TWI240728B - Method of recycling crosslinked foamed plastic waste with adequately controlled cracking condition - Google Patents

Method of recycling crosslinked foamed plastic waste with adequately controlled cracking condition Download PDF

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TWI240728B
TWI240728B TW92107590A TW92107590A TWI240728B TW I240728 B TWI240728 B TW I240728B TW 92107590 A TW92107590 A TW 92107590A TW 92107590 A TW92107590 A TW 92107590A TW I240728 B TWI240728 B TW I240728B
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foamed plastic
materials
catalyst
plastic waste
patent application
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TW92107590A
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TW200420623A (en
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Yi-Fan Wu
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Plastics Industry Dev Ct
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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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

A kind of method of recycling crosslinked foamed plastic waste with adequately controlled cracking condition comprises steps of (a): feeding materials into a pulverizer to be pulverized so that reaction rate can be increased; (b): sending the above-mentioned materials into a specific gravity tank for selecting to classify materials with similar specific gravity so that suitable catalyst can be chosen; (c): sending the materials into a recycling machine so that the processed materials can be cut, compressed and melted; (d): adding the catalyst to provide compatible interfaces for the materials; (e): sieving and palletizing; (f): injection and extrusion molding to produce finished product so that crosslinked foamed plastics can be recycled.

Description

1240728 五、發明說明(1) 【發明所屬之技術領域】 本發明係有關一種回收交聯發泡塑膠廢料之方法,尤 指一種交聯發泡塑膠廢料添加催化劑,並以外力控制反應 速率而將交聯發泡塑膠廢料回收的方法。 【先前技術】 塑膠廢料回收最大的問題,在於必須花費大量的人力 以及機器設備,用以將廢料清洗以及選別,而且這些設備 造價昂貴,效率卻不高。而交聯發泡後之塑膠廢料,因為 回收困難,而被使用作固態燃料,或經過裂解而成為低分 子量重油。 上述之回收方法,雖然解決了塑膠廢料回收再利用的 問題,但上述方法所得之結果,只提供了塑膠廢料之最終 出路,且為低價值與低利用率之方法,並未達到廢料重複 使用之較高價值與高利用率的效果。 熱可塑性塑膠雖然遇熱可熔融,但一般若以萬馬力機 或雙滾桶機,無法同時融熔兩種熔點(t m )差異甚大之 塑膠,因為實際提供塑料熔融之熱來自於材料與機台之剪 切,如E V A與P P各占一半之混膠,即使溫度上升至2 ◦ ◦ °C,大部分熱會被E V A吸收而溶融,使P P打滑( 因為E V A於2 0 0 °C已熔融,過熱只會使E V A濃度變 稀,使剪切變低,不足以使P P在2 0 0 °C熔融),但是 ,如果將上述之混膠投入雙螺桿,由於雙螺桿基本上為飢 餓式進料,原料較不會因為個別熔融而打滑,但互不相容 之混膠會造成雙螺桿加熱熔融過程中極不穩定且無法控制1240728 V. Description of the invention (1) [Technical field to which the invention belongs] The present invention relates to a method for recovering cross-linked foamed plastic waste, especially a catalyst for adding cross-linked foamed plastic waste, and controlling the reaction rate by external force. Method for recycling cross-linked foamed plastic waste. [Previous technology] The biggest problem of plastic waste recycling is that it must spend a lot of manpower and machinery and equipment to clean and sort the waste. Moreover, these equipments are expensive and not efficient. The cross-linked foamed plastic waste is used as a solid fuel because of difficult recovery, or it is cracked to become a low molecular weight heavy oil. Although the above-mentioned recycling method solves the problem of recycling plastic waste, the results obtained by the above method only provide the final outlet of plastic waste, and it is a low-value and low-utilization method, which does not reach the reuse of waste materials. The effect of higher value and high utilization. Thermoplastic plastics can be melted when heated, but generally, if a 10,000 horsepower machine or a double barrel machine is used, two plastics with very different melting points (tm) can not be melted at the same time, because the actual heat of plastic melting comes from the materials and the machine. Shearing, such as EVA and PP each half of the mixed glue, even if the temperature rises to 2 ◦ ◦ ° C, most of the heat will be absorbed by EVA and melt, making PP slip (because EVA has melted at 200 ° C, Overheating will only dilute the EVA concentration and make the shear low, which is not enough to melt the PP at 200 ° C). However, if the above-mentioned mixed rubber is put into a twin screw, the twin screw is basically hungry. , The raw materials are less likely to slip due to individual melting, but the incompatible mixed glue will cause the twin-screw heating and melting process to be extremely unstable and uncontrollable

1240728 五、發明說明(2) 之湧流(s u r g i n g )及溶融破裂(f r a c t u r e ),因此傳統上慣用相容化劑提供一個混膠的介面,但 是此種技術需要事先知道混膠的種類,以便選擇適當適量 的相容催化劑,基本上,材料之受熱面積越大,熔融速率 越快,材料之斷鍵塑化與裂解燒焦實屬競爭反應,觀察機 台扭力實為卸料之關鍵。 中華明國專利公告第1 9 0 4 2 7號從聚合泡體萃取 及回收發泡劑之方法及裝置,雖然可以回收發泡劑,但是 需要極為複雜的設備,而且所達到之效率極低。 中華明國專利公告第4 1 1 3 1 0號發泡塑膠的回收 與再生方法,其利用溶劑將發泡塑膠溶解,再回收溶劑循 環使用,然而此方法在回收過程中,所使用之化學溶劑, 亦會對於生態環境產生污染。 中華明國專利公告第2 9 4 0 0 0號混合廢料之發泡 鞋底構造,其將橡膠廢料回收後混入發泡塑膠,其實只是 將廢料混入發泡鞋,以補強該發泡鞋,並沒有為發泡塑膠 提供本質上回收之方法。 綜上,發泡塑膠之回收再利用上,存在著低價值利 用、污染、成本高等缺點,實在需要研究出一種高利用價 值、低污染、低成本之回收方法。 【發明内容】 本發明之主要目的,在於解決上述的問題而提供一種 適度控制裂解條件回收交聯發泡塑膠廢料之方法,包括: a :將待處理之材料投入粉碎機之步驟,俾以增加反應之1240728 V. Description of the invention (2) The surging and melting fracture (fracture), so traditionally used compatibilizers provide a mixed glue interface, but this technology requires the type of mixed glue to be known in advance in order to choose the appropriate With a proper amount of compatible catalyst, basically, the larger the heated area of the material, the faster the melting rate. The broken plasticization of the material and cracking and scorching are competitive reactions. Observing the torque of the machine is the key to discharging. Zhongming Mingguo Patent Bulletin No. 19 0 4 2 7 The method and device for extracting and recovering the foaming agent from the polymer foam, although the foaming agent can be recovered, requires extremely complicated equipment, and the efficiency achieved is extremely low. Zhongming Mingguo Patent Bulletin No. 4 1 1 3 1 0 Recovery and regeneration method of foamed plastic, which uses a solvent to dissolve the foamed plastic, and then recycles the solvent for recycling. However, the chemical solvent used in this method during the recovery process It will also cause pollution to the ecological environment. Zhongming Mingguo Patent Bulletin No. 2 94 0 0 0 The foamed sole structure of mixed waste material, which recycles the rubber waste material and mixes it into the foamed plastic. In fact, it only mixes the waste material into the foamed shoes to reinforce the foamed shoes. Provides essentially recycled methods for foamed plastic. In summary, the recycling and reuse of foamed plastics have the disadvantages of low value utilization, pollution, and high costs. It is really necessary to develop a recovery method with high utilization value, low pollution, and low cost. [Summary of the invention] The main purpose of the present invention is to solve the above problems and provide a method for recovering cross-linked foamed plastic waste by appropriately controlling the cracking conditions, including: a: the step of putting the material to be processed into a pulverizer, so as to increase Response

1240728 五、發明說明(3) 速率。 b :將步驟a所得之材料送入比重槽之步驟,俾以比重法 將待處理材料作區分,並藉不同之比重以選擇適當之 催化劑,以及作為設定機台融熔溫度之參考。 c :將步驟b所得之材料,送入回收機器之步驟,俾使材 料融溶塑化,且該回收機器必須同時具有壓縮、剪 切、融溶,並設有濾網,可以是押出機、滚桶機、捏 合機與萬馬力機其中之一。 d :投入催化劑之步驟,俾以控制回收加工時之裂解條 件; e :過網造粒之步驟,俾以將材料製成塑膠粒。 f :射、押出製作成品,俾將塑膠粒以射、押出而製程成 品。 本發明之方法係將回收料粉碎,以增加反應之速率, 並經過比重槽之區分,俾以選擇適當之催化劑,而融熔之 過程中,選擇了同時具有剪斷與壓縮之料缸,並利用外加 催化劑,而產生裂解條件,使發泡塑膠架橋之三度空間網 狀結構加以破壞,利用外力促進融溶介面之接觸,可以避 免裂解時所產生之燒焦現象,所以可以在不增加設備投資 下,以傳統塑膠加工之現有機台,只要控制上述之加工條 件,即可回收交聯發泡塑膠廢料,實符合高利用價值、低 污染、低成本之回收方法。 本發明中所指之之比重槽,係於一長型流動水槽之上 方,設置擋板,而可達到區分粉碎後之回收料之比重,其1240728 V. Description of the invention (3) Rate. b: The step of sending the material obtained in step a into the specific gravity tank, and using the specific gravity method to distinguish the materials to be processed, and using the different specific gravity to select an appropriate catalyst, and as a reference for setting the melting temperature of the machine. c: The material obtained in step b is sent to the recycling machine step to melt and plasticize the material, and the recycling machine must have compression, shearing and melting at the same time, and is equipped with a filter screen, which can be an extruder, One of the drum machine, kneader and ten thousand horsepower machine. d: the step of inputting the catalyst, to control the cracking conditions during recovery processing; e: the step of passing through the net to granulate, to make the material into plastic pellets. f: Shoot and extrude to make finished products. 俾 Plastic pellets are shot and extruded to make finished products. The method of the present invention is to pulverize the recycled material to increase the reaction rate, and to distinguish the specific gravity tank, to select an appropriate catalyst, and in the melting process, a cylinder with both shearing and compression is selected, and The use of external catalysts generates cracking conditions to destroy the three-dimensional spatial network structure of the foamed plastic bridge. External forces are used to promote the contact of the melting interface, which can avoid the scorching phenomenon generated during cracking, so it can be used without adding equipment. Under the investment, the existing machine using traditional plastic processing, as long as the above-mentioned processing conditions are controlled, can recover the cross-linked foamed plastic waste, which is in line with the high-utilization value, low pollution, and low cost recycling method. The specific gravity tank referred to in the present invention is located above a long flowing water tank and is provided with a baffle, so that the specific gravity of the crushed recycled material can be distinguished.

1240728 五、發明說明(4) 中比重大於1 P E T ,而比 餘之發泡產品 定機台融熔溫 本發明中 媒如過度金屬 時間等外加條 道,或材料本 ),並針對交 縮、剪斷與混 塑膠連續炼融 ,俾使機台所 本發明之 實施例之詳細 當然,本 所不同,但所 說明,並於附 【實施方式】 請參閱第 實施例之數據 數據之限制。 請參閱第 交聯發泡塑膠 a ·將待處理 者一般 重小於 可依燃 度之參 所指之 或過氧 件使材 身顏色 聯發泡 合,本 之介面 提供之 上述及 說明與 發明在 選用之 圖中展 為P V 1者, 燒性狀 考。 裂解條 化物等 料產生 已改變 廢料施 發明所 ,使混 剪切力 其他目 附圖中 某些另 實施例 示其構 件,係 ,或因 降解而 ,但在 與不同 指之催 膠之間 發揮功 的與優 ,獲得 件上, ,則於 造0 包含加 為高溫 塑化, 容許範 之外力 化劑, 加工軟 效之添 點,不 深入了 或另件 本說明 6 6與 S,其 利於設 外加觸 轉速、 燒灼味 深色料 產生壓 可提供 度減小 1圖至第6圖,圖中所示者為本發明所選用 ,此僅供說明之用,在專利申請上並不受此 1圖,本發明之一種適度控制裂解條件回收 廢料之方法,係包括以下之步驟: 之材料投入粉碎機之步驟,俾以增加反應之 C,ABS,PA6& 一般為PE ,PP與P 況簡單判別區分,而有 工過程中 、高壓、 甚而產生 圍者(如 ,使材料 係指一種 化溫度梯 加劑。 難從下述所選用 解。 之安排上容許有 書中,予以詳細1240728 V. Description of the invention (4) The specific gravity is greater than 1 PET, and the ratio of the foaming product is more than the melting temperature of the machine. In the present invention, the medium (such as excessive metal time, etc., plus a road or material), and for shrinking, The continuous smelting and melting of the cut and mixed plastics makes the details of the embodiment of the invention of the machine, of course, different from the one, but it is explained, and attached [Embodiment] Please refer to the data limitation of the embodiment. Please refer to the cross-linked foamed plastic a. · The weight of the person to be treated is generally less than the flammable reference or peroxy parts to make the color of the body foamed. The above and description and invention provided by this interface are in The selected picture shows PV 1 and the burning characteristics are examined. The production of cracked strips and other materials has been changed. The waste material is applied to the invention, so that the mixed shear force is shown in some other examples in the drawings. Its components, systems, or due to degradation, but play a role between the glue with different fingers. If you get the best, you can add plasticizers at high temperature, which can be used as high-temperature plasticizers, allow external force modifiers, and add softness to processing. They do not go deeper or separate the instructions 66 and S in this description. The contact speed and the burning pressure can reduce the degree of supply of dark materials. Figures 1 to 6 are shown in the figure for the purpose of the present invention. This is for illustrative purposes only and is not subject to this figure in patent applications. A method for recovering waste materials by appropriately controlling cracking conditions of the present invention includes the following steps: The step of putting materials into a pulverizer to increase the reaction C, ABS, PA6 & generally PE, PP and P are simply distinguished from each other In the process of employment, high pressure, and even siege (such as making the material refers to a temperature ladder additive. It is difficult to understand from the following choices. The arrangement allows detailed information in the book.

1240728 五、發明說明(5) 速率,其中,待處理之材料係為具有電子架橋、物理 與化學及其中一種交聯發泡之塑膠回收料。 b :將步驟a所得之材料送入比重槽之步驟,俾以比重法 將待處理材料作區分,並藉不同之比重以選擇適當之 催化劑。 c :將步驟b所得之材料,送入回收機器之步驟,俾使材 料融溶塑化,且該回收機器必須同時具有壓縮、剪 切、融溶,並設有濾網,可以是押出機、滾桶機、捏 合機與萬馬力機其中之一。 d :投入催化劑之步驟,俾以控制回收加工時之裂解條 件。 e :過網造粒之步驟,俾以將材料製成塑膠粒。 f :射、押出製作成品,俾將塑膠粒以射、押出而製程成 品。 本發明人係以下列之實驗步驟及其所得之結果,經過 不斷的研究,而巧妙地依據其步驟與結果,運用於於交聯 發泡塑膠回收: 1 ·將回收之E V A交聯發泡廢料,經液態氮急速冷卻 後,並以球磨粉碎機粉碎並過篩,收取2 0 0毫米之 不規則之粉碎料,各外加0 · 0 1 g至0 · 1 g之催 化劑,於本實施例中,該催化劑係包含有過氧化物、 起始觸媒及利於接枝官能基之常用酸酐或偶合劑,主 要是為了增加裂解的條件與環境,並提供材料介面相 容的機會,且該液態催化劑之製作過程如下:取適當1240728 V. Description of the invention (5) Rate, in which the material to be processed is a plastic recycling material with electronic bridging, physical and chemical and one of the cross-linked foaming materials. b: The step of sending the material obtained in step a into the specific gravity tank, and using the specific gravity method to distinguish the materials to be treated, and using different specific gravity to select an appropriate catalyst. c: The material obtained in step b is sent to the recycling machine step to melt and plasticize the material, and the recycling machine must have compression, shearing and melting at the same time, and is equipped with a filter screen, which can be an extruder, One of the drum machine, kneader and ten thousand horsepower machine. d: The step of putting in the catalyst to control the cracking conditions during recovery and processing. e: The step of granulating through a net, to make the material into plastic granules. f: Shoot and extrude to make finished products. 俾 Plastic pellets are shot and extruded to make finished products. The inventors have used the following experimental steps and the results obtained through continuous research, and cleverly applied them to the recovery of cross-linked foamed plastics based on their steps and results: 1 · Recycled EVA cross-linked foamed waste After being rapidly cooled by liquid nitrogen, it is pulverized by a ball mill and sieved to collect an irregular crushed material of 200 mm, each of which is additionally added with a catalyst of 0. 0 1 g to 0. 1 g. In this embodiment, The catalyst system contains peroxides, starting catalysts and commonly used anhydrides or coupling agents that are useful for grafting functional groups, mainly to increase the conditions of cracking and the environment, and to provide opportunities for material interface compatibility, and the liquid catalyst The production process is as follows:

1240728 五、發明說明(6) 比例之過氧化物及混酸溶液以丙酮稀釋,外加丙酮之 功用在於穩定、稀釋與放大催化劑及材料接觸之面 積,本實施例中之催化劑為D C P ,而上述之混酸溶 液為1 : 4之M A H : A A,並經由熱重損失分析儀 (T G A )讀取不同添加劑後,回收裂解1 〇 %及5 0%之溫差,作為回收裂解溫度之參考,並觀察其無 外力(壓縮、剪斷)作用下之受熱融溶變化曲線,而 其參數及測試結果如第4圖所示,其中,以0 · 0 3 g之催化劑添加量,可得到最佳之融溶曲線。 2 ·以上一步驟所得之最適添加量(每2 0 0毫米之不規 則之粉碎料加入0 · 〇 3 g之催化劑),並製作不同 粒徑之粉碎粒’並經由熱重損失分析儀(T G A )加 以測試,得到當無外加壓力下,不同外徑之粉碎粒受 液態觸媒催化之融溶速率差異圖(如第5圖所示), 作為回收裂解溫度之參考,由其結果得知,除了最小 粒徑有明顯之差異外,其餘對於此添加量之液態催化 劑,並無明顯變化,亦即,在無外加壓力下粒徑與促 進裂解之催化劑添加量有密切關係,其中最小粒徑之 粉碎料可得到最佳之融溶曲線。 3 ·以步驟1之方法,研磨E V A化學交聯發泡海灘鞋之 回收材料,經過融溶指數測試儀,改變不同荷重下 (2-16Kg、5.1Kg與9.9Kg),溫度 設定2 5 0°C及3 0 0°C受熱3 0分鐘,並觀察其受 外力(壓縮但無剪斷)作用下之受熱融溶指數之變1240728 V. Description of the invention (6) The proportion of peroxide and mixed acid solution is diluted with acetone. The function of acetone is to stabilize and dilute the area in contact with the enlarged catalyst and materials. The catalyst in this example is DCP, and the above mixed acid The solution was 1: 4 MAH: AA, and after reading the different additives via a thermogravimetric loss analyzer (TGA), the temperature difference between 10% and 50% of the cracking was recovered as a reference for recovering the cracking temperature, and observed that there was no external force (Compression, shearing) under the melting curve of heat, and its parameters and test results are shown in Figure 4, where the best amount of melting curve can be obtained with a catalyst addition amount of 0.30 g. 2 · The optimal addition amount obtained in the previous step (adding 0.03 g of catalyst to every 200 millimeters of irregular crushed material), and produce crushed particles of different particle diameters, and pass the thermogravimetric loss analyzer (TGA ) Test to obtain the difference in melting rate of pulverized granules with different outer diameters catalyzed by liquid catalyst when no external pressure is applied (as shown in Figure 5). As a reference for recycling cracking temperature, from the results, Except for the obvious difference in the minimum particle size, there is no significant change in the amount of liquid catalyst added, that is, the particle size is closely related to the amount of catalyst that promotes cracking under no external pressure. The crushed material can get the best melting curve. 3. According to the method of step 1, grind the recycled material of EVA chemical cross-linked foamed beach shoes, and pass the melt index tester to change the load under different loads (2-16Kg, 5.1Kg and 9.9Kg), and set the temperature to 250 ° C and 300 ° C for 30 minutes, and observe the change of the heat-melt index under the action of external force (compressed but not sheared)

1240728 五、發明說明(7) 化,結果發現交聯後之發泡體雖然如預期有極高之耐 熱強度,但是回收料在高壓及受熱下,外觀已有融溶 之現象產生(如第2圖所示)◦ 4 ·將回收之E V A化學交聯發泡海灘鞋之回收材料剪切 成各約1立方公分之塊狀(如第6圖所示),並取 1 · 5g ,再分別加入0 · Olg至0 · lg之液態 觸媒,以交聯發泡儀測試並觀察其受外力(壓縮但無 剪斷)作用下之内塑壓力(如第3圖所示),並記錄 融溶外觀之結果,本實施例中以〇 · 〇 5 g添加量得 到較低的内塑壓力,而且融溶介面之外觀並無變化, 如果液態觸媒之添加量超過0 · 〇 5 g ,雖然内塑壓 力會減小,但融溶介面之外觀會變黃甚至變黑,相對 的,如果液態觸媒之添加量不到〇 · 〇 5 g ,雖然融 溶介面之外觀不會有變化,但是内塑壓力卻會增大。 5 ·將粉碎回收之P P果汁瓶及E V A化學交聯發泡海難 鞋之回收材料,以1 : 9的比例,及加入適量之添加 劑,投入回收機器中,本實施例中係使用萬馬力機, 其溫度設定為2 5 0°C,轉速設定為5 0 r pm,壓 力設定為5 0 kg / cm 2 ,測試並觀察其受外力(壓縮 且倶剪斷)作用下,受熱融溶之變化情形。 6 ·將粉碎回收之的1 0 0 % E V A化學交聯發泡海灘鞋 之回收材料及適當之添加劑,投入溫度設定為2 5〇 °C ,轉速設定為5〇r p m,壓力設定為5〇kg / cm 2之萬馬力機,測試並觀察其受外力(壓縮且倶剪斷1240728 V. Description of the invention (7) The results show that although the crosslinked foamed body has extremely high heat resistance as expected, the appearance of the recycled material under high pressure and heat has been melted (such as the second (Shown in the figure) ◦ 4 · Cut the recycled EVA chemically cross-linked foamed beach shoes into a piece of about 1 cubic centimeter each (as shown in Figure 6), take 1 · 5g, and add them separately Liquid catalyst from 0 · Olg to 0 · lg, tested with a crosslinked foaming instrument and observed its internal plastic pressure under external force (compressed but not sheared) (as shown in Figure 3), and recorded the melt As a result of the appearance, in this example, a low internal plastic pressure is obtained with an addition amount of 0.05 g, and the appearance of the melt interface does not change. If the addition amount of the liquid catalyst exceeds 0, 0.05 g, The plastic pressure will decrease, but the appearance of the melt interface will turn yellow or even black. In contrast, if the amount of liquid catalyst is less than 0.5 g, although the appearance of the melt interface will not change, Plastic pressure will increase. 5 · The crushed and recovered PP juice bottles and EVA chemical cross-linked foamed shipwreck shoes are recycled materials at a ratio of 1: 9 and added with appropriate additives into the recycling machine. In this embodiment, a ten-horsepower machine is used. The temperature is set to 250 ° C, the rotation speed is set to 50 r pm, and the pressure is set to 50 kg / cm 2. Test and observe the change of heat and melt under external force (compressed and sheared). . 6 · The crushed and recycled 100% EVA chemically cross-linked foamed beach shoes are recycled materials and appropriate additives. The input temperature is set to 250 ° C, the speed is set to 50rpm, and the pressure is set to 50kg. / cm 2 10,000 horsepower machine, test and observe its external force (compressed and sheared)

第10頁 1240728 五、發明說明 )作 7 ·將實 準試 2圖 其中 之回收材 拉強度以 請參 用於1 0 漱口杯, 入粉碎機 5 0 °C, 2之萬馬 粒,並使 綜上 發泡塑膠 速率,並 劑,以及 發泡塑膠 連續熔融 機台所提 之接觸, 而將交聯 低污染、 (8) 用下, 施例5 片,測 所示。 ,回收 料,經 及耐衝 閱第1 0 % E 其係將 粉碎, 轉速設 力機並 用射出 所述, 廢料之 利用比 機台融 架橋之 的介面 供之剪 以避免 發泡塑 低成本 之的1〇 過上述方 擊強度。 〇圖,其 V A交聯 回收之1 並經過比 定為5 0 加入適當 成型機製 由於本發 方法,先 重槽將回 '溶溫度之 三度空間 ,使混膠 切力發揮 裂解之連 膠廢料回 等多重效 受熱融溶之變化情形(如第8圖所示)。 與6所製得之顆粒,以射出成型機製作標 試其抗拉強度與耐衝擊性,所得結果如第 〇% E V A化學交聯發泡海灘鞋 法而裂解後,仍然具有良好之抗 係為依據本發明之步驟,實際運 發泡海灘鞋廢料之回收所製成之 〇0 % E V A交聯發泡鞋廢料投 重槽之區分,投入溫度設定為2 r p m,壓力設定為5 0 kg / cm 之比例之添加劑,以製得塑膠顆 作成漱口杯。 明之適度控制裂解條件回收交聯 將回收料粉碎,俾以增加反應之 收料區分,俾以選擇適當之催化 參考,藉以產生裂解條件,而將 網狀結構加以破壞,並提供一個 之加工軟化溫度梯度減小,俾使 功效,且利用外力促進融溶介面 鎖反應時催化劑造成材料燒焦, 收使用,俾以達到高利用價值、 果。Page 10 1240728 V. Description of the invention) Work 7 • Use the tensile strength of the recovered material in the actual test 2 as shown in the figure for 10 mouthwash cups, enter the grinder at 50 ° C, and 2 million horsepower, and In summary, the speed of foamed plastics, the blending agent, and the continuous melting of the foamed plastics machine were brought into contact, and the cross-linked low pollution, (8) was used, Example 5 tablets, as shown. Recycling material, after the first 10% of the impact resistance, it is crushed, set the speed of the force machine and use the injection, the use of waste materials than the machine melt bridge bridge interface to avoid the low cost of foam plastic The strength of 10 is above the above-mentioned strike. 〇, the VA cross-linked recovery of 1 and the ratio is set to 50. Add the appropriate molding mechanism. Due to the method of the present invention, the first heavy tank will return to the three-degree space of the melting temperature, so that the mixed rubber cutting force will play a role in cracking the connected rubber waste. The change of multiple effects of heat and melting (see Figure 8). The pellets prepared with 6 were tested by injection molding machine for tensile strength and impact resistance. The obtained results are as follows: 0% EVA chemically cross-linked foamed beach shoes and cracked, and still have good resistance. According to the steps of the present invention, the OO% EVA cross-linked foamed shoe waste made from the actual weight of the trough is distinguished from the weight trough made by recycling the foamed beach shoe waste. The input temperature is set at 2 rpm and the pressure is set at 50 kg / cm. The ratio of the additive is to make a plastic cup into a mouthwash cup. Mingzhi moderately controls the cracking conditions. Recycling and cross-linking will crush the recycled materials, to increase the separation of the reaction materials, and to choose an appropriate catalytic reference to generate cracking conditions to destroy the network structure and provide a processing softening temperature. The gradient is reduced, and the effect is reduced, and the material is burnt by the catalyst when the external interface is used to promote the melt interface lock reaction, and the material is used, so as to achieve high utilization value and fruit.

1240728 五、發明說明(9) 以上所述實施例之揭示係用以說明本創作,並非用以 限制本創作,故舉凡數值之變更或等效元件之置換仍應隸 屬本創作之範疇。 由以上詳細說明,可使熟知本項技藝者明瞭本創作的 確可達成前述目的,實已符合專利法之規定,爰提出專利 申請。 _1240728 V. Description of the invention (9) The disclosure of the above embodiment is used to explain the creation, not to limit the creation. Therefore, any numerical change or replacement of equivalent components should still belong to the scope of the creation. From the above detailed description, those skilled in the art can understand that this creation can indeed achieve the aforementioned purpose, and it has indeed complied with the provisions of the Patent Law, and filed a patent application. _

第12頁 1240728 圖式簡單說明 第1圖係本發明之方法的流程圖。 第2圖係本發明之物性圖之一。 第3圖係本發明之物性圖之二。 第4圖係本發明之受熱融熔變化曲線圖之一。 第5圖係本發明之受熱融熔變化曲線圖之二。 第6圖係本發明之回收海灘鞋經外力粉碎增大面積參考 圖。 第7圖係本發明之經壓縮但無剪斷之裂解融熔狀之參考 圖。 第8圖係本發明之經壓縮且剪斷之造粒之參考圖。 第9圖係本發明之融熔指數儀中塑化無流動外觀參考圖。 第1 0圖係本發明經射出成型所製作之漱口杯參考圖。Page 12 1240728 Brief Description of Drawings Figure 1 is a flowchart of the method of the present invention. Fig. 2 is one of the physical property diagrams of the present invention. Fig. 3 is the second physical property map of the present invention. Fig. 4 is one of the thermal melting curve of the present invention. Fig. 5 is the second graph of the melting and melting curve of the present invention. Fig. 6 is a reference view of the recovered beach shoes of the present invention pulverized by external force to increase the area. Fig. 7 is a reference drawing of the cracked and melted state of the present invention which is compressed but not sheared. Figure 8 is a reference drawing of the compressed and sheared granulation of the present invention. FIG. 9 is a reference view of the plasticized non-flowing appearance in the melt index meter of the present invention. Fig. 10 is a reference view of a mouthwash cup made by injection molding according to the present invention.

第13頁Page 13

Claims (1)

1240728 六、申請專利範圍 1 · 一種適度控制裂解條件回收交聯發泡塑膠廢料之方法 ,該方法包括以下之步驟: a :將待處理之材料投入粉碎機之步驟,俾將待處理 之材料粉碎,增加表面積,以增加反應之速率, 其中,待處理之材料係為具有電子架橋、物理架 橋與化學架橋其中一種交聯發泡之塑膠回收料; b :將步驟a所得之材料送入比重槽之步驟,俾以比 重法將待處理材料作區分,以選擇適當之催化劑 c :將步驟b所得之材料,送入回收機器,俾將材料 融溶塑化; d :投入催化劑,以控制回收加工時之裂解條件; e :過網造粒; f :射、押出製作成品。 2 ·依申請專利範圍第1項所述之一種適度控制裂解條件 回收交聯發泡塑膠廢料之方法,其中,該步驟a所稱 待處理之材料,為回收料及具有回收料與新料之混合 料,俾以促進回收料之流動、粘合、融溶及改質。 3 ·依申請專利範圍第1項所述之一種適度控制裂解條件 回收交聯發泡塑膠廢料之方法,其中,該步驟d所稱 之裂解條件,係為加入催化劑、過渡金屬或過氧化物 等添加劑,及因為高溫、高壓、轉速與時程等外加條 件使材料產生降解而塑化,並施以外力,使材料產生 壓縮、剪斷及混合。1240728 VI. Scope of patent application 1 · A method for recovering cross-linked foamed plastic waste with moderately controlled cracking conditions, the method includes the following steps: a: the step of putting the material to be processed into a pulverizer, and pulverizing the material to be processed Increase the surface area to increase the reaction rate. Among them, the material to be treated is a cross-linked foamed plastic recycled material with electronic bridge, physical bridge and chemical bridge; b: send the material obtained in step a into the specific gravity tank In step 俾, the material to be processed is differentiated by specific gravity method to select an appropriate catalyst c: The material obtained in step b is sent to a recycling machine, and the material is melt-melted and plasticized; d: The catalyst is put in to control the recycling process The cracking conditions at the time; e: granulation through the net; f: shooting, extrusion to make the finished product. 2 · A method for recovering cross-linked foamed plastic waste material according to a moderately controlled cracking condition as described in item 1 of the scope of the patent application, wherein the material to be treated referred to in step a is a recycled material and a mixture of recycled material and new material Materials to promote the flow, adhesion, melting and modification of recycled materials. 3. A method for recovering cross-linked foamed plastic waste material according to a moderately controlled cracking condition described in item 1 of the scope of the patent application, wherein the cracking condition referred to in step d is the addition of a catalyst, transition metal or peroxide, etc. Additives, and plasticization due to external conditions such as high temperature, high pressure, rotation speed and time history, etc., and exert external forces to compress, shear and mix materials. 第14頁 1240728 六、申請專利範圍 4 ·依申請專利範圍第1項所述之一種適度控制裂解條件 回收交聯發泡塑膠廢料之方法,其中,該步驟c所稱 之回收機器,必須同時具有壓縮、剪切、混合、融溶 及加熱單元並設有濾網,而可以是押出機、滾桶機、 捏合機與萬馬力機其中之一者。 5 ·依申請專利範圍第1項所述之一種適度控制裂解條件Page 14 1240728 6. Scope of patent application 4 · A method for recovering cross-linked foamed plastic waste material under a moderately controlled cracking condition as described in item 1 of the scope of patent application, wherein the recycling machine referred to in step c must also have The compressing, shearing, mixing, melting and heating unit is provided with a filter screen, and may be one of an extruder, a barrel machine, a kneader and a ten thousand horsepower machine. 5 · A moderately controlled cracking condition as described in item 1 of the scope of patent application 回收交聯發泡塑膠廢料之方法,其中,該催化劑係包 括過渡金屬、過氧化物、起始觸媒、及利於接枝官能 基之常用酸酐或偶合劑與其中之一種與其混合物,俾 以增加裂解條件,以提供材料連續融熔之介面。 6 ·如申請專利範圍第5項所示,其中該催化劑為D C P 與混酸溶液之混合液體,其中該混酸溶液為1 : 4之 M A H : A A 。A method for recovering cross-linked foamed plastic waste, wherein the catalyst includes transition metals, peroxides, starting catalysts, and commonly used acid anhydrides or coupling agents for grafting functional groups, and one of them and a mixture thereof to increase Cracking conditions to provide an interface for continuous melting of the material. 6. As shown in item 5 of the scope of patent application, wherein the catalyst is a mixed liquid of D C P and a mixed acid solution, wherein the mixed acid solution is M A H: A A of 1: 4. 第15頁Page 15
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