鄰的绻維之間保持側面分開,從而阻止相互之 間有明顯的粘并。 基本預浸漬纱的製備方法如下。作為原料的纖維纱由 很多單纖維組成,它們被分散開,造成單纖維之間的相互 分離。樹脂基髏材料然後塗覆在這些分散開的纖維表面。 當足夠的塗覆量達到以後,樹脂液化,從而形成被樹脂充 分潤濕的纗維纱。隨著液化的樹脂基體沿著纖維舖散開來 ,樹脂基體的厚度變薄,最後樹脂薄膜在單纖維之間破裂 。如果纖維纱充分分散,並一直維持此分散狀態,則樹脂 液膜在凝固時,將在單鐵維之間破裂。塗覆過的纖維,不 論是以單根纖維塗覆的,還是以小股纖維束塗覆的,然後 都冷卻下來,樹脂基體凝固。在此過程中,纖維分成小股 。有時一些單纱維會連接在相鄰的兩股纱之間,成為股間 連結體。各個纱股不停地受到拉力,從而使纖維纱連缠向 (請先閱讀背面之注意事項再填寫本頁) 裝- 線. 本紙張尺度边用中Η B家標準(CNS)甲4規格(210X297公釐) -11 - 經濟部中央標準局β工消t合作社印製 2U ㈤ _D6_ 五、發明説明(9 ) 前移動,同時也使纖維受到一軸向張力,而不致于向我鬆 弛。浸好的纱股可以並結在一起以形成各種厚度的預浸漬 纱,它們可再用來缠繞,做成帶狀或紡織品,或按需要做 進一步的加工。 本發明中的柔韌的多股預浸漬纱帶的特點是具有一定 的寛度和厚度。通常用纖維纱股做成的柔韌的多股預浸漬 纱沒有確定的幾何尺寸,使得用這種預浸漬纱加工成尺寸 精密的高質量製品往往很困難。本發明中的這種柔韌的多 股預浸漬纱帶具有一定的幾何尺寸,可適合于長絲缠繞, 先進的缕維舖放工藝和擠拉。 用來生産這種柔韌的預浸漬纱帶的裝置可以有很多種 。本發明最傾向于使用的裝置是採用兩値相匹配的锟子, 一個棍子表面下凹,另一個锟子表面上凸;或者一個棍子 表面刻有凹槽,而另一锟子則表面上帶有與其相配的凸塊 。當柔韌的多股預浸漬纱通過兩個棍子之間幾何形狀一定 的空隙時,就形成了該幾何尺寸的預浸漬纱帶。其次傾向 使用的裝置是獨立地採用一個表面下凹的棍子。當柔靱的 預浸漬纱在張力下通過此锟子外圍的某一部分時,張力和 棍子的下凹形狀共同作用,迫使柔韌的多股預浸漬纱逐漸 移向锟子凹面的最低處,從而形成一個具有適當的幾何形 狀的帶子。 本發明中的柔坜的多股預浸漬纱的非織造的織物可以 用來生産成本低廉的2維織物,而它又可用作原料再進一 步加工成2維和3維的織物,預成型物和各種覆合材料結 (請先閲讀背面之注意事項再塡寫本頁) 本紙張尺度边用中国a家搮準(CNS) «Μ規格(210父297公龙) -12 - 經濟部屮央標準局負工消t合作社印製 五、發明説明(1C)) 構。因此,採用本發明中的柔靱的非織造織物所生産的産 品要比用柔韌的多股預浸漬纱所生産的编織物和紡織物便 宜。採用本發明的技術,用室溫下為固體狀的樹脂基體做 成的織物可以是很柔韌的,而用常理技術所生産的織物則 是硬挺的。本發明中柔韌的多股預浸漬纱可用來生産柔韌 的多股預浸漬纱的非織造鐵物,這種織物使用固體樹脂基 體,既柔韌且纖維表面浸潤良好。採用雙纖維結構,即, 樹脂基體和增強材料同為纖維狀,比如交混纱,交混编織 ,或用纖維,樹脂交替舖放的結構所做成的紡織物,一般 來説也很柔韌,但卻不具備像本發明中的織物這樣樹脂纖 雒的浸潤,因而在固結過程中,這種雙纖維結構就需要採 用更加苛刻的加工條件。 本發明中的這種織物的製備是將組成柔韌的多股預浸 漬纱的相互之間連接著的各纱股和各纖維相互舖疊,連在 一起而成。本發明是傾向于將兩股或多股預浸漬纱舖叠在 一起,形成重量約50克/平方米到500克/平方米的 織物,再具體一些是傾向于約為150克/平方米到 35◦克/平方米。適合于將多股預浸漬纱連接在一起的 方法有很多種,本發明傾向于使用熱融點連接和針脚式線 連接。典型的做法是將舖叠在一起的多股預浸漬纱在選擇 4好的地方加熱熔融,這樣既可將預浸漬纱連接在一起,同 時又保持了它們原有的柔思;性。其它適合的連接技術包括 有針剌法,纖維相互缠結法以及局部加壓法。 用回收塑料做成的預浸漬料中的樹脂基體含有大量的 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國國家標準(CNS)甲4規格(210X297公藿) -13 - 經濟部屮央楳準局员工消费合作社印製 Λ ‘ ’一* Λ 6 从_ 13 6_ 五、發明説明( 回收的廢塑料,但也會含有一些未用過的原塑料。盡管各 種塑料都可用作這種預浸漬料的基體樹脂,熱塑性塑料更 為合適。回收的塑料首先被切短,磨成粉末。如果回收料 中混染有各種不同的塑料,則要採用密度分離法將它們部 分淨化,然後用此粉末塗覆並熔融到增強纖維表面做成預 浸漬纱。用這種預浸漬纱製成覆合材料結構的方法同一般 預浸漬纱相同。使用以增強纖維可以是各種形式,如圖格 布,紡織物或纖維纱,增強纖維可以以纺織布或分散的纖 維纱的形式來進行表面塗覆。如果使用纖維纱,一般做成 多股預浸漬纱,它們可用于纺織,编織,長絲缠繞,製帶 ,製非織造布,等等。 本發明的主要目的在于生産一種柔韌的多股預浸漬纱 ,適合于紡織,编織,長絲纏繞,擠拉,製帶,非織造織 物,還可加工成散狀模塑料的原料。 本發明的進一步目的是能夠使用多種纖維和基體樹脂 來生産具有商業價值的預浸漬纱。 本發明的另一目的是生産一種柔韌的預浸漬纱,這種 預浸漬纱中含有足夠數量的纖維,適合于經濟地製備各種 覆合材料結構。 本發明還有一個目的是生産一種纖維被充分浸潤的預 浸漬纱,因而在覆合材料固結過程中,不需使用過高的壓 力去使纖維充分浸潤。 本發明的再一目的是能在很高的速率下生産預浸漬纱 ,因而可以減少生産過程中樹脂的固化或固化階段的升级 (請先閱讀背面之注意事項再塡寫本頁) 本紙張尺度逍用中困S家標準(CNS)甲4規格(210X297公龙) -14 - Λ 6 Β 6 經濟部屮央標準局员工消費合作社印製 五、發明説明( Ο 本發明的另一目的是採用價格便宜的粗粒狀的樹脂基 體來生産預浸漬纱*,樹脂粒度可比缕維直經大兩倍以上, 短纖維狀樹脂也可使用。 本發明一進一步目的是採用各種纖維和基髏樹脂生産 具有商業價值的預浸漬纱帶。 本發明一再一目的是生産一種柔韌以預浸漬非織造布 ,可適用于擠拉,長絲缠繞,或做成散狀模塑料的原料, 或做成各種預製品和覆合材料結構。 本發明還有一目的是生産一種柔韌的預浸漬非織造織 物,其中含有足夠的纖維,適合于經濟地生産2維和3維 的預製品和覆合材料結構。 本發明的另一目的是生産一種非織造預浸漬鐡物,它 可採用類似于粘性的熱固性預浸漬帶的加工方法舖製成高 级覆合材料結構。 本發明的再一目的是生産一種非織造預浸漬織物,可 用來製備樹脂傳遞模型工藝中使用的預製品,比如管狀預 製品,它可採用滾管方式製作。 本發明還有一目的是生産一種預浸漬纱,其中纖維表 面上塗覆的基體樹脂主要是由回收塑料組成。 本發明另一目的是産生一種預浸漬纱,它採用價格低 廉的廢塑料作為基體材料。 本發明的再一目的是提供一種生産方法,可使用對加 工設備或對最終産品危害很小的原料作為基體樹脂來生産 本紙張尺度逍用中Η國家標準(CNS)甲4規格(210X297公进) "" -15 - (請先閱讀背面之注意事項再填寫本頁) 2ΐΛύ43 Λ 6 Β6 經濟部屮央標準局β工消費合作社印製 五、發明説明( 預浸漬纱。 本發明的最後的一値目的是採用部分混染了的或被污 染了的樹脂,不用淨化而直接用來生産預浸漬纱,其最終 的覆合材料性能仍能逹到要求。 下面將通過附圖和詳細的解釋進一步描述上述的各個 目的以及其它一些雖未列出,但内行人可以很容易推算出 來的目標。 附圖的詳細說明 圖一是本發明中用于生産多股柔韌預浸漬纱的 的工 藝流程圖解;\ 圖二表示本發明的基本的柔靭預浸漬纱中的纱股; 圖三是一般的預浸漬纱(圖3 a)與本發明的預浸漬 紗(圖3 b )的對比; 圖四表示本發明的預浸漬纱中,增強纖維表面上的樹 脂基體固化以後各股的情況。圖4 a為合股之前,圖4 b 為合股之後; 圔五是本發明中樹脂基體材料在纖維表面上熔融過程 的說明。圖5 a是纖維受到側面約束時的情況,圖5 b是 不受側面約束時的情況,圖5c是樹脂基體材料在單纖維 之間形成的收縮頸的截面; 圖六為本發明的纱股的厚度對不同抗撓剛度的纱股的 彈性模量作圖; 圖七是採用靜電流化床作為塗覆裝置的本發明的總工 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國Β家標準(CNS)甲4規格(210x297公龙) -16 - 211^2 Λ 6 Β6 經濟部屮央標準局員工消费合作社印製 五、發明説明( 藝流程圖; 圖八是採用本發明的方法生産預浸漬纱帶的詳細圖解 i 圖九是採用本發明的無爐裝置生産預浸漬纱帶的詳細 圖解; 圖十為製備預浸漬纱帶用的分別帶有凸塊和凹槽的兩 値锟子的截面圖,也即圖八中的6 — 6截面; 圖1 1 a和圖1 1 b是圖十所示的锟子的另外兩種形 式; 圖12是採用一個棍子製備預浸漬纱帶的截面示意圖 « f 圖13是圖12所示的採用一個锟子製備預浸漬纱帶 的側面示意圖; 圖14是本發明的單向非織造預浸漬纱織物的示意圖 ,其中14 a為舖叠在一起的預浸漬纱的軸向截面示意圖 ;14b表示舖叠在一起的預浸漬纱的點連接,· 圖15為本發明的多向預浸漬纱非織造織物的示意圖 。預浸漬纱相鄰各層排向不同。其中1 5 a表示預浸漬纱 的舖叠;1 5 b表示舖叠在一起的預浸漬纱的點連接·/ 圖16為圖14b所示的單向非織造織物的俯視圖, 表明一種典型的點連接形式; 圖17為圖14a所示的單向非織造織物的俯視圖, 表明一種典型的針腳式線連接形式; 圖18為本發明的基本預浸漬纱股的顯微鏡照片(放 各紙張尺度通用中國S家標準(CNS)甲4規格(210X297公埂) (請先閲讀背面之注意事項再填寫本頁) -17 - 21i〇42 Λ 6 13 6 經濟部屮央標準局貝工消费合作社印製 五、發明説明(15 大3 9 . 9倍); 圖19為本發明的基本預浸漬纱的顯徹鏡照片(放大 倍數為1)。該纱中樹脂基體材料已固結到增強纖維表面 ,但尚未含股; 圖20為在◦ psi壓力下用聚丙烯浸漬玻璃纖維製成 的預浸漬纱帶的截面的顯徹鏡照片(放大倍數50); 圖2 1為在2 0 psi壓力下用聚丙烯浸漬玻璃纖維製 成的預浸漬纱帶的截面的顯微鏡照Η (放大倍數50); 圖22為在20 psi壓力下用聚丙烯浸漬玻璃纖維製 成的預浸漬纱帶的截面的顯微鏡照片(放大倍數200) 9 圖2 3為本發明中用聚丙烯和玻璃纖維製成的預浸漬 纱帶的照Η; 圖24為本發明中通過交織一種粘結劑纖雒製成的非 織造預浸漬纱織物的照片。 本發明詳細說明 1 .綜述 本發明的一個重要特點是促進對纖維的浸潤,並減小 相鄰的已浸潤的纖維之間的粘并。為防止已塗覆的纖維相 粘并,在樹脂基體固結之前,纖維之間必須要保持分開。 實現纖維相互分開的方法之一是維持對纖維的軸向拉力, 限止它們向側面鬆弛。圖5表示位于兩根纖維上的一粒樹 脂基體的熔融過程。圖5 a中,由于纖維受到較高的軸向 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度边用中國國家標準(CNS)甲4規格(210X297公¢) -18 - Λ 6 B 6 經濟部屮央標準局貝工消费合作社印製 五、發明説明(id 張力,因而限止了纖維之間的相互靠攏;而圖5b中,纖 維受到的軸向拉力很低,當樹脂基體顆粒熔融,在纖維表 面上浸潤時,兩根纖維被拉攏到一起。 在圖5b (c)中,當纖維被充分浸潤後,兩根纖維 之間的樹脂熔體的厚度仍很大,相比之下,圖5a (c) 中,由于纖維横向移動受阻,熔體的厚度要大大小于5b (c),這樣兩根纖維之間的樹脂膜很容易破碎,從而將 兩根塗覆了樹脂的纖維分開,結果如圖5 a (b)所示。 由于纖維的阻礙,樹脂融體頸縮,産生于一垂直于纖 維軸向的拉伸應力,如圖5 c所示。這値拉伸應力的産生 是由于纖維之間的樹脂傾向于去覆蓋纖維而被拉開所致。 如果此應力超過了融體的破壞應力(Ty,則縮頸破損。 樹脂基體的破壞應力可用做判據來確定該樹脂的加工條件 。比如説,通常低分子量的樹脂融體的拉伸破壞應力非常 低。而高分子量的熔融高分子的強度隨加工溫度升高而降 低。另外,部分溶劑化的或增塑過的高分子的拉伸強度比 其對應的純高分子的強度要低。 被分散開的預浸漬纱的厚度很低,因此可以在一很短 的時間内將高分子樹脂熔融,並且熔化溫度可以高于該樹 脂的安全使用溫度。在這種情況下,樹脂熔體的彈性強度 可以變得很低,從而有助于預浸漬纱分裂成多股。 通常樹脂基體成型時,操作溫度應等于或略高于該樹 脂的熔融溫度。而按本發明的塗覆工藝,操作溫度可力大 高于樹脂基體的軟化溫度,只要能保證在操作中的滯留時 (請先閱讀背面之注意事項再塡寫本頁) 本紙張尺度逍用中國H家標準(CNS)甲4規格(210x297公龙) -19 - Λ 6 Β6 經濟部中央標準局员工消費合作社印製 五、發明説明(^ 間内,基體樹脂不會降解或進升到下一固化階段即可。在 本發明中,滯留時間可以很短,因而沒有明顯的基體材料 降解或樹脂的固化階段升级。加熱爐或加熱器的操作溫度 與纖維和樹脂在爐中的滯留時間有關。如果滯留時間很短 ,則溫度可調高,反之也一樣。在這種條件下,操作溫度 可以高于基體樹脂材料開始降解或固化階段開始升级的溫 度。只要保證滯留時間很短,基體樹脂材料不會較長久地 停留在這樣溫度之中以致降解或固化升级。 在一粘彈性液體中,導致其拉伸強度降低的因素也同 樣會導致其表面張力降低和液體的粘度降低。因此,有利 于纖維分散的條件也同樣有利于液體沿纖維的擴散。這樣 ,圔5 a所示的液滴形狀就可通過改變材料和改變加工條 件,降低液體彈性來進行轉變。通過限制或阻礙缕維之間 相互靠攏,在破碎之前,樹脂基體縮頸的長度,L„·可以 大大減小,從而截面積,可以變薄。因此,造成縮頸 破壊所需的力,Fn»降低。在樹脂浸潤和固結的過程中保 持纖維分散將有助于達到纖雒的單根塗覆。施加外力則可 «助實現纖維之間的液膜的破裂。在垂直于纱維分散平面 的方向上鼓吹熱空氣會有助于破碎鐵維之間的液膜,使分 散開的纱維通過一刻有凹槽的棍子,纖維在锟軸上受壓, 這也會有助于分裂纖維之間的液膜。很多類似的機械裝置 都可用來常助纖維相互之間的分散。 為了生産出本發明中的這種基本預浸漬纱,樹脂基體 必須要很好地浸潤纖維,只有這樣才能不採用外加的粘結 (請先閲讀背面之注意事項再塡寫本頁) 裝- 本紙張尺度逍用中B B家樣準(CNS)甲4規格(210><297公放) -20 - 9.1 1ϋ4^ _Β6 9.1 1ϋ4^ _Β6 經濟部屮央標準局员工消費合作社印製 五、發明説明(id 劑而仍可達到樹脂基體與纖維之間的粘結。樹脂對纖維的 浸潤可以採用一樹脂基體液化器,比如熔融器或爐子,通 過加熱使樹脂液化。要達到較好的浸潤,就需要使基體樹 脂在選用的液化設備内保留足夠的滯留時間,從而使樹脂 將纖維充分浸潤。市售的液化器種類有很多種,包括任何 輻射式或傳導式的爐子。對于乾燥樹脂粉末,採用輻射式 爐子要更好一些。另外;也可用加熱的模具來取代爐子用 做液化器。 樹脂基體的液化方法是本發明的一個部分。任何粒度 的基髏樹脂材料都可以用來塗覆纖維,包括粗顆粒和短纖 維。由于本發明中,基體樹脂液化並且沿纖維表面潤濕舖 展,從而減小了通常在使用大粒度樹脂和直徑很細的增強 纖維時所遇到的樹脂基體與纖維之間混合分散的問題。因 此,在本發明的工藝中,基體樹脂材料的粒度大小f是一 個十分關鍵的因素,其範圍可以從塗覆工蕤中一般採用的 相當于或小于纖維的直徑或厚度到比纖維直徑大很多倍, 包括採用短纖維。在本發明之前,從還没有人成功地採用 大直徑的粒子的樹脂作為基髏材料。這種做法可大大節約 成本。 2 .原材料的選擇 可用做纖維纱的纖維種類有很多種,其中包括:玻璃 纖維,碩纖維和石墨纖維;有機纖維,特別是諸如醛胺和 芳香族聚酯一類的液晶纖維;陶瓷纖維,比如碩化硅;混 本紙張尺度逍用中國國家楳準(CNS)甲4規格(210X297公货) (請先閲讀背面之注意事項再填寫本頁) 裝- *tT. -21 - 經濟部屮央標準局貝工消费合作社印製 Λ 6211^^-- 五、發明説明(id 紡纖維,比如醯胺/硪,醛胺/玻璃,醛胺/碩/玻璃和 碩/玻璃。 一般來説,如果纖維的直徑或厚度超過2 5微米,則 不可使用。例如,如使用直徑為140微米的硼缕維就毫 無意義,因為如此尺寸的纖維不可能做得很柔軟。另外, 所選用的纖雒應是用做增強材料的纖維,並且是連缠纖維 。適合于此工藝的繼維應能在樹脂基體固結時的工藝溫度 下保持熱穩定。另外纖維的玻璃化轉挨溫度和熔融溫度要 高于室溫,並且熔融溫度要高于覆合材料固結加工溫度。 熱塑性和熱固性高分子均可用作基體樹脂材料。本發 明中傾向于使用的高分子材料通常不應發粘,在固化以後 使用過程當中,其玻璃化溫度或熔融溫度應高于室溫,特 別是玻璃化溫度應高于室溫。因此,一些彈性材料,橡膠 和皮革,它們在室溫下很柔軟,不可用做基體材料。有些 熱固性高分子,在通常的操作溫度下發粘。可以在低溫下 操作以減少粘性,從而可用作樹脂基體材料。一些非高分 子材料,比如銅,低熔點金屬,陶瓷母髏等也可用作基體 材料。基體材料可以為任何形狀,如粒子、粉末和短纖維 Ο 高分子材料的類別很多,舉例如下:A B S条列、縮 醛類、丙烯酸類、醇酸聚酯、烯丙基類、胺基類、環氣類 、氣塑料、呋喃類、蜜胺類、尼龍類、酚醛類、苯基氧化 物和苯基醚類、聚醯胺、聚醯胺一亞醛胺、聚丁烯類、聚 碩酸酯類、聚酯類、聚雙醚酮、聚醚酮類、聚並醯胺醚類 張尺度通用中國國家標準(CNS)甲4規格(210x297公货) (請先閲讀背面之注意事項再填寫本頁) 裝. - -22 - _136_ Λ 6 經濟部屮央橾準局兵工消f合作社印级 五、發明説明(20) 、聚乙烯類、聚並醯胺類、聚甲基戊烯類、聚硫化苯類、 聚丙烯類、聚苯乙烯類、聚尿烷類、硒類、脲類和乙烯基 類。共聚物,混合物也可用做高分子基體材料。 在上面列舉的這些高分子類別中,本發明傾向于使用 那些在多股預浸漬纱形成後,高分子一旦凝結就立刻不再 發粘的材料。另外,對于熱固性高分子,預浸漬纱剛剛開 始凝結時,高分子不應完全固化,從而保證在覆合材料製 品最後固化時纖維和樹脂之間的良好粘結。本發明傾向于 使用的高分子基體材料包括有各種工程高分子材料,如聚 雙醚酮類、聚醯胺類、環氧類和聚酯類。 用做生産回收塑料預浸漬纱的基體材料,本發明傾向 于使用的是那些含有大量回收的廢塑料的材料。回收的混 合塑料,或回收塑料與新鮮母體塑料的混合物也可以使用 。盡管任何塑料都可用作樹脂基體材料,熱塑性塑料要更 好一些。被選用做基體材料的塑料首先切碎,然後研磨成 粉末。如果回收的廢塑料是混合物,或含有一些新鮮母體 塑料,則此粉末可以通過密度分離法來進行淨化。樹脂基 體的粉末被塗覆並熔融粘結在增強纖維表面,做成預浸漬 製品。用這種預浸漬製品製成預浸漬纱和覆合材料結構的 方法與通常的預浸漬製品相同。使用回收塑料做成的預浸 漬纱並不非要柔韌才有使用價值。本發明方法可生産各種 具有不同柔韌性的預浸漬纱。能將有不同量的回收塑料的 基體材料與增強纖維結合使用,不論其柔韌性如何總是有 用的。 (請先閱讀背面之注意事項再填寫本頁) 裝- 訂' 本紙張尺度逍用中國困家樣準(CNS)甲4規格(210x297公;Ϊ) -23 - Λ 6 B6 經濟部屮央標準局兵工消t合作社印製 五、發明説明(2]j 採用了回收塑料,基體材料的成本總是要大大低于其 它基體材料。有時在回收塑料中會含有一些不融的物質, 它們可以夾帶在預浸漬纱製品中而不至于損壊加工設備或 産品質量。這些塑料並不是在一精密的擠出機中熔融,而 是在一無直接接觸的爐子中熔融,因此,那些不熔物質不 會損壊加工設備。另外,預浸漬纱和覆合材料製品的性能 主要是由增強纖維控制,因此有些混染的或污染的基體材 料是可以允許的。採用本發明的方法,回收塑料並不一定 要高度淨化即可保證預浸漬纱和覆合材料能達到合格的性 能。 一般來説,不同的塑料是不相容的,因此混合的塑料 的物理性能通常較差。工業塑料的邊角廢料在回收時往往 是按類分開的,因而是一較好的回收源。消費者使用的廢 塑料是一混合物,其混合度取決于回收方式。比如,同聚 斜苯二甲酸二乙酯瓶子混合在一起的有不是聚苯苯二甲酸 二乙酯的瓶蓋,紙紋簽和其它類型的瓶子和塑料消費品。 因此,在一聚對苯二甲酸二乙酯的廢塑料中,可能只有 80%聚對苯二甲酸二乙酯。在過去,這剩下20%是一 件麻煩事,需要採用一値昂貴的淨化過程來處理。在本發 明中,卻可允許一値很大比例的染質存在。比如,一個典 型的預浸漬纱可由50%的纖維,40%的聚對苯二甲酸 二乙酯樹脂基體和19%的染質組成。由于纖維主導著預 浸漬纱以及由此做成的任何覆合材料的性能,預浸漬纱中 可以允許一個較高百分含量的染質以無害填料的形式存在 (請先閱讀背面之注意事項再填寫本頁) 裝. •可, 本紙張尺度逍用中BH家榣準(CNS)甲4規格(210X297公釐) -24 - Λ 6 B6 2li〇4<i 五、發明説明( Ο 盡管其它類型的塑料也可以使用,但由于回塑料主要 是著重于熱塑性塑料,故本發明傾向于使用的回收是熱塑 性塑料。數種熱塑性塑料的混合物也適合于用做基體材料 。來經化學處理的固化了的熱固性塑料基本上是用作填料 。另外,回收塑料同新鮮母體塑料的混合物也可使用,並 可;能更適合于商品生産。 3.預浸漬纱的特點 美國標準ASTM — D 1 388是用于测定紡織物剛 度的標準測試方法。此法可用來表激預浸漬纱的剛性。標 準測試樣品一般是一英时寬,小于一英吋寬的樣品也可進 行測量,此差距可在最後結果中進行校正。在此對 ASTM-D1388進行描述的目的是用做參考。 標準的熱塑性預浸漬纱,比如1C I公司生産的 APC2,厚度為5密耳,或127撤米,抗撓剛度約為 216, 000毫克一厘米。具有如此剛度的預浸漬纱很 難用于纺織、編織或製成帶狀或柔韌的織物。在這些場合 中,人們傾向于使用較薄的預浸漬纱,即多股預漬纱,平 均每股厚度不超過5 0微米,這就是本發明所生産的産品 Ο 對于紡織,成帶和非織造織物製備,柔韌性很重要。 ASTM-D-1388 — 64 (1975)中規定的懸 臂染測試法就是通過测量預浸漬纱的彎曲長度來計算其抗 本紙張尺度边用中B困家標準(CNS)甲4規格(210X297公釐) (請先閲讀背面之注意事項再塡窝本頁) 裝· 線.The size of this paper is printed in Chinese National Standard (CNS) Grade A (210X297mm) -4-V. 211542 Λ 6 Β 6 Employee's Consumer Cooperative of the Central Standards Bureau of the Ministry of Economy V. Invention Instructions (2), impact strength And corrosion resistance is more advantageous. The prepregs made of thermoplastic polymers can have an infinite storage period, guarantee the quality of post-processing, and solve the problem of storage and freezing of thermosetting polymer prepregs. Thermoplastic polymer prepregs are tougher than most thermoset polymers' rigid high-joint networks. Few thermosetting polymers can meet the damage resistance and wet heat compressive strength required by the composite materials used in the aviation field. When the thermoplastic polymer is used as the matrix resin of the covering material, it is difficult to uniformly coat the fiber surface due to its high melt viscosity. Under normal circumstances, thermoplastic high molecular prepregs are very stiff, not very suitable for weaving, weaving or paving into pre-formed products, fabrics made with it are very stiff. Similarly, it is very difficult to use such a stiff thermoplastic polymer prepreg for filament winding or to prepare a shape-dyed product. During the paving process, heat must be concentrated on the contact points to make the prepreg fit the mold. Thermosetting polymers are also used as matrix resins for prepregs. Although prepregs made of thermosetting polymer prepolymers are relatively soft, they are usually very sticky and require a layer of protective release agent. This layer of anti-sticking must be removed before the prepreg is used. Although the thermosetting polymer prepreg can be used in certain occasions, such as filament winding, but because it is sticky, it needs to use a protective anti-sticking agent, so it cannot be used for textiles, numbering, or loose or The raw material of the fiber in the center of the sheet molding compound. There are two other types of prepreg yarns. One is a metal matrix prepreg yarn, which is similar to a thermoplastic prepreg yarn; one is a partially cured ceramic prepreg yarn, which is similar to a thermosetting prepreg yarn. Due to the limited market for the use of metal and ceramic laminate materials, these two prepreg yarns are generally not available in stock, and this paper standard is easy to use (CNS) A4 specifications (210X297 public goods) (please read first (Notes on the back will be written on this page.) Binding-Order · Line · -5-Printed by Employee Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs 2ii642 λ 6 __B_6 V. Description of invention (3) It has not been paid attention to in the research and development of production technology . Metal and ceramic prepregs can be produced in a processing method similar to thermoplastic and thermosetting prepregs. The prepregs of entangled fibers can be produced by a variety of impregnation methods, including hot melt method, solution method, emulsion method, suspension method, Surface polymerization method, fiber blending method, film interweaving method, electroplating method and solid powder method. In the hot melt process, fibers and resin are forced through a high-temperature mold at high shear rates to achieve impregnation. Due to the high temperature, the thermoplastic polymer may degrade. The other disadvantage of this method is that the fiber yarn is subjected to high stresses and it is difficult to impregnate the thermoplastic. The solution coating method is to dissolve the resin matrix material in a solvent, and then pass the fiber yarn through this solution, and then dry to remove the solvent. This technology has two drawbacks. First, the solubility of thermoplastic polymers is limited, and most engineering plastics are insoluble in low-boiling solvents at room temperature. In addition, as with the problems encountered with the hot melt method, the high solution viscosity makes impregnation difficult. Another problem with this process is that it is difficult to remove the solvent. Residual solvent in the prepreg can cause undesirable vapor bubbles in the coating material. The emulsion method uses a surfactant to prepare the resin into an aqueous emulsion, thereby coating a powdery matrix material with a very small particle size onto the fiber surface. The disadvantage of this process is that it is difficult to remove the surfactant from the final prepreg. The suspension coating method is also called wet powder method. This method does not use solvents and aims to solve the problem that most thermoplastic polymers do not dissolve at room temperature. In this method, the powdered resin suspension is in a liquid medium, usually water. Tree (please read the precautions on the back before filling in this page) Installation · Line · This paper standard uses the Chinese National Standard (CNS) A 4 specifications (210x297 Gonglu) -6 _ Ministry of Economic Affairs Standards Bureau Bei Gong Xiao # Printed by cooperatives Λ 6 益 4 ^ 以 _ «6_ V. Description of the invention (4) The fat does not dissolve in the liquid medium. The fibers pass through this suspension. The granular matrix resin suspension does not infiltrate the fiber surface, and higher pressure is required to consolidate the resin and the fiber to make a covering material. This prepreg is generally very sticky, so it is not suitable for weaving or weaving. Another disadvantage of this process is that it is necessary to remove the liquid medium, and the volatile substances, suspending agents or surfactants used in preparing the polymer / liquid colloid. In addition, if the suspension is improperly stirred, it may cause particles to coagulate, and polymer particles may appear during processing. In the emulsion or suspension coating process, the particle size of the suspension or latex body is smaller than that of the fiber to achieve intimate mixing. For many thermoplastic polymers that cannot be prepared by emulsion polymerization or suspension polymerization, it is very difficult to make such small particles. As the size of the particles increases, the quality of the mixture decreases, resulting in poor dispersion of the matrix resin in the coated material after consolidation and poor performance of the coated material. In the surface polymerization method, the polymer matrix material is polymerized on the fiber surface and coated. The disadvantage of this method is the need to remove solvents, polymerization inhibitors, or by-products of polymerization. Surface polymerization can only be achieved with some special techniques, such as electrochemical polymerization. Many polymer materials with commercial value cannot be produced by this method. In the fiber blending process, the polymer matrix material is made into a fibrous shape, and then mixed with the reinforcing fibers under dry conditions. Until the composite material is consolidated, these polymer matrix fibers are infiltrated to the surface of the reinforcing fiber by some method, such as melting. The effect of wetting depends on the degree of mixing of resin and fiber in the finished product. Because the resin matrix in this blend is not available (please read the precautions on the back before filling in this page), this paper scale uses the Chinese Najia Standard (CNS) A 4 specifications (210x297 male dragon) Λ 6 13 6 211542 V. Description of the invention (5) (Please read the precautions on the back before filling in this page) There are infiltrated reinforcing fibers. Under the same processing time and temperature, this yarn needs a higher pressure than the fully wetted prepreg yarn to be solidified. The method of forming a laminated material Ο film casting can solve some problems encountered by the thermoplastic polymer in the hot melting method. In this method, a film of a base material formed by hot melt method or solution method is laid on the fiber. The fiber is sandwiched between two layers of film, and then heated and pressed to press the resin into the strand. American Cyanamid Company (American Cyanamid) used electroplating to prepare a Roule metal matrix prepreg yarn. Each fiber in the yarn is fully infiltrated by the metal matrix and evenly coated. This prepreg yarn has all the properties required for weaving, weaving, filament winding, and making into bulk or sheet molding compounds. In addition, this prepreg yarn can be consolidated without high pressure. However, the disadvantage of the electroplating method is that the types of raw materials available for electroplating are limited. Most ceramic or polymer materials with commercial value cannot be plated on the surface of the reinforcing fiber. In addition, because the fiber lobe itself is used as one of the telegraphs in this method, it must be electrically conductive, so glass fibers or organic fibers cannot be electroplated. Printed by the Beigong Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs. The solid powder coating method is the latest method for the production of prepregs. The main advantage of this method is that it does not use any solvents and does not introduce large stresses during processing. In most applications using this method, the ultimate goal is to effectively form a thin, uniform, high-quality coating. The powder-forming resin must be able to maintain a solid state at ambient (temperature) or higher storage temperature. When heated, it can melt into a low-viscosity fluid and penetrate into the nonwoven fabric tow. The dry powder coating method has many advantages. The size of this paper is printed in China Standards (CNS) A4 specifications (210x297 male dragon) -8-Λ 6 13 6 Printed by the A Gong Xiao Zhi Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention Instructions (6) It does not use solvents Or water, not damp, which helps the recycling of the covering material. This is economically advantageous, making it possible for the powder to achieve a utilization rate of 10%. In addition, this method does not use expensive solvents, reducing solvent evaporation and waste. It is mainly because of these advantages that the powder coating method has been developed and further developed. Another method of coating fibers with a powdered resin matrix was invented by Atochem, which first coated the surface of the fiber with dry thermoplastic polymer powder, and then wrapped it with a thermoplastic material. However, in this process, since the resin matrix is not melted, only part of the fibers directly in contact with the foreskin are infiltrated by the resin. Compared with prepregs that are completely impregnated with resin, under the same processing conditions, such prepregs require higher pressure to be strong. In addition, similar to suspension coating, this value process requires the use of very small particles, generally less than 2◦ microns. It is costly to process thermoplastic polymers into such fine powders. The volume content of the resin matrix in the prepreg yarn generally exceeds 25% to consolidate and form a clad material structure that does not contain bubbles. If the resin content is less than 25%, additional resin will be added during the consolidation process. Pre-impregnated yarns are one-dimensional linear, but through textile, braided fiber, filament winding and other processing methods, they may become two-dimensional and three-dimensional products. In addition, the prepreg yarn can also be cut or otherwise made into a fiber-reinforced raw material for the molding process. A brief summary of the present invention The minimum bending half-length of the basic prepreg in the present invention does not exceed 15 (please read the precautions on the back before filling this page). This paper is used in the national standard (CNS) A 4 specifications (210X297 公 ®) -9-Printed by Beigongxiaot Cooperative of the Central Bureau of Economics, Ministry of Economic Affairs. Λ 6-Li 5. Description of invention (7) mm, the average thickness of the yarn per share does not exceed 10〇wm, so it is suitable It is used for weaving, weaving, filament winding, and deep processing into various useful shapes and structures. Textile and weaving processes require that the thickness of each yarn does not exceed the above limits. However, if the strands constituting the prepreg yarn are not pinned to each other, the size of the prepreg yarn need not be constrained. Each strand in the prepreg yarn is a divided unit in the overall prepreg yarn, which is much more consolidated than the prepreg yarn as a whole. The distance between strands is at least 30 times the thickness of each strand. They are neither sticky nor separate from each other, so they can be deformed independently to a large extent. The multi-strand flexible prepreg yarn in the present invention is prepared by the following three steps: (1) the reinforcing fiber yarn is dispersed to the side, all the single fibers are exposed to the surrounding environment, (2) the resin matrix is separated from The fibers are in contact with each other, causing interfacial bonding. (3) Before the resin matrix solidifies into a non-stick state; each strand of the prepreg yarn is kept separate from each other, thereby preventing significant adhesion between the strands. The basic prepreg formed in this way can be further processed into various useful products. The multi-strand flexible prepreg yarn tape of the present invention is prepared by the following three steps: (1) the reinforcing fiber yarn is dispersed to the side, all the single fibers are exposed to the surrounding environment, (2) the resin matrix and dispersion The open fibers are in contact, resulting in interfacial bonding. (3) The coated fiber yarn forms a certain shape under the action of external force, thereby making a flexible band of a certain size. The multi-ply Roule pre-impregnated yarn nonwoven fabric in the present invention is prepared by the following four steps: (1) The reinforcing fiber yarn is dispersed to the side, all the single fibers are exposed to the surrounding environment, (2 ) Resin matrix and points (please read the precautions on the back before filling in this page) The paper size is easy to use China B Jiaxiu (CNS) V4 specification (2 丨 0X297mm) -10-21 Λ 6 B 6 Ministry of Economic Affairs Printed by the Beiyang Standard Bureau Beigongxiaot Cooperative V. Description of the invention (8) The loose fibers are in contact, resulting in interfacial bonding, (3) Before the resin matrix solidifies into a non-stick state, each strand of the prepreg yarn Keep them separate from each other, thereby preventing the obvious adhesion between strands. In this way, the base fabric of the prepreg woven fabric is formed. (4) The prepreg yarn base fabric is made into a nonwoven fabric by superposition, point connection or needle punching and connection. The flexible prepreg yarn made of the resin matrix composed of recycled plastics in the present invention is prepared in the following three steps: (1) The reinforcing fibers are dispersed to the side, all the single fibers are exposed to the surrounding environment, (2) The fiber matrix composed of recycled plastic is in contact with the dispersed fibers, resulting in interfacial bonding. (3) Before the resin matrix composed of recycled plastic solidifies into a non-sticky state, the side of the adjacent dimensional dimension is kept apart, thereby Prevent obvious adhesion between each other. The basic prepreg yarn is prepared as follows. The fiber yarn as a raw material is composed of many single fibers, which are dispersed, causing the single fibers to separate from each other. The resin-based skull material is then coated on the surface of these dispersed fibers. When a sufficient coating amount is reached, the resin is liquefied, thereby forming a weft yarn that is fully wetted by the resin. As the liquefied resin matrix spreads out along the fibers, the thickness of the resin matrix becomes thinner, and finally the resin film breaks between the single fibers. If the fiber yarn is sufficiently dispersed and the dispersion state is maintained at all times, the resin liquid film will break between the single iron dimensions when it solidifies. The coated fiber, whether it is coated with a single fiber or a small bundle of fibers, is then cooled down and the resin matrix solidifies. In this process, the fiber is divided into small strands. Sometimes some single yarn dimensions will be connected between two adjacent yarns to become an inter-strand link. Each yarn strand is constantly being pulled, so that the fiber yarn is entangled (please read the precautions on the back before filling in this page). Binding-thread. The standard size of this paper is the Chinese Standard (CNS) A 4 specification ( (210X297 mm) -11-Printed by the Central Standards Bureau of the Ministry of Economic Affairs β Gongxiaot Cooperative 2U ㈤ _D6_ V. Description of the invention (9) Before the movement, it also causes the fiber to be subjected to an axial tension without slackening to me. The impregnated yarn strands can be joined together to form prepreg yarns of various thicknesses, which can then be used for winding, forming ribbons or textiles, or further processing as required. The flexible multi-strand prepreg tape of the present invention is characterized by a certain width and thickness. The flexible multi-ply prepregs usually made of fiber yarns have no definite geometric dimensions, making it difficult to process high-precision high-quality products with such prepregs. The flexible multi-strand prepreg tape of the present invention has a certain geometric size, and can be suitable for filament winding, advanced thread laying process and pultrusion. There are many types of devices that can be used to produce this flexible prepreg tape. The device most preferred to be used in the present invention is the use of two matching rollers, one with a concave surface and the other with a convex surface; or one with a groove on the surface and the other with a surface There are matching bumps. When a flexible multi-strand prepreg yarn passes through a certain geometric gap between two sticks, a prepreg yarn of this geometric size is formed. The second preferred device is the independent use of a stick with a concave surface. When the soft prepreg yarn passes a certain part of the periphery of this roller under tension, the tension and the concave shape of the stick work together to force the flexible multi-strand prepreg to gradually move to the lowest point of the concave surface of the roller, thus forming A strap with appropriate geometry. The nonwoven fabric of the multi-ply prepreg yarns in the present invention can be used to produce low-cost 2-dimensional fabrics, and it can be used as raw materials for further processing into 2-dimensional and 3-dimensional fabrics, preforms and Various laminated materials (please read the precautions on the back before writing this page). This paper uses the Chinese standard (CNS) «M specifications (210 father 297 male dragons) -12-Ministry of Economy Standards Printed by the bureau of work and the cooperative. 5. Description of invention (1C)). Therefore, the products produced using the soft nonwoven fabric of the present invention are more convenient than the woven and woven fabrics produced by using flexible multi-ply prepreg yarns. With the technique of the present invention, fabrics made with a resin matrix that is solid at room temperature can be very flexible, while fabrics produced using common sense techniques are stiff. The flexible multi-strand prepreg yarns of the present invention can be used to produce non-woven iron of flexible multi-strand prepreg yarns. This fabric uses a solid resin matrix, which is both flexible and has good fiber surface wetting. The double-fiber structure, that is, the resin matrix and the reinforcing material are both fibrous, such as mixed yarn, mixed weave, or a fabric made of a structure in which fibers and resin are alternately laid, is generally very flexible However, it does not have the infiltration of the resin fiber such as the fabric of the present invention, so in the consolidation process, this dual fiber structure requires more severe processing conditions. The fabric of the present invention is prepared by stacking and connecting the yarn strands and fibers that are connected to each other to form a flexible multi-ply prepreg yarn. The present invention tends to stack two or more prepreg yarns together to form a fabric with a weight of about 50 g / m2 to 500 g / m2, and more specifically, it tends to be about 150 g / m2 to 35◦g / m². There are many methods suitable for joining multiple strands of prepreg together, and the present invention tends to use hot-melt point connections and pin-type thread connections. The typical method is to heat and melt the multiple prepreg yarns laid together in a good choice, so that the prepreg yarns can be connected together while maintaining their original softness; Other suitable connection techniques include needle puncture, inter-fiber entanglement, and local compression. The resin matrix in the prepreg made of recycled plastic contains a large amount (please read the precautions on the back before filling in this page). This paper scale is used in accordance with the Chinese National Standard (CNS) A 4 specifications (210X297 common potion) -13 -Printed by the Employee Consumer Cooperative of the Ministry of Economic Affairs, Biyang Bureau, Λ '' 1 * Λ 6 From _ 13 6_ V. Description of the invention (Recycled plastic waste, but also contains some unused raw plastic. Although all kinds of plastic are Thermoplastics are more suitable as the matrix resin for this prepreg. The recycled plastics are first cut into short pieces and pulverized into powder. If the recycled materials are mixed with various plastics, they should be separated by density separation method. Partially purified, then coated with this powder and fused to the surface of the reinforcing fiber to make a prepreg yarn. The method of using this prepreg yarn to make a composite material structure is the same as the general prepreg yarn. The reinforcing fiber used can be in various forms , Such as grid cloth, textile or fiber yarn, reinforcing fibers can be surface coated in the form of woven fabric or dispersed fiber yarn. If fiber yarn is used, it is generally made into multiple strands of prepreg Yarns, they can be used for weaving, weaving, filament winding, tape making, non-woven fabric making, etc. The main purpose of the present invention is to produce a flexible multi-strand prepreg yarn suitable for weaving, weaving, long Wire winding, pultrusion, tape making, non-woven fabrics, and can also be processed into raw materials for bulk molding compounds. A further object of the present invention is to be able to use a variety of fibers and matrix resins to produce prepreg yarns of commercial value. Another objective is to produce a flexible prepreg yarn that contains a sufficient amount of fibers and is suitable for the economical preparation of various covering material structures. Another object of the invention is to produce a pre-impregnated fiber Impregnated yarn, therefore, during the consolidation process of the covering material, there is no need to use excessive pressure to fully infiltrate the fiber. Another object of the present invention is to produce prepreg yarn at a very high rate, which can reduce the production process The curing of the medium resin or the upgrade of the curing stage (please read the precautions on the back before writing this page) This paper standard is easy to use. The Sjia Standard (CNS) A 4 specification (210 X297 Gonglong) -14-Λ 6 Β 6 Printed by the Employee Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs V. Description of invention (Ο Another object of the present invention is to produce prepreg yarns using a cheap, coarse-grained resin matrix *, The resin particle size can be more than two times larger than the straight warp, and the short fiber resin can also be used. A further object of the present invention is to use a variety of fibers and base resins to produce prepreg tapes of commercial value. It is a kind of flexible pre-impregnated non-woven fabric, which can be used for pultrusion, filament winding, or as a raw material for bulk molding compound, or as a variety of pre-products and laminated material structures. Production of a flexible pre-impregnated non-woven fabric, which contains sufficient fibers, suitable for the economical production of 2D and 3D preforms and laminated material structures. Another object of the present invention is to produce a nonwoven prepreg, which can be laid into a high-grade laminated material structure using a processing method similar to an adhesive thermosetting prepreg tape. A further object of the present invention is to produce a non-woven prepreg fabric that can be used to prepare preforms used in the resin transfer model process, such as tubular preforms, which can be produced using a rolling tube method. Still another object of the present invention is to produce a prepreg yarn in which the matrix resin coated on the fiber surface is mainly composed of recycled plastic. Another object of the present invention is to produce a prepreg yarn which uses inexpensive plastic waste as a base material. Still another object of the present invention is to provide a production method that can use raw materials that are less harmful to processing equipment or to the final product as a matrix resin to produce this paper-scale medium-use national standard (CNS) A 4 specification (210X297 public ) " " -15-(please read the precautions on the back before filling in this page) 2 ΙΛύ43 Λ 6 Β6 Printed by the β-Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs V. Invention description (pre-impregnated yarn. The end of the invention One of the purpose is to use partially contaminated or contaminated resin, which is directly used to produce prepreg yarn without purification, and its final coating material performance can still meet the requirements. The following will pass the drawings and detailed The explanation further describes the above objectives and some other objectives that are not listed, but can be easily calculated by insiders. Detailed description of the drawings Figure 1 is the process flow for producing multiple strands of flexible prepreg in the present invention Diagram; Figure 2 shows the yarn strands in the basic flexible prepreg of the present invention; Figure 3 is the general prepreg (Figure 3a) and the prepreg of the present invention (Figure 3b ); Figure 4 shows the situation of each strand after the resin matrix on the surface of the reinforcing fiber is cured in the prepreg of the present invention. Figure 4a is before the plying, and Figure 4b is after the plying; 圔 五 is the resin in the present invention Description of the melting process of the matrix material on the fiber surface. Figure 5a is the situation when the fiber is constrained by the side, Figure 5b is the situation when it is not constrained by the side, and Figure 5c is the shrinkage neck formed by the resin matrix material between the single fibers Figure 6 is the thickness of the yarn strands of the present invention plotted against the elastic modulus of the yarn strands with different flexural rigidities; Figure 7 is the chief engineer of the present invention using a static fluidized bed as a coating device (please read first (Notes on the back and then fill out this page) The size of this paper is freely printed in accordance with the Chinese BS Standard (CNS) A4 specification (210x297 male dragon) -16-211 ^ 2 Λ 6 Β6 Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. 2. Description of the invention (Art flow chart; Figure 8 is a detailed illustration of the production of prepreg tape using the method of the present invention i Figure 9 is a detailed illustration of the production of prepreg tape using the furnaceless device of the present invention; Figure 10 is the preparation of prepreg Gauze The cross-sectional views of the two rollers with bumps and grooves respectively, that is, the 6-6 cross-section in Figure 8; Figures 1 1 a and 1 1 b are the other two types of rollers shown in Figure 10 Figure 12 is a schematic cross-sectional view of the preparation of a prepreg tape using a stick «f Figure 13 is a schematic side view of the preparation of a prepreg tape using a roller shown in Figure 12; Figure 14 is a unidirectional non-woven preform of the present invention A schematic diagram of the impregnated yarn fabric, where 14 a is a schematic axial cross-sectional view of the prepreg yarns laid together; 14b represents the point connection of the prepreg yarns laid together; Schematic diagram of non-woven fabric. The adjacent layers of prepreg are arranged in different directions. Where 1 5 a represents the laying of prepreg yarns; 1 5 b represents the point connection of the prepreg yarns laid together.// Figure 16 is a top view of the unidirectional nonwoven fabric shown in Figure 14b, indicating a typical point Connection form; FIG. 17 is a top view of the unidirectional nonwoven fabric shown in FIG. 14a, showing a typical stitch-type thread connection form; FIG. 18 is a microscope photo of the basic prepreg strands of the present invention. S Family Standard (CNS) Grade 4 (210X297) (please read the precautions on the back before filling in this page) -17-21i〇42 Λ 6 13 6 Printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 3. Description of the invention (15 large 39.9 times); Figure 19 is a photograph of the basic pre-impregnated yarn of the present invention (magnification is 1). The resin matrix material in this yarn has been consolidated to the surface of the reinforcing fiber, but The strands are not included yet; Figure 20 is a photomicrograph of the cross section of a prepreg tape made of polypropylene impregnated glass fiber under psi pressure (magnification factor 50); Figure 21 is a polyimide tape used at 20 psi pressure Cross-section of prepreg yarn tape made of acrylic impregnated glass fiber Microscope photo Η (magnification 50); Figure 22 is a microscope photograph of a cross section of a prepreg tape made of polypropylene impregnated glass fiber at a pressure of 20 psi (magnification 200) 9 FIG. 2 3 is a polymer used in the present invention Photograph of a prepreg tape made of acrylic and glass fibers; Figure 24 is a photograph of a nonwoven prepreg fabric made by interweaving a binder fiber in the present invention. Detailed description of the invention 1. Summary of the invention An important feature is to promote the infiltration of fibers and reduce the adhesion between adjacent infiltrated fibers. In order to prevent the coated fibers from sticking together, before the resin matrix is consolidated, the fibers must be Keep apart. One way to achieve fiber separation is to maintain the axial tension on the fibers and limit them to relax laterally. Figure 5 shows the melting process of a resin matrix on two fibers. In Figure 5a, due to the fiber Subject to high axial direction (please read the precautions on the back before filling in this page) This paper uses the Chinese National Standard (CNS) A 4 specifications (210X297 g) -18-Λ 6 B 6 Ministry of Economic Affairs Standard Local shellfish consumption Printed by Zuosha. Description of the invention (id tension, thus limiting the mutual closeness of the fibers; and in Figure 5b, the axial tensile force of the fiber is very low. When the resin matrix particles are melted and infiltrated on the fiber surface, The root fibers are drawn together. In Figure 5b (c), when the fibers are fully infiltrated, the thickness of the resin melt between the two fibers is still very large, in contrast, in Figure 5a (c), because The lateral movement of the fiber is blocked, and the thickness of the melt is much less than 5b (c), so that the resin film between the two fibers is easily broken, thereby separating the two resin-coated fibers, the result is shown in Figure 5 a (b) As shown. Due to the obstruction of the fiber, the resin melt necked, resulting in a tensile stress perpendicular to the fiber axis, as shown in Figure 5c. This tensile stress is due to the fact that the resin between the fibers tends to cover the fibers and be pulled apart. If the stress exceeds the fracture stress of the melt (Ty, the neck is broken. The fracture stress of the resin matrix can be used as a criterion to determine the processing conditions of the resin. For example, the tensile fracture stress of the low molecular weight resin melt is usually Very low. The strength of high molecular weight molten polymers decreases with increasing processing temperature. In addition, the tensile strength of partially solvated or plasticized polymers is lower than the strength of their corresponding pure polymers. The thickness of the dispersed prepreg is very low, so the polymer resin can be melted in a short time, and the melting temperature can be higher than the safe use temperature of the resin. In this case, the elasticity of the resin melt The strength can become very low, which helps the prepreg yarn split into multiple strands. Generally, when the resin matrix is formed, the operating temperature should be equal to or slightly higher than the melting temperature of the resin. According to the coating process of the present invention, the operating temperature It can be much higher than the softening temperature of the resin matrix, as long as it can be retained during operation (please read the precautions on the back before writing this page). China H Family Standard (CNS) Grade A 4 (210x297 gongs) -19-Λ 6 Β6 Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Description of invention (^ In the room, the matrix resin will not degrade or rise to the bottom Only one curing stage is required. In the present invention, the residence time can be very short, so there is no obvious degradation of the matrix material or the resin curing stage upgrade. The operating temperature of the heating furnace or heater is related to the residence time of the fiber and resin in the furnace If the residence time is very short, the temperature can be adjusted higher, and vice versa. Under this condition, the operating temperature can be higher than the temperature at which the matrix resin material starts to degrade or the curing stage begins to upgrade. As long as the residence time is kept short, the matrix resin The material will not stay at such a temperature for a long time to cause degradation or curing upgrade. In a viscoelastic liquid, the factors that cause its tensile strength to decrease will also cause its surface tension to decrease and the viscosity of the liquid to decrease. Therefore, there are The conditions conducive to fiber dispersion are also conducive to the diffusion of liquid along the fiber. In this way, the shape of the droplet shown in Figure 5a can be changed by Change the material and change the processing conditions, reduce the elasticity of the liquid to carry out the transformation. By restricting or preventing the strands from moving closer to each other, the length of the neck of the resin matrix before crushing, L · · can be greatly reduced, so that the cross-sectional area can be changed It is thin. Therefore, the force required to cause neck collapse is reduced by Fn ». Keeping the fiber dispersed during resin infiltration and consolidation will help to achieve a single coating of the fiber. Application of external force can help achieve fiber The rupture of the liquid film between them. Blowing hot air in the direction perpendicular to the plane of the yarn dimension will help to break the liquid film between the iron dimensions, so that the dispersed yarn dimension passes through a grooved stick, and the fibers are The pressure on the roller shaft will also help to split the liquid film between the fibers. Many similar mechanical devices can be used to help the dispersion of the fibers between each other. In order to produce the basic prepreg of this invention , The resin matrix must infiltrate the fiber well. Only in this way can the additional bonding not be used (please read the precautions on the back before writing this page) 4 Cells (210 > < 297 public release) -20-9.1 1ϋ4 ^ _Β6 9.1 1ϋ4 ^ _Β6 Printed by the Employee Consumer Cooperative of the Bureau of Standards and Economy of the Ministry of Economic Affairs V. Invention description (id agent can still achieve adhesion between the resin matrix and the fiber. Resin A resin matrix liquefier, such as a melter or furnace, can be used to infiltrate the fiber. The resin is liquefied by heating. To achieve better infiltration, the matrix resin needs to be kept in the selected liquefaction equipment for a sufficient residence time, so that The resin fully wets the fiber. There are many types of liquefiers available on the market, including any radiant or conductive furnace. For drying resin powder, it is better to use a radiant furnace. In addition; the furnace can also be replaced by a heated mold Used as a liquefier. The liquefaction method of the resin matrix is a part of the present invention. Any size of base resin material can be used to coat fibers, including coarse particles and short fibers. Because in the present invention, the matrix resin liquefies and along the fiber Wetting and spreading of the surface, thereby reducing the resins normally encountered when using large-grain resins and fine-diameter reinforcing fibers The problem of mixing and dispersion between the matrix and the fiber. Therefore, in the process of the present invention, the particle size f of the matrix resin material is a very critical factor, and its range can be generally equal to or less than that of the fiber used in the coating process. The diameter or thickness is many times larger than the fiber diameter, including the use of short fibers. Prior to the present invention, no one has successfully used large diameter particles of resin as the base material. This approach can greatly save costs. 2. The choice of raw materials There are many types of fibers that can be used as fiber yarns, including: glass fibers, strontium fibers and graphite fibers; organic fibers, especially liquid crystal fibers such as aldamine and aromatic polyester; ceramic fibers, such as suohua Silicone; Mixed-copy paper scales are used in China National Standard (CNS) A4 specifications (210X297 public goods) (please read the precautions on the back and then fill out this page) Pack-* tT. -21-Ministry of Economic Affairs Bureau of Standards Printed by Beigong Consumer Cooperative Society Λ 6211 ^^-V. Description of the invention (id spun fibers, such as amide / glass, aldamine / glass, aldamine / glass / glass and glass / glass. Generally come If the diameter or thickness of the fiber exceeds 25 microns, it cannot be used. For example, it is meaningless to use boron strands with a diameter of 140 microns, because such a size of fiber cannot be made very soft. In addition, the selected The fiber fiber should be used as the reinforcing material fiber and entangled fiber. The following dimension suitable for this process should be able to maintain thermal stability at the process temperature when the resin matrix is consolidated. In addition, the glass transition of the fiber is subjected to temperature and melting The temperature is higher than room temperature, and the melting temperature is higher than the consolidation processing temperature of the covering material. Both thermoplastic and thermosetting polymers can be used as the matrix resin material. The polymer materials tending to be used in the present invention should generally not be sticky, During use after curing, the glass transition temperature or melting temperature should be higher than room temperature, especially the glass transition temperature should be higher than room temperature. Therefore, some elastic materials, rubber and leather, are very soft at room temperature and cannot be used as a matrix material. Some thermosetting polymers are sticky at normal operating temperatures. It can be operated at a low temperature to reduce tackiness and thus can be used as a resin matrix material. Some non-high molecular materials such as copper, low melting point metals, ceramic mother skulls, etc. can also be used as matrix materials. The matrix material can be any shape, such as particles, powder and short fibers. There are many types of polymer materials. Examples are as follows: ABS, acetals, acrylics, alkyd polyesters, allyls, amines, Ring gas, gas plastic, furan, melamine, nylon, phenolic, phenyl oxide and phenyl ether, polyamidoamine, polyamido-aldialdehyde, polybutene, polybasic acid Esters, polyesters, polydiether ketones, polyether ketones, polyacrylamide ethers Zhang Scale General Chinese National Standard (CNS) A 4 specifications (210x297 public goods) (please read the notes on the back before filling This page) installed.--22-_136_ Λ 6 Printed Level 5 of the Ordnance Service Cooperative of the Central Bureau of the Ministry of Economic Affairs, Fifth, Invention Instructions (20), Polyethylenes, Polyamides, Polymethylpentenes , Polysulfide benzenes, polypropylenes, polystyrenes, polyurethanes, seleniums, ureas and vinyls. Copolymers and mixtures can also be used as polymer matrix materials. Among the categories of polymers listed above, the present invention tends to use materials that, after the formation of multiple prepreg yarns, once the polymer coagulates, no longer become tacky. In addition, for thermosetting polymers, the polymer should not be completely cured immediately after the prepreg yarn starts to coagulate, so as to ensure good adhesion between the fiber and the resin when the laminated material product is finally cured. The polymer matrix materials tending to be used in the present invention include various engineering polymer materials, such as polydiether ketones, polyamides, epoxys, and polyesters. Used as a base material for the production of recycled plastic prepreg yarns, the present invention tends to use materials that contain large amounts of recycled waste plastic. Recycled mixed plastic, or a mixture of recycled plastic and fresh parent plastic can also be used. Although any plastic can be used as the resin matrix material, thermoplastics are better. The plastic selected as the base material is first shredded and then ground into a powder. If the recovered waste plastic is a mixture, or contains some fresh parent plastic, the powder can be purified by density separation. The powder of the resin matrix is coated and melt-bonded to the surface of the reinforcing fiber to make a prepreg. The method for forming the structure of the prepreg yarn and the covering material with this prepreg is the same as that of the usual prepreg. Pre-impregnated yarn made from recycled plastics is not necessarily flexible to be useful. The method of the invention can produce various prepreg yarns with different flexibility. It is possible to combine matrix materials with different amounts of recycled plastic and reinforcing fibers, regardless of their flexibility. (Please read the precautions on the back and then fill out this page) Binding-Ordering This paper size is easy to use Chinese Standards (CNS) A 4 specifications (210x297; Ϊ) -23-Λ 6 B6 Ministry of Economics Standard Printed by the Bureau of Ordnance Industry Co., Ltd. V. Description of the invention (2) j Recycled plastics are used, and the cost of the base material is always much lower than other base materials. Sometimes the recycled plastics contain some insoluble substances, they Can be entrained in prepreg yarn products without damaging processing equipment or product quality. These plastics are not melted in a precision extruder, but in a furnace without direct contact. Therefore, those non-melted materials It will not damage the processing equipment. In addition, the performance of prepreg yarns and laminate materials is mainly controlled by reinforcing fibers, so some mixed or contaminated matrix materials are allowed. With the method of the present invention, recycled plastics are not It must be highly purified to ensure that the pre-impregnated yarn and covering materials can achieve qualified performance. Generally speaking, different plastics are incompatible, so the physical properties of mixed plastics are usually Poor. The corner waste of industrial plastics is often separated by category when recycling, so it is a good recycling source. The waste plastics used by consumers are a mixture, and the degree of mixing depends on the recycling method. For example, homopolymer oblique Diethyl phthalate bottles are mixed with non-diethyl phthalate bottle caps, paper labels and other types of bottles and plastic consumer products. Therefore, in a polyethylene terephthalate In waste plastics, there may be only 80% polyethylene terephthalate. In the past, the remaining 20% was a hassle, requiring an expensive purification process. In the present invention, it is allowed A large proportion of chromaticity exists. For example, a typical prepreg yarn can be composed of 50% fiber, 40% polyethylene terephthalate resin matrix and 19% chromaticity. Since fibers dominate The performance of impregnated yarn and any covering materials made from it, a higher percentage of chromatin can be allowed to exist in the form of harmless filler in the pre-impregnated yarn (please read the precautions on the back before filling this page) . • Yes, Scale paper Xiao Yao home registration with the BH (CNS) A 4 size (210X297 mm) -24 - Λ 6 B6 2li〇4 < i V. Description of the invention (Ο Although other types of plastics can also be used, since recycled plastics are mainly focused on thermoplastics, the recycling used in the present invention tends to be thermoplastics. A mixture of several thermoplastics is also suitable for Used as a matrix material. The chemically cured thermosetting plastic is basically used as a filler. In addition, a mixture of recycled plastic and fresh parent plastic can also be used, and can be more suitable for commercial production. 3. Pre-impregnation Yarn characteristics ASTM-D 1 388 is a standard test method for determining the rigidity of textiles. This method can be used to express the rigidity of prepreg yarn. The standard test sample is generally one inch wide and less than one inch wide Samples can also be measured, and this gap can be corrected in the final result. The purpose of describing ASTM-D1388 here is for reference. Standard thermoplastic prepreg yarn, such as APC2 produced by 1C I, has a thickness of 5 mil Ears, or 127 meters, the flexural rigidity is about 216,000 milligrams per centimeter. Pre-impregnated yarns with such rigidity are difficult to use for weaving, weaving or It is made into a ribbon or flexible fabric. In these occasions, people tend to use thin prepreg yarns, that is, multi-strand prepreg yarns, with an average thickness of not more than 50 microns per share, which is the product produced by the present invention Ο For the preparation of textile, tape and nonwoven fabrics, flexibility is very important. The cantilever dyeing test method specified in ASTM-D-1388 — 64 (1975) is to measure the bending length of the prepreg yarn to calculate its paper resistance. Use the middle-B sleepy home standard (CNS) A 4 specifications (210X297 mm) (please read the precautions on the back before you go to this page) to install the line.

經濟部屮央標準局员工消t合作社印M -25 - 經濟部屮央標準局员工消费合作社印製 ^11542_Μ 五、發明説明( 撓剛度。彎曲長度是預浸漬纱的重量和其剛度之間相互作 用的量度,是通過預浸漬纱在其自身重量下的彎曲表徴的 。它表示預浸漬纱在一平面上受重力而彎曲時的剛度。 預浸漬纱的外表面的彈性應變最大。一般來說,當增 強纖維受到◦. 3%以上的壓縮形變時,就會産生皺折。 對于一個彈性層,它的應度同該彈性層的厚度及最小彎曲 半徑有下列的關係: h = 2 R· , ♦ e 弟山 其中,h是彈性層的厚度 RB是彈性層的彎曲半徑 e為所能承受的最大表面應變 比如,當一個彈性層受到一値最小彎曲半徑為1〇毫 米,最大應變為◦. 3%的時候,其厚度不可能超過60 微米。最小彎曲半徑取決于産品的幾何形狀,而最大應變 取決于增強纖維,因此彈性層的厚度既取決于材料性質, 也取決于它的實際使用。這種關僳如圖6所示。 4.預浸漬纱及産品的生産 用來生産預浸漬纱的方法在圖1中已用一簡化了的流 程圖進行了說明。下面對選用的設備加以描述。下面的描 述應同圖1結合在一起閲讀,這樣可加深理解本生産方法 。圖1中101為纖維纱的送纱裝置,可以是纱筒或卷纱 (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國B家標準(CNS)甲4規格(210x297公釐) -26 - Λ 6 13 6 五、發明説明( 盤。纖維纱可以直接由前一道生産工藝提供,也可由其它 來源供貨。纖維纱是由許許多多的單纖維104組成,在 分散工藝過程103中,這些單缕維相互之間被分散開, 形成在截面方向分散的單纖維104。對于含有6000 根單纖維的纱,通常分散的寬度為2英吋。在塗覆工藝過 程1 05中,分散開的單纖維1 04被塗上基體材料。當 塗覆量達到要求以後,即成為塗覆過的纖維10 6。然後 這些塗覆在纖維表面的基體材料在潤濕工蕤過程17中液 化,最後形成充分浸潤的缕維纱10 8。 經濟部屮央標準局员工消费合作社印製 (請先閱讀背面之注意事項再填寫本頁) 當液化了的基髏樹脂沿著纖維104表面舖展開時, 基體樹脂的厚度逐漸變薄,最後,位于纖維104之間的 樹脂薄膜破裂(見圖5),這一現象發生在分裂步驟 1 09的過程之中或之前。如果被浸潤的纖維纱1 08分 散得很好,並且一直維持的話,則分裂步驟109就可免 掉,因為位于纖雒104之間的樹脂膜會在固結過程中破 碎。另外,如果纖維纱分散得很好,樹脂膜就不會將各纱 股并連在一起,因此也就不再需要一個過程去破碎股與股 之間的樹脂膜了。塗覆後的纖維1 1 0可以是單根的,也 可以是分股的,通過一冷卻過程112冷卻,樹脂基體在 此過程中凝固,而纖維110也在此過程中集束成許多獨 立的纱股。有時在冷卻過程112中,單根纖維110會 與鄰近的纱粘并而成為股間連接纖維1 1 1。纱股1 1 3 通過一牽引裝置114不斷被拉牽,以維持纖維纱102 不斷地輸送到条統中來,并對纖維104産生一個軸向拉 本紙張尺度边用中國B家«準(CNS)甲4規格(210x297公釐) -27 - Λ 6 Β6 經濟部屮央標準局员工消贽合作社印製 211 _ 五、發明説明(y 力,使其不會自行鬆散,從而維持樹脂和纖維結合為一體 。各個獨立的纱股在過程115中集合起來,組成厚度不 同的預浸漬纱,然後通過步驟116收卷起來,或根據不 同要求作進一步的加工。 預浸漬纱帶的生産是通過將塗覆好的纖維纱引入一餾 具有一定幾何形狀的缝隙,迫使纖維纱在此缝隙内壓合在 —起,從而形成一個已知幾何形狀的柔韌的纱帶。用于生 産柔韌預浸漬纱帶的裝置有多種,如圖8至圖13所示。 但最傾向于使用的則是如圖10和圖11所示的兩個相配 合的锟子,一個下凹,一個上凸,或者一個刻有凹槽,另 一個則帶有對應此凹槽的凸塊,凸塊可正好嵌入另一棍子 的凹槽内。當塗覆好的纖維通過兩個锟子之間已知幾何尺 寸的縫隙時,就形成了該幾何形狀的預浸漬纱帶。兩個棍 子一般是採用常用的方法在一定的壓力下相互作用的,比 如汽缸、彈簧或液壓缸,安裝在其中的一値棍子上。棍子 裝置位于塗覆生産線的出口端,或者代替塗覆熔融生産線 中的熔融爐。 其次傾向于採用的生産柔韌預浸漬纱帶的裝置是一個 表面下凹的滾棍,如圖12和圖13所示。塗覆過的纖維 纱受牽引力通過滾棍圓周表面上的某一點,在拉力和滾棍 凹面構型的雙重影響下,纖維纱逐漸移向滾锟凹面的最低 點,從而形成了具有一定外形的帶子。加在纖維纱上的張 力可以通過糸統中的收卷裝置施加。該凹面滾锟可以裝在 塗覆生産線的産品終端,如果滾锟被加熱,並且對纖維纱 (請先閱讀背面之注意事項再塡、窝本頁) 裝· -·»- 線. 本紙張尺度边用中國國家標準(CNS)甲4規格(210x297公货) -28 - Λ 6 13 6 經濟部屮央櫺準局员工消費合作社印製 五、發明説明(y 的壓力足夠大時,它可以取代塗覆熔融生産線中的熔融爐 。其次,採用表面平直的滾锟也可用來生産預浸漬纱帶。 用預浸漬纱生産非織造織物的方法描述如下,請參考 閲謓圖1 4至圖1 7。 纱股113,股間連接纖維111和獨立的單纖維 1 1 0共同組成了預浸漬纱1 33。該預浸漬纱包括有增 強纖維132和塗覆在其表面上的樹脂基體。預浸漬纱 133通過冷卻過程112冷卻以後,按所需的織物構型 排列。圖14a是按單向叠加形式排列,圖15a是多向 昼加形式排列。為了增加織物139的強度,在排列時最 好將預浸漬纱1 3 3相互搭接起來。 當預浸漬纱排列好以後,就將它們結合在一起。圖 1 4 b和圖1 5 b所示的方法是通過熱熔融將叠放好的預 浸漬纱133在選定好的一些地點粘結起來,從而形成了 點粘接的織物139。在結合預浸漬纱133時,採用一 個或多個點粘接1 3 7。採用這種點粘結的方法,各點之 間相分散,並不連缠,可以得到柔韌的織物139。除此 之外,採用縫紉、針刺、壓力點連接或噴水錘也可將預浸 漬纱結合在一道。圖17是採用縫紉方法的一個例子。縫 線可同預浸漬纱133的進行方向成一角度,以便有助于 連接加工。本發明的非織造織物中設有相互交織在一起的 增強纖維。但如圖24所示,可以用粘結劑纖維或粘結劑 纱線將增強纖維交織在一起。在這種情況下,所得到的織 物是由不同的纖維紡織而成,但是單就增強纖維來說,仍 (請先間讀背面之注意事項再塡寫本頁) 本紙張尺度逍用中a Η家標準(CNS)甲4規格(210x297公龙) -29 - 經濟部屮央橾準局员工消赀合作社印製 Λ 6 Β6 五、發明説明( 是非織造的。 製備好的織物139,用繾繞的方法收卷起來,以備 進一步使用。另外,預浸漬纱133或織物139還可以 進加工成2維或3維的非織造織物,甚至做成形狀覆染的 預成型體。例如,採用多類舖放或滾管工蓊,可作成管式 預成型髏,常用于生産各種結構的別品,如高爾夫球桿, 網球拍、帆船桅桿等。 要達到良好的樹脂浸潤,需保證有足夠的滯留時間, 以使得樹脂基體液化並潤濕纖維。在此浸潤過程中,纖維 不能允許横向鬆散,這一點甚為重要。這一點可以通過在 纖維纱上施加一定的張力來實現。當纖維被浸潤得比較充 分時,液化樹脂基體通常包覆在由多根缕維组成的纖維股 上。為了生産出本發明的預浸漬纱,缕維股之間一定相互 分開·,如圖2所示。只有這樣才能實現單獨塗覆的多股預 浸漬纱。在圖2中,單獨塗覆的纖維股用134表示,它 是由增強纖維132和基體樹脂材料131組成的。每一 股纱134若能完全獨立,如136所示的那樣是最理想 的。但股纱1 34之間也可能會有一些股間連接物1 3 5 ,這些股間連接物通常是由單纖維132和在其表面塗覆 的樹脂材料131所組成。塗覆過的股纱的抗彎剛度比完 全固結的預浸漬纱要低。 現在請參看圖3和圖4。在通常的預浸漬纱生産中, 纖維纱多是由含800到1 3, 000根單纖維132的 股纱所組成。每根單纖維132的直徑或厚度一般為4到 本紙5t又度逍用中國國家標準(CNS)甲4規格(210x297公址) (請先閲讀背面之注意事項再填寫本頁) 裝- 線_ -30 _ Λ 6 Β6 經濟部屮央標準局CX工消费合作社印製 五、發明説明( 1 6微米,這些纖維纱塗覆上預浸漬纱基體材料1 3 1後 就形成了預浸漬纱1 3 0。用通常的生産工藝製備的預浸 漬纱的纱股1 34,寬度為1/8到1/2英吋。這褢所 說的纱股,在通常的工藝中是指獨立的,一般只含有一股 的預浸漬纱1 30。它們可以獨立使用,也可同其它只含 一股的預浸漬纱130—道使用,製備成覆合材料結構。 而本發明中的纱股134是獨立的,由充分浸潤了的纖維 132組成,每一股的平均厚度等於或小於100微米, 小於5 0微米則更好。這些纱股集合起來,從而形成任意 厚度的多股預浸漬纱1 3 3。 在整値加工過程中,如果纖維132通過纖維分散器 充分分散開,並維持一個足夠的張力,則纖維132就不 會横向鬆散,從而就可産生或維持纱股之間的分離。纖股 之間的分離可在加熱爐内進行的樹脂浸潤過程之前或同時 發生。而通常情況下,這種分離是在液化的樹脂1 3 1沿 著纖維132軸向浸潤時發生的。分離的方法有多種,比 如可採用機械分離器,包括帶有刻槽的锟子,刀子,激光 切割器,還有向垂直於分散開的纖維纱方向提供對流,等 等。 單股預浸漬纱130含有多個纱股134,它們的厚 度和寬度不等。纱股134的平均厚度小於100微米, 但小於50徹米則更好。纱股134的最大厚度是100 微米,而最小的厚度則為該纱股中所使用的增強纖維 132的未浸漬樹脂時的單纖維直徑或厚度。一般來説, (請先閱讀背面之注意事項再塡寫本頁) 裝- 訂 本紙張尺度逍用中B國家櫺準(CNS)甲4規格(210x297公世) -31 - r* 66 經濟部屮央標準局员工消t合作社印製 五、發明説明( 纱股134的長度大於其寬度,而其長度和寛度均大於它 的厚度。通常纱股134的厚度要遠遠小於其寬度,其寬 度一般小於2,◦00徹米。另外,纱股134的平均長 度最好是大於其厚度的3 0倍以上。 5.傾向於使用的設備 有一點需要說明一下,以上描述的各個步驟閫明了本 發明的生産方法,但它們並不僅僅局限於本文中所列舉的 各値實例。為了更好地理解前面所提到的各個工藝步驟, 下面將列舉一個例子。此例是採用了圖7中所示的設備8 〇 現在請參看圖7。缕維纱1 1受到牽引,從送纱棍 10通過設備8,最後收集在收卷輪12上。收卷輪12 受到驅動,在一可變的速度下旋轉,而送纱輪則不需用動 力去驅動。線速度一般為每分鐘3到3 0米。較慢的速度 也可採用,但從經濟角度上則不可取,因為預浸漬纱的單 位時間産量降低,並且由於爐内滯留時間長,基體樹脂會 降解,或固化度升级,從而樹脂受到破壞。更高的線速度 也是可行的,只要能夠保證以下幾點:應配好輔助裝置, 減少纖維纱的振動;塗覆樹脂材料的單元設備應有足夠的 長度以保證足夠的塗覆量;加熱爐的長度和溫度足以能使 基體樹脂液化。在某些情況下,只要條件合適,每分鐘 3 ◦米以上的線速度也是可採用的,夾送輪14的作用是 牽引從加熱爐1 6中出來的纖維1 1。收卷輪1 2在一恒 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國國家標準(CNS)甲4規格(210X297公埂) -32 - 211042 經濟部屮央標準局员工消费合作社印製 五、發明説明(3(j 定的張力下缠繞,這是藉著使用一張力控制器來調節缠繞 器速度來實現的(圖中没有顯示)。纖維纱通過設備8的 速度可由夾送輪的旋轉速度來控制。 在本實例中,纖維纱的供給是直接從預先缠繞好的纖 維纱筒上提供的。纖維纱的供給也可直接來自前一道生産 工藝。在送纱過程中,應避免將纖維纱1 1中的纖維1 3 捻轉。纖維加捻以後很難分散。另外,毎卷纱自身張力應 控制好,這將有助於維持在整個浸漬過程中張力恒定。在 送纱裝置與纖維纱分散器18之間也可設置一纖維纱導向 板,以幫助引導纖維通過分散器18。 在本實例中,纖維纱分散器18採用了一糸列的锟子 1 7和一空氣梳1 9,從而將纖維纱1 1分散成單根纖維 1 3。通常設有兩組辊子1 7,一組設在空氣梳1 9之前 ,一組設在其之後。棍子17主要有兩個作用:(1)是 給纖維纱施加張力從而減少在操作中纖維纱的横向鬆弛; (2)是減少纖維纱的振動。锟子可更用任何適宜的材料 做成,可以具有各種不同表面特擻。但是採用平滑的聚四 氟乙烯棍子更為合適,因為這種材料可使纖維分散良好。 在所有使用的锟子當中,至少要有一個,最好是最造近塗 覆裝置20的入口處的锟子,一定要採用導體材料,最好 是不锈銅,這樣纖雒纱在進入塗覆糸統2 0之前可以接地 。空氣梳19則已是一項眾所周知的工藝技術。 纖維纱11在離開送纱輪10以後,進入第一組棍子 1 7,纖維被分散開。第一組棍子的排列方式可使纖維纱 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度边用中國租家樣準(CNS) f 4規格(210x297公茇) -33 - Λ 6 Β6 經濟部屮央標準局员工消费合作社印製 五、發明説明( 11在通過時像紡織一樣,先從第一個棍子的上面,然後 緊接著從第二値輥子的下面通過,這樣可對纖維施加一個 衡定的張力,並減少纖維13的振動。纖維纱11然後進 入空氣流19,在那褢受到強制的空氣流的作用進一步分 散。舉例來說,含有3,◦◦0根纖維的纱通常要分散成 1英时以上的寬度才可保證所得到的預浸漬纱性質柔韌。 由於同樣的原因,第二組棍子的排列與第一組棍子的排列 方式相類似。這組锟子的最後一値最好是由導電材料做成 ,這樣纖維就可在進入覆合塗覆裝置前接地。 分散器18的裝置可以採用各種不同類型,其中包括 :平滑的,或刻有凹槽或有凸面的辊子或滾筒;空氣梳; 空氣梳和棍子或滾筒結合使用;噴氣流;超磬波分散器; 以及液體浴。在選擇纖維纱分散器時主要應考慮的是其是 否能將缕維分散成一寬帶,最好此寬度僅有單纖維厚,並 且此分散器不會損壊纖維。 在分散裝置18和塗覆器20之間,還可隨不同的應 用情況增加其它的工藝步驟。比如,在生産特殊用途的預 浸漬纱時,可能還要採用清除纖維表面浸潤劑,表面活化 和施加粘結劑的裝置。 纖維13然後進入塗覆裝置20,基體樹脂材料在此 裝置中塗覆到纖維13的表面。在纖雒13進入和通過塗 覆裝置20時,仍然保持分散狀態。可以使用的塗覆裝置 有很多種類,下面將舉例説明。不過粉末噴塗裝置和靜電 流化床兩種方法更為合適。採用粉末噴塗裝置時,一般來 本紙張尺度逍用中a國家標準(CNS)甲4規格(210X297公龙) ~ -34 - (請先閱讀背面之注意事項再塡寫本頁)Printed by the Ministry of Economic Affairs, Bureau of Standards, Employee Consumer Cooperative M-25-Printed by the Ministry of Economic Affairs, Bureau of Standards, Employee Consumer Cooperative ^ 11542_Μ V. Description of invention (Flexural stiffness. The bending length is the weight of the prepreg and its stiffness. The action is measured by the bending of the prepreg under its own weight. It represents the stiffness of the prepreg when it is bent by gravity on a plane. The external surface of the prepreg has the largest elastic strain. Generally speaking , When the reinforcing fiber is compressed and deformed by more than 3%, wrinkles will be generated. For an elastic layer, its degree of compliance has the following relationship with the thickness and minimum bending radius of the elastic layer: h = 2 R · , ♦ e Dishan where h is the thickness of the elastic layer RB is the bending radius of the elastic layer e is the maximum surface strain it can withstand. For example, when an elastic layer is subjected to a minimum bending radius of 10 mm, the maximum strain is ◦ . At 3%, the thickness cannot exceed 60 microns. The minimum bending radius depends on the geometry of the product, and the maximum strain depends on the reinforcing fiber, so the thickness of the elastic layer is taken The nature of the material also depends on its actual use. This concern is shown in Figure 6. 4. Production of prepreg yarns and products The method used to produce prepreg yarns has been simplified in Figure 1 The figure explains. The following describes the selected equipment. The following description should be read in conjunction with Figure 1, so as to deepen the understanding of the production method. 101 in Figure 1 is the fiber yarn feeding device, which can be a bobbin Or roll the yarn (please read the precautions on the back before filling in this page). The paper size is easy to use Chinese B family standard (CNS) A 4 specifications (210x297 mm) -26-Λ 6 13 6 V. Description of invention (disk. The fiber yarn can be directly provided by the previous production process, or it can be supplied from other sources. The fiber yarn is composed of many single fibers 104, and in the dispersion process 103, these single strands are dispersed from each other to form Single fibers 104 dispersed in the cross-sectional direction. For yarns containing 6000 single fibers, the width of the dispersion is usually 2 inches. In the coating process 105, the dispersed single fibers 104 are coated with a matrix material. The coating amount meets the requirements After that, it becomes the coated fiber 106. Then the matrix material coated on the surface of the fiber is liquefied in the wetting process 17 and finally forms a fully wetted strand yarn 108. Employee of the Central Standards Bureau of the Ministry of Economic Affairs Printed by a consumer cooperative (please read the precautions on the back before filling in this page). When the liquefied base resin spreads along the surface of the fiber 104, the thickness of the base resin gradually becomes thinner. Finally, the resin between the fibers 104 The film ruptures (see Figure 5), this phenomenon occurs during or before the splitting step 09. If the infiltrated fiber yarn 1 08 is well dispersed and maintained, the splitting step 109 can be avoided Because the resin film located between the fibers 104 will break during the consolidation process. In addition, if the fiber yarns are well dispersed, the resin film will not tie the yarn strands together, so there is no longer a process to break the resin film between the strands. The coated fibers 1 1 0 can be single or split, which is cooled by a cooling process 112, the resin matrix solidifies during this process, and the fibers 110 are also bundled into many independent yarns during this process share. Sometimes during the cooling process 112, a single fiber 110 will stick to the adjacent yarn and become the inter-strand connecting fiber 11. The yarn strands 1 1 3 are continuously pulled by a traction device 114 to maintain the continuous delivery of the fiber yarn 102 into the system, and an axial drawing of the fiber 104 is generated. ) A4 specifications (210x297 mm) -27-Λ 6 Β6 211 printed by the Employee Consumers ’Cooperative of the Ministry of Economic Affairs ’s Central Standards Bureau _ V. Description of invention (y force, so that it will not loose itself, thereby maintaining the combination of resin and fiber As a whole, the individual yarn strands are assembled in process 115 to form prepreg yarns with different thicknesses, which are then rolled up in step 116, or processed further according to different requirements. The production of prepreg yarns is carried out by coating The covered fiber yarn introduces a gap with a certain geometric shape, forcing the fiber yarn to be pressed together in this gap, thereby forming a flexible ribbon with a known geometry. It is used to produce flexible prepreg tape There are many kinds of devices, as shown in Figures 8 to 13. But the most preferred ones are the two matched rollers shown in Figure 10 and Figure 11, one concave, one convex, or one engraved Groove, another There is a bump corresponding to this groove, and the bump can fit into the groove of another stick. When the coated fiber passes through the gap of the known geometric size between the two rollers, the Geometry pre-impregnated tape. The two sticks are generally interacted under a certain pressure using common methods, such as cylinders, springs or hydraulic cylinders, which are installed on one of the sticks. The stick device is located on the coating production line Or replace the melting furnace in the coating and melting line. The second preferred device for producing flexible prepreg tape is a roller with a concave surface, as shown in Figures 12 and 13. Coated The fiber yarn is pulled by a point on the circumferential surface of the roller under traction. Under the dual influence of tension and the concave configuration of the roller, the fiber yarn gradually moves to the lowest point of the concave surface of the roller, thereby forming a belt with a certain shape. The tension on the fiber yarn can be applied by the winding device in the system. The concave roller can be installed at the product terminal of the coating line. If the roller is heated and the fiber yarn (please read first Read the precautions on the back of this page, and then on this page) Install ·-· »-line. This paper uses the Chinese National Standard (CNS) A 4 specifications (210x297 public goods) -28-Λ 6 13 6 Ministry of Economic Affairs Printed by the Employee Consumer Cooperative of the Bureau of Employee V. Description of invention (When the pressure of y is large enough, it can replace the melting furnace in the coating melting production line. Secondly, the roller with a flat surface can also be used to produce prepreg tape The method for producing nonwoven fabrics with prepreg yarns is described below, please refer to Figure 14 to Figure 17. Yarn strands 113, inter-strand connecting fibers 111 and independent single fibers 1 1 0 together constitute prepreg yarns 1 33 The prepreg yarn includes reinforcing fibers 132 and a resin matrix coated on its surface. After the prepreg yarn 133 is cooled by the cooling process 112, it is arranged according to the desired fabric configuration. Fig. 14a is arranged in a unidirectional superposition, and Fig. 15a is arranged in a multidirectional diurnal form. In order to increase the strength of the fabric 139, it is preferable to overlap the prepreg yarns 1 3 3 in the arrangement. When the prepregs are aligned, they are combined. The method shown in Fig. 14b and Fig. 15b is to bond the stacked prepreg yarns 133 at selected locations by hot fusion, thereby forming a point-bonded fabric 139. When bonding the prepreg 133, one or more point bonds 137 are used. With this point bonding method, the phases between the points are dispersed without being intertwined, and a flexible fabric 139 can be obtained. In addition to this, pre-preg yarns can also be combined using sewing, needle punching, pressure point connection or water jet hammer. Fig. 17 is an example of a sewing method. The stitching may be at an angle to the direction of advancement of the prepreg 133 to facilitate the joining process. The nonwoven fabric of the present invention is provided with reinforcing fibers intertwined with each other. However, as shown in Fig. 24, the reinforcing fibers may be interwoven with binder fibers or binder yarns. In this case, the resulting fabric is woven from different fibers, but as far as the reinforcing fibers are concerned (please read the precautions on the back side before writing this page). Η Standard (CNS) A4 specifications (210x297 gongs) -29-Printed Λ 6 Β6 by the Employee Consumers ’Cooperative of the Ministry of Economic Affairs of the Central Committee of the Ministry of Economic Affairs Λ 6 Β6 V. Description of invention (It is non-woven. The prepared fabric 139, used The winding method is wound up for further use. In addition, the prepreg yarn 133 or the fabric 139 can also be processed into a 2-dimensional or 3-dimensional nonwoven fabric, or even made into a shape-dyed preform. For example, using Various types of laying or rolling pipe cutters can be made into tubular preformed skulls, which are often used to produce other products of various structures, such as golf clubs, tennis rackets, sailing masts, etc. To achieve good resin infiltration, make sure that there are enough The residence time is such that the resin matrix liquefies and wets the fiber. In this infiltration process, the fiber cannot be allowed to loosen laterally. This is very important. This can be achieved by applying a certain tension on the fiber yarn. When the fiber is When the infiltration is relatively sufficient, the liquefied resin matrix is usually coated on the fiber strands composed of multiple strands. In order to produce the prepreg of the present invention, the strands must be separated from each other, as shown in Figure 2. Only In this way, individually coated multiple prepreg yarns can be realized. In FIG. 2, the individually coated fiber strands are represented by 134, which is composed of reinforcing fibers 132 and matrix resin material 131. If each yarn 134 can be completely Independent, as shown by 136 is ideal. However, there may be some inter-strand connections 1 3 5 between the yarns 1 34, these inter-strand connections are usually composed of single fibers 132 and resin coated on the surface It is composed of material 131. The bending stiffness of the coated strand yarn is lower than that of the fully consolidated prepreg yarn. Now please refer to Figure 3 and Figure 4. In the general production of prepreg yarn, the fiber yarn is mostly composed of 800 to 3,000 strands of single fiber 132. The diameter or thickness of each single fiber 132 is generally 4 to 5t of this paper, and the Chinese National Standard (CNS) A 4 specification (210x297 public address) is used. Please read the precautions on the back before filling in this page) _ -30 _ Λ 6 Β6 Printed by the CX Industrial and Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (16 microns, these fiber yarns are coated with a prepreg yarn base material 1 3 1 to form a prepreg yarn 1 30. The strands of prepreg yarns prepared by the usual production process 1 34, the width is 1/8 to 1/2 inches. The yarn strands referred to in this book are independent in the usual process, generally It contains only one strand of prepreg yarns 1 to 30. They can be used independently, or they can be used together with other prepreg yarns containing only one strand of 130 to prepare a laminated material structure. The yarn strand 134 in the present invention is independent It is composed of fully infiltrated fibers 132, and the average thickness of each strand is equal to or less than 100 microns, preferably less than 50 microns. These yarn strands are assembled to form a plurality of prepreg yarns 1 3 3 of arbitrary thickness. During the entire processing, if the fibers 132 are sufficiently dispersed by the fiber disperser and a sufficient tension is maintained, the fibers 132 will not loosen in the transverse direction, so that the separation between the yarn strands can be generated or maintained. The separation between the strands can occur before or at the same time as the resin infiltration process in the furnace. Normally, this separation occurs when the liquefied resin 131 is infiltrated in the axial direction of the fiber 132. There are many methods of separation, such as mechanical separators, including grooved knives, knives, laser cutters, and convection in the direction perpendicular to the scattered fiber yarns. The single prepreg yarn 130 contains a plurality of yarn strands 134, which have different thicknesses and widths. The average thickness of the yarn strand 134 is less than 100 microns, but preferably less than 50 cm. The maximum thickness of the yarn strand 134 is 100 microns, and the minimum thickness is the single fiber diameter or thickness of the reinforcing fiber 132 used in the yarn yarn without resin impregnation. Generally speaking, (please read the precautions on the back before writing this page) Binding-The size of the paper used in the national standard B (CNS) A4 (210x297) -31-r * 66 Ministry of Economic Affairs Printed by the Employees' Cooperative of the Central Standards Bureau V. Description of invention (The length of the yarn strand 134 is greater than its width, and its length and width are both greater than its thickness. Usually the thickness of the yarn strand 134 is much smaller than its width and its width Generally less than 2, ◦00 metre. In addition, the average length of the yarn strand 134 is preferably greater than 30 times its thickness. 5. The equipment that tends to be used needs one point to explain. The steps described above are clear. Invented production methods, but they are not limited to the examples listed in this article. In order to better understand the various process steps mentioned above, an example will be listed below. This example uses the The device 8 shown is now shown in Figure 7. The ray yarn 11 is pulled, passes from the yarn feeder 10 through the device 8, and is finally collected on the winding wheel 12. The winding wheel 12 is driven at a variable speed Lower rotation, and the yarn feed wheel does not need to be used Force to drive. The linear speed is generally 3 to 30 meters per minute. Slower speeds can also be used, but they are not desirable from an economic point of view, because the production of prepreg yarn per unit time is reduced, and due to the long residence time in the furnace , The matrix resin will degrade, or the degree of curing will be upgraded, and the resin will be damaged. Higher linear speed is also feasible, as long as the following points can be guaranteed: auxiliary equipment should be equipped to reduce the vibration of the fiber yarn; the unit coated with resin material The equipment should have sufficient length to ensure a sufficient coating amount; the length and temperature of the heating furnace are sufficient to liquefy the matrix resin. In some cases, as long as the conditions are suitable, a linear speed of more than 3 ◦ meters per minute can also be used , The function of pinch roller 14 is to pull the fiber 11 coming out of the heating furnace 16. The winding roller 1 2 is in a constant (please read the precautions on the back before filling this page). (CNS) A4 specification (210X297 Gongji) -32-211042 Printed by the employee consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Fifth, the invention description (3 (j winding under a certain tension, this is by using a The force controller adjusts the winder speed (not shown in the figure). The speed of the fiber yarn passing through the device 8 can be controlled by the rotation speed of the pinch wheel. In this example, the supply of fiber yarn is directly from the pre-winding It is provided on the wound fiber bobbin. The supply of fiber yarn can also come directly from the previous production process. During the yarn feeding process, the fiber 1 3 in the fiber yarn 1 1 should be avoided from twisting. It is difficult to twist the fiber after twisting Dispersion. In addition, the tension of each yarn should be controlled well, which will help maintain a constant tension throughout the impregnation process. A fiber yarn guide plate can also be provided between the yarn feeding device and the fiber yarn diffuser 18 to help The fibers are guided through the disperser 18. In this example, the fiber yarn disperser 18 uses a row of knives 17 and an air comb 19 to disperse the fiber yarn 11 into individual fibers 13. Usually two sets of rollers 17 are provided, one set before the air comb 19 and one set after it. The stick 17 mainly has two functions: (1) is to apply tension to the fiber yarn to reduce the lateral relaxation of the fiber yarn during operation; (2) is to reduce the vibration of the fiber yarn. The roller can be made of any suitable material and can have various surface characteristics. However, smooth Teflon sticks are more suitable, because this material can disperse the fibers well. Among all the rollers used, there must be at least one, preferably the one closest to the entrance of the coating device 20, and the conductor material must be used, preferably stainless copper, so that the fiber yarn enters the coating It can be grounded before covering the system. Air comb 19 is already a well-known process technology. After leaving the yarn feed wheel 10, the fiber yarn 11 enters the first set of sticks 17, and the fibers are dispersed. The arrangement of the first group of sticks can make the fiber yarn (please read the precautions on the back before filling in this page). The size of this paper uses the Chinese rental house standard (CNS) f 4 specifications (210x297 gong) -33-Λ 6 Β6 Printed by the Employee Consumer Cooperative of the Bureau of Standards and Economics of the Ministry of Economic Affairs 5. Description of invention (11. Like textile, when passing, first pass above the first stick, then immediately pass under the second roll, so that the fiber Apply a constant tension and reduce the vibration of the fiber 13. The fiber yarn 11 then enters the air flow 19, where it is further dispersed by the forced air flow. For example, a yarn containing 3, ◦0 fibers It is usually dispersed to a width of more than 1 inch to ensure the flexibility of the resulting prepreg. For the same reason, the arrangement of the second group of sticks is similar to the arrangement of the first group of sticks. The last of this group of kunzi The first is preferably made of a conductive material so that the fibers can be grounded before entering the overlay coating device. The device of the diffuser 18 can be of various types, including: smooth, or engraved or Convex rollers or rollers; air combs; air combs in combination with sticks or rollers; air jets; ultra-chamber dispersers; and liquid baths. The main consideration when selecting fiber yarn dispersers is whether they are capable Disperse into a wide band, preferably this width is only single fiber thick, and this disperser will not damage the fibers. Between the dispersing device 18 and the applicator 20, other process steps can be added according to different applications. For example, In the production of special-purpose prepreg yarns, a device for removing the fiber surface infiltrant, surface activation and application of a binder may also be used. The fiber 13 then enters the coating device 20 where the matrix resin material is applied to the fiber 13 The surface of the fiber Luo 13 remains in a dispersed state when entering and passing through the coating device 20. There are many types of coating devices that can be used, which will be illustrated below. However, the two methods of powder spraying device and static fluidized bed are more Appropriate. When using a powder spraying device, generally use this paper standard for the national standard (CNS) A 4 specifications (210X297 male dragon) ~ -34-(please read the back (Notes to write this page again)

2UW Λ 6 Β6 經濟部屮央標準局兵工消费合作社印製 五、發明説明( 說操作費用較低。其它各種塗覆条統,比如濕粉末法,熱 熔法以及溶液塗覆也可採用。 a .流化床 流化床裝置的最簡化的描述就是由一箱體21組成, 其内放有基體樹脂粉末2 2。在一空氣流和機械振動的相 互作用下,粉末22流體化,另外,通過一安裝在外殼 28底部的高壓電極26使粉末帶電。電極26可由鋒利 的尖狀物或像通常所用的細電線做成。在塗覆裝置的箱體 21頂端有一出口32,用於流化的空氣24可以由此出 口逸出。 該纖維依次從連接在一金屬框架上的幾値棍子的上部 和下部通過,不同時達到接地和分散的目的。分散得好, 則纱維纱很薄,更多粉末可塗上去,並且得到的産品更柔 勸。如果纖維纱在塗覆之前不經分散,這樣則得的預浸漬 紗則很硬挺,其中的纖維也不可能塗覆完全。 粉末粒子2 2均勻地分散在塗覆裝置的外殼2 8之内 。使用靜電塗覆,粉末粒子的粒度範圍盡量控制在20到 80微米之間,平均粒度約為50微米。比此粒度更小和 更大的粉末也曾被分別使用,製備出柔韌的預浸漬纱。粒 度小於2 0徼米的粉末用得很成功。實際上這些徹細粉末 ,特別是粒度小於10微米的粒子,在流化床中聚結成較 大的粒子。粒度最大達250微米的粗粒粉末也進行了使 用。但是預浸漬纱的柔靱度隨所使用的粉末粒度的減小而 (請先閱讀背面之注意事項再塡寫本頁) 本紙張尺度边用中國國家標準(CNS)甲4規格(210x297公货) -35 - 經濟部屮央標準局貝工消费合作社印製 五、發明説明( 增加。短纖維狀的樹脂也同樣可以用作粉末2 2。在使用 回收塑料時,由於回收塑料粉末通常都是用磨碎的方法得 到的,而磨碎工藝的成本隨平均粒度減小而增加,因此一 般傾向於使用粗顆粒。在考慮使用較粗粒度的粉末時,必 須要結合柔靱性和預浸漬纱後加工中所要求的混合度這兩 個相反因素綜合平衡。微孔板34對於通過此板的空氣 24産生一個很高的阻力,從而可使得有足夠的空氣在一 較低的速度下通過,將粉末22流化。對微孔板34施加 機械振動可加強流化,並減少空氣在粉末床中的溝流和粉 末結塊。流化床中粉末的厚度一般為2到4英吋。(50 到1 0 0毫米) 在流化床裝置20中,粉末22的粒子對纖維産生靜 電吸附。帶電的粉末粒子22相互推斥,最後上升到箱體 21的上部,形成一帶電的粒子層,而纖維就通過此粒子 層。在本文列舉的這値實例中,採用的是靜電技術公司生 産的C30型靜電流化床塗覆機。床身的尺寸為15X 15cm。輸出電壓為0 — 90kV,空氣進量為每分鐘 0-0.4標準立方米。流化床裝置20内使用了離子化 空氣36,它是通過液化床33下面的電極通電而産生, 以防止由於電火花引起流化粒子2 2的意外引發。 用來流化的空氣24必須乾燥、清潔。空氣中的髒物 會堵塞微孔板34,造成流化不均勻。空氣中的濕氣會引 起粉末22在流化床33中結塊。通常乾燥空氣24的壓 力在200到700kPa,每分鐘流過每平方米擴散板 本紙張尺度逍用中國國家猱準(CNS)甲4規格(210X297公;¢) (請先閲讀背面之注意事項再填寫本頁) 裝- 線· -36 - 經濟部屮央標準局员工消费合作社印製 _Β_6 五、發明説明( 34的流量約為i. 5m3。流化的粉末是通過控制流化 空氣24來維持流化狀態。一個常用的乾燥流化空氣的方 法是採用一裝満硅膠的乾燥柱(圖中未顯示)。另外,空 氣還可通過冷凍方式乾燥。濕空氣通入乾燥柱中,經過一 絲網後與硅膠接觸。濕氣在乾燥柱中被分離掉。乾燥空氣 24然後再由乾燥柱的出口通入·到流化床3 3中。 流化裝置2 0中所採用的電壓一般在_ 3 0到 —lOOkV之間。多數情況下,採用負電。輸出電壓大 約不超過一1 OOkV。在裝置2 ◦短路接地時,最大輸 出功率不能超過所使用的粉末粒子22的引燃能量。所需 使用的高電壓,取決於正在使用的粉末的性能,一般在 —3 5到一 9 0 k V之間。例如,聚酯樹脂在電壓小於或 等於一40kV時,塗覆效果較好。而環氧樹脂則在 —40到一7 0 kV之間操作較好。乙烯類樹脂通常需要 —較高的操作電壓,範圍在一60到_75kV。而對 PEEK,較好的塗覆效果則出現在一70到一 90kV 之間。 為了將過量的塗覆粉末收集並送回到粉末供應貯槽( 圖中未顯示),在塗覆条統中還裝有一個真空排除裝置( 圖中未顯示)。典型的排除裝置是由一個或多個旋風分離 器或袋示過濾器組成(圖中未顯示),或兩者結合使用。 排除裝置可以裝在頂部,進口和出口,或者四周。空氣排 出速度應該大致與進口空氣24的速度相同。在本實例中 ,排除裝置採用一値濾筒式排氣裝置,將粉末收集在一値 (請先閲讀背面之注意事項再填寫本頁) 裝- 訂_ 線· 本紙張尺度边用中國國家標準(CNS)甲4規格(210X297公货) -37 - 經濟部屮央標準局员工消费合作社印製 五、發明説明( 真空袋過濾器中進行回收。排氣筒將空氣吸入,進而帶入 粉末,最後通過搖晃裝在筒内的過濾袋將粉末回收。 纖維在樹脂塗覆容器内的滯留時間一般為大約1至5 秒鐘。這個時間的確定應取決於纖維的種類,纖維分散的 程度,塑料樹脂的種類,粒子的大小,塗覆器的操作條件 ,(比如空氣流速和靜電電場),以及預浸漬纱中所要求 的樹脂含量。 纖維塗覆以後,就如圖1和圖8所示,送入加熱爐 16,或者如圖9所示,直接通過一個陶瓷或其它材料的 加熱器7 0。這一加熱過程應在纖維離開流化床以後盡快 實施,以保證粉末22熔融,粘結在纖維上。否則電荷衰 減或杜弛就會發生,粉末會脱離纖維。加熱爐1 6或加熱 器7 0的溫度取決於纖維和樹脂粉末2 2。但是在確定加 熱爐16或加熱器70的溫度和在加熱爐16或加熱器 7 0内的滯留時間時,應該要保證塗覆過的纖維在加熱爐 中的滞留時間之内,樹脂粉末22不會達到其分解溫度。 加熱爐的溫度應該要高到足以能將所有的塑料基髏熔融。 對塗覆過的纖維可以採取傳導或輻射方式進行加熱。 在本實例中,加熱爐16是採用了一個倫德伯格一段加熱 管式爐,最高操作溫度為1 200*0,長度75cm,内 徑5 cm。預浸漬纱在爐内的典型滯留時間大約為2到 20秒。在多數情況下,低於10秒鐘的滯留時間,足以 將塑料液化,熔結到縱維表面。對於一些粘性熔體,比如 高分子是聚乙烯,往往需要較長一些時間才可促使樹脂沿 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國國家標準(CNS)甲4規格(210乂297公龙) —38 - 21104^ Λ 6 Β6 經濟部屮央標準局Α工消贽合作社印製 五、發明説明( 纖維表面的浸潤。 在回收的廢塑料製品當中,聚對苯二甲酸二乙酯通常 要算作熔點最高的塑料。聚對苯二甲酸二乙酯的熔點將近 2 5 01C,因此加熱爐的溫度至少也要達到其熔點溫度, 即250T:,最好設在300t:,甚至更高。為了減少在 爐内的滯留時間,並且加強樹脂浸潤,加熱嫿的溫度可以 設得很高,而物料溫度並不會達到爐溫。當加熱爐溫度超 過400度時,大多數回收塑料在一定滯留時間内都會降 解。在這種情況下,必須要採取一定的措施將以缕維纱上 滴落到加熱爐内的樹脂粉末除去,否則,會增加火災的可 能性。 b.粉末噴塗 利用粉末噴塗工蕤將樹脂基體材料粒子塗覆到纖維表 面,可以使用靜電噴射槍或者摩擦靜電噴射槍來進行。靜 電噴射槍的最基本的設計就是一根管子帶有一個與高壓發 電機相連的供電電極。粉末粒子用某種方式,一般是用驅 動氣流,通過槍管,並受電極作用帶電。帶電的粉末粒子 然後被輸送到纖維表面,與纖維粘結,從而塗覆上去。纖 維由於是接地的,這樣在帶電的粉末粒子和纖維之間就産 生了一個相反的極性。 在本實例中,靜電噴射槍是裝在一値粉末容器内的, 該容器取代了流化床。纖維在離開分散器以後,進入粉末 容器内。粉末狀樹脂被輸送到噴射槍内,接收電荷,然後 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中B B家標準(CNS)甲4規格(210x297公龙) -39 - 2 a - 4 A c 66 ΛΒ 五、發明説明( 再噴射到接地的纖維上面。部分帶電的粉末粒子粘結並塗 覆到纖維表面,而其餘的則被循環使用到噴射槍中。塗覆 過的缕維離開粉末容器,然後進入加熱爐。 此方法的工藝參數包括有通過噴射槍的空氣流速,粉 末流入量,以及靜電大小。這些參數的選擇主要是根據所 使用的纖維和樹脂材料的性質。比如,當使用!^!^!^!^-Gema AG 7 0 1 — 6型靜電噴射槍;樹脂基體材料為粒度 小於150微米的尼龍11粉末,並混有一些磺黑顔料; 纖維纱為12K的碩纖維,已被分散成5 cm寬,在這種 條件下,所採用的工藝條件是:空氣流動水平為0—7, 粉末流動水平為0—10,靜電大小為0到一80kV。 表一列出了塗覆工藝參數和數值。 (請先閲讀背面之注意事項再填寫本頁) 經濟部屮央標準局員工消费合作杜印製 表一 塗覆工藝數值 線速度 空氣流 粉末流 靜電大小 樹脂重量 (米/分鐘) 速水平 速水平 (~kV) 含量(%) 3.54 1.5 4.5 25 34.8 6.21 2.0 6.0 15 41-0 8.25 2.0 10.0 7 43.5 13.65 2.0 10.0 7 30.0 c.濕粉末塗覆工藝 在濕粉末塗覆工藝中,比如懸浮液法或乳液塗覆法, 樹脂基體材料是潮濕的粉末。纖維纱在進入塗覆条統20 本紙張尺度通用中國鼷家橾準(CNS)甲4規格(210乂297公藿) -40 - 211^¾ Λ 6 156 經濟部中央標準局员工消費合作社印製 五、發明説明(3$ 之前不需要接地。因此,前面所提到的不銹鏑棍子1 7在 此法中就不再需要。纖維在離開分散器1 8以後,如需要 ,還可通過一個裝置塗上粘結促進劑。 塗完粘結促進劑以後,纖維就進入濕粉末塗覆糸統, 它是由一値棍子塗覆器,一個濕粉末或乳液儲槽和一値懸 浮液泵組成。樹脂基體材料懸浮在液體媒解之中,該液體 可以是水或溶劑。水質的液體媒解中包括有水,有時還有 一水溶性粘結劑。溶劑質的液體媒解包括有溶劑,需要時 也含有一種可溶性粘結劑。纖維通過輥子塗覆器的上表面 ,锟子在與纖維進行相反的方向上缓慢地旋轉。棍子塗覆 器的下表面與儲槽内的懸浮液或乳液相接由。隨著不停地 旋轉,锟子將懸浮液或乳液帶到上表面,使之與正在通過 的缕維接觸從而塗覆上去。懸浮液泵可以維持懸浮液或乳 液的濃度均勻。 塗覆了的纖維離開锟子塗覆器後,進入一乾燥器,懸 浮液塗覆過程中帶入的水份或溶劑在這褢蒸發掉。如果樹 脂融合到纖維表面,則水溶性粘結劑也可以除去。然後, 乾燥的纖維就進入一個熔融器,在那褢樹脂基體材料液化 並浸潤纖維表面。在濕粉末塗覆工藝法中,還有一個方法 是不用棍子塗覆器,而直接該纖維通過懸浮液或乳液,然 後直接進入乾燥器。 d.熱熔融塗覆工藝 熱熔融塗覆糸統通常是由一個棍子塗覆器或一個擠出 (請先閱讀背面之注意事項再填寫本頁) 裝- 訂 線- 本紙張尺度逍用中國國家標準(CNS)甲4規格(210X297公垃) -41 - Λ 6 136 經濟部屮央櫺準局貝工消t合作社印製 五、發明説明(3d 機和一個模具所組成。熱熔融法使用棍子時,其操作方式 與上述的濕粉末法相同,只是在這褢,不再使用懸浮液或 乳液貯槽,而是使用了一個含有樹脂基體材料的熱熔體貯 槽。同濕粉末塗覆工藝一樣,棍子塗覆器也可以不用,纖 維可直接通過熱熔體貯槽。 熱熔融法使用擠出機和模具操作時,是將分散開的纖 維牽引通過一個扁口模具,而擠出機不停地向此模具提供 熱熔體基體材料,在模具内將纖維塗覆。模具底面刻有凹 模以將預浸漬纱分成多股。當樹脂基體的熱熔體與纖維接 觸以後,纖維立即就被浸潤。因此,可能就沒有必要再另 設一個加熱爐去進一步完成樹脂浸潤。在此工藝中,一些 特殊的裝置,比如帶有刻槽的模具,或者棍子塗覆器,可 能需要使用,以幫助將預浸漬纱分成多股。 e .溶液塗覆 溶液塗覆工藝要使用各種溶劑。在此方法中,樹脂基 體材料溶解在一個適當的溶劑當中,然後纖維通過此溶液 ,或者浸有溶液的棍子,從而將纖維塗覆。塗覆過的纖維 通過一個乾燥器,將溶劑蒸發掉。 6.預浸漬纱樣品 a.硪纖維纱/PEEK樹脂基體材料 使用Hercules公司的6 K AS4碩纖維纱,未加 任何浸潤劑,單纖維直徑8微米。纖維通過一噴氣流,纖 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度逍用中國困家標準(CNS)甲4規格(210x297公放) -42 - Λ 6 Β6 五、發明説明(4() 維纱被分散成大約6Omm寬。位於分散器入口和出口處 的锟子對纖維纱産生張力。然後纖維纱通過一靜電床,床 内裝有ICI公司生産的PEEKV150VPF樹脂粉 末,平均粒度為90微米。纖維纱與地相接,而粉末在負 65kV的電壓下充電。纖維纱在張力下以分散開的形式 通過一管式加熱爐,爐内溫度為45〇υ,將PEEK熔 融。纖維纱然後在空氣中冷卻,再通過驅動棍子,最後到 達裝有張力調節的缠繞卷裝器。纖維纱在粉末塗覆器内和 加熱爐内的滯留時間分別為1 . 4秒和6 . 7秒。線速度 為每分鐘6. 8米。預浸漬纱中纖維的體積含量為60% 。預浸漬纱的抗撓剛度是8 9 0mg_ cm,而未經塗覆的纖 維纱的抗撓剛度則是6 7 OlDg — cm。通過對比分析,固結 後的預浸漬纱的剛度大約是216, OOOfflg — cm。 b.玻璃纖維纱/PE ΕΚ樹脂基體材料 使用Owens Corning玻璃纖維公司的S 2玻璃纖維纱 ,每股纱含單纖維4, 080根,經高溫浸潤劑處理,單 經濟部屮央櫺準局员工消费合作社印製 (請先閱讀背面之注意事項再填寫本頁) 纖維直徑9微米。樹脂基體材料是與上例相同的P E E K 。玻璃纖維纱在與最後一個接地的棍子接觸之前,表面用 一濕泡沫塊進行清洗,以增加表面電導。然後纖維纱通過 —靜電床,床内裝有ICI公司生産的PEEKV150 PF樹脂粉末,平均粒度為9 0徹米。纖維與地相接,而 粉末在負70kV電壓下充電。纖維纱在張力下以分散開 的形式通過一管式加熱爐,爐内溫度為45 0C,將 本紙張尺度边用中國S家標準(CNS)甲4規格(210x297公龙) -43 - Λ 6 Β6 經濟部屮央標準局貞工消費合作社印製 五、發明説明 (4]) PEEK熔融。纖雒纱然後在空氣中冷卻,再通過驅動提 子,最後到達裝有張力調節的缠繞卷裝器。纖維纱在粉末 塗覆器内和加熱爐内的滯留時間分叩為5 . 2秒和 26. 3秒。線速度為每分鐘1. 7米。預浸漬纱中的體 含量為6 0 %。 c.磺纖雒纱/LaRC — TPI樹脂基體材料 使用Hercules公司的6 K A S4碳纖維纱,未經 任何浸潤劑處理,單纖維直徑8微米。樹脂基體材料是熱 塑性聚亞醯胺L a RC TR I。預浸漬纱的製備方法如 例a所述。當碩纖維纱通過空氣流分散器以及位於其前、 後的棍子以後,進入一靜電床,床中裝有Rogers公司生 産的LaRC TP I粉末,平均粒度為35微米。纖維 纱與地相接,而粉末在負67kV電壓下充電。纖維纱在 張力下以分散開的形式通過一管式加熱爐,爐内溫度為 400C,將TPI熔融。纖維纱然後在空氣中冷卻,再 通過驅動棍子,最後到達裝有張力調節的缠繞卷裝器。纱 維纱在粉末塗覆器内和加熱爐内的滯留時間分別為3. 2 秒和16秒。線速度為每分鐘2. 9秒。預浸漬纱中纱維 的體積含量為3 7%。預浸漬纱的抗撓剛度為7,0〇〇 mg_ cm,而未經塗覆的纖維纱的抗撓剛度則是6 7 Omg- 7.預浸漬纱的後處理加工 本紙張尺度逍用中國a家樣準(CNS)甲4規格(210x297公¢) (請先閱讀背面之注意事項再塡寫本頁) -44 - 211542 Λ 6 Β6 經濟部屮央標準局貝工消费合作社印製 五、發明説明( a .綜述 當纖維13在塗覆裝置20中被樹脂基髏材料浸潤以 後,預浸漬纱50可以視情況需要通過一組拋光棍子46 。這組锟子46可以設置在加熱爐16或加熱器70内, 也可設置在緊靠加熱爐16或加熱器70的出口處。但是 不管在任何情況下,棍子46裝在設備8中的位置,都要 處於樹脂基體材料仍然是液體狀態。拋光輪46的作用是 迫使液態基體樹脂進入纖維纱股内,以得到較好的浸潤, 並減小由於遣留並固結在纱股外表面上的樹脂基髏液滴所 造成的股與股之間的表面阻力。 由於成預浸漬纱的纱股很細,預浸漬纱50在離開加 熱爐16或加熱器70以後很快冷卻。通常空氣冷卻就足 夠了。當然在某些場合下,若使用鼓風器,冷卻棍子或類 似裝置·也可帶來某些益處。在冷卻過程中很重要的一點是 要使分散開的纱股保持足夠的張力,否則預浸漬纱中的各 値纱股就會鬆散,相互粘並,使得預浸漬纱的抗撓剛度很 高。另外還有一點很重要的是不要該預浸漬纱中的單根纖 維在固結時相互接觸,這樣會産生很強的股間粘結。需要 時,也可在加熱爐16或加熱器70之後設置一對流冷卻 (圖中未顯示)。傳導冷卻的方式也可以使用。傳導冷卻 需要表面接觸,這樣可以很止纖維纱的横向移動。在冷卻 以後,也可以採用前面描述過的一些機械裝置進行分股。 但是單單依靠冷卻以後再進行分股是很不好的,因為這會 導致超過限量的纖維破損。一般來說,預浸漬纱中的樹脂 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度边用中國國家標準(CNS)甲4規格(210x297公龙) -45 - 211d43_Be 經濟部屮央標準局员工消費合作杜印製 五、發明説明(4¾ 基體的體積含量一定要在25%以上,只有這樣才能形成 —個基本不含氣泡的結構,可用於進一步加工成最終覆合 材料結構。 夾送輪的主要作用是在加工過程中牽引纖維纱1 1 , 並對缕維纱施加足夠的張力,以防止其横向自我鬆散。用 於牽引纖維的裝置可以有很多種,其中包括機械驅動的夾 送輪,最好是表面塗有橡膠;還有摩擦锟輪,最好也是有 橡膠表面塗層。卷裝設備12可以是任何一種常用的帶有 張力調節的纖維纱卷裝器。另外,預浸漬纱50也可直接 輸送到下一道加工工藝,比如切割機,用以生産片狀或散 狀模塑料的原料。 b .帶狀製品 生産預浸漬纱的帶狀製品,就像圖8和圖9所表示的 那樣,纖維13在塗覆糸統20中被樹脂基體材料潤濕以 後,預浸漬纱49就被送到成帶區20。本發明最傾向於 使用的成帶裝置是採用兩個相匹配的棍子,一個棍子表面 刻有凹槽(60),而另一棍子62則帶有凸塊。圖10 和圖1 1 a表明了锟子60和锟子62的構造。锟子62 的凸塊與輥子60的凹槽相互匹配,吻合。當粉末熔結塗 覆的纖維纱4 9通過帶有凹槽的棍子6 0和帶有凸塊的棍 子62之間時,就將粉末熔結塗覆的纖維49轉變成具有 已知幾何尺寸的預浸漬纱帶狀製品。圖11b表示帶有凹 槽的锟子6 0和帶有凸塊的锟子6 2的另一種構造。在這 本紙張尺度逍用中國困家標準(CNS)甲4規格(210x297公货) (請先閲讀背面之注意事項再塡寫本頁) 裝· 訂 線. -46 - 211542 Λ 6 Β6 經濟部屮央標準局貝工消费合作社印製 五、發明説明(Π 裏,凹槽是一連缠下凹的形狀,而凸塊則成了一個連缠上 凸的形狀,下凹面與上凸面之間相互匹配。如圖1 1 a所 示,锟子6 2的凸塊結構與锟子6 0的凹槽相互匹配,相 互吻合。柔韌的多股預浸漬纱通過棍子6 0和6 2之間, 這樣預浸漬纱4 9就轉變成幾何形狀一定的帶狀製品5 0 。棍子60和62—般是通過裝在其中一個棍子上的汽缸 64,在一定的壓力下相互作用的,也可採用其它加壓的 方法,如彈簧或液壓缸。 锟子60、 62裝在熱熔結塗覆生産線的出口處,即 成帶區,它取了圖1中所示的分離步驟109。圖8中表 明,锟子6 ◦和62安裝在熔融步驟107,也就是加熱 爐1 6和卷裝步驟1 07,也就是收卷器1 2之間。在這 値例子當中,柔靱的多股預浸漬纱自加熱爐16中出來, 由一安裝在兩锟之間棍隙附近的加熱器6 6對纱股4 9加 熱,保持其溫度。聚焦石英紅外燈是一種合適的加熱器 66對纱股49加熱,保持其溫度。聚焦石英紅外燈是一 種合適的加熱器6 6。比如Argus公司生産的 74. 285型,功率大約250◦瓦,由 — 3PN 1 0 1 0型Staio自耦變壓器控制。刻有凹槽的 提子60的直徑大約為12. 5cm,寬度為2. 5cm ,凹槽的寬度為1. 25cm,深0. 31cm。帶有凹 塊的棍子62的直徑大約為12. 5cm,寬2. 5cm ,與凹槽相匹配的凸塊的寬度為1. 25cm,高度為 0. 3 1 cm。通常是冷的锟子,可以鬆纖維1 04分離 本紙張尺度边用中國8家標準(CNS)甲4規格(210x297公货) (請先閱讀背面之注意事項再填寫本頁) 裝. 訂 線· -47 - Λ 6 136 經濟部屮央標準局员工消費合作社印製 五、發明説明(4今 ,因此分離步驟109常常並不需要。另外,冷卻步驟 112常常也可以通過這些棍子來完成,或通過纖維 104與周圍空氣接觸來完成。 預浸漬纱49是通過一收卷裝置12被牽引通過锟子 60和62。當纖雒通過時,通過壓力裝置64,—個棍 子被壓到另一棍子上。氣缸是一種合適的壓力裝置64, 比如Bimba公司生産的091. 5D型,配有Speedaire 公司生産的1Z838B型壓力控制器。一個合適的氣缸 可以對0 . 5英吋寬的預浸漬纱4 9産生大約2 0 psig的 力。當使用帶有凸塊的棍子62時,預浸漬纱受力作用, 進入到凹槽與凸塊之間的縫隙,帶有凹槽的輥子與帶有凸 塊的锟子60、 62之間的缝隙的幾何尺寸是一定的。預 浸漬纱在此缝隙當中壓合在一起,就形成了具有一定幾何 尺寸的柔靱的帶狀製品50。生産者根據需要選擇锟子 6 0的凹槽與錕子6 2的凸塊的尺寸以生産出所需幾何尺 寸的帶狀製品5◦。當使用帶有凸面的棍子62時,預浸 漬纱在外力作用下,進入凹面與凸面之間,在那褢壓合在 一起,從而形成一已知幾何尺寸的柔韌帶狀製品50。生 産者根據需要選擇凹面棍子6 0和凸面棍子6 2的相對半 徑,從生産出所需幾何尺寸的帶狀製品50。锟子6〇、 62通常是用空氣冷卻,以使樹脂基體固化,這樣帶狀製 品50就可以操作處理。帶狀製品50然後再經過一導向 輪6 8,通過收卷裝置卷裝起來。 在圖9顯示的例子中,棍子取代了加熱爐16。如果 (請先閱讀背面之注意事項再塡寫本頁) 裝- 訂· 線· 本紙張尺度边用中困8家榇準(CNS) Ή規格(210X297公釐) -48 - 211^42 Λ 6 Β 6 經濟部屮央標準局员工消费合作社印製 五、發明説明(叫 不使用加熱爐1 6,通常要用一値第二加熱器70。陶瓷 加熱器可以適合此用途,比如GTE Sylvanza公司生産的 陶瓷加熱器,功率為500瓦,尺寸12. 5X6. 25 〇111,裝有8&1^61*-(1:〇1611^115 6〇型控制器。這値加熱 器70的作用是用來將粉末22熔化,以得到粉末熔結塗 覆的預浸漬纱4 9。預浸漬纱4 9然後再通過以上結合圖 8描述過的成帶區。 加熱器6 6和7 ◦的功率大小取決於材料和生産的線 速度。對於生産6K的碩纖維纱,用PEEK樹脂塗覆, 線速度每分鐘1. 5米,製成1. 25cm寬的帶子,上 面所提到的加熱器就可適用。 現在另舉一個例子。成帶區是由一個凸面或凹面的棍 子60組成,如圖1 2和1 3所示。粉末熔結塗覆的纖維 纱49在張力下通過棍子60圓周上的某一點。在張力和 锟子的凹面形狀的共同作用下,纖維纱移到凹面的最低點 ,從而由預浸漬纱49轉變成一定幾何形狀的帶狀材料 5◦。預浸漬纱所受到的張力可通過收卷裝置12或圖中 未顯示的其它種類的裝置來提供。通過改變锟子60凹面 結構的相對半徑以及作用在纖維纱49上的張力,就可得 纖維纱49並合在一起,轉變成一定幾何尺寸的柔韌的帶 狀材料50。同前例一樣,棍子60也可以加以冷卻,從 而可使樹脂基體材料固化,使帶狀材料50便於操作處理 。帶狀材料50然後通過導向輪68,通過收卷裝置12 卷裝起來。另外,只要纖雒纱上受到的張力足以能使柔韌 本紙張尺度逍用中a B家標準(CNS)甲4規格(210X297公¢) (請先閱讀背面之注意事項再填寫本頁) -49 - 211^42 Λ 6 L36 經濟部屮央橾準局员工消#合作社印製 五、發明説明( 的多股預浸漬纱轉變成帶狀,也可使用一個或多値平面提 子。 圖20、 21和22是用本發明生産的預浸漬纱的截 面的照片。這些預浸漬纱是用玻璃纖維和聚丙烯基體材料 做成。圖23是用本發明製備的聚丙烯和玻璃纖維的帶狀 材料的照片。圖2 3 a的帶狀材料是在每分鐘3米的線速 度,採用一個114紅外燈熔融樹脂材料的條件下製備的 ,棍子所受的壓力為275kPa。圖23b的帶狀材料 的製備條件為:線速度每分鐘1. 4米,樹脂基體材料在 37010下熔融,棍子上的壓力為275kPa。 由本發明的方法,用粉末熔結塗覆的預浸漬纱製成的 帶狀材料,具有一特定的幾何形狀,適合於長絲纗繞,先 進的舖放工藝以及擠拉等不同的加工方法。在長絲繾繞方 法中,·採用一個與最終産品形狀相同的芯軸,將_維纱缠 繞在芯軸上。纖維舖放架沿著芯軸來回移動一定的距離, 這是通過一個開環的控制器加以控制的。由於是開環的, 控制器並不監測纖維纱的寬度。如果舖放的纖維纱的寬度 太窄,則在相鄰的纖維纱之間會産生一空隙;相反如果太 寬,相鄰舖放的纖維纱就會相互璺加。這兩種情況都會影 響最終産品的質量。先進舖放工藝對纖維纱也有同長絲纏 繞類似的要求。 在擠拉工藝中,纱維束受拉力通過模具,形成一連續 的兩維的形狀。如果被送進模具褢的孅維纱没有一定的幾 何形狀,勢必會在模具内重新排列,造成最終産品中纖維 (請先閱讀背面之注意事項再填寫本頁) 冬紙張尺度逍用中國因家標準(CHS)甲4規格(210X297公¢) -50 - Λ 6 Β 6 211542 五、發明説明(叫 分散不均勻,否則纖維或模具就會破壊。這種纖維的重新 排列,産生了摩擦阻力,導致了牽引力的增加,也會引起 纖維,甚至模具損壊。這些問題的出現,都表明需要採用 具有一定幾何尺寸的預浸漬纱。另外,長絲缠繞和擠拉等 加工工藝都需要柔韌的預浸漬纱作為原料,才能保證最終 産品的質量。而本發明的柔靭的多股預浸漬纱帶狀材料正 可以達到幾何形狀準確,並且性質柔靭。 c .非織造織物 如圖14— 17所示,在預浸漬纱133冷卻時,或 冷卻以後,將它們用手工或機械排列組合起來,成為所需 要的或者合適的結構,這樣就可以製備成理想的織物 139。比如,預浸漬纱133可以像圖14a所示的那 樣,排列成單向的,也可像15 a那樣,排列成多向的, 或者任意其它方向。然後將預浸漬纱133相互舖叠,結 合在一起,即可成為本發明的非織造、柔韌、多股預浸漬 纱織物。將預浸漬纱133結合在一起的方法很多。對舖 簦在一起的預浸漬纱,在選定的點用熱熔方式連接起來, 可做成點連接137的預浸漬纱織物。其它結合預浸漬纱 133的方法還有用粘結劑纖維或纱線縫纫或紡織;針剌 ;水錘或壓力點連接。圖17表明,缝線138做出的織 物139很好。圖24的照Η是用纖維交織結合而成的單 向預浸漬纱非織造織物。 採用多頭舖放設備可以將預浸漬纱133製成3維非 本紙張尺度边用中國國家標準(CNS)甲<1規格(210x297公煃) (請先閱讀背面之注意事項再塡寫本頁) 訂_ 線_ 經濟部屮央櫺準局貞工消费合作社印製 -51 經濟部屮央標準局貝工消费合作社印製 釭如,_B6_ 五、發明説明(4弓 織造織物,具有覆染外形的非織造織物以及二維或三維的 預成型髏。舖放纖維的芯軸的形狀可以按不同的表求製作 ,最終製出所需形狀的織物或預成型髏。本發明的這些産 品可適合於製造各種覆合材料結構。非織造織物可以像加 工粘手的熱固性預浸漬纱帶那樣,舖放成高级覆合材料結 構。非織造織物可做成預成型體用於樹脂傳遞模塑或模壓 工藉。採用管子壓研法可製成管狀預成型體,這種工蓊常 用於製備高爾夫球桿,網球拍和帆船桅桿。 除此之外,一種價格低廉的二維織物也可製備,再用 於後道工藝加工。本發明産品比較起用柔韌多股預浸漬纱 製成的織織或编織織物,價格要低。用本發明的技術,含 有室溫下為固體的樹脂材料的織物可以做得很柔韌。而通 常的技術生産出來的織物卻很硬挺。本發明使用固體樹脂 基體做成的織物既達到柔韌,而且又浸潤很好。樹脂基體 和增強纖維都採用纖維形狀的織物結構,例如交混纱、交 混编織,或纖維層,樹脂層交替舖放的結構,盡管也很柔 韌,但卻不能實現樹脂對纖維的浸潤,因而在固結過程中 ,這種雙纖維結構就需要採用比本發明織物更加苛刻的加 工條件。 上面的所有描述,只是用作說明解釋之用,而並不是 用來限止本發明方法的範圍。下面即為本發明的申請專利 範圍。 (請先閲讀背面之注意事項再塡寫本頁) 裝- 訂_ 線- 本紙張尺度边用中S國家標準(CNS)甲4規格(210x297公龙) -52 -2UW Λ 6 Β6 Printed by the Ordnance Consumption Cooperative of the Ministry of Economic Affairs, Biaoyang Bureau of Standardization V. Invention Instructions (Said the operating cost is lower. Various other coating systems, such as wet powder method, hot melt method and solution coating can also be used. a. The most simplified description of the fluidized bed fluidized bed device consists of a box 21 in which the matrix resin powder 22 is placed. Under the interaction of an air flow and mechanical vibration, the powder 22 fluidizes, in addition , The powder is charged by a high-voltage electrode 26 installed at the bottom of the housing 28. The electrode 26 can be made of a sharp pointed object or a thin wire like usual. There is an outlet 32 at the top of the box 21 of the coating device for flow The air 24 can escape through this outlet. The fiber passes through the upper and lower parts of several sticks connected to a metal frame in sequence, and does not achieve the purpose of grounding and dispersion at the same time. If it is well dispersed, the yarn is very thin , More powder can be applied, and the product obtained is more persuasive. If the fiber yarn is not dispersed before coating, the resulting prepreg yarn is very stiff, and the fibers in it cannot be coated completely. The final particles 22 are evenly dispersed within the housing 28 of the coating device. With electrostatic coating, the particle size range of the powder particles is controlled between 20 and 80 microns, and the average particle size is about 50 microns. It is smaller than this particle size And larger powders have also been used separately to produce flexible prepreg yarns. Powders with a particle size of less than 20 gm have been used successfully. In fact, these fine powders, especially particles with a particle size of less than 10 microns, are in flow Larger particles are coalesced in the bed. Coarse-grained powder with a maximum particle size of 250 microns is also used. However, the softness of the prepreg yarn decreases with the particle size of the powder used (please read the notes on the back side first Re-write this page) This paper uses the Chinese National Standard (CNS) A4 specifications (210x297 public goods) -35-Printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention description (Increase. Short fiber The resin can also be used as powder 22. When using recycled plastics, because recycled plastic powders are usually obtained by grinding, and the cost of the grinding process increases with the decrease of the average particle size, so generally Coarse particles are preferred. When considering the use of coarser-grained powders, it is necessary to balance the two opposite factors of flexibility and the degree of mixing required in the post-preg yarn post-processing. The microplate 34 is The air 24 creates a high resistance, which allows sufficient air to pass at a lower speed to fluidize the powder 22. Applying mechanical vibration to the microplate 34 can enhance fluidization and reduce air in the powder bed Gully flow and powder agglomeration in the fluid. The thickness of the powder in the fluidized bed is generally 2 to 4 inches. (50 to 100 mm) In the fluidized bed device 20, the particles of the powder 22 electrostatically adsorb the fibers. The charged powder particles 22 repel each other, and finally rise to the upper part of the box 21 to form a charged particle layer through which the fibers pass. In this example listed in this article, the C30 type electrostatic fluidized bed coating machine produced by Electrostatic Technology Co., Ltd. is used. The bed size is 15X 15cm. The output voltage is 0-90kV, and the air intake is 0-0.4 standard cubic meters per minute. Ionized air 36 is used in the fluidized bed device 20, which is generated by energizing the electrodes below the fluidized bed 33 to prevent accidental initiation of fluidized particles 22 due to electrical sparks. The air 24 used for fluidization must be dry and clean. Dirt in the air can clog the microplate 34 and cause uneven fluidization. The moisture in the air causes the powder 22 to agglomerate in the fluidized bed 33. Normally the pressure of the dry air 24 is between 200 and 700 kPa, and it flows through the diffusion plate per square meter every minute. The paper size is easy to use. China National Standard (CNS) A 4 specifications (210X297; ¢) (Please read the precautions on the back first (Fill in this page) 装-线 · -36-Printed by the Employee Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs _Β_6 5. Description of the invention (the flow rate of 34 is about 1.5m3. The fluidized powder is obtained by controlling the fluidized air 24 Maintain fluidization. A common method of drying fluidized air is to use a silica gel drying column (not shown). In addition, the air can be dried by freezing. Moist air is passed into the drying column and passes through After a screen, it comes into contact with the silica gel. The moisture is separated in the drying column. The drying air 24 is then passed from the outlet of the drying column to the fluidized bed 3 3. The voltage used in the fluidizing device 20 is generally Between _ 3 0 and -100 kV. In most cases, negative electricity is used. The output voltage does not exceed approximately 1 kV. When the device is short-circuited to ground, the maximum output power cannot exceed the ignition energy of the powder particles 22 used. High required The voltage, depending on the properties of the powder being used, is generally between -35 and -90 k V. For example, polyester resins have a better coating effect when the voltage is less than or equal to-40 kV, while epoxy resins It is better to operate between -40 and 70 kV. Ethylene resins usually require a higher operating voltage, ranging from 60 to _75 kV. For PEEK, better coating results appear between 70 and 70 kV. Between 90kV. In order to collect and return the excess coating powder to the powder supply tank (not shown in the figure), a vacuum evacuation device (not shown in the figure) is also installed in the coating system. Typical exclusion The device is composed of one or more cyclones or bag filters (not shown in the figure), or a combination of the two. The exclusion device can be installed on the top, inlet and outlet, or around. The air discharge speed should be roughly the same as the inlet The speed of the air 24 is the same. In this example, the exclusion device uses a filter cartridge type exhaust device to collect the powder in one (please read the precautions on the back before filling in this page). Binding-Order _ Line · This paper China Standard (CNS) A4 specifications (210X297 public goods) -37-Printed by the Employee Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs V. Invention description (Recovered in a vacuum bag filter. The exhaust tube draws air into the powder Finally, the powder is recovered by shaking the filter bag installed in the drum. The residence time of the fiber in the resin-coated container is generally about 1 to 5 seconds. The determination of this time should depend on the type of fiber and the degree of fiber dispersion. The type of plastic resin, the size of the particles, the operating conditions of the applicator, (such as air flow rate and electrostatic field), and the required resin content in the prepreg. After the fiber is coated, it is shown in Figures 1 and 8. , Into the heating furnace 16, or as shown in Figure 9, directly through a ceramic or other material heater 70. This heating process should be carried out as soon as possible after the fiber leaves the fluidized bed to ensure that the powder 22 melts and adheres to the fiber. Otherwise, charge decay or relaxation will occur and the powder will break away from the fiber. The temperature of the heating furnace 16 or the heater 70 depends on the fiber and resin powder 22. However, when determining the temperature of the heating furnace 16 or heater 70 and the residence time in the heating furnace 16 or heater 70, it should be ensured that the coated fiber stays in the heating furnace, the resin powder 22 does not Will reach its decomposition temperature. The temperature of the furnace should be high enough to melt all the plastic bases. The coated fiber can be heated by conduction or radiation. In this example, the heating furnace 16 is a Lundberg one-stage heating tube furnace with a maximum operating temperature of 1 200 * 0, a length of 75 cm, and an inner diameter of 5 cm. The typical residence time of prepreg in the furnace is approximately 2 to 20 seconds. In most cases, a residence time of less than 10 seconds is sufficient to liquefy the plastic and fuse to the longitudinal dimension. For some viscous melts, for example, the polymer is polyethylene, it often takes a longer time to promote the resin (please read the precautions on the back and then fill out this page). This paper standard is used in China National Standard (CNS) A Specifications (210 to 297 male dragons) — 38-21104 ^ Λ 6 Β6 Printed by the Ajiongzhi Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Description of the invention (Infiltration of the fiber surface. Among the recycled waste plastic products, polyparaphenylene Diethyl dicarboxylate is usually counted as the plastic with the highest melting point. The melting point of polyethylene terephthalate is nearly 2 5 01C, so the temperature of the heating furnace must at least reach its melting point temperature, that is, 250T :, preferably set at 300t :, or even higher. In order to reduce the residence time in the furnace and strengthen the resin infiltration, the heating temperature can be set very high, and the material temperature will not reach the furnace temperature. When the heating furnace temperature exceeds 400 degrees, Most recycled plastics will degrade within a certain residence time. In this case, certain measures must be taken to remove the resin powder that has dripped into the heating furnace from the yarn, otherwise it will increase the fire. The possibility of powder coating. Powder coating uses powder coating to apply resin matrix material particles to the surface of the fiber. It can be carried out using an electrostatic spray gun or a friction electrostatic spray gun. The most basic design of an electrostatic spray gun is a tube It has a power supply electrode connected to a high-voltage generator. The powder particles are charged in a certain way, usually by driving airflow, through the barrel, and by the action of the electrodes. The charged powder particles are then transported to the surface of the fiber and bonded to the fiber , Thus coated. Since the fiber is grounded, a reverse polarity is generated between the charged powder particles and the fiber. In this example, the electrostatic spray gun is housed in a powder container, which is The fluidized bed is replaced. After leaving the disperser, the fiber enters the powder container. The powdered resin is transported into the spray gun to receive the charge, and then (please read the precautions on the back before filling this page). China BB home standard (CNS) A 4 specifications (210x297 male dragon) -39-2 a-4 A c 66 ΛΒ V. Description of invention (Re-spray to ground Above the fiber. Part of the charged powder particles are bonded and coated on the surface of the fiber, while the rest are recycled to the spray gun. The coated strands leave the powder container and enter the heating furnace. Process parameters of this method Including the air flow rate through the spray gun, the amount of powder inflow, and the size of static electricity. The selection of these parameters is mainly based on the nature of the fiber and resin material used. For example, when used! ^! ^! ^! ^-Gema AG 7 0 1-6 type electrostatic spray gun; the resin matrix material is nylon 11 powder with a particle size of less than 150 microns, and is mixed with some sulfonic black pigment; the fiber yarn is a 12K master fiber, which has been dispersed into 5 cm wide, under this condition Under the following conditions, the process conditions used are: air flow level is 0-7, powder flow level is 0-10, static electricity is 0 to -80kV. Table 1 lists the coating process parameters and values. (Please read the precautions on the back and then fill out this page) Employee consumption cooperation of the Ministry of Economic Affairs, Bureau of Standards, Du Printing, Table 1 coating process, value, linear velocity, air flow, powder flow, electrostatic size, resin weight (m / min), speed level, speed level (~ kV) content (%) 3.54 1.5 4.5 25 34.8 6.21 2.0 6.0 15 41-0 8.25 2.0 10.0 7 43.5 13.65 2.0 10.0 7 30.0 c. Wet powder coating process In the wet powder coating process, such as the suspension method or In the emulsion coating method, the resin matrix material is a wet powder. The fiber yarn enters the coating system. The standard of this paper is 20. The general specifications of China National Standards (CNS) A 4 (210 to 297 kg) -40-211 ^ ¾ Λ 6 156 Printed by the Employees Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (3 $ is not required to be grounded before. Therefore, the previously mentioned stainless dysprosium stick 17 is no longer needed in this method. After leaving the diffuser 18, the fiber can also pass through a The device is coated with an adhesion promoter. After the adhesion promoter is applied, the fiber enters the wet powder coating system, which consists of a stick applicator, a wet powder or emulsion storage tank, and a suspension pump The resin matrix material is suspended in a liquid medium, which can be water or a solvent. Aqueous liquid medium includes water, and sometimes a water-soluble binder. Solvent-based liquid medium includes a solvent, It also contains a soluble binder when needed. The fiber passes through the upper surface of the roller applicator, and the roller slowly rotates in the opposite direction to the fiber. The lower surface of the stick applicator and the suspension or emulsion in the storage tank Connected by. With non-stop Rotate, the roller will bring the suspension or emulsion to the upper surface, make it contact with the passing thread to be coated. The suspension pump can maintain the concentration of the suspension or emulsion uniform. The coated fiber leaves the roller coating After the coating, it enters a dryer where the water or solvent brought in during the suspension coating evaporates. If the resin is fused to the fiber surface, the water-soluble binder can also be removed. Then, the dried fiber It enters a melter, where the resin matrix material liquefies and wets the surface of the fiber. In the wet powder coating process, there is also a method that does not use a stick coater, but directly passes the fiber through the suspension or emulsion, and then directly Enter the dryer. D. Hot melt coating process Hot melt coating system is usually made by a stick applicator or an extruder (please read the precautions on the back before filling this page) Binding-Strapping-This paper size Use the Chinese National Standard (CNS) Grade 4 specifications (210X297 public waste) -41-Λ 6 136 Printed by the Ministry of Economic Affairs, Pingyang Bureau, Pinggongxiaot Cooperative V. Invention description (3d machine and a mold group) When the stick is used in the hot melt method, the operation method is the same as the wet powder method described above, but in this case, a suspension or emulsion storage tank is no longer used, but a hot melt storage tank containing a resin matrix material is used. Like the powder coating process, the stick coater can also be used, and the fiber can be directly passed through the hot melt storage tank. When the hot melt method uses an extruder and a mold operation, the dispersed fiber is drawn through a flat die, and The machine constantly supplies hot-melt matrix material to the mold and coats the fibers in the mold. The bottom of the mold is carved with a concave mold to divide the prepreg into multiple strands. When the hot melt of the resin matrix contacts the fibers, The fiber is immediately infiltrated. Therefore, it may not be necessary to set up another furnace to further complete the resin infiltration. In this process, some special equipment, such as a die with a groove or a stick applicator, may be required Use to help split the prepreg into multiple strands. e. Solution coating The solution coating process uses various solvents. In this method, the resin matrix material is dissolved in an appropriate solvent, and then the fiber is passed through this solution, or a stick soaked in the solution, to coat the fiber. The coated fibers pass through a dryer to evaporate the solvent. 6. Pre-impregnated yarn samples a. Heave fiber yarn / PEEK resin matrix material Use Hercules 6 K AS4 fiber yarn without any infiltrant, single fiber diameter 8 microns. The fiber passes through a jet of air, and the fiber (please read the precautions on the back before filling in this page) The paper size is free to use the China Sleepy Standard (CNS) A 4 specification (210x297 public release) -42-Λ 6 Β6 V. Description of the invention (4 () dimensional yarn is dispersed to about 60mm wide. The rollers located at the inlet and outlet of the diffuser create tension on the fiber yarn. The fiber yarn then passes through an electrostatic bed with PEEKV150VPF resin powder produced by ICI, average The particle size is 90 microns. The fiber yarn is connected to the ground, and the powder is charged at a negative voltage of 65kV. The fiber yarn passes through a tube heating furnace in a dispersed form under tension, and the temperature in the furnace is 45〇υ, melting PEEK The fiber yarn is then cooled in the air, and then passes through the driving stick, and finally reaches the winding package equipped with tension adjustment. The residence time of the fiber yarn in the powder applicator and the heating furnace is 1.4 seconds and 6 respectively. 7 seconds. Linear velocity is 6.8 meters per minute. The volume content of the fiber in the prepreg yarn is 60%. The flexural rigidity of the prepreg yarn is 890 mg_ cm, while the flexural resistance of the uncoated fiber yarn The stiffness is 6 7 OlDg — cm. By comparison After analysis, the stiffness of the pre-impregnated yarn after consolidation is about 216, OOOfflg — cm. B. Glass fiber yarn / PE EK resin matrix material uses S 2 glass fiber yarn of Owens Corning glass fiber company, each yarn contains single fiber 4 , 080 roots, treated with a high-temperature infiltrant, printed by the Employee Consumer Cooperative of the Ministry of Economic Affairs, Pyongyang Bureau (please read the precautions on the back before filling in this page). The fiber diameter is 9 microns. The resin matrix material is the same as the above example PEEK. Before contacting the last grounded stick, the glass fiber yarn is cleaned with a wet foam block to increase the surface conductivity. Then the fiber yarn passes through an electrostatic bed with PEEKV150 PF resin powder produced by ICI. The average particle size is 90 cm. The fiber is connected to the ground, and the powder is charged at a negative 70kV voltage. The fiber yarn passes through a tube heating furnace in a dispersed form under tension, and the temperature in the furnace is 45 0C. The standard side uses the Chinese S home standard (CNS) A4 specification (210x297 male dragon) -43-Λ 6 Β6 Printed by the Zhengong Consumer Cooperative of the Bureau of Standards, Ministry of Economic Affairs V. Invention Description (4)) PEEK melted. Fiber yarn Then cooled in the air, and then through the drive lifter, and finally reached the winding package equipped with tension adjustment. The retention time of the fiber yarn in the powder applicator and the heating furnace is 5.2 seconds and 26. 3 seconds. Linear velocity is 1.7 meters per minute. The body content of the prepreg yarn is 60%. C. Sulfon fiber yarn / LaRC — TPI resin matrix material uses Hercules ’6 KA S4 carbon fiber yarn without Any infiltrant treatment, single fiber diameter 8 microns. The resin matrix material is thermoplastic polyimide La RC TR I. The preparation method of prepreg is described in Example a. After the fiber yarn passes through the air flow disperser and the sticks located in front of and behind it, it enters an electrostatic bed containing LaRC TP I powder produced by Rogers with an average particle size of 35 microns. The fiber yarn is connected to ground, and the powder is charged at a negative voltage of 67 kV. The fiber yarn passes through a tube heating furnace in a dispersed manner under tension, and the temperature in the furnace is 400C, melting TPI. The fiber yarn is then cooled in the air, then passed through the driving stick, and finally reaches the winding package equipped with tension adjustment. The residence time of the yarns in the powder applicator and the heating furnace was 3.2 seconds and 16 seconds, respectively. The line speed is 2.9 seconds per minute. The volume content of the yarn dimension in the prepreg yarn is 37%. The flexural rigidity of the prepreg yarn is 7,000 mg_cm, while the flexural rigidity of the uncoated fiber yarn is 6 7 Omg- 7. Post-processing of the prepreg yarn. Home Sample Standard (CNS) Grade A 4 (210x297cm) (please read the precautions on the back before writing this page) -44-211542 Λ 6 Printed by Beigong Consumer Cooperative, Bureau of Standards, Ministry of Economic Affairs Description (a. Overview After the fiber 13 is infiltrated by the resin-based skeleton material in the coating device 20, the prepreg yarn 50 may pass through a set of polishing sticks 46 as needed. This set of rollers 46 may be set in the heating furnace 16 or heated The device 70 can also be placed close to the outlet of the heating furnace 16 or the heater 70. However, in any case, the position where the stick 46 is installed in the device 8 must be in a state where the resin matrix material is still liquid. The role of the wheel 46 is to force the liquid matrix resin into the fiber yarn strands for better wetting, and to reduce the strand-to-strand ratio caused by the resin-based skull droplets retained and consolidated on the outer surface of the yarn strands The surface resistance between them. Because the strands of the prepreg are very thin The prepreg yarn 50 cools quickly after leaving the heating furnace 16 or heater 70. Air cooling is usually sufficient. Of course, in some occasions, if a blower, cooling stick or similar device is used, it can also bring certain Benefits. It is very important during the cooling process to maintain sufficient tension in the dispersed yarn strands, otherwise the various yarn strands in the prepreg yarn will loosen and stick to each other, making the prepreg yarn very flexible in stiffness It is also important to prevent the individual fibers of the prepreg from contacting each other during consolidation, which will result in strong inter-strand bonding. If necessary, the heating furnace 16 or heater 70 can also be used. After that, convection cooling is provided (not shown in the figure). Conductive cooling can also be used. Conductive cooling requires surface contact, which can prevent the lateral movement of the fiber yarn. After cooling, some of the mechanical devices described above can also be used Carry out the split. But it is not good to rely on the split after cooling alone, because it will cause fiber damage beyond the limit. Generally speaking, the resin in the prepreg yarn (Please read the precautions on the back before filling out this page) This paper uses the Chinese National Standard (CNS) A4 specifications (210x297 male dragon) -45-211d43_Be printed by the consumer cooperation of the Bureau of Standards of the Ministry of Economic Affairs. Description of the invention (4¾ The volume content of the substrate must be above 25%. Only in this way can a structure be substantially free of bubbles, which can be used for further processing into the final laminated material structure. The main function of the pinch wheel is in the processing process Pull the fiber yarn 1 1, and apply sufficient tension to the strand yarn to prevent it from loosening laterally. There are many types of devices used to pull the fiber, including mechanically driven pinch wheels, preferably coated with rubber ; There is also a friction roller, preferably with a rubber surface coating. The package device 12 may be any conventional fiber yarn package with tension adjustment. In addition, the prepreg yarn 50 can also be directly transported to the next processing process, such as a cutting machine, to produce raw materials for sheet or bulk molding compound. b. Ribbon-shaped product The ribbon-shaped product of the prepreg is produced, as shown in FIGS. 8 and 9, after the fiber 13 is wetted by the resin matrix material in the coating system 20, the prepreg 49 is sent到 成 带 区 20。 The zone 20. The tape forming device most preferred for use in the present invention is the use of two matching sticks, one with a groove (60) engraved on its surface, and the other stick 62 with a bump. Fig. 10 and Fig. 11a show the structures of the rollers 60 and 62. The bumps of the roller 62 and the grooves of the roller 60 are matched with each other and coincide. When the powder sinter-coated fiber yarn 49 passes between the grooved stick 60 and the bumped stick 62, the powder sinter-coated fiber 49 is transformed into a known geometry Pre-impregnated yarn ribbon products. Fig. 11b shows another configuration of the roller 6 0 with recesses and the roller 6 2 with protrusions. In this paper, please use the China Sleepy Family Standard (CNS) Grade 4 specifications (210x297 public goods) (please read the precautions on the back before writing this page). Binding and binding. -46-211542 Λ 6 Β6 Ministry of Economic Affairs Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards V. Description of the invention (In Π, the groove is a continuous concave shape, and the convex block becomes a continuous convex shape, the concave surface and the convex surface are mutually Matching. As shown in Figure 1 1 a, the bump structure of the roller 6 2 matches the groove of the roller 6 0, matching each other. The flexible multi-strand prepreg passes between the sticks 60 and 62, so The pre-impregnated yarn 4 9 is transformed into a belt-shaped product 50 of a certain geometric shape. The sticks 60 and 62 generally interact through a cylinder 64 mounted on one of the sticks under a certain pressure, and other Pressing methods, such as springs or hydraulic cylinders. The rollers 60, 62 are installed at the exit of the thermal fusion coating production line, that is, the belt zone, which takes the separation step 109 shown in Figure 1. Figure 8 shows , Kunzi 6 ◦ and 62 are installed in the melting step 107, which is the heating furnace 16 and the package step 10 07, also It is between the winders 1 and 2. In this example, the flexible multi-ply prepreg yarns come out of the heating furnace 16 and consist of a heater 6 6 pairs of yarn strands 4 installed near the gap between the two rollers. 9 Heating to maintain its temperature. Focused quartz infrared lamp is a suitable heater 66 to heat the yarn 49 to maintain its temperature. Focused quartz infrared lamp is a suitable heater 66. For example, 74.285 type produced by Argus company , The power is about 250 watts, controlled by -3PN 1 0 1 0 Staio autotransformer. The diameter of the grooved handle 60 is about 12. 5cm, the width is 2. 5cm, the width of the groove is 1. 25cm, depth 0.31cm. The diameter of the stick 62 with the concave block is about 12. 5cm, width 2.5cm, the width of the convex block matching the groove is 1. 25cm, and the height is 0.3 1 cm. It is usually cold roller. It can be loosened by fiber 04. Separate the size of the paper. Use 8 Chinese standard (CNS) A4 specifications (210x297 public goods) (please read the precautions on the back and fill in this page). · -47-Λ 6 136 Printed by the employee consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of invention (4 present, so separate step 1 09 is often not needed. In addition, the cooling step 112 can often be accomplished by these sticks, or by contacting the fiber 104 with the surrounding air. The prepreg 49 is drawn through a roller 60 and 62 by a winding device 12 When the fiber passes through the pressure device 64, a stick is pressed to another stick. The cylinder is a suitable pressure device 64, such as the type 091.5D produced by Bimba, equipped with the type 1Z838B produced by Speedaire pressure controller. A suitable air cylinder can produce a force of about 20 psig on a 0.5 inch wide prepreg 4 9. When the stick 62 with bumps is used, the prepreg is forced into the gap between the groove and the bump, and the roller between the groove and the rollers 60, 62 with bumps The geometric dimensions of the gap are fixed. The pre-impregnated yarns are pressed together in this gap to form a flexible strip 50 with a certain geometric size. The producer selects the size of the groove of the roller 6 0 and the bump of the roller 6 2 according to the needs to produce the band-shaped product 5◦ with the desired geometric size. When a stick 62 with a convex surface is used, the prepreg yarn enters between the concave surface and the convex surface under the action of an external force, and is pressed together at the jacket, thereby forming a flexible band-shaped product 50 of known geometric size. The producer selects the relative radii of the concave stick 60 and the convex stick 62 as needed to produce a band-shaped article 50 of a desired geometric size. The rollers 60 and 62 are usually cooled with air to solidify the resin matrix, so that the belt-shaped product 50 can be handled. The strip-shaped product 50 is then rolled by a guide wheel 68, and is wound up by a winding device. In the example shown in FIG. 9, the stick replaces the heating furnace 16. If (please read the precautions on the back before writing this page) Binding-Thread · Thread · This paper is used in the edge of the home 8 standards (CNS) Ή specifications (210X297 mm) -48-211 ^ 42 Λ 6 Β 6 Printed by the Employee Consumer Cooperative of the Bureau of Standards and Economics of the Ministry of Economic Affairs 5. Description of the invention (called not using a heating furnace 1 6, usually a second heater 70 is used. Ceramic heaters can be suitable for this purpose, such as GTE Sylvanza Ceramic heater with a power of 500 watts and a size of 12. 5X6.25 〇111, equipped with an 8 & 1 ^ 61 *-(1: 〇1611 ^ 115 6〇 type controller. The function of this heater 70 is to use To melt the powder 22 to obtain a powder sinter-coated prepreg yarn 49. The prepreg yarn 49 then passes through the belt forming zone described above in conjunction with Fig. 8. The power of the heaters 6 6 and 7 depends on the power For the material and the linear speed of production. For the production of 6K fiber yarns, coated with PEEK resin, the linear speed is 1.5 meters per minute to make a 1.25cm wide belt, the heater mentioned above can be applied Now another example. The banding zone is composed of a convex or concave stick 60, as shown in Figures 12 and 13 The fiber yarn 49 coated with powder sintering passes a certain point on the circumference of the stick 60 under tension. Under the combined effect of the tension and the concave shape of the roller, the fiber yarn moves to the lowest point of the concave surface, so that the pre-impregnated yarn 49 is transformed into a strip material of a certain geometric shape 5◦. The tension on the prepreg yarn can be provided by the winding device 12 or other types of devices not shown in the figure. By changing the relative radius of the concave structure of the roller 60 and The tension acting on the fiber yarn 49 will result in the fiber yarn 49 being merged together and transformed into a flexible ribbon material 50 of a certain geometric size. As in the previous example, the stick 60 can also be cooled, thereby allowing the resin matrix material It is cured to make the ribbon material 50 easy to handle. The ribbon material 50 is then rolled up by the guide wheel 68 through the winding device 12. In addition, as long as the tension on the fiber yarn is sufficient to make the flexible paper size easy to use a B Standard (CNS) Grade A 4 specifications (210X297) (Please read the precautions on the back before filling in this page) -49-211 ^ 42 Λ 6 L36 Ministry of Economic Affairs 屮 央 橾 准 局 员 消 #Cooperative print System 5. Description of the invention (The multi-stranded prepreg yarns are transformed into ribbons, and one or more flat surface lifters can also be used. Figures 20, 21 and 22 are photographs of the cross-sections of prepreg yarns produced by the present invention. The impregnated yarn is made of glass fiber and polypropylene matrix material. Figure 23 is a photo of the polypropylene and glass fiber ribbon material prepared by the present invention. Figure 2 3 a ribbon material is a line at 3 meters per minute The speed is prepared under the condition of a 114 infrared lamp molten resin material, and the pressure on the stick is 275kPa. The preparation conditions of the belt-shaped material of Fig. 23b are: linear velocity of 1.4 meters per minute, the resin matrix material is melted at 37010, and the pressure on the stick is 275 kPa. The band material made of powder sintered pre-impregnated yarn by the method of the present invention has a specific geometry and is suitable for different processing methods such as filament winding, advanced laying processes, and pultrusion. In the filament winding method, a mandrel with the same shape as the final product is used, and the _dimensional yarn is wound around the mandrel. The fiber placement rack moves a certain distance back and forth along the mandrel, which is controlled by an open loop controller. Since it is open loop, the controller does not monitor the width of the fiber yarn. If the width of the laid fiber yarns is too narrow, a gap will be generated between adjacent fiber yarns; on the contrary, if it is too wide, the adjacent fiber yarns will add to each other. Both cases will affect the quality of the final product. The advanced laying process also has similar requirements for filament yarn winding. In the pultrusion process, the yarn bundle is pulled through the die to form a continuous two-dimensional shape. If the veil yarn fed into the mold does not have a certain geometric shape, it will inevitably be rearranged in the mold, resulting in fibers in the final product (please read the precautions on the back before filling in this page) Standard (CHS) A 4 specifications (210X297 ¢) -50-Λ 6 Β 6 211542 V. Description of invention (called uneven dispersion, otherwise the fiber or mold will break. The rearrangement of this fiber creates friction resistance, It leads to an increase in traction, which can also cause fibers and even die damage. The emergence of these problems indicates the need to use prepreg yarns with a certain geometric size. In addition, flexible pre-impregnation processes such as filament winding and pultrusion are required. Impregnated yarn is used as a raw material to ensure the quality of the final product. The flexible multi-strand prepreg ribbon material of the present invention can achieve accurate geometric shape and flexible properties. C. Non-woven fabrics are shown in Figure 14-17 It is shown that when the prepreg yarns 133 are cooled, or after cooling, they are combined manually or mechanically to form a desired or suitable structure. It can be prepared into an ideal fabric 139. For example, the prepreg yarn 133 can be arranged in a unidirectional direction as shown in FIG. 14a, or can be arranged in a multidirectional direction as in 15a, or any other direction. The impregnated yarns 133 are laid on top of each other and combined together to become the nonwoven, flexible, multi-strand prepreg yarn fabric of the present invention. There are many ways to combine the prepreg yarns 133 together. At the selected point, they are connected by hot melt to make a prepreg yarn fabric with point connection 137. Other methods of combining prepreg yarn 133 include sewing or weaving with binder fiber or yarn; needle punch; water Hammer or pressure point connection. Figure 17 shows that the fabric 139 made by the suture 138 is very good. The photo Η in Figure 24 is a unidirectional prepreg non-woven fabric formed by interweaving fibers. The multi-head placement equipment can be used to Pre-impregnated yarn 133 is made into 3D non-standard paper, and the Chinese National Standard (CNS) < 1 Specification (210x297 gong) (Please read the precautions on the back before writing this page) Order _ Line _ Printed by the Ministry of Economic Affairs, Pyongyang Bureau of Zhengong Consumer Cooperatives-51 Printed by the consumer cooperative, for example, _B6_ V. Description of the invention (4-bow woven fabric, non-woven fabric with overdyed shape and two-dimensional or three-dimensional pre-formed skeleton. The shape of the fiber-laying mandrel can be obtained from different tables The final shape of the fabric or preformed skeleton is produced. These products of the present invention can be suitable for the manufacture of various laminated material structures. Nonwoven fabrics can be laid into high-grade like the thermosetting prepreg yarns for sticky hands Laminated material structure. Non-woven fabrics can be made into preforms for resin transfer molding or molding. Tubing method can be used to make tubular preforms. This type of work is often used to prepare golf clubs and nets. Rackets and sailing masts. In addition, a low-cost two-dimensional fabric can also be prepared and used in the subsequent process. The product of the present invention compares with the weaving or weaving of flexible multi-ply prepreg yarns The price is low. With the technology of the present invention, fabrics containing resin materials that are solid at room temperature can be made very flexible. However, the fabrics produced by the conventional technology are very stiff. The present invention is made of a solid resin matrix The fabric is both flexible and well infiltrated. Both the resin matrix and the reinforcing fibers use a fiber-shaped fabric structure, such as mixed yarn, mixed weave, or fiber layer, and the resin layer is alternately laid, although it is also flexible However, it can not achieve resin infiltration of fibers, so in the consolidation process, this dual-fiber structure requires more harsh processing conditions than the fabric of the present invention. All the above descriptions are for illustrative purposes only, and It is not intended to limit the scope of the method of the present invention. The following is the scope of patent application for the present invention. (Please read the precautions on the back before writing this page) Binding-Binding-Line-This paper standard is used in the S national standard (CNS) A 4 specifications (210x297 male dragon) -52-

Claims (1)

4.1〇 AT B7 C7 D7 經濟部中央標準局員工消費合作社印製 六'申锖專利範園 1 種用於生産一種性能改進且柔韌的並由許多預 浸漬纱股所組成之預浸漬纱的方法,這些預浸漬纱股中含 有增強纖維和樹脂基體材料,該生産辦法包括有下列各個 步驟: (a) 將一股由很多增強單纖維組成的纖維纱分散, 使這些增強纖維分散開來但仍保持一體; (b) 用樹脂基體材料塗覆增強纖維,在樹脂基體材 料與增強纖維之間産生界面粘結; (c )將與增強材料相接觸的樹脂基體材料液化,使 其塗覆在增強材料上面,形成預浸漬纱股。 2. 如申請專利範圍第1項的方法,還進一步包括有 下列步驟: (d) 將預浸漬纱股冷卻,在此冷卻過程中,阻止相 鄰的纱股粘並,直至樹脂基體材料固化。 3. 如申請專利範圍第2項的方法,還進一步包括有 下列步驟: (e) 將塗覆過的增強纖維相互分離開。 4. 如申請專利範圍第1項的方法,還進一步包括有 下列步驟: (d)將熱熔結塗覆過的預浸潰纱通過一成型裝置, 製成經熔結塗覆的預浸漬纱帶狀材料。 5. 如申請專利範圍第4項的方法,其中該成型裝置 對經熔結塗覆的預浸漬纱産生壓力。 6. 如申請專利範圍第5項的方法,其中製備經熔結 (-先閲讀背面之注意事項再填寫本ΐ ) ”本紙張尺度通用十闽《家標準(CNS)T4規格(210x297公^ 81. 2. 2.500(H) -53 — AT B7 C7 D7_ 六、申请專利範SB 塗覆的預浸漬纱帶狀材料是在樹脂基體材料適宜的溫度下 進行。 7. 如申請專利範圍第6項的方法,還進一步包括對 預浸漬紗股冷卻的步驟,在此冷卻丨過程中,阻止相鄰的預 浸漬纱股相互粘結,直至經熔結塗覆的預浸漬纱轉變成經 熔結塗覆的預浸漬纱帶狀材料。 8. 如申請專利範圍第4項的方法,其中該帶狀材料 成型過程是通過兩個或多個相匹配的锟子完成的,在這些 棍子中,至少有一個锟子,其圓周是逐步凸出的形狀,同 時也至少有一個輥子,其圓周呈逐步凹下的形狀,令經熔 結塗覆的預浸漬纱通過上凸和下凹的棍子之間的空隙,至 少有一値辊子受力作用,從而進一步將力傳遞給正在通過 此輥子的經熔結塗覆過的預浸漬纱。 '9.如申請專利範圍第4項的方法,其中該帶狀材料 的成型過程是通過一個圓周逐步下凹的結構的辊子完成的 ,熔結塗覆過的預浸漬纱受到張力,並位於下凹圓周結構 内的某一部位。 10.如申請專利範圍第2項的方法,還進一步包括 下列各步驟: (e) 將多層預浸漬纱舖昼在一起,形成一多層預浸 漬纱結構; (f) 將舖疊在一起的預浸漬纱連接在一起,形成一 非織造預浸漬纱織物。 1 1 .如申請專利範圍第1 〇項的方法,其中該多層 本紙诋尺度適;丨Η,Η Η家櫺準(CNS)〒4規格(210 X '297公"^) 21154221164- (靖先聞讀背面之;±意事項再填寫本頁) 81. 2. 2.500(H) -54 - 211^)42 A 經濟部中央標準局員工消費合作社印製 六、申m利範so 預浸漬纱在步驟e中舖疊成單向結構。 12. 如申請專利範圍第10項的方法,其中該多層 預浸漬纱在步驟e中舖叠成多向結構。 13. 如申請專利範圍第1〇項的方法,其中將該預 浸漬纱連接在一起的方法包括:熱熔融,線縫,針剌,壓 力點連接,液體錘,缠結,粘結劑纖維混紡,粘結劑纱線 混纺。 14. 如申請專利範圍第1〇項的方法,其中步驟e 和f多次重覆。 15. 如申請專利範圍第2項的方法,進一步包括有 下列各步驟/ (e)將多層預浸漬纱舖疊在一起,形成一多層預浸 漬纱結構; (f)將預浸漬纱排列成所需的預成型體結構; (g)將預浸漬纱連接在一起,形成一預成型體。 16. 如申請專利範圍第15項的方法,其中步驟e 、f、g以任意順序進行。 17. 如申請專利範圍第15項的方法,其中步驟e 、:f、g同時進行。 1 8.如申請專利範圍第1 5項的方法,其中步驟e 、f、 g多次重量進行。 19.如申請專利範圍第2項的方法,進一步包括下 列步驟: (e)將多股預浸漬纱構造成複合材料製品。 (-先W讀背面之注意事項再琪寫本頁) .線· -本紙张尺度適;Π屮S W家標iMCNS) T4规格(210x297公If) 81. 2. 2.500(H) -55 一 … B7 ct — ----------- D t -------- --- 六、申鲭專利苑a 20. 如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,其中該樹脂基體材料另包含未經使 用過的新鮮塑料。 21. 如申請專利範圍第1、2、3、4、10、 15或18項的方法,其中該樹脂基髏材料主要是由回收 的塑料組成。 22. 如申請專利範圍第2、3、4、10、 1 5或1 8項的方法,其中該樹脂基體材料首先切碎,然 後再研磨成粉末,然後塗覆到增強纖維上去。 23. 如申請專利範圍第22項的方法,其中該樹脂 基髏材料主要是由新鮮塑料和回收塑料的混合物組成。 24. 如申請專利範圍第21項的方法,其中該樹脂 基髏材料主要是由一種回收塑料組成。 _2 5.如申請專利範圍第1、2、3、4、10、 1 5或1 8項的方法,其中該分散是橫向分散。 26. 如申請專利範圍第1、 2、 3、 4、 10、 1 5或1 8項的方法,其中該增強纖維的分、散是由增強纖 維的軸向張力來維持的。 經濟部中央標準局員工消費合作社印製 27. 如申請專利範圍第1、2、3、4、10、 1 5或1 8項的方法,其中該樹脂基體材料是以粉末狀與 增強纖維相接觸的。 28. 如申請專利範圍第27項的方法,其中該粉末 所含粒子的平均直徑比增強纖維的平均直徑大兩倍以上。 29. 如申請專利範圍第1、2、3、4、10、 81. 2. 2.500(H) (請先閱讀背面之注意事項再填寫本頁) 、本紙跟尺度適川,丨,Η «家櫺準(CNS) 規格(210x297公If) -56 - A 7 B7 CT DT 2ii042 六'申請專利苑® (;ί先閱讀背面之注意事項再填寫本頁) 1 5或1 8項的方法,樹脂基體材料包括下列種類: ABS条列,縮醛類,丙烯酸類,醇酸樹脂,烯丙基類, 胺基類,環氧類,氟塑料,呋喃類,蜜胺類,尼龍類,酚 醛類,苯基氧化物和苯基醚類,聚醒胺,聚醛胺一亞醛胺 ,聚丁烯類,聚碩酸酯,聚酯,聚雙醚酮,聚醚酮,聚亞 醯胺醚,聚乙烯類,聚亞醯胺類,聚甲基戊烯類,聚硫化 苯類,聚丙烯類,聚苯乙烯類,聚尿烷類,砚類,脲類和 乙烯基類,上述材料的混合物,銅,低熔點金屬,陶瓷的 母髏化合物。 30. 如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,其中該纖維的平均直徑不超過25 撤米。 31. 如申請專利範圍第30項方法,其中該纖維是 連缠谶維。 32. 如申請專利範圍第31項的方法,其中該纖維 的熔點高於所製得的預浸漬纱的固結溫度。 33. 如申請專利範圍第1、2、3、4、10、 經 濟 部 中 夬 標 準 局 員 工 消 費 合 作 社 印 製 1 5或1 8項的方法,其中該纖維是接地的。 34. 如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,其中該纖維選自由玻璃纖維,碩纖 維,石墨纖維,有機纖維,陶瓷纖維,金屬纖維和混纺纖 維所組成集團。 35. 如申請專利範圍第34項的方法,其中該有機 纖維僳選自那些熔點很高的液晶纖維。 81. 2. 2.500(H) -57 - AT 一 BT2110^^ ct -- -~~-_ D7 六、申綺專利.《L® 36. 如申請專利範圍第35項的方法,其中該混纺 纖維選自由醛胺/碩;醯胺/玻璃;醯胺/碩/玻璃和 碩/玻璃纖維所組成集團。 37. 如申請專利範圍第1、2、3、4、10、 1 5或1 8項的方法,其中該纖維在冷卻過程中相互分離 38·如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,其中該纖維在冷卻過程之前相互分 離。 39. 如申請專利範圍第1、 2、 3、 4、 10、 1 5或1 8項的方法,其中該增強纖維在相當大的程度上 被樹脂基體材料浸潤。 40. 如申請專利範圍第1、2、3、4、10、 (ίί先閱讀背面之注意事項再填窍本頁 經 濟 部 中 央 標 準 局 貝 工 消 費 合 作 杜 印 製 15或18項的方法,其中該纱股的平均長度大於其平均 寬度。 4 1 .如申請專利範圍第4 0項的方法,其中該纱股 的平均寬度大於其平均厚度。 42. 如申請專利範圍第41項的方法,其中該平均 長度至少是寬度的3 0倍。 43. 如申請專利範圍第1、2、3、4、10、 15或18項的方法,其中該預浸漬纱股中的樹脂基體材 料的體積含量超過2 5%。 44. 如申請專利範圍第1、2、3、4、10、 15或18項的方法,其中該預浸漬纱股的平均每股厚度 ^纸狀皮剌·丨,(5W5:辟(CNSVP倾if(21〇x2{)7公D gi" 2 2 500 -58 - , -訂· -:線· Λ I 2ϋ〇4<^ Β7 C7 D7 六、申請專利苑® 小於大約1 0 〇微米。 (請先聞讀背面之注意本項再填寫本VK ) 45. 如申請專利範圍第44項的方法,其中該預浸 漬纱股的平均每股厚度小於7 5微米。 46. 如申請專利範圍第45項的方法,其中該預浸 漬抄股的平均每股厚度大約為i 〇到5 0微米之間。 47. 如申請專利範圍第46項的方法,其中該預浸 漬纱股的平均每股厚度大約為i 5到30微米之間。 48. 如申請專利範圍第2、3、10、15或18 項的方法,其中該塗覆過的增強纖維在冷卻過程中分組形 成預浸漬纱股。\ 49·如申請專利範圍第丄、2、3、4、10、 15或18項的方法,其在分散步驟和塗覆步驟之間,進 一步包括一個脱除增強纖維的浸潤劑的步驟。 •5 0.如申請專利範圍第1、2、3、4、10、 15或18項的方法,其在分散步驟和塗覆步驟之間,還 包括一個對增強纖維施加粘結促進劑或浸潤劑的步驟。 51. 如申請專利範圍第1、2、3、4、10、 經 濟 部 中 央 標 準 局 員 工 消 費 合 作 印 製 15或18項的方法,其在分散步驟和塗覆步驟之間,還 包括一個對增強纖維進行表面活化的步驟。 52. 如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,還進一步包括一個收集步驟。 53. 如申請專利範圍第1、 2、 3、 4、 10、 15或18項的方法,還進一步包括一個抛光步驟。 54. 如申請專利範圍第1、2、3、4、10、 81. 2. 2.500(H) 木紙張尺度逋)IH,B Η家標準(CNS) 规格(21〇><297公^ -59 i 21:Lo4<J ---- -D7_ 六、申請專利苑園 15或18項的方法,其中該塗覆步驟是通過一個靜電流 化床裝置來完成的。 55.如申請專利範圍第1、2、3、4、1〇、 15或18項的方法,其中該塗覆步驟是通過一個粉末噴 摧裝置來完成的。 56· —種性能改進了的且柔韌的預浸漬纱,其由許 多預浸漬纱股組成;預浸漬纱股是由增強纖維和樹脂基體 材料組成;增強材料被分散開來,但仍保持一體,然後在 很大程度上被樹脂基體材料浸潤,這樣做成的預浸漬纱股 再充分固結成複合材料製品,且該預浸漬纱股的平均厚度 小於1 0 0微米。 57. —種已知幾何形狀及性能經改進的且柔韌的預 浸漬纱帶狀材料,其包含如申請專利範圍第56項的預浸 漬纱,其中該預浸漬纱股轉變成預浸漬纱帶,所以預浸漬 纱股中所含的空隙要少於預浸漬纱帶狀材料。 58. 如申請專利範圍第57項的預浸漬纱帶狀財料 ,其俗由包括有如下步驟的過程而製得: (a )提供增強纖維和樹脂基體材料; 經濟部中央標準局員工消費合作杜印製 (b) 用樹脂基體材料塗覆增強纖維; (c) 對增強纖維和樹脂基體材料加熱,使與增強纖 維接觸的樹脂基體材料液化,並塗覆在增強纖維表面,從 而製成熔結塗覆的預浸漬纱; (d) 將熔結塗覆的預浸漬纱通過一成型裝置,對其 施以成型力,從而將其轉變成熔結塗覆的預浸漬纱帶狀材 81. 2. 2.500(H) (-先聞讀背面之注意事項再填寫本^) '木紙张又度適川中ffl W家標準(CNS)T4規格(210x297公ϋ -60 - 申锖專利範a AT B7 C7 D7 經 濟 部 中 央 標 準 局 員 工 消 費 合 杜 印 製 料。 59.—種非織造預浸漬纱的織物,其是由多層如申 請專利範圍第56項的預浸漬纱組成,其中多層該預浸漬 纱被舖疊在一起,然後再連接起來,從而製成非織造預浸 漬纱的織物。 6 0.—種多維預成型髏,其僳由申請專利範圍第 59項的非織造預浸漬纱的織物所製成,其中將一層以上 的預浸漬纱舖叠起來,然後連接成所需要的構型,從而製 成預成型體。 6 1 . —種複合材料製品,其係由許多如申請專利範 圍第56項的預浸漬纱製成,其中將許多預浸漬纱排列成 所需要的構型,然後將它們連接成複合材料製品結構的預 成型體,再將此預成型體進一步加工成複合材料製品。 '6 2. —種複合材料製品,其係由許多如申請專利範 圍第56項的預浸漬纱組成,其中在預浸漬纱中的樹脂基 體材料是由回收塑料组成;增強纖維在很大程度上被樹脂 基體材料浸潤,預浸漬纱股的空隙含量要低於多股預浸漬 纱。 63. 如申請專利範圍第56_62項中任一項的預 浸漬纱,其中該預浸漬纱股的平均厚度小於75微米。 64. 如申請專利範圍第6 3項的預浸漬纱,其> 中該 預浸漬纱股的平均厚度為1 ◦到5 0徹米。 65. 如申請專利範圍第64項的預浸漬纱,其中該 預浸漬纱股的平均厚度為1〇到30徹米。 (請先閣讀背面之注意事項再填寫本頁) 本紙诋尺度適丨丨】屮Η Η家標準(CNS) f 4規格(210 X 297公 81. 2. 2.500(H) 一 61 — 211542 B7 C7 D7 濟 部 中 央 標 準 局 員 工 消 費 合 作 杜 印 製 66. 如申請專利範圍第56 — 62項中任一項的預 浸漬纱帶狀材料,其中該預浸漬纱中各纱股之間藉由共有 的增強纖維相連接。 67. 如申請專利範圍第59項的非織造預浸漬纱的 織物,其中該多層預浸漬纱舖叠成單向構型。 68. 如申請專利範圍第59項的非織造預浸漬纱的 織物,其中多層預浸漬纱舖*成多向構型。 69. 如申請專利範圍第59項的非織造預浸漬纱的 織物,其中該預浸漬纱像利用一種選自下述的方法而連接 在一起:熱熔融,線縫,針剌,壓力將樹脂基體材料熔化 ,壓力點連接,液體錘,鏵結,粘結劑纖維混紡,粘結劑 纱線混紡。 70. 如申請專利範圍第62項的複合材料製品,其 中該樹脂基體材料是由未經使用過的新鮮塑料組成。 71. 如申請專利範圍第62項的複合材料製品,其 中該樹脂基體材料主要是由回收塑料組成。 72. 如申請專利範圍第62項的複合材料製品,其 中該樹脂基體材料主要是由塑料混合物組成。 73. 如申請專利範圍第62項的複合材料製品,其 中該樹脂基體材料主要是由一種回收塑料組成。 74. 如申請專利範圍第56 — 6 1項的製品,其中 該預浸漬纱股中的空隙含量要低於預浸漬纱。 (熗先聞讀背面之注意事項再填笃本?{) 本紙張尺度適川十H W家標準(CNS) T4规格(210x297公《) 81. 2. 2.500(H) -624.1〇AT B7 C7 D7 The Ministry of Economic Affairs Central Standards Bureau employee consumer cooperative printed six 'Shen Yong Patent Fan Garden 1 method for producing a kind of improved and flexible prepreg yarn composed of many prepreg yarns, These prepreg yarns contain reinforcing fibers and resin matrix materials. The production method includes the following steps: (a) Disperse a fiber yarn composed of many reinforcing single fibers, so that these reinforcing fibers are dispersed but still maintained Integral; (b) Coat the reinforcing fibers with a resin matrix material to create an interfacial bond between the resin matrix material and the reinforcing fibers; (c) Liquefy the resin matrix material in contact with the reinforcing material to coat it on the reinforcing material Above, prepreg yarns are formed. 2. The method as claimed in item 1 of the patent scope further includes the following steps: (d) Cooling the prepreg strands. During the cooling process, the adjacent yarn strands are prevented from sticking until the resin matrix material solidifies. 3. The method as claimed in item 2 of the patent scope further includes the following steps: (e) Separating the coated reinforcing fibers from each other. 4. The method as claimed in item 1 of the patent scope further includes the following steps: (d) Passing the hot-sintered prepreg yarn through a forming device to produce the sinter-coated prepreg yarn Band material. 5. The method as claimed in item 4 of the patent application, in which the forming device generates pressure on the sintered prepreg yarn. 6. For example, the method of claim 5 of the patent scope, in which the preparation is fused (-read the precautions on the back side and fill in this one) ”The paper size is generally applicable to the“ Family Standard (CNS) T4 specification (210x297 ^ 81 2. 2.500 (H) -53 — AT B7 C7 D7_ VI. Patent application SB Coated prepreg ribbon material is carried out at a suitable temperature of the resin matrix material. 7. As claimed in item 6 of the patent scope The method further includes the step of cooling the prepreg strands. During the cooling process, the adjacent prepreg strands are prevented from bonding to each other until the sinter-coated prepreg yarn is converted to the sinter-coated yarn Pre-impregnated yarn ribbon material 8. The method as claimed in item 4 of the patent application, in which the ribbon material molding process is completed by two or more matching rollers, at least one of these sticks The circumference of the roller is gradually convex, and there is at least one roller whose circumference is gradually concave, so that the sintered prepreg yarn passes through the gap between the convex and concave sticks , At least one roller is under force , So as to further transmit the force to the prepreg yarn that is being sintered and coated by this roller. '9. The method as claimed in item 4 of the patent application, in which the forming process of the strip material is stepped down by a circle After the roller of the concave structure is completed, the sintered coated prepreg yarn is under tension and is located at a certain position in the concave circumferential structure. 10. The method of item 2 of the patent application scope further includes the following steps : (E) Lay multiple layers of prepreg yarns together to form a multi-layered prepreg yarn structure; (f) Connect laid together prepreg yarns to form a nonwoven prepreg yarn fabric. 1 1 . The method as claimed in item 10 of the patent scope, wherein the multi-layered paper is suitable for size; 丨 Η, Η 掂 渂 准 (CNS) 〒 4 specifications (210 X '297 public " ^) 21154221164- (Jing Xianwen Read the back of the page; ± Issues and then fill out this page) 81. 2. 2.500 (H) -54-211 ^) 42 A Printed by the employee consumer cooperative of the Central Bureau of Standards of the Ministry of Economy VI. Shenm Lifan so prepreg in step e The middle paving is stacked into a one-way structure. 12. If the patent application scope item 10 Method, wherein the multi-layer prepreg yarns are laid up in a multi-directional structure in step e. 13. The method as claimed in item 10 of the patent application, wherein the method of connecting the prepreg yarns together includes: hot melting, seam stitching , Needle punch, pressure point connection, liquid hammer, entanglement, binder fiber blending, binder yarn blending. 14. The method as described in item 10 of the patent application, in which steps e and f are repeated multiple times. 15. The method as claimed in item 2 of the scope of patent application further includes the following steps / (e) laying multiple layers of prepreg yarns together to form a multilayer prepreg yarn structure; (f) arranging the prepreg yarns into The required preform structure; (g) The prepreg yarns are connected together to form a preform. 16. The method as claimed in item 15 of the patent scope, wherein steps e, f, g are performed in any order. 17. The method as claimed in item 15 of the patent scope, in which steps e, f and g are performed simultaneously. 1 8. The method as claimed in item 15 of the patent scope, in which steps e, f, g are carried out multiple times by weight. 19. The method as claimed in item 2 of the scope of patent application further includes the following steps: (e) Constructing multiple strands of prepreg into a composite product. (-W read the precautions on the back and then write this page). Line ·-The paper size is suitable; Π 屮 SW home standard iMCNS) T4 specification (210x297 public If) 81. 2. 2.500 (H) -55 One ... B7 ct — ----------- D t -------- --- VI. Shenmao Patent Court a 20. If applying for patents No. 1, 2, 3, 4, 10 , 15 or 18, wherein the resin matrix material further contains unused fresh plastic. 21. The method of items 1, 2, 3, 4, 10, 15, or 18 of the patent application scope, in which the resin-based skeleton material is mainly composed of recycled plastic. 22. The method as claimed in items 2, 3, 4, 10, 15 or 18, wherein the resin matrix material is first chopped, then ground into a powder, and then coated onto the reinforcing fiber. 23. The method of claim 22, where the resin matrix material is mainly composed of a mixture of fresh plastic and recycled plastic. 24. The method as claimed in item 21 of the patent scope, in which the resin-based skeleton material is mainly composed of a recycled plastic. _2 5. The method as claimed in items 1, 2, 3, 4, 10, 15 or 18, wherein the dispersion is lateral dispersion. 26. The method as claimed in items 1, 2, 3, 4, 10, 15 or 18, wherein the distribution and dispersion of the reinforcing fibers are maintained by the axial tension of the reinforcing fibers. Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 27. The method of applying for items 1, 2, 3, 4, 10, 15 or 18 of the patent application, in which the resin matrix material is in contact with reinforcing fibers in powder form of. 28. The method of claim 27, wherein the average diameter of the particles contained in the powder is more than twice the average diameter of the reinforcing fibers. 29. If applying for patents 1, 2, 3, 4, 10, 81. 2. 2.500 (H) (please read the precautions on the back before filling out this page), the paper and the standard are appropriate, 丨, Η home Standard (CNS) specification (210x297 public If) -56-A 7 B7 CT DT 2ii042 Six 'patent application ® (; ί first read the precautions on the back and then fill out this page) 1 5 or 18 method, resin The matrix materials include the following types: ABS, acetals, acrylics, alkyds, allyls, amines, epoxy, fluoroplastics, furans, melamines, nylons, phenolic, Phenyl oxides and phenyl ethers, polyamines, polyaldimine-aldialdehydes, polybutenes, polyesters, polyesters, polydiether ketones, polyether ketones, polyimide ethers, Polyethylenes, polyimides, polymethylpentenes, polysulfide benzenes, polypropylenes, polystyrenes, polyurethanes, inkstones, ureas and vinyls, mixtures of the above materials , Copper, low-melting metal, ceramic mother compound. 30. The method as claimed in items 1, 2, 3, 4, 10, 15 or 18, wherein the average diameter of the fiber does not exceed 25 meters. 31. The method as claimed in item 30 of the patent application, in which the fiber is intertwined. 32. The method of claim 31, wherein the melting point of the fiber is higher than the consolidation temperature of the prepared prepreg. 33. For example, if the patent application is 1, 2, 3, 4, 10, the Ministry of Economy, Central Standards, Bureau of Labor and Consumers Cooperatives printed a method of item 15 or 18, where the fiber is grounded. 34. The method as claimed in items 1, 2, 3, 4, 10, 15 or 18, wherein the fiber is selected from the group consisting of glass fiber, primary fiber, graphite fiber, organic fiber, ceramic fiber, metal fiber and blended fiber Form a group. 35. The method of claim 34, wherein the organic fiber is selected from those liquid crystal fibers having a high melting point. 81. 2. 2.500 (H) -57-AT one BT2110 ^^ ct--~~ -_ D7 Sixth, Shen Qi patent. "L® 36. The method of applying for patent scope item 35, in which the blended fiber It is selected from the group consisting of aldamine / master; amide / glass; amide / master / glass and master / glass fiber. 37. The method of items 1, 2, 3, 4, 10, 15 or 18 of the patent application scope, in which the fibers are separated from each other during the cooling process 38. If the patent application scope is 1, 2, 3, 4, The method of item 10, 15 or 18, wherein the fibers are separated from each other before the cooling process. 39. The method as claimed in items 1, 2, 3, 4, 10, 15 or 18, wherein the reinforcing fibers are impregnated with the resin matrix material to a considerable extent. 40. If applying for patent scope items 1, 2, 3, 4, 10, (Li first read the precautions on the back and then fill in this page. The method of printing 15 or 18 items in the Beihang Consumer Cooperation of the Central Standards Bureau of the Ministry of Economic Affairs, of which The average length of the yarn strand is greater than its average width. 4 1. The method as claimed in item 40, wherein the average width of the yarn strand is greater than its average thickness. 42. The method as claimed in item 41, wherein The average length is at least 30 times the width. 43. The method as claimed in item 1, 2, 3, 4, 10, 15 or 18, wherein the volume content of the resin matrix material in the prepreg strand exceeds 2 5%. 44. The method as claimed in item 1, 2, 3, 4, 10, 15 or 18, wherein the average thickness per share of the prepreg strands ^ paper-like leather 剌, (5W5: (CNSVP tilt if (21〇x2 {) 7 male D gi " 2 2 500 -58-,-order ·-: line · Λ I 2ϋ〇4 < ^ Β7 C7 D7 VI. Application for patent court ® less than about 1 0 〇 Micron. (Please read the note on the back first and then fill in this VK) 45. If the method of applying for patent scope item 44 The average thickness of the prepreg strands per share is less than 75 microns. 46. The method as claimed in item 45 of the patent application, wherein the average thickness of the prepreg strands is about 100 to 50 microns per share. 47. The method as claimed in item 46, wherein the average thickness of the prepreg strands is approximately between 5 and 30 microns. 48. As claimed in item 2, 3, 10, 15 or 18 Method, in which the coated reinforcing fibers are grouped to form prepreg strands during the cooling process. 49. As in the method of patent application scope item 2, 2, 3, 4, 10, 15 or 18, it is dispersed Between the step and the coating step, a step of removing the sizing agent of the reinforcing fiber is further included. • 50. The method as described in items 1, 2, 3, 4, 10, 15 or 18 of the patent application scope, which is dispersed Between the step and the coating step, there is also a step of applying an adhesion promoter or wetting agent to the reinforcing fibers. 51. For example, if the scope of patent applications is 1, 2, 3, 4, 10, the Ministry of Economic Affairs Central Standards Bureau employee consumption cooperation The method of printing 15 or 18 items, which is scattered Between the step and the coating step, a step of surface activation of the reinforcing fiber is also included. 52. The method of items 1, 2, 3, 4, 10, 15 or 18 of the patent application scope further includes a collecting step 53. If the method of applying for items 1, 2, 3, 4, 10, 15 or 18 of the patent application scope further includes a polishing step. 54. If applying for patents No. 1, 2, 3, 4, 10, 81. 2. 2.500 (H) wood paper standard) IH, B Η home standard (CNS) specifications (21〇 > < 297 public ^ -59 i 21: Lo4 < J ---- -D7_ 6. The method of applying for patent gardens 15 or 18, wherein the coating step is completed by a static current fluidized bed device. The method of item 1, 2, 3, 4, 10, 15, or 18, wherein the coating step is performed by a powder spraying device. 56 ·-A flexible and pre-preg yarn with improved properties, It is composed of many prepreg yarns; the prepreg yarns are composed of reinforcing fibers and resin matrix materials; the reinforcing materials are dispersed, but still remain integrated, and then largely infiltrated by the resin matrix material, so doing The prepreg strands are fully consolidated into a composite product, and the average thickness of the prepreg strands is less than 100 microns. 57. A flexible and flexible prepreg ribbon material with known geometric shapes and properties , Which contains the prepreg yarn as claimed in item 56 of the patent application, wherein the prepreg The strands are converted into prepreg tapes, so the gaps contained in the prepreg strands are less than those of the prepreg tapes. 58. For the prepreg tapes of item 57 of the patent application, the common reasons include It is produced by the following steps: (a) providing reinforcing fibers and resin matrix materials; the Ministry of Economic Affairs Central Bureau of Standards and Staff's consumer cooperation du printing (b) coating resin matrix materials with reinforcing fibers; (c) reinforcing fibers and The resin matrix material is heated to liquefy the resin matrix material in contact with the reinforcing fibers and coated on the surface of the reinforcing fibers, thereby making a sintered coated prepreg yarn; (d) passing the sintered coated prepreg yarn through a The forming device applies a forming force to transform it into a frit-coated prepreg ribbon 81. 2. 2.500 (H) (-Read the precautions on the back side before filling in this book ^) 'Wood The paper is also suitable for the Sichuan FLL W Family Standard (CNS) T4 specification (210x297 ϋ -60-Shen Yong Patent Range a AT B7 C7 D7 Ministry of Economic Affairs Central Standards Bureau staff consumption of printed materials. 59.-kind of nonwoven Pre-impregnated yarn fabric, which is made up of many It is composed of the prepreg yarn in the 56th range of the patent application, in which multiple layers of the prepreg yarn are laid together and then connected together to make a fabric of nonwoven prepreg yarn. It is made of a non-woven prepreg yarn with patent application scope item 59, in which more than one layer of prepreg yarn is laid up and then connected into a desired configuration to make a preform. 6 1. A composite material product made of many prepreg yarns as claimed in item 56 of the patent application, in which many prepreg yarns are arranged into a desired configuration, and then they are connected into a composite material product structure The preform is then further processed into a composite material product. '6 2. A composite material product, which is composed of many prepreg yarns as claimed in item 56 of the patent application range, in which the resin matrix material in the prepreg yarns is composed of recycled plastics; the reinforcing fibers are largely Wetted by the resin matrix material, the void content of the prepreg strands is lower than that of multiple prepreg yarns. 63. The prepreg yarn according to any one of claims 56-62, wherein the average thickness of the prepreg strands is less than 75 microns. 64. As for the prepreg yarn of item 63 in the scope of the patent application, the average thickness of the prepreg strands in > is from 1 ◦ to 50 metre. 65. The prepreg yarn as claimed in item 64 of the patent application, wherein the average thickness of the prepreg strands is 10 to 30 cm. (Please read the precautions on the back first and then fill out this page) The size of this paper is suitable 丨】 屮 Η Η family standard (CNS) f 4 specifications (210 X 297 public 81. 2. 2.500 (H) 61-211542 B7 C7 D7 Employee's consumer cooperation of the Central Bureau of Standards of the Ministry of Economic Development and Printing 66. For example, the prepreg tape material of any one of the patent application items 56-62, in which the yarn strands in the prepreg yarn are shared by 67. Non-woven prepreg fabrics as claimed in item 59, wherein the multi-layer prepreg yarns are laid in a unidirectional configuration. 68. Non-woven fabrics as claimed in item 59 A fabric of prepreg yarns, in which multiple layers of prepreg yarns are laid out in a multi-directional configuration. 69. A fabric of nonwoven prepreg yarns as claimed in item 59 of the patent application, wherein the prepreg yarns utilize a material selected from Connected together by methods: thermal fusion, seam, needle punch, pressure to melt the resin matrix material, pressure point connection, liquid hammer, ring knot, binder fiber blending, binder yarn blending. 70. Patent application Scope 62 of composite materials , Where the resin matrix material is composed of unused fresh plastic. 71. As for the composite material product of the patent application scope item 62, wherein the resin matrix material is mainly composed of recycled plastic. 72. If the patent scope application 62 items of composite materials, wherein the resin matrix material is mainly composed of a plastic mixture. 73. For example, in the scope of the patent application of item 62, the resin matrix material is mainly composed of a recycled plastic. 74. If the application Articles of patent range 56-61, in which the content of voids in the prepreg strands is lower than that of the prepreg. (Kong first read the precautions on the back and fill in this copy? {) The paper size is suitable for Sichuan. HW Home Standard (CNS) T4 specification (210x297 mm) 81. 2. 2.500 (H) -62
TW081105390A 1992-07-07 1992-07-07 Flexible multiply towpreg, products therefrom and methods of production therefor TW211542B (en)

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