201237077 六、發明說明： 【發明所屬之技術領域】 本發明係與一種塑粒之製造方法有關，特別是指一種片狀高分子 塑粒之製造方法。 【先前技術】 知：’習知塑粒之製造方法，通常係先將一含之異氰酸鹽聚合 物、一含0H之羥化合物以及一架橋劑，同時輸送至一定量混合機内加 熱熔融成一液態之熱塑性聚氨酯樹脂（TPU)，接著再透過一雙軸押出 機將該熱塑性聚氨酯樹脂押出至一造粒設備進行水中造粒，以取得塑 粒成品’其中，該种造粒係將該熱塑性聚氨§旨細旨由該雙軸押出機 之押出模職出，使雜聚錢旨形祕狀，再透過該造粒設 備將雜塑性聚氨自旨樹脂蝴細形或圓柱形之塊狀，並讓該塊狀的 熱塑性聚氨_脂落人-水槽巾冷卻形成—難，最後再藉由一加熱 器將該塑粒烘乾，便可將該塑粒包裝後送至下游’以後製成各式產品。 惟’上述習知塑粒之製造方法係存有下列缺點： 1、該製造方法補驗繁雜，且需要制錄㈣鱗高耗電設 備’而會耗用較多的能源，根據實際測試，該製造方法整體所耗電能 約為500至8〇〇千瓦，非常不環保。 該製le方法所製成的塑粒係形成塊狀而導熱較慢，所以下游的 使財在後製加工時’需要使用較多的能源才能加熱炫融該塑粒，徒 增此源的消耗。 3、該製造方法必_雜押出機進行混煉與輸送，導致該醜 3 201237077 性聚氨_脂之分子結構會發生斷鏈裂解，叫健麵的分子量， 進而造成_粒的延展性不佳，尤其是下_使用者麵行後製加工 時，通常還會再次利用雙轴押出機進行混煉輪送，而使該熱塑性聚氨 酉曰树知之分子結構會再次斷鏈，延展性會吏差。 4、该製造方法為了避免該塑粒在造粒過程中發生相黏的狀況，通 常會在該水射添加賴，如销康賴等，但是騎齡使該塑粒 表面產生滑潤感’而料造成下游的使用者在後製加工時發生黏度不 足之窘況。 【發明内容】 ▲本^之目的係在提供—種分子量較高、延展性較佳且製程耗能 較低而具節能省碳效果之片狀高分子麵之製造方法。 為達上述目的，本發明所提供之一種片狀高分子塑粒之製造方 法’其係包含有混合顧、灌唯旨、_冷卻以及錄造粒等步驟， 其中’該混合·步驟聽—含_之魏酸躲合物、-含QH之經 化合物以及-架橋綱時定量輸送至—定量混合勒，均勻混合成一 液態之=_氨§旨旨；該·樹脂铸係先透過—輸送設備緩緩 _該定纽合機施放—第―離贱，再將鎌態之熱_聚氨賴 脂灌注於該第—離型紙上形成—樹脂薄層，之後再透過該輸送設備於 該樹脂^之另侧賴貼覆一第二離型紙，使該樹脂薄層形成均句片 狀士亚Ik著輪送自然冷卻；該強制冷卻步驟係將該樹脂薄層兩侧之第 離型紙與鄉二離型紙撕離，並讓該樹脂_經過—冷卻設備進行 強制冷部使雜脂薄層完全熟成硬化；制狀雜步驟係透過一轉1 4 201237077 切設備對該樹脂薄層進行裁切，以取得片狀之高分子塑粒。 本發明所提供之-種片狀高分子塑粒之製造方法，因為不 用大功率的雙軸押出機來騎輯輸送，且該樹_層在輪送過輕中 會自然冷卻科需使狀健冷卻設備進行冷卻，所以與習知塑 程相較’本發明不僅消耗的能源較少，且由於該高分子塑粒係呈片狀， 因此當下游的使用者在後製加工時，只需使时量能源便可加熱溶融 該高分子錄’錢本發日脱_節能省碳之目的，此外，因為該古 分子塑粒不需透過雙軸押錢進行混煉輸送，所以不會受到結構: 壞產生斷鏈，而與習知錄她會具錄高的分子數，_㊃古八 子塑粒會具有較佳之延展性。 Λ回刀 【實施方式】 請參閱第i、第二_及第三晒示，係為本發明之較佳實施 例之製造流程圖、製造示意圖以及高分子塑粒之立體圖，其係揭露有 一種片狀高分子塑粒之製造方法，該製造方法係包含有下列步驟： 混合原料：將一含NC0之異氰酸鹽聚合物、一含〇H之羥化合物以 及一架橋劑分別儲放在一儲料桶10，並同時定量輸送至一定量混合機 20内’均勻混合成一液態之熱塑性聚氨酯樹脂（TPU)。 灌注樹脂：先透過一輸送設備30緩緩的朝該定量混合機20施放 —第一離型紙4〇，再將該液態之熱塑性聚氨酯樹脂灌注於該第一離型 、、、氏40上形成一樹脂薄層50，之後再透過該輸送設備30於該樹脂薄層 50之另側滾壓貼覆一第二離型紙60,使該樹脂薄層5〇形成均勻片狀， 並隨著輸送自然冷卻，其中，該樹脂薄層50的厚度係被控制在〇 5 [5 3 5 201237077 至2公厘之間，而該輸送設備3〇則具有一輸送平台31，且該輸送平 台31上係設有一第一鏈齡32卩及一第二鍵輪組泊，該帛一鍵輪組 32係具有-設置於該定量混合機2〇翁之第一施放輪321，以及一設 置於該疋里混合機20後方之第-捲收輪322，可供分顧以施放與捲 收該第-離型紙4G ’而該第二鏈輪組33則設置於該第_鏈輪組32上 方’並具有-位於該定量混合機2〇與第一捲收輪犯2 μ之第二施放輪 33卜以及一位於該第二施放輪331後方之第二捲收輪咖，可供分別 用以施放與捲收該第一離型紙6〇，此外，於本實施例中，該第一離型 紙40與該第二離型紙60係為一霧面離型紙，而使該樹脂薄層之兩側 會形成霧面狀。 強制冷卻：將該樹脂薄層50兩側之第一離型紙4〇與該第二離型 、、’氏60撕離，並讓該樹脂薄層5〇經過一冷卻設備進行強制冷卻，使 該樹脂薄層50完全減硬化，其中，該冷卻設備7()係為—冷氣機。 片狀造粒：透過一裁切設備80對該樹脂薄層5〇進行裁切，以取 得如第二圖所示之片狀之尚分子塑粒9〇，其中，該裁切設備別係可 為-壓切機或為-模切機’而可姻模切献壓切的方式將該樹脂薄 層50裁切成片狀之高分子塑粒90，且於本實施例中，由於該第一離 型紙40與該第二離型紙60係為一霧面離型紙，因此該高分子塑粒9〇 之兩侧會形成霧面狀，同時，該高分子雜9G之最佳裁娜狀係為六 角形。 為供進一步瞭解本發明構造特徵、運用技術手段及所預期達成之 功致，茲將本發明使用方式加以敘述，相信當可由此而對本發明有汽 6 201237077 深入且具體之瞭解，如下所述： 請繼續參閱第-圖、第二圖以及第三圖所示，透過上述製造步驟， 使用者只需將原料分別置放於該等儲料桶1〇，並輸送至該定量混合機 2〇内均勻混合成該熱塑性聚氨醋樹脂，之後製該熱塑性聚氨醋樹脂 灌注於該第一離型紙40上形成該樹脂薄層5〇，並在該樹脂薄層之 另側貼覆該第二離形紙60，最後再撕離該第一離型紙4〇與該第二離 型紙60 ’並經過該冷卻設備70進行強制冷卻，以及透過該裁切設備 8〇進行裁切，便可取得該高分子塑粒90，藉此，使本發明之片狀高分 子塑粒之製造方法，减整體製程較習知簡短，且由於μ要使用大 功率的雙軸押出機，以及該樹脂薄層5〇在輸送過程中會自然冷卻，而 不而要使用大噸數的冷卻設備7〇，因此本發明相較於習知製程的耗電 量會更少’同時，因為該高分子塑粒9〇係呈片狀，所以當下游的使用 者在後製加工時’亦只需使用少量能源便可加熱熔融該高分子塑粒 9〇 ’而使本發明能夠達到節能省碳之效果。 ―值得-提的是’由於本發明之製造方林需要制雙轴押出機進 ^輪送’因此使該高分子錄9G不會受舰構性破壞產生_，而與 S知塑粒條會具有較高的分子數，進而讓該高分子雜⑽會具有較 佳之延展性，此外，因為在製造過程中，該第一離型紙40與該第二離 型紙60係為一霧面離型紙，使該高分子塑粒9〇之兩側會形成霧面狀， 所以使該高分子難9G本身即具有抗倾果，並不需科使用滑劑進 仃潤滑，而能夠在後製加工時，有效改善該高分子塑粒90黏度不足之 狀況。 7 201237077 請再同時參閱第四圓所示，係為本發明之另一較佳實施例之製造 示意圖，該片狀高分子塑粒之製造方法與前述較佳實施例不同之處係 在於，該混合原辭驟時，該含之異氰酸鹽聚合物、該含〇h之輕 化合物以及該架橋劑係先分別儲放在—第―儲料桶n内，之後再將該 含NC0之異驗贱合物與該含GiJ之触合物定量触至—第一定量 混。機21先行/ttt合成一混合物，並儲放在一第二儲料桶η内，最後 再將該混合物與該架橋_時輸送至—第二定量混合機&内均勾混 口成該㈣之熱塑性聚氨g旨細旨，藉此，能夠翻與前雜佳實施例 相同之效果。 兹，再將本發日狀概及其可達成之職功效陳述如下： 卜本發明之片狀高分子塑粒之製造方法，與習知麵製程相較不 僅製程較飾具有提高產量、節紅权絲，朋林需要使用大 功率的雙购出機以及大倾的冷卻設備，所以本侧她於習知製 程的耗電量會較少，而㈣達·能省碳之效果。 2、本發明之>}狀高分子雛之製造方法，因為該高分子塑粒係呈 片狀所以當下游的使用者在後製加工時，只需使用少量能源便可加 熱炫融該高分子錄，而具節省能源之效果。 3、本發日月之片狀高分子錄之製造方法，因為不需要使用雙轴押 機進仃輪送，所以該高分子塑粒不會受到結構性破壞產生斷鍵，而 ^習知錄她會具雜高齡子數，進而使該高分子難會具有較 佳之延展性。 平又 4、本發明之片狀高分子塑粒之製造方法，因為在製造過程中，辑 8 201237077 第-離型紙與該第二離型紙係為-霧面離型紙，使該高分子塑粒之兩 侧會形祕面狀，所贿該高籽_材即具有触絲，並不需 要再使用·進行爾，*涵錢製加工時，有效改善該高分子塑 粒黏度不足之狀況。 綜上所述，本發日月在_產品中實有其難之進步實雜，同時 遍查國内賴於此類結構之技術資料，文獻中亦未發現有相同的構造 存在在先’是以’本發明實已具備發料利要件，纽法提出申請。 惟’以上所述者，僅縣發明之—較佳可行實關而已，故舉凡 應用本發明制書对料雜騎為之粒結構變化，理應包含在 本發明之專利範圍内。 201237077 【圖式簡單說明】 第一圖係為本發明之較佳實施例之製造流程圖。 第二圖係為本發明之較佳實施例之製造示意圖。 第三圖係為本發明之較佳實施例之高分子塑粒之立體圖。 第四圖係為本發明之另一較佳實施例之製造示意圖。 【主要元件符號說明】 10 儲料桶 11 第一儲料桶 12 第二儲料桶 20 定量混合機 21 -第一疋置混合機 22 第一疋1混合機 30 輸送設備 31 輸送平台 32 第一鍵輪組 321 弟一施放輪 322 第一捲收輪 33 第—鍵輪組 331 第二施放輪 332 第二捲收輪 40 第一離型紙 50 樹脂薄層 60 第—離型紙 70 冷卻設備 80 裁切設備 90 高分子塑粒201237077 VI. Description of the Invention: [Technical Field of the Invention] The present invention relates to a method for producing a plastic pellet, and more particularly to a method for producing a pellet polymer pellet. [Prior Art] It is known that 'the manufacturing method of the conventional plastic granules is usually to first transfer an isocyanate polymer, a hydroxy compound containing 0H and a bridging agent to a certain amount of mixer for heating and melting into one. a liquid thermoplastic polyurethane resin (TPU), which is then extruded through a twin-axis extruder to a granulation apparatus for granulation in water to obtain a finished plastic product, wherein the granulation system polymerizes the thermoplastic The ammonia § is intended to be used by the two-axis extrusion machine to make the miscellaneous money, and then the heteroplastic polyurethane is made into a thin or cylindrical block through the granulation equipment. And let the block of thermoplastic polyurethane-fat-water towel sinking to form - difficult, and finally by a heater to dry the plastic pellets, the plastic pellets can be packaged and sent downstream. Various products. However, the manufacturing method of the above-mentioned conventional plastic pellets has the following disadvantages: 1. The manufacturing method is complicated to be complicated, and it is necessary to record (4) scale-high power-consuming equipment', and consumes more energy, according to actual tests, The overall energy consumption of the manufacturing method is about 500 to 8 kW, which is very environmentally friendly. The plastic pellets produced by the method of forming the method form a block shape and the heat conduction is slow, so that the downstream material needs to use more energy to heat and smear the plastic pellet during the post-processing, thereby increasing the consumption of the source. . 3. The manufacturing method must be mixed and transported by the miscellaneous extruder, resulting in the cleavage of the molecular structure of the ugly 3 201237077 urethane _ lipid, which is called the molecular weight of the healthy surface, which in turn causes poor ductility of the granules. In particular, when the user is going to perform the post-processing, the two-axis extruder is usually used again for the mixing and rotation, so that the molecular structure of the thermoplastic polyurethane tree will be broken again, and the ductility will be reduced. difference. 4. The manufacturing method is generally used to prevent the plastic particles from sticking during the granulation process, and is usually added to the water spray, such as the sale of Kanglai, but the riding age makes the surface of the plastic granules smooth. This causes the downstream users to have insufficient viscosity during post-processing. SUMMARY OF THE INVENTION The purpose of the present invention is to provide a method for producing a sheet-like polymer surface having a high molecular weight, a good ductility, a low process energy consumption, and an energy-saving and carbon-saving effect. In order to achieve the above object, a method for producing a sheet-like polymer plastic granule provided by the present invention includes the steps of mixing, irrigating, cooling, and granulating, wherein the mixing and the step are included. _ Slowly _ the fixed button machine is applied - the first - away from the enthalpy, and then the hot _ lysine is poured onto the first release paper to form a thin layer of resin, and then through the conveying device to the resin The other side is attached to a second release paper, so that the thin layer of the resin forms a uniform sentence, and the forced cooling step is to separate the first release paper on both sides of the thin layer of the resin. The paper is peeled off, and the resin _ passing through the cooling device is subjected to a strong cooling portion to completely harden the thin layer of the grease; the preparation step is to cut the resin layer through a turn 1 4 201237077 cutting device to obtain Sheet-shaped polymer plastic particles. The method for manufacturing the flaky polymer plastic granule provided by the invention is because the high-power double-axis extruder is not used for riding and transporting, and the tree _ layer will be naturally cooled in the light transmission. The cooling device is cooled, so compared with the conventional plastic process, the invention not only consumes less energy, but since the polymer plastic particles are in the form of a sheet, when the downstream user is in the post-processing, it is only necessary to make At the same time, the energy can be heated and melted. The polymer is recorded as the purpose of energy saving and carbon saving. In addition, since the ancient molecular plastic particles do not need to be mixed and transported through the double-axis money, they are not subject to the structure: Badness produces a broken chain, and with the knowledge of her, she will have a high number of molecules, and the _ four ancient eight plastic granules will have better ductility. Λ 刀 【 实施 实施 实施 实施 实施 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造 制造A method for producing a sheet-like polymer plastic granule comprising the following steps: mixing a raw material: storing an isocyanate polymer containing NC0, a hydroxy compound containing hydrazine H, and a bridging agent separately The hopper 10 is simultaneously metered into a quantity of the mixer 20 to uniformly mix into a liquid thermoplastic polyurethane resin (TPU). Injecting resin: firstly, a first release paper 4 is applied to the quantitative mixer 20 through a conveying device 30, and then the liquid thermoplastic polyurethane resin is poured onto the first release type, and the 40 is formed. The resin thin layer 50 is then rolled and coated on the other side of the resin thin layer 50 by the conveying device 30 to cover a second release paper 60, so that the resin thin layer 5〇 is uniformly formed into a sheet shape and naturally cooled with the conveyance. Wherein, the thickness of the resin thin layer 50 is controlled between 〇5 [5 3 5 201237077 to 2 mm, and the conveying device 3 具有 has a conveying platform 31, and the conveying platform 31 is provided with a a first chain age 32 卩 and a second key wheel group 228, the 帛 one-key wheel set 32 has a first application wheel 321 disposed on the quantitative mixer 2 ,, and a 设置 mixer a rear-rewinding wheel 322 of 20 is provided for dispensing and retracting the first release paper 4G' and the second sprocket set 33 is disposed above the first sprocket set 32 and has The quantitative mixer 2 〇 and the first take-up wheel 2 μ of the second application wheel 33 and one of the second application wheel 3 The second reel of the rear reel can be used to respectively apply and retract the first release paper 6 〇. In addition, in the embodiment, the first release paper 40 and the second release paper 60 are A matte release paper forms a matte surface on both sides of the thin layer of the resin. Forced cooling: the first release paper 4 两侧 on both sides of the resin thin layer 50 is peeled off from the second release type, and the resin layer 5 〇 is subjected to forced cooling by a cooling device to make the The thin resin layer 50 is completely hardened, wherein the cooling device 7() is an air conditioner. Sheet granulation: the resin layer 5 is cut through a cutting device 80 to obtain a sheet-like molecular plastic granule 9 as shown in the second figure, wherein the cutting device is The resin thin layer 50 is cut into a sheet-like polymer plastic particle 90 by a die-cutting machine or a die-cutting machine, and in this embodiment, The release paper 40 and the second release paper 60 are a matte release paper, so that the sides of the polymer plastic particles 9 are formed into a matte surface, and at the same time, the optimum shape of the polymer 9G is It is hexagonal. In order to further understand the structural features of the present invention, the technical means, and the intended accomplishment, the mode of use of the present invention will be described. It is believed that the present invention can be deeply and specifically understood by the present invention 6 201237077, as follows: Please continue to refer to the first, second and third figures. Through the above manufacturing steps, the user only needs to place the raw materials in the storage tanks 1 and transport them to the quantitative mixer 2 The thermoplastic polyurethane resin is uniformly mixed, and then the thermoplastic polyurethane resin is poured on the first release paper 40 to form the resin thin layer 5〇, and the second separation is applied on the other side of the resin thin layer. The paper 60 is finally peeled off from the first release paper 4 and the second release paper 60' and forced cooling by the cooling device 70, and the cutting device 8 is cut through the cutting device 8 to obtain the height. Molecular plastic granule 90, whereby the method for producing the flaky polymer granule of the present invention is shorter than the conventional one, and a high-power biaxial extruder is used for μ, and the resin thin layer 5〇 During the transport process It will naturally cool down, instead of using a large number of cooling devices, so the power consumption of the present invention will be less than that of the conventional process. At the same time, because the polymer plastic granules are in the form of flakes. Therefore, when the downstream user uses the small amount of energy to heat and melt the polymer plastic particles 9' during the post-processing, the invention can achieve the effect of energy saving and carbon saving. ―It’s worth mentioning that 'because the manufacturing of the invention requires a two-axis extrusion machine to send the wheel', so that the polymer recorded 9G will not be damaged by the shipbuilding _, and the S-shaped plastic strip will The higher the number of molecules, so that the polymer (10) will have better ductility, and further, because the first release paper 40 and the second release paper 60 are a matte release paper during the manufacturing process. The polymer plastic granules are formed into a matte surface on both sides of the granules. Therefore, the polymer is difficult to be 9G itself, and the anti-pour fruit is not required to be lubricated by the use of a slip agent, and can be used in post-processing. The condition that the viscosity of the polymer plastic particle 90 is insufficient is effectively improved. 7 201237077 Please refer to the fourth circle at the same time, which is a schematic view of manufacturing according to another preferred embodiment of the present invention. The manufacturing method of the sheet polymer plastic pellet is different from the foregoing preferred embodiment in that In the mixing of the original words, the isocyanate polymer, the light compound containing 〇h and the bridging agent are first stored in the first storage tank n, and then the NC0 is different. The test compound and the GiJ-containing conjugate are quantitatively touched - the first amount is mixed. The machine 21 first/ttt synthesizes a mixture and stores it in a second storage tank η, and finally transfers the mixture to the bridge _ to the second quantitative mixer & The thermoplastic polyurethane is intended to achieve the same effects as the prior art examples. Hereby, the statement of the date of the present invention and its achievable functions are as follows: The manufacturing method of the sheet-like polymer plastic granule of the invention is compared with the conventional surface preparation process, not only the process decoration, but also the improvement of the yield and the redness Quan Silk, Peng Lin needs to use a high-power dual-purchase machine and a large tilting cooling device, so on this side, she will consume less power in the conventional process, and (4) can save carbon. 2. The method for producing a polymer of the present invention, wherein the polymer plastic particles are in the form of a sheet, so that when the downstream user is in the post-processing, the heat can be heated and reduced by using a small amount of energy. Molecular recording, and has the effect of saving energy. 3. The manufacturing method of the sheet-like polymer recorded in the date of the present day, because it is not necessary to use the twin-axis machine to enter the wheel, so the polymer plastic particles will not be broken by structural damage, and the master will record her. It has a high number of old ages, which makes it difficult for the polymer to have better ductility. 4. In addition, in the manufacturing process of the sheet-like polymer plastic granule of the present invention, in the manufacturing process, the series 8 201237077 first release paper and the second release paper are - matte release paper, so that the polymer plastic granule The two sides will have a secret surface shape, and the high-seed _ material will have a touch of silk, and it does not need to be used again. When it is processed, the viscosity of the polymer plastic granule is insufficiently improved. In summary, the daily sun and the moon have made it difficult to make progress in the _ product. At the same time, the technical data on the structure of the structure in China was investigated. The same structure was not found in the literature. In the case of the present invention, it is already indispensable for the issue of materials, and Newfa has applied for it. However, the above-mentioned ones are only invented by the county, and it is preferable to be practical and feasible. Therefore, the use of the book of the present invention for the change of the grain structure of the material is intended to be included in the patent scope of the present invention. 201237077 BRIEF DESCRIPTION OF THE DRAWINGS The first drawing is a manufacturing flow diagram of a preferred embodiment of the present invention. The second drawing is a schematic view of the manufacture of the preferred embodiment of the invention. The third drawing is a perspective view of a polymer shaped plastic according to a preferred embodiment of the present invention. The fourth drawing is a schematic view of the manufacture of another preferred embodiment of the invention. [Main component symbol description] 10 Storage tank 11 First storage tank 12 Second storage tank 20 Quantitative mixer 21 - First 混合 mixer 22 First 疋 1 mixer 30 Conveying equipment 31 Conveying platform 32 First Key wheel set 321 brother one application wheel 322 first winding wheel 33 first key wheel set 331 second apply wheel 332 second take-up wheel 40 first release paper 50 resin thin layer 60 first - release paper 70 cooling device 80 Cutting equipment 90 polymer plastic