TW379169B - Method of making compound resin foaming agents - Google Patents
Method of making compound resin foaming agents Download PDFInfo
- Publication number
- TW379169B TW379169B TW85115941A TW85115941A TW379169B TW 379169 B TW379169 B TW 379169B TW 85115941 A TW85115941 A TW 85115941A TW 85115941 A TW85115941 A TW 85115941A TW 379169 B TW379169 B TW 379169B
- Authority
- TW
- Taiwan
- Prior art keywords
- resin
- plant
- water
- residue
- foam
- Prior art date
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
A7 _____ B7________ 五、發明説明(丨) 〔發明之技術領域〕 (請先閩讀背面之注意事項再填寫本頁) 本發明係有關用於汽車零件,電器零件,食品用容器 ’捆包用緩衝材,建築用資材,農業用資材等各種領域之 複合樹脂發泡體(以下稱複合發泡體)的製造方法。更詳 細係有關能取代熱塑性樹脂發泡體(以下稱爲樹脂發泡體 )的複合發泡體,即具有以熱塑性樹脂(以下稱爲樹脂) 及食品加工所產生之植物殘渣爲主成分之發泡結構之複合 發泡體的製造方法。 〔發明的背景〕 食品加工業使用榖類,豆類,種子類等大量加工成豆 腐’油等各種食品,且大量產生這些食品所不要的成分, 豆腐渣,大豆渣等的植物殘渣。 這些植物殘渣一部分可作爲食品,飼料,肥料等,但 大部分被廢棄。又因植物殘渣量多使廢棄處理困難。因此 希望植物殘渣被有效地作爲資源使用。 經濟部中央標準局員工消費合作社印製。 普偏被用於汽車零件,電氣零件,食品用容器,捆包 用緩衝材,建築用材料,農業用材料等之各種領域的樹脂 發泡體經使用後大部分被埋入土中或焚燒處理。但埋入土 中時,因無生物分解性而仍保留原有狀態,使得掩埋處理 困難。焚燒處理時會產生黑煙,或產生有害氣體污染,破 壞自然環境,因此焚燒處理也有困難。因此,要求能夠容 易廢棄處理的樹脂發泡體。 此樹脂發泡體之製造時使用加熱分解產生氮氣或二氧 本多氏張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(2 ) _ ~ 化碳氣體之加熱分解型發泡劑(通稱化學發泡劑),氟隆 —1 1 ,氟隆一1 2,氟隆一1 14等的氟隆系發泡劑, 及由丙烷,丁烷,戊烷等低沸點液體或液化氣體所構成之 石油系發泡劑等的發泡劑。但發泡劑昂貴,或使用時必須 特別小心等使得無法以安全,廉價製造樹脂發泡體。因此 提案使用廉價且使用上較安全的水作爲發泡劑(例如參照 特開昭5 9 — 1 7 2 5 3 1號公報,特開昭5 9 — 213738號公報等)。例如,特開昭59_ 1 7 2 5 3 1號公報所揭示之樹脂發泡體的製造方法係以 樹脂以熔融溫度攪拌混合粉粒狀之樹脂與澱粉,麵粉等榖 物粉,然後將熔融之樹脂與榖物粉的混合物予以冷卻,粗 粉碎後再粉碎成多孔性聚集塊,以水性媒介物處理此多孔 性聚集塊’.再於加壓熔融混練後釋放壓力形成具有獨立氣 泡結構的發泡體。但因用榖物原料使得價格昂貴。形成多 孔性聚集塊的步驟複雜。多孔性聚集塊其表面係以榖物粉 披覆之樹脂粉粒體經部分熔合所成者,以水性媒介物處理 時水分雖附著於澱粉及樹脂粉粒體間的孔上,但通常很難 維持在相當於高發泡之水量以上,很難提高至比一般更高 的發泡倍率。因有這些問題而仍無法實際使用。 〔發明欲解決的問題〕 經種種檢討結果得知可以植物殘渣作爲樹脂發泡體的 原枓,能得到具有獨立氣泡結構,且廢棄處理容易之樹脂 發泡體。即,植物殘渣爲有機質,容易與樹脂混合。植物 本紙張尺度適用中國國家標率(CNS ) A4規格(210X297公釐) (諳先閔讀背面之注意事項再填寫本頁) <π A7 B7 五、發明説明(3 ) 殘渣本來就含有水分,與樹脂攪拌混合及熔融混練能將水 分均勻微分散於熔融之樹脂中。而且,容易調整植物殘渣 的水量,因植物殘渣爲吸水性,容易補充水分,且取得容 易等。將含水之植物殘渣與粉粒狀樹脂攪拌混合,以成形 機加熱熔融混練成形時可得到連續氣泡較少,獨立氣泡幾 乎成均勻分佈的發泡體。藉由調整植物殘渣的含水率,樹 脂與植物殘渣的混合比例等可容易改變發泡倍率,同時也 容易改變剛性,緩衝性等之機械持性》製得之發泡體爲以 樹脂及植物殘渣爲主成分的複合發泡體,且有與以往之樹 脂發泡體類似的機械特性,也可作爲替代品使用。而且具 有生物分解性,發熱量低,黑煙或有害氣體較少,廢棄處 理容易》 本發明係檢討上述的結果而完成者,其問題係有效地 利用植物殘渣提供一種安全,廉價且簡單製造具有以樹脂 與植物殘渣爲主成分之發泡結構之複合發泡體的方法。 〔解決問題的手段〕 經濟部中央標準局員工消費合作社印製 (諳先閣讀背面之注意事項再填寫本頁) 爲了解決上述問題,本發明係攪拌混合物粒狀樹脂及 食品加工所產生之粉粒且含水分之植物殘渣,且加熱熔融 混練,使得介於植物殘渣將水微分散於熔融的樹脂中。藉 此,防止發泡成形時產生連續氣泡,形成具有許多獨立氣 泡之發泡結構之複合發泡體。 即,本發明之複合發泡體的製造方法係將以粉粒狀樹 脂與食品加工所產生之粉粒狀且含水之植物殘渣爲主成分 本紙張尺度適用中國國家標準(CNS ) A4规格(210X297公釐) _ 6 - A7 B7 五、發明説明(4 ) 的原料在比樹脂軟化溫度更低的低溫區域攪拌混合,此原 料在壓力下加熱熔融混練後,降低壓下予以發泡成形。將 原料在比樹脂軟化溫度更低的低溫區域攪拌混合,使植物 殘渣成微粒子狀均勻分散於樹脂中,再經加熱熔融混練而 形成更微細的微粒子狀均勻分散於熔融的樹脂中》因此, 植物殘渣所載持的水分被微分散於熔融的樹脂中。植物殘 渣局部凝集時該部分不會形成樹脂膜,而且,植物殘渣的 水分聚集產生極大的蒸氣壓,破壞周圍的樹脂膜形成連續 氣泡,因此,充分地攪拌混合及混練避免植物殘渣局部凝 集較理想。 植物殘渣原來含有許多水分,使用乾燥後調整水分表 較理想。設定高發泡倍率時,攪拌混合後及/或加熱熔融 時添加水使含水量增加。即,乾燥後之植物殘渣具有吸水 性,吸收被添加的水。藉此,添加的水也被微分散至熔融 的樹脂中,抑制產生連續氣泡,可提高發泡倍率。 〔發明之實施形態〕 經濟部中央標準局員工消費合作社印製 (讀先聞讀背面之注意事項再填寫本頁) 以下說明本發明之實施形態。製造複合發泡體時,首 先以所定的比例配合粉粒狀樹脂及食品加工所產生之粉粒 狀且含水分的植物殘渣,調製原料。將此原料以公知的混 合機,且在比樹脂軟化溫度更低的低溫領域充分攪拌混合 ,使植物殘渣均勻地分散在樹脂中。接著將攪拌混合後的 原料供給擠壓機,射出成形機等公知的成形機內,加壓下 加熱熔融充分混練,使植物殘渣均匀地分散在熔融樹脂中 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -7 - 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(5 ) 。然後將熔融的混合物藉由塑模成形模等形成所定形狀 ,同時使之發泡。 使用的樹脂種類可使用以往用於塑膠成形者。例如有 高密度聚乙烯’低密度聚乙烯,聚丙烯,聚丁烯,乙烯韓 酸乙烯酯共聚物’乙烯-丙烯共聚物,石油樹脂等之烯烴 系樹脂(聚烯烴系樹脂),聚丁二烯,聚異戊二烯等之二 烯系樹脂,聚氯化乙烯’聚醋酸乙烯,聚氯化偏氯乙烯, 聚乙烯醇等的乙烯系樹脂,聚甲基丙烯酸甲酯等的丙烯酸 系樹脂’聚苯乙烯,丙烯一苯乙烯共聚物,丙烯一 丁二烯 -苯乙烯共聚物等的苯乙烯系樹脂,尼龍一6,尼龍 —6 6,尼龍一 1 2等聚醯胺系樹脂,聚對於酞酸乙二醇 酯等的聚酯系樹脂等。特別是生物分解性樹脂例如使用聚 丙酸己內酯(商品名「Plaksel」等,聚一 2 — D比咯氧基 丙酸(商品名「Lacty」等)等的化學合成系樹脂及Nobon (商品名)等之天然高分子系樹脂等時,埋入土中在短時 間內分解消失,故使用後之廢棄處性容易。樹脂的形態只 要是粉粒狀即可,粉末較理想,也可爲顆粒狀。又,樹脂 可組合2種以上使用。 植物殘渣只要是食品加工所產生之粉粒狀且含水分者 即可’不論種類,但以使用榖類,豆類,種子類等進行食 品加工時所產生之粉碎成粉粒狀者較理想。例如小麥精製 時所產生的麥糠,植物莖粉,豆腐製造時所產生的豆腐渣 ’豆腐渣已去除脂肪成分之脫脂豆腐渣,咖啡渣,米精製 時所產生的米糠,米糠脫脂之脫脂米糠,啤酒製造時所產 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 一 8 - —· J---;---' J裝— . ,,ίκ (祷先聞讀貲面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印製 A7 __B7 _ 五、發明説明(6 ) 生的啤酒釀,榨油之大豆渣,胡麻.渣或玉蜀黍渣,榨糖之 糖渣,醬油渣等。脫脂豆腐渣,大豆渣等使用大豆的植物 殘渣統稱爲大豆殼。這些的植物殘渣係以加工步驟粉碎成 粉粒狀,故可直接使用,但爲配合發泡的程度,混合之樹 脂的種類,複合發泡體所要求的物性等可以粉碎機再行粉 碎後使用。又可組合使用2種以上的植物殘渣。 植物殘渣的功能係因含有水分而具有作爲水分載持體 的功能,使水分微分散於熔融的樹脂中,因其主成分之脂 肪分,蛋白質,纖維質,粗灰分等達到以下各功能。脂肪 分係具有提高成形時之成形性,提高樹脂之滲入,同時提 高樹脂殘渣對於樹脂的分散性等的功能,植物殘渣的含量 以0_ 2〜20重量%較理想,2〜6重量%更理想。超 過2 0重量%時易分離或污染成形模蛋白質具提高熱熔融 後與樹脂的結合力,同時具有植物殘渣對樹脂的混合比的 功能,植物殘渣含量以5〜4 0重量%較理想,更理想爲 1 2〜30重量%。纖維質具纏繞熔融的樹脂具有彌補複 合發泡體的脆性,提高強度的功能,植物殘渣之理想含量 爲3重量%以上’更理想爲5重量%以上。粗更分具有增 量劑的功能,植物殘渣之理想含量爲2 0重量%以下,更 理想爲1 5重量%以下。粗灰分係有機質,使用複合發泡 體後進行焚燒處理時大部分被燃燒,只有少量的殘留物( 殘餘灰分)。 植物殘渣原本含有多量水分,例如榖殼含水8 0 %左 右。因此’保管時,攪拌混合時等使用上應將植物殘渣乾 本&張尺度適财國國家標準(CNS )八4胁(210X297公釐.) ^ -9 - nn —Μ I ; I I n I n ^ 、-J (請先E讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 A7 __—__B7_ ._ 五、發明説明(7 ) 燥調整成含水1 5〜7 5重量%。對原料整體的水量係依 發泡的程度,混合之樹脂的種類,及複合發泡體所要求的 物性等來設定,一般提高發泡倍率時增加水量,而降低發 泡倍率時減少水量。對原料整體的水量基本上係依據植物 殘渣的配合比例,提高植物殘渣的配合比例時水量增加, 反之減少。若植物殘渣之配合比例一定時配合設定之發泡 倍率調整植物殘渣的水分或添加水分。特別是提高發泡倍 率時,攪拌混合樹脂及植物殘渣後及/或加熱熔融時添加 適量的水較理想。 樹脂與植物殘渣的配合比例係依發泡的程度,混合樹 脂的種類,及複合發泡體所要求的物性等來設定,但一般 提高發泡倍率時則增加植物殘渣的比例,反之則減少植物 殘渣的比例。因植物殘渣的含水率而不同,但一般樹脂 1 0 0重量份時植物殘渣爲4 0〜4 0 0重量份(對全量 之比例爲2 8 . 5〜8 0 · 0重量?6 ),理想爲6 〇〜 200重量份(37. 5〜6 6. 7重量%),更理想爲 100〜150重量份(50. 0〜60. 0重量%)。 樹脂與植物殘渣的攪拌混合係使用公知的混合機,混 合機可用Henschel混合機(三井三池製作所製),A7 _____ B7________ V. Description of the Invention (丨) [Technical Field of Invention] (Please read the notes on the back before filling out this page) The present invention relates to buffers used for packaging of automotive parts, electrical parts, and food containers. Manufacturing methods of composite resin foams (hereinafter referred to as composite foams) in various fields such as wood, construction materials, and agricultural materials. In more detail, it is a composite foam that can replace a thermoplastic resin foam (hereinafter referred to as a resin foam), that is, a composition containing a thermoplastic resin (hereinafter referred to as a resin) and plant residues generated from food processing as a main component. Manufacturing method of composite foam with foam structure. [Background of the Invention] The food processing industry uses a large number of processed foods such as coriander, beans, seeds and the like to produce various kinds of food such as tofu 'oil, and produces a large amount of unwanted components of these foods, such as plant residues such as tofu residue and soybean residue. Some of these plant residues can be used as food, feed, fertilizer, etc., but most of them are discarded. In addition, due to the large amount of plant residues, disposal is difficult. It is therefore expected that plant residues will be effectively used as resources. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. Commonly used in automotive parts, electrical parts, food containers, packaging buffers, building materials, agricultural materials, and other resin foams. After use, most of them are buried in the ground or incinerated. However, when buried in the soil, it remains in its original state because it is non-biodegradable, making it difficult to bury it. During the incineration process, black smoke or harmful gas pollution will be generated, and the natural environment will be damaged. Therefore, the incineration process is also difficult. Therefore, a resin foam capable of being easily discarded is required. This resin foam is produced by thermal decomposition to produce nitrogen or dioxo. This scale is applicable to China National Standard (CNS) A4 (210X297 mm). Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. A7 B7. V. Invention Explanation (2) _ ~ Thermal decomposition type foaming agent of carbonized gas (commonly known as chemical foaming agent), Fluon-1 1, Fluon-12, Fluon-1 14, etc. Foaming agents such as propane, butane, pentane and other petroleum-based foaming agents composed of low boiling point liquids or liquefied gases. However, the foaming agent is expensive, or special care must be taken during use, which makes it impossible to manufacture the resin foam safely and inexpensively. Therefore, it is proposed to use cheap and relatively safe water as a foaming agent (for example, refer to Japanese Patent Application Laid-Open No. 5 9 — 1 7 2 5 3 1 and Japanese Patent Application Laid-Open No. 5 9 — 213738). For example, the method for manufacturing a resin foam disclosed in JP-A-Sho 59_ 1 7 2 5 3 1 is to stir and mix powdery granular resin with starch, flour, and other powdered materials at the melting temperature of the resin, and then melt the The mixture of resin and powder is cooled, coarsely pulverized, and then pulverized into porous aggregates. The porous aggregates are treated with an aqueous medium. After the pressure is melted and kneaded, the pressure is released to form a foam with an independent bubble structure. body. However, it is expensive due to the use of raw materials. The steps to form a porous aggregate are complicated. Porous aggregates are formed by partially melting resin powder and granules covered with powder. When treated with an aqueous medium, although water adheres to the pores between starch and resin powder, it is usually difficult. It is difficult to increase the foaming ratio to a higher foaming ratio than the amount of water equivalent to high foaming. Due to these problems, it is still not practical to use. [Problems to be Solved by the Invention] As a result of various reviews, it was found that plant residues can be used as the raw material of resin foams, and resin foams having an independent cell structure and easy disposal can be obtained. That is, the plant residue is organic matter and is easily mixed with the resin. The paper size of the plant is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) (read the notes on the back of the book before filling in this page) < π A7 B7 V. Description of the invention (3) The residue originally contains moisture , Stirring and melting with resin can evenly and finely disperse moisture in the molten resin. In addition, it is easy to adjust the amount of water in the plant residues. Since the plant residues are water-absorptive, it is easy to replenish moisture, and it is easy to obtain. When the water-containing plant residues are mixed with the powdered and granular resins, they are heated and melted with a molding machine to form a foam with less continuous air bubbles and almost uniform air bubbles. By adjusting the moisture content of the plant residue, the mixing ratio of the resin and the plant residue, etc., it is easy to change the expansion ratio, and it is also easy to change the mechanical properties such as rigidity and cushioning. The foam produced is made of resin and plant residue. A composite foam with a main component and similar mechanical properties to conventional resin foams can also be used as a substitute. Moreover, it has biodegradability, low heat generation, less black smoke or harmful gas, and easy disposal. The present invention was completed by reviewing the above results. The problem is to effectively use plant residues to provide a safe, cheap and simple manufacturing method. A method for a composite foam having a foam structure with resin and plant residues as main components. [Means of Solving the Problem] Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (read the precautions on the back of the first cabinet and fill out this page) In order to solve the above problems, the present invention is a mixture of granular resin and powder produced by food processing The plant residues, which are granular and water-containing, are heated and melted to knead, so that the water is finely dispersed in the molten resin between the plant residues. Thereby, continuous bubbles are prevented from being generated during foam molding, and a composite foam having a foam structure with many independent bubbles is formed. That is, the manufacturing method of the composite foam of the present invention is mainly composed of powdery granular resin and powdery and water-containing plant residues produced by food processing. The paper size applies the Chinese National Standard (CNS) A4 specification (210X297). (Mm) _ 6-A7 B7 V. Description of the invention (4) The raw materials are stirred and mixed in a low temperature region lower than the softening temperature of the resin. This raw material is heated and melted and kneaded under pressure, and then foamed under reduced pressure. The raw materials are stirred and mixed in a low temperature region lower than the softening temperature of the resin, so that the plant residues are uniformly dispersed in the resin into fine particles, and then heated and melted to form finer particles uniformly dispersed in the molten resin. The water carried by the residue is finely dispersed in the molten resin. This part of the plant residue does not form a resin film when it is locally aggregated. In addition, the moisture accumulation of the plant residue generates a great vapor pressure, which destroys the surrounding resin film to form continuous bubbles. Therefore, it is ideal to fully stir and mix to avoid the local aggregation of plant residue. . Plant residues originally contained a lot of moisture, and it is ideal to adjust the moisture meter after use. When a high expansion ratio is set, water is added to increase water content after stirring and / or heating and melting. In other words, the dried plant residues are water-absorbing and absorb the added water. Thereby, the added water is also finely dispersed in the molten resin, and the occurrence of continuous bubbles is suppressed, and the expansion ratio can be increased. [Implementation Mode of the Invention] Printed by the Consumer Cooperatives of the Central Bureau of Standards of the Ministry of Economic Affairs (Read the notes on the back and then fill out this page) The following describes the embodiment of the invention. When manufacturing a composite foam, firstly mix the powdery granular resin and the powdery and moisture-containing plant residues produced by food processing at a predetermined ratio to prepare raw materials. This raw material is sufficiently stirred and mixed in a well-known mixer in a low temperature region lower than the softening temperature of the resin to uniformly disperse the plant residues in the resin. Next, the mixed raw materials are supplied to a known molding machine such as an extruder, injection molding machine, etc., and heated and melted under pressure to fully knead them so that the plant residues are uniformly dispersed in the molten resin. This paper applies Chinese national standards (CNS) A4 Specifications (210X297 mm) -7-Printed by the Consumers Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs A7 B7 V. Invention Description (5). Then, the molten mixture is formed into a predetermined shape by a mold forming mold or the like and foamed at the same time. The type of resin used can be conventionally used for plastic molding. For example, there are high-density polyethylene, low-density polyethylene, polypropylene, polybutene, ethylene vinyl acetate, ethylene-propylene copolymer, olefin resins (polyolefin resins) such as petroleum resins, and polybutadiene. Diene resins such as olefin, polyisoprene, vinyl resins such as polyvinyl chloride, polyvinyl acetate, polyvinylidene chloride, polyvinyl alcohol, and acrylic resins such as polymethyl methacrylate 'Styrenic resins such as polystyrene, propylene-styrene copolymer, propylene-butadiene-styrene copolymer, nylon-6, nylon-6, nylon-12, etc. For polyester resins such as ethylene phthalate. In particular, biodegradable resins include chemically synthesized resins such as polycaprolactone (trade name "Plaksel", etc., poly-2-D-pyroxypropionic acid (trade name, "Lacty", etc.), and Nobon (commodity (Name)), natural polymer resins, etc., are buried in the soil and decomposed in a short time, so they are easy to be discarded after use. The resin can be in the form of powder and granules. The powder is ideal, and it can also be granules. Resin can be used in combination of two or more types. Plant residues can be used as long as they are powdery, granular, and moisture-produced from food processing. Regardless of the type, they are used when processing foods using coriander, beans, and seeds. The pulverized granules produced are ideal. For example, wheat bran produced during wheat refining, plant stem powder, tofu residue produced during tofu production, tofu residue, fat-free defatted tofu residue, coffee residue, and rice refining Rice bran produced at the time, degreased rice bran degreased from rice bran, and the paper size produced during beer manufacturing is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm)-8--· J ---; --- 'J —. ,, ίκ (please read the precautions before reading this page, and then fill out this page) Order printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs A7 __B7 _ V. Description of the invention (6) Raw beer brewing, great oil extraction Bean dregs, flax dregs or maize dregs, sugared sugar dregs, soy sauce dregs, etc. Plant residues using soybeans such as defatted tofu dregs, soybean dregs are collectively referred to as soybean husks. These plant dregs are pulverized into powder and granules by processing steps. It can be used directly, but in order to match the degree of foaming, the type of resin to be mixed, and the physical properties required for the composite foam, etc., it can be pulverized and pulverized. It can also be used in combination of two or more plant residues. Plant residues The functional system has the function of a water carrier because it contains water, which makes the water finely disperse in the molten resin, and its main components include fat, protein, fiber, and coarse ash. The following functions are achieved. Fat system It has the functions of improving the moldability during molding, increasing the penetration of resin, and improving the dispersibility of resin residues to the resin. The content of plant residues is reasonably adjusted at 0_2 to 20% by weight. It is thought that 2 to 6% by weight is more ideal. When it exceeds 20% by weight, it is easy to separate or contaminate the mold protein. It has the function of improving the binding force to the resin after hot melting, and also has the function of the mixing ratio of plant residues to the resin. 5 to 40% by weight is more desirable, and more preferably 12 to 30% by weight. The resin with a tangled fiber melt has the function of making up the brittleness of the composite foam and improving the strength. The ideal content of plant residue is 3% by weight or more. 'It is more preferably more than 5% by weight. The coarse fraction has the function of an extender. The ideal content of the plant residue is 20% by weight or less, and more preferably 15% by weight or less. The coarse ash is an organic substance and a composite foam is used. After incineration, most of them are burned with only a small amount of residue (residual ash). Plant residues originally contained a large amount of water, for example, the husks contained about 80% water. Therefore, 'storage of plant residues should be used during storage, stirring, mixing, etc. & National Standards (CNS) of Japan (210X297 mm.) ^ -9-nn —Μ I; II n I n ^, -J (please read the notes on the back of E first, and then fill out this page) Printed by A7 __—__ B7_ ._ 5. Description of the invention (7) Dry and adjust to moisture 1 5 ~ 7 5% by weight. The amount of water in the whole material is set according to the degree of foaming, the type of resin to be mixed, and the physical properties required of the composite foam. Generally, the amount of water is increased when the expansion ratio is increased, and the amount of water is decreased when the expansion ratio is decreased. The amount of water for the whole raw material is basically based on the proportion of plant residues. When the proportion of plant residues is increased, the amount of water increases, and vice versa. If the proportion of plant residues is constant, adjust the moisture content of plant residues or add water with the set foaming ratio. In particular, when the expansion ratio is increased, it is desirable to add an appropriate amount of water after stirring and mixing the resin and plant residues and / or heating and melting. The blending ratio of resin and plant residues is set according to the degree of foaming, the type of mixed resin, and the physical properties required of the composite foam. Generally, when the foaming ratio is increased, the proportion of plant residues is increased, and vice versa. The proportion of residue. It varies depending on the moisture content of plant residues, but in general, the plant residue is 40 ~ 4 0 0 parts by weight (the ratio to the total amount is 2 8. 5 ~ 8 0 · 0 weight? 6) at 100 parts by weight of resin, ideal 0〜60. 0 重量 %)。 6 0 ~ 200 parts by weight (37.5 to 66.7 wt%), more preferably 100 to 150 parts by weight (50. 0 ~ 60. 0 wt%). The resin and plant residues are stirred and mixed using a well-known mixer. The mixer can be a Henschel mixer (Mitsui Miike Co., Ltd.).
Super Mixer (川田製作所製之SMG 1 0 0 )等的高 速混合機,且在低於樹脂軟化溫度之低溫區域充分地攪拌 混合較理想。攪拌混合後之原料的熔融混練後使用公知的 成形機,例如可用無排出口之混練用雙軸擠壓機(日立造 船產業製之HMT 57 — 40DSF,日本製鋼所製之 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐)~ -10 - I —_ I . /"^一 裝 I I I I 訂— I I I I —^'^ (諸先聞讀背面之注意事領再填寫本頁) 經濟部中央標準局負工消費合作社印製 A 7 ____ B7 五、發明説明(8 ) TEX47F-20AW)等充分混練較理想《充分地攪 拌混合及混練更能提高植物殘渣在熔融樹脂中之分散狀態 ,即,水之微分散,也可添加促進分散之分散促進劑。爲 了提高氣泡的微細化,均勻化也可添加滑石粉,碳酸鈣' 二氧化矽,氧化鋁,玻璃粉等之無機質粉粒體的核劑。又 必要時可添加氧化防止劑,界面活性劑,著色劑,紫外線 吸收劑,難燃劑等的樹脂添加物。 製成之複合發泡體依據成形機的塑模,成形模等製造 各種的形狀,成爲均勻形成微細之獨立氣泡的發泡結構, 幾乎具有與樹脂發泡體相同的檄械特性。發泡倍率高的複 合發泡體其表面形成薄的表皮層,具有相當於本材的表面 硬度,強度等,也可作爲木材的代替品使用。 複合發泡體具有在土中分解對於樹脂發泡體而言無法 期待的特性。複合發泡體中的植物殘渣經腐蝕分解,例如 以3 0比7 0重量比配合樹脂與植物殘渣所得之混合物, 若樹脂爲聚丙烯時約6個月植物殘渣則全部分解。樹脂爲 生物分解性樹脂時,比使用生物分解性樹脂之樹脂發泡體 在更短時間內分解消失,約3個月內包括樹脂幾乎完全分 解,約4個月全部分解消失。因此複合發泡體之掩埋處理 不需要如樹脂發泡體的大容積,處理較容易。又燒毀處理 時黑煙或有毒氣體之發生情形較少,而且發熱量較低。例 如以3 0比7 0之重量比配合聚丙烯及榖殼所得之混合物 ,當使用聚丙烯之樹脂發泡體其發熱量爲1 2,0 〇 〇 c a Ι/g,而該混合物的發熱量爲約1/2的 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 一 —————— :I ~ I I I 訂I I I I v 义) V I y . (諳先閣讀背面之注意事項再填寫本頁) -11 - 經濟部中央標準局負工消費合作社印製 A7 ____B7_ 五、發明説明(9 ) 6,020cal/g。因此,可抑制燃燒氣體所造成之 環境污染或破壞及因熱損壞焚燒爐等,焚燒處理比樹脂發 泡體容易。 〔實施例〕 以下說明具體的實施例。各實施例係使用麥糠,植物 莖粉,豆腐渣,脫脂豆腐渣,咖啡渣,米糠,脫脂米糠及 啤酒酿之植物殘渣,分別將這些植物殘渣與聚丙烯,Super Mixer (SMG 1 0 0 manufactured by Kawata Seisakusho) and other high-speed mixers, and it is ideal to stir and mix sufficiently in a low temperature region below the resin softening temperature. After melting and kneading the raw materials after stirring, use a known forming machine, such as a twin-shaft extruder for kneading without discharge ports (HMT 57-40DSF manufactured by Hitachi Shipbuilding Industry). The paper standard made by Japan Steel is applicable to China. Standard (CNS) A4 specification (210X297 mm) ~ -10-I —_ I. / &Quot; ^ 一 装 IIII Order — IIII — ^ '^ (Please read the note on the back before filling this page) Economy Printed by the Central Standards Bureau of the Ministry of Work and Consumer Cooperatives A 7 ____ B7 Fifth, the invention description (8) TEX47F-20AW) and other sufficient mixing is ideally "full stirring and mixing can improve the dispersion of plant residues in the molten resin, That is, a fine dispersion of water may be added with a dispersion accelerator to promote dispersion. In order to improve the miniaturization and homogenization of air bubbles, nucleating agents such as talc, calcium carbonate, silica, alumina, glass powder and other inorganic powders can be added. If necessary, resin additives such as oxidation inhibitors, surfactants, colorants, ultraviolet absorbers, and flame retardants can be added. The finished composite foam is manufactured in various shapes according to the molds and molding dies of the molding machine, and has a foam structure that uniformly forms fine, independent cells. It has almost the same mechanical properties as resin foams. The composite foam having a high expansion ratio has a thin skin layer on the surface, and has a surface hardness and strength equivalent to that of the material. It can also be used as a substitute for wood. A composite foam has characteristics that it cannot be expected for a resin foam to decompose in the soil. The plant residues in the composite foam are decomposed by corrosion. For example, a mixture of resin and plant residues is mixed at a weight ratio of 30 to 70. If the resin is polypropylene, the plant residues are all decomposed in about 6 months. When the resin is a biodegradable resin, it decomposes and disappears in a shorter period of time than a resin foam using a biodegradable resin. The resin is almost completely decomposed in about 3 months, and all decomposes and disappears in about 4 months. Therefore, the buried treatment of the composite foam does not require a large volume such as a resin foam, and the processing is easy. When it is burnt, the occurrence of black smoke or toxic gas is less, and the calorific value is lower. For example, a mixture obtained by blending polypropylene and shells at a weight ratio of 30 to 70, when a polypropylene resin foam is used, the calorific value is 12,000 ca / l, and the calorific value of the mixture is The size of this paper is about 1/2. The Chinese National Standard (CNS) A4 specification (210X297 mm) is applicable. I ——————: I ~ III order IIII v meaning) VI y. Please fill in this page again for matters) -11-Printed A7 ____B7_ by the Consumers' Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs 5. Description of the invention (9) 6,020cal / g. Therefore, it is possible to suppress environmental pollution or damage caused by the combustion gas, and damage to the incinerator due to heat, and the incineration treatment is easier than the resin foam. [Examples] Specific examples will be described below. Each example uses wheat bran, plant stem powder, tofu residue, defatted tofu residue, coffee grounds, rice bran, defatted rice bran, and beer-derived plant residues. These plant residues and polypropylene are separately used,
Lac ty (生物分解性樹脂),聚氯化乙烯及聚苯乙烯之各 種樹脂組合作爲原料。分別使用2種含水率不同之植物殘 渣。混合機使用高速混合機(川田製作所製S M G 100)。成形機使用如圖1概念之無排出口之混合用雙 軸擠壓機9日本製鋼所製ΤΕΧ- 3 0 )。圖1之混合用 雙軸擠壓機1係將投入給料斗6之原料W利用汽缸2之外 周上所設置的加熱器5的熱量加熱熔融,以螺旋4混練往 前進,將熔融之混合物Μ由設置於汽缸2前端之塑模3擠 壓發泡成形。塑模3可依製品更換。 實施例1〜8如表1所示使用聚丙烯樹脂(德山製之 P N 150G,MI爲15者),與各植物殘渣的配合 重量比分別設定爲4 0比6 0。發泡成形時使用中央部具 有2 mm孔之前述擠壓機的塑模,塑模的前端設置熱刀將 擠壓混合物切成4 0〜1 0 〇 m m。擠壓機汽缸的溫度設 定由給料斗側往塑模側依序昇高,最高溫度爲1 4 5 °C, 塑模溫度爲1 5 0 °C,被擠壓混合物的溫度爲1 6 4 °C。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (讀先«讀背面之注意事項再填寫本頁) -J裝. 訂 i. A7 B7 五、發明説明(10 ) 被擠壓混合物離開塑模瞬間藉由水蒸氣壓發泡得到棒狀的 複合發泡體。此複合發泡體的表面形成薄的表皮層,真有 緩衝性,還原性及透氣性,適合作爲緩衝材使用。以這些 的複合發泡體爲素材藉由壓製成形機一體成形成塊狀可作 爲捆包材料等的塊狀緩衝材料。 (請先閲讀背面之注項再氣寫本頁) 訂. -Ί. 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X 297公釐) -13 - A7 B7 五、發明説明(U ) 經濟部中央標準局員工消費合作社印製 表1 實施例 熱塑性樹脂 植物 殘渣 給水率 配合比 壓力 發泡倍率 表面硬度 (樹脂/植物) 殘渣名 粒徑 含水率 β % % 重量% kg/cm2 倍 D type 1 聚丙烯 麥糠 50 16.5 - 40/60 90 約30 - 2 植物莖粉 Μ 16.0 ― If 約35 - 3 豆腐渣 m 18.3 一 40 約15 - 4 JT 脫脂豆腐渣 fr 22.5 - 50 約25 ― 5 »r 咖啡渣 ¥ 19.0 一 Μ 40 約10 - 6 tr 米糠 • 18.8 - /f • 約15 - 7 tr 脫脂米糠 m 20· 7 ― Μ 50 約20 ' - 8 Μ 啤酒酿 16.3 - ¥ 80 約30 ― g 聚丙烯 麥糠 » 12.0 7.5 ff 70 約45 - 10 植物莖粉 tr Λ» 6.7 80 約50 ― 11 /t 豆腐渣 tr /r 10.5 40 約35 - 12 » 脫脂豆腐渣 tf If 17.5 60 約40 ― 13 /f 咖啡渣. /t 11.7. • 20 約25 - 14 >r 米糠 M 歸 11.3 40 約30 - 15 脫脂米糠 » 14.5 50 約35 - 16 /f 啤酒酿 Μ 7.2 ff 70 約45 - ('n^i 1^1 .—^i i^i^i HJ^ .^1^1 ^ϋ 1^1 ml -""* . „ i • i I '(#先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 14 - A7 B7 五、發明説明()Lacty (biodegradable resin), various resin combinations of polyvinyl chloride and polystyrene are used as raw materials. Use 2 types of plant residues with different moisture contents. As the mixer, a high-speed mixer (S M G 100 manufactured by Kawata Seisakusho) was used. As the forming machine, a hybrid biaxial extruder without a discharge port as shown in the concept of FIG. 1 was used (TEX-3 0 manufactured by Nippon Steel). The biaxial extruder 1 for mixing shown in FIG. 1 is used to heat and melt the raw material W fed to the hopper 6 by the heat of the heater 5 provided on the outer periphery of the cylinder 2 and knead it forward with the spiral 4 to move the molten mixture M from A plastic mold 3 provided at the front end of the cylinder 2 is extruded and foamed. The mold 3 can be replaced according to the product. Examples 1 to 8 used polypropylene resins (P N 150G manufactured by Tokuyama, MI 15) as shown in Table 1, and the weight ratio of each resin residue to each plant residue was set to 40 to 60. For the foam molding, a mold of the aforementioned extruder having a 2 mm hole in the center was used. A hot knife was set at the front end of the mold to cut the extruded mixture into 40 to 100 mm. The temperature setting of the cylinder of the extruder is sequentially increased from the hopper side to the mold side. The maximum temperature is 14.5 ° C, the mold temperature is 150 ° C, and the temperature of the extruded mixture is 16 4 °. C. This paper size applies Chinese National Standard (CNS) A4 specification (210X297 mm) (read «Read the precautions on the back before filling this page) -J Pack. Order i. A7 B7 V. Description of the invention (10) When the mixture leaves the mold, it is foamed by water vapor pressure to obtain a rod-like composite foam. The surface of this composite foam is formed with a thin skin layer, which is really cushioning, reducing and breathable, and is suitable for use as a cushioning material. These composite foams are used as a raw material and integrated into a block by a press molding machine to form a block-shaped cushioning material such as a packing material. (Please read the note on the back before writing this page) Order. -Ί. The paper size printed by the Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs applies the Chinese national standard (CNS) A4 specification (210 X 297 mm) -13 -A7 B7 V. Description of the invention (U) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. Table 1 Example of the thermoplastic resin plant residue water supply ratio pressure foaming ratio surface hardness (resin / plant) particle size water content β %% Weight% kg / cm2 times D type 1 polypropylene wheat bran 50 16.5-40/60 90 about 30-2 plant stem powder M 16.0 ― If about 35-3 bean curd m 18.3-40 about 15-4 JT degreased tofu Ground coffee fr 22.5-50 Approx. 25 ― 5 »r Coffee grounds ¥ 19.0 One M 40 Approx. 10-6 tr Rice bran • 18.8-/ f • Approx. 15-7 tr Skimmed rice bran m 20 · 7 ― Μ 50 Approx. 20 ′-8 Μ Beer brewed 16.3-¥ 80 about 30 ― g polypropylene wheat bran »12.0 7.5 ff 70 about 45-10 plant stem flour tr Λ» 6.7 80 about 50 ― 11 / t tofu residue tr / r 10.5 40 about 35-12 »skim Tf If 17.5 60 about 40 ― 13 / f coffee grounds. / t 11.7. • 20 about 25-14 > r rice bran M 11.3 40 about 30-15 defatted rice bran »14.5 50 about 35-16 / f beer brew M 7.2 ff 70 about 45-('n ^ i 1 ^ 1 .— ^ ii ^ i ^ i HJ ^. ^ 1 ^ 1 ^ ϋ 1 ^ 1 ml-" " *. „i • i I '(#Read the notes on the back before filling in this Page) This paper size is applicable to Chinese National Standard (CNS) A4 specification (210X297 mm) 14-A7 B7 V. Description of the invention ()
\L 實施例9〜1 6依實施例1〜8的變形例,如表1所 示將各植物殘渣的含水率減少至1 2重量%,以擠壓機加 熱熔融混練時供給水分。水的供給位置係靠近擠壓機汽缸 的給料斗’水的供給係當投入給料斗之原料開始產生熔融 時。成形的複合發泡體的發泡倍率遠高於實施例1〜8, 至少在1 _ 4倍以上,具有更高的緩衝性,還原性,透氣 性。 實施例1 7〜2 4係實施例1〜8的變形例,如表2 所示將各植物殘渣的含水率減少至1'2重量%,樹脂與植 物殘渣之配合重量比設定爲6 0 : 4 0。樹脂使用聚丙烯 ,德山製之PN 1 50G,MI爲6. 5者。發泡成形 經濟部中央標準局負工消費合作社印製 (諳先Μ讀背面之注意事領再填寫本頁) 時擠壓_塑模係使用厚度2 Omm,寬1 5 Omm,模唇 內具有3 0個1mm孔者,塑模前端設置細條集束用輥, 拉伸被擠壓的混合物,經切斷形成板狀。擠壓成形機汽缸 的最高溫度爲1 5 2°C,塑模溫度爲1 5 8°C,被擠壓之 混合物的溫度爲1 7 8°C,成形後之複合發泡體其表面形 成薄的表皮層,具有與木材相當的強度及表面硬度,適合 作爲木材的替代品。又提高植物殘渣的含水率可得到較高 發泡倍率者。 本紙張尺度適用中國國家標準(CNS )八4規格(21〇χ 297公釐) -15 ~ A7 B7 五、發明説明(13 ) 經濟部中央標準局員工消費合作社印製 表2 實施例 熱塑性樹脂 植物 殘渣 給水率 配合比 壓力 發泡倍率 表面硬度 (樹脂/植物) 殘渣名 粒徑 含水率 β % % 重量% kg/cm2 倍 D type 17 聚丙烯 麥糠 50 12.0 - 60/40 60 約4.0 約20〜30 18 • 植物莖粉 /Τ It - tr • 約25〜35 19 豆腐渣 Μ If 一 30 約3.0 約30〜38 20 Μ 脫脂豆腐渣 • , — 60 約3. 5 約15〜25 21 咖啡渣 Μ ft — 20 約2.5 約30〜40 22 ff 米糠 • M — • 40 約3.0 約28〜35 23 /f 脫脂米糠 /*· — 60 約3. 5 約15〜25 24 » 啤酒釀 Jf — 50 ¥ 約20〜30 25 Lacty 麥糠 17.5 — 40/60 50 約20 — 26 Μ 植物莖粉 17.0 — 約25 - 27 豆腐渣 • 19.2 —, 40 約10 - 28 » 脫脂豆腐渣 9 24.0 — 60 約15 - 29 Jf 咖啡渣 If 20.4 一 20 約5 一 30 Μ 米糠 ft 20.0 - Μ 40 約10 - 31 tr 脫脂米糠 tr 22.5 — If 50 約15 - 32 ir 啤酒釀 fr 18.1 — 40 約20 — (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 16 - A7 __^_B7_____^_ 五、發明説明(1/f) 14 實施例2 5〜3 2如表2所示,樹脂係使用生物分解 性樹脂Lacty (島津製作所製MI爲1〜2者),樹脂與 植物殘渣的配合重量比設定爲4 0 : 6 0,使用同實施例 1〜8之具有附屬設備的擠壓機來成形。擠壓機之汽缸的 最高溫度爲1 30°C,塑模的溫度爲1 3 5°C,被擠壓之 混合物的溫度爲1 3 8°C。成形後之複合發泡體的發泡倍 率比實施例1〜8低,具有緩衝性,還原性,透氣性等。 實施例3 3〜4 0依實施例2 5〜3 2的變形例,如 表3所示將各植物殘渣的含水率減少至1 2重量%,以擠 壓機加熱熔融混練時供給水分。水的供給位置係靠近擠壓 機汽缸的給料斗’水的供給係當投入給料斗之原料開始產 生熔融時。成形的複合發泡體的發泡倍率遠高於實施例 2 5〜3 2,至少在1 . 4倍以上,具有更高的緩衝性, 還原性,透氣性等. (讀洗閣讀背面之注意事項再蜞寫本頁) 裝. 訂 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家橾準(〇阳)八4規格(210'乂297公釐)— -17 - A7 B7 五、發明説明()\ L Examples 9 to 16 According to the modified examples of Examples 1 to 8, as shown in Table 1, the water content of each plant residue was reduced to 12% by weight, and water was supplied during the heat-melting and kneading by an extruder. The water supply position is the feed hopper 'near the cylinder of the extruder. The water supply is when the raw materials put into the hopper begin to melt. The foaming ratio of the formed composite foam is much higher than that of Examples 1 to 8, and at least 1 to 4 times, and it has higher cushioning, reducing and air permeability. Example 1 7 ~ 2 4 is a modification of Examples 1-8. As shown in Table 2, the moisture content of each plant residue is reduced to 1'2% by weight, and the weight ratio of the resin to the plant residue is set to 60: 4 0. 5。 Polypropylene resin, Tokuyama made PN 1 50G, MI is 6.5. Printed by the Consumer Standards Cooperative of the Central Standards Bureau of the Ministry of Economics of Foam Molding (I read the precautions on the back and then fill out this page) when extruding_The mold system uses a thickness of 2 Omm and a width of 15 Omm. For 30 1mm holes, a thin-strand bundling roller is set at the front end of the mold to stretch the extruded mixture and cut into a plate shape. The maximum temperature of the cylinder of the extrusion molding machine is 15 2 ° C, the mold temperature is 158 ° C, the temperature of the extruded mixture is 178 ° C, and the surface of the composite foam after forming is thin. The skin layer has the same strength and surface hardness as wood and is suitable as a substitute for wood. Increase the moisture content of plant residues to obtain higher expansion ratio. This paper size applies to China National Standards (CNS) 8.4 specifications (21〇χ 297 mm) -15 ~ A7 B7 V. Description of the invention (13) Table 2 printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Example 2 Thermoplastic resin plant Residual water supply ratio, pressure foaming ratio, surface hardness (resin / vegetable) Residual particle size, moisture content β%% weight% kg / cm2 times D type 17 polypropylene wheat bran 50 12.0-60/40 60 about 4.0 about 20 ~ 30 18 • Plant stem powder / Τ It-tr • about 25 ~ 35 19 Tofu residue Μ If-30 about 3.0 about 30 ~ 38 20 Μ non-fat tofu residue •, — 60 about 3.5 5 about 15 ~ 25 21 coffee ground Μ ft — 20 about 2.5 about 30 ~ 40 22 ff rice bran • M — • 40 about 3.0 about 28 ~ 35 23 / f skimmed rice bran / * · — 60 about 3.5 5 about 15 ~ 25 24 »Beer Jf — 50 ¥ about 20 ~ 30 25 Lacty wheat bran 17.5 — 40/60 50 about 20 — 26 Μ plant stem powder 17.0 — about 25-27 bean curd • 19.2 —, 40 about 10-28 »skim bean curd 9 24.0 — 60 about 15-29 Jf coffee grounds If 20.4 to 20 about 5 to 30 Μ Bran ft 20.0-Μ 40 about 10-31 tr skim rice bran tr 22.5 — If 50 about 15-32 ir beer brewed fr 18.1 — 40 about 20 — (Please read the notes on the back before filling out this page) This paper size applies to China National Standard (CNS) A4 specification (210X297 mm) 16-A7 __ ^ _ B7 _____ ^ _ V. Description of the invention (1 / f) 14 Example 2 5 ~ 3 2 As shown in Table 2, the resin is made of biodegradable resin Lacty (MI made by Shimadzu Corporation is 1 to 2). The compounding weight ratio of resin to plant residue is set to 40:60, and it is formed using the extruder with auxiliary equipment as in Examples 1 to 8. The maximum temperature of the cylinder of the extruder is 130 ° C, the temperature of the mold is 135 ° C, and the temperature of the extruded mixture is 138 ° C. The foaming ratio of the composite foam after molding is lower than that of Examples 1 to 8, and it has cushioning properties, reducing properties, and air permeability. Example 3 3 to 40 In accordance with the modified examples of Examples 2 5 to 32, as shown in Table 3, the moisture content of each plant residue was reduced to 12% by weight, and water was supplied during heating and kneading by an extruder. The water supply position is near the feed hopper 'of the cylinder of the extruder. The water supply is when the raw materials put into the hopper begin to melt. The foaming ratio of the formed composite foam is much higher than that of Example 2 5 ~ 32, at least 1.4 times or more, and has higher cushioning, reduction, and air permeability. (Notes are reproduced on this page.) Binding. Order printed by the Central Consumers Bureau of the Ministry of Economic Affairs, Consumer Cooperatives. The paper size is applicable to China National Standard (〇 阳) 8 4 size (210 '乂 297 mm) — -17-A7 B7 Five, description of the invention ()
ID 經濟部中央標準局員工消費合作社印製 表3 實施例 熱塑性樹脂 植物 殘渣 給水率 配合比 壓力 發泡倍率 表面硬度 (樹脂/植物) 殘渣名 粒徑 含水率 β % % 重量% kg/cm2 倍 D type 33 Lacty 麥糠 50 12,0 14· 0 40/60 40 約30 — 34 歸 植物莖粉 ¥ /Τ 12.5 If 40 約35 — 35 It 豆腐渣 ” 10.0 » 20 約20 — 36 /r 脫脂豆腐渣 Μ 24.0 Μ 30 約25 - 37 ” 咖啡渣 • Μ 8.0 20 約15 — 38 tr 米糠 ¥ /f 11.7 ft 30 約20 - 39 脫脂米糠 If 0 18.3 30 約25 — 40 啤酒釀 0 13.0 40 約30 — 41 聚氯化乙烯 麥糠 50 12.0 — 60/40 60 約4 約25〜35 42 /f 植物莖粉 /r /r - 9 • 約30〜40 43 fr 豆腐渣 ir ft -丨 fr 40 約3 約 35~45 44 脫脂豆腐渣 /f — rr 80 約3. 5 約20〜30 45 咖啡渣 /r - 30 約2. 5 約35〜45 46 At 米糠 Μ - 40 約3 約30〜40 47 IT 脫脂米糠 /r If - ” 60 約3. 5 約20〜30 48 fr 啤酒酸 — 0 >r 緣 約25〜35 (請先閲讀背面之注意事項再填寫本頁) 裝. 訂 本紙張尺度適用中國國家標準(CNS ) A4規格(2l〇X2.97公釐) A7 B7 五、發明説明(16) 實施例4 1〜4 8如表3所示,樹脂係使用聚氯化乙 烯(東裝製之E — 430),各植物殘渣係使用含水率減 至1 2重量%者。樹脂與植物殘渣的重量比例爲6 0 : 4 0,使用同實施例1〜8之具有附屬設備的擠壓機來成 形◊擠壓機之汽缸的最高溫度爲1 3 5°C,塑模的溫度爲 1 4 5°C,被擠壓之混合物的溫度爲1 5 8°C。成形後之 複合發泡體具有與實施例17〜2 4相同之相當木材的表 面硬度,強度等。 實施例4 9〜5 6如表4所示,樹脂係使用聚苯乙烯 (電氣化學工業製之QP-2Β),與各植物殘渣的配合 重量比分別設定爲4 0 : 6 0。使用具有與實施例1〜8 相同之附屬設備之擠壓機。擠壓機之汽缸的最高溫度爲 1 5 5°C,塑模的溫度爲1 6 0°C,被擠壓之混合物的溫 度爲1 7 8°C。成形後之複合發泡體的發泡倍率比實施例 1〜8低,具有緩衝性,還原性,透氣性等。 (背先閲讀背面之注意事項再填寫本頁) -° 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(.2丨〇><297公釐) -19 - A7 B7 五、發明説明(17 ) 經濟部中央標準局員工消費合作社印製 表4 實施例 熱塑性樹脂 植物 殘渣 給水率 配合比 壓力 發泡倍率 表面硬度 (樹脂/植物) 殘渣名 粒徑 含水率 β % % 重量% kg/cm2 倍 D type 49 聚苯乙烯 麥糠 50 16.8 — 40/60 140 約20 — 50 植物莖粉 JT 16.2 - 約25 一 51 JT 豆腐渣 18.3 — • 100 約10 — 52 脫脂豆腐渣 21.8 — If 150 約15 - 53 Μ 咖啡渣 » 18.5 - Μ 90 約10 - 54 米糠 fr 18.6 — Μ 100 — 55 脫脂米糠 tr 20.9 — If 120 約15 — 56 啤酒釀 tr 16.5 — If 130 約20 - 57 聚苯乙烯 麥糠 » 12.0 8.0 It » 約40 — 58 If 植物莖粉 Μ If 7.0 M fr 約45 — 59 » 豆腐渣 >r • 10.3 Jf 70 約30 — 60 ff 脫脂豆腐渣 /r 16.3 >r 120 約35 — 61 ff 咖啡渣 If rr 10.8 ir 50 約20 — 62 ft 米糠 » 11.0 tr 60 約30 — 63 tf 脫脂米糠 14.8 m 120 約35 — 64 fr 啤酒酿 tr 7.5 M 約40 — (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -20 - A7 B7 五、發明説明() 實施例5 7〜6 4依實施例4 9〜5 6的變形例,如 表4所示將各植物殘渣的含水率減少至1 2重量%,以濟 壓機加熱熔融混練時供給水分。水的供給位置係靠近擠壓 機汽缸的給料斗’水的供給係當投入給料斗之原料開始.產 生溶融時。成形的複合發泡體的發泡倍率遠高於實施例 49〜56’至少在1. 8倍‘以上,具有更高的緩衝性, 還原性,透氣性。 實施例6 5〜72依實施例49〜5 6的變形例,如 表5所示將各植物殘渣的含水率減少至1 2重量%,樹脂 與植物殘渣之配合重量比例設定爲6 0 : 4 0。使用具有 與實施例1 7〜2 4相同之附屬設備的擠壓機。擠壓機之 汽缸的最高溫度爲15 5°C,塑模的溫度爲1 4 5°C,被 擠壓之混合物的溫度爲1 5 8°C。成形後之複合發泡體幾 乎與實施例1 7〜2 4相同,具有相當木材之表面硬度, 強度等。 (婧先閲讀背面之注意事項再填寫本頁) 訂 經濟部中央標準局員工消費合作社印裝 本紙張尺度適用中國國家標準(CNS ) A4規格(210 X 297公釐) -21 -ID Printed by the Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. Table 3 Example of the thermoplastic resin plant residue water supply ratio pressure foaming rate surface hardness (resin / plant) residue name particle size moisture content β%% weight% kg / cm2 times D type 33 Lacty wheat bran 50 12,0 14 · 0 40/60 40 about 30 — 34 stem powder of plant ¥ / Τ 12.5 If 40 about 35 — 35 It tofu residue ”10.0» 20 about 20 — 36 / r non-fat tofu residue Μ 24.0 Μ 30 about 25-37 ”coffee grounds Μ 8.0 20 about 15 — 38 tr rice bran ¥ / f 11.7 ft 30 about 20-39 skim rice bran If 0 18.3 30 about 25 — 40 beer brewing 0 13.0 40 about 30 — 41 Polyvinyl chloride wheat bran 50 12.0 — 60/40 60 about 4 about 25 ~ 35 42 / f plant stem powder / r / r-9 • about 30 ~ 40 43 fr tofu residue ir ft-丨 fr 40 about 3 about 35 ~ 45 44 skim bean curd residue / f — rr 80 about 3.5 5 about 20 ~ 30 45 coffee grounds / r-30 about 2.5 5 about 35 ~ 45 46 At rice bran M-40 about 3 about 30 ~ 40 47 IT skim rice bran / r If-”60 about 3.5 5 about 20 ~ 30 48 fr beer acid — 0 > r margin about 25 35 (Please read the precautions on the reverse side before filling out this page) Binding. The size of the paper is applicable to the Chinese National Standard (CNS) A4 specification (210 × 2.97 mm) A7 B7 V. Description of the invention (16) Example 4 1 ~ 4 8 As shown in Table 3, the resin is made of polyvinyl chloride (E-430 made by Tojo), and each plant residue is used when the moisture content is reduced to 12% by weight. The weight ratio of resin to plant residue is 60:40, the maximum temperature of the cylinder of the extruder is 1 3 5 ° C, and the temperature of the mold is 1 4 5 ° C. The temperature of the extruded mixture was 158 ° C. The formed composite foam had the same surface hardness and strength as those of Examples 17 to 24. Examples 4 9 to 5 6 are shown in Table 4 As shown, the resin is made of polystyrene (QP-2B manufactured by Denka Kogyo Kagaku Kogyo), and the weight ratio of each resin residue to each plant residue is set to 40:60. An extruder having the same auxiliary equipment as in Examples 1 to 8 was used. The maximum temperature of the cylinder of the extruder is 15 5 ° C, the temperature of the mold is 160 ° C, and the temperature of the extruded mixture is 178 ° C. The foaming ratio of the composite foam after molding is lower than that of Examples 1 to 8, and has cushioning properties, reducing properties, and air permeability. (Please read the precautions on the back before filling this page)-° The paper size printed by the Employees' Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs applies the Chinese National Standard (CNS) A4 specification (.2 丨 〇 > < 297 mm) -19-A7 B7 V. Description of the invention (17) Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs. Table 4 Example of thermoplastic resin plant residue water supply ratio pressure foaming rate surface hardness (resin / plant). Rate β%% Weight% kg / cm2 times D type 49 Polystyrene wheat bran 50 16.8 — 40/60 140 about 20 — 50 plant stem powder JT 16.2-about 25-51 JT tofu residue 18.3 — • 100 about 10 — 52 Defatted tofu residue 21.8 — If 150 about 15-53 Μ coffee grounds »18.5-Μ 90 about 10-54 rice bran fr 18.6 — Μ 100 — 55 skimmed rice bran tr 20.9 — If 120 about 15 — 56 beer brewed tr 16.5 — If 130 about 20-57 Polystyrene wheat bran »12.0 8.0 It» about 40 — 58 If plant stem powder M If 7.0 M fr about 45 — 59 »tofu residue > r • 10.3 Jf 70 about 30 — 60 ff skim Rot / r 16.3 > r 120 about 35 — 61 ff coffee grounds If rr 10.8 ir 50 about 20 — 62 ft rice bran »11.0 tr 60 about 30 — 63 tf skimmed rice bran 14.8 m 120 about 35 — 64 fr beer brewed tr 7.5 M about 40 — (Please read the notes on the back before filling in this page) This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) -20-A7 B7 V. Description of the invention () Example 5 7 ~ According to the modified examples of Examples 4 9 to 5 6, as shown in Table 4, the water content of each plant residue was reduced to 12% by weight, and water was supplied during heating and kneading by a press machine. The water supply position is near the feed hopper of the cylinder of the extruder. The water supply is when the raw material input to the hopper starts to melt. The foaming ratio of the formed composite foam is much higher than that of Examples 49 to 56 'and at least 1.8 times' or more, and has higher cushioning properties, reducing properties, and air permeability. Example 6 5 to 72 In accordance with the modified examples of Examples 49 to 56, as shown in Table 5, the water content of each plant residue was reduced to 12% by weight, and the weight ratio of the resin to the plant residue was set to 60: 4 0. An extruder having the same auxiliary equipment as in Examples 17 to 24 was used. The maximum temperature of the cylinder of the extruder is 15 5 ° C, the temperature of the mold is 145 ° C, and the temperature of the extruded mixture is 158 ° C. The formed composite foam is almost the same as that of Examples 1 to 24, and has a surface hardness, strength, and the like of the wood. (Jing first read the precautions on the back before filling this page) Order Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) -21-
AA
7 B 五、發明説明(1n)1 y 表5 實施例 熱塑性樹脂 植物 殘渣 給水率 配合比 (樹脂/植物) 壓力 發泡倍率 表面硬度 殘渣名 粒徑 含水率 β % % 重量% kg/cm2 倍 D type 65 聚苯乙烯 麥糠 50 12,0 - 60/40 70 約5.0 約 25~35 66 . 植物莖粉 m — 鼸 約30〜40 67 Μ 豆腐渣 ¥ — ¥ 50 約4.0 摩 68 Μ 脫脂豆腐渣 雜 m - m 80 約4. 5 約15〜25 69 • 咖啡渣 雔 ¥ - • 40 約3. 5 約25〜35 70 0 米糠釀 Μ - 50 約4.0 71 Μ 脫脂米糠 0 — • _ 70 約4. 5 約15〜25 72 Ρ 睥酒壤 Μ — It 60 歡 約25〜35 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 22 經濟部中央標準局員工消費合作社印製 §?δΐ63 at Β7 五、發明説明(2()) 實施例7 3係使用生物分解性樹脂之聚己內酯樹脂, 植物殘渣係使用植物莖粉,兩者之配合重量比設定爲4 0 :60。擠壓機之塑模係使用PS發泡成形用圓筒模,汽 缸之最高溫度爲1 4 0°C,最低溫爲9 0°C,塑模溫度爲 1 2 5°C,塑模前端溫度爲1 1 0°C,被擠壓之混合物的 溫度爲1 4 5°C,壓力爲1 〇 〇kg/cm2,然後形成 薄片狀體。成形後之複合發泡體其發泡倍率約3 5倍,表 面形成薄的表皮層,具有緩衝性,還原性,柔軟性,透氣 性等,適合作爲緩衝材,發泡薄片。又具有生物分解性, 埋入土中約4個月分解9 5%。 實施例74係使用聚丙烯及聚乙烯樹脂,植物殘渣係 使用植物莖粉,發泡之核劑使用碳酸鈣。這些的配合重量 比設定爲聚丙烯4 0重量%,聚乙烯5重量%,麥糠5 0 重量%,碳酸鈣5重量% »擠壓機之塑模係使用P S發泡 成形用圓筒模,汽缸之最高溫度爲1 5 0 °C,最低溫爲 9 0°C,塑模溫度爲1 4 5°C,塑模前端溫度爲1 4 0°C ’被擠壓之混合物的溫度爲1 8 0°C,壓力爲1 2 0 kg / c m2,然後形成薄片狀體。成形後之複合發泡體其發 泡倍率約4 0倍,表面形成薄的表皮層,具有緩衝性,還 原性,柔軟性,透氣性等,適合作爲緩衝材》 〔發明的效果〕 依據本發明時,將樹脂及含水分之植物殘渣予以攪拌 混合’加熱熔融狀態下混練,植物殘渣不会凝集而成均匀 -.- _ 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (谛先閲讀背面之注意事項再填寫本頁) "° -23 - 你物 A7 __^_ B7 _ 五、發明説明(21 ) 分散於熔融之樹脂中,然後可將水微分散於熔融之樹脂中 。即,以植物殘渣所含的水分作爲發泡劑使用,植物殘渣 係使水微分散於熔融樹脂中之媒介物。因此,不需要如以 往以水爲發泡劑之製造方法,爲了保持水分而預先形成多 孔性集合塊的複雜步驟,而只要以簡便廉價且安全地形成 獨立氣泡結構的複合發泡體。 植物殘渣原來含有許多水分,故將植物殘渣乾燥很容 易調整水分。因此,比以往以水爲發泡劑之製造方法能使 更多的水分分散於樹脂中,可形成極高發泡倍率的複合發 泡體,又藉由改變植物殘渣的配合比例也能調整原料整體 的水分量,形成各種物性的複合發泡體。植物殘渣具有吸 水性,故以成形機加熱熔融混練時添加水分,水分會被植 物殘渣吸收添加的水分也被微分散於熔融的樹脂中,更 能提高發泡倍率。藉由改變樹脂與植物殘渣的配合比例也 能同時調整水量,故能簡單進行原料之調整作業。 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 利用植物殘渣更能降低製造成本,可提供一種廉價的 複合發泡體。植物殘渣大部分當作廢棄物處理,而作爲複 合發泡體成形使用有助於資源之再利用及廢棄物處理等》 而且,製得之複合發泡體具生物分解性,埋入土中體積縮 .小,且焚燒時發熱量低,可抑制焚燒爐之損壞,故廢棄處 理比以往更容易。 製得之複合發泡體幾乎無連續氣泡,係微細之獨立氣 泡成均勻分佈的發泡結構,具有幾乎與以往之樹脂發泡體 相同的機械特性,故可作爲代替品使用。發泡倍率高的複 本矣艮張尺度適用中國國家標率(CNS > A4規格(210X297公釐} ~~ -24 - 8^^169 A7 __ _________B7 ___;__ 五、發明説明(22 ) 合發泡體因具有緩衝性,還原性,柔軟性等,故可作爲捆 包用緩衝材料。特別是具有透氣性,故非常適合水果,蔬 菜等之捆包用緩衝材料,可長期防止這些果菜類之腐敗。 發泡倍率低的複合發泡體具有相當木材之表面硬度,強度 等可作爲木材的替代品使用。 - 〔圖式之簡單說明〕 〔圖1〕係表示本發明之各實施例中使用之擠壓機之 —例的斷面圖。 〔符號說明〕 1 擠壓機 2 .汽缸 3 塑模(蓋子,模) 4 螺旋 5 加熱器 經濟部中央標準局員工消費合作社印製 (請先閲讀背面之注意事項再填寫本頁) 6 給料斗 W 原料 Μ 熔融之混合物 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) -25 -7 B V. Description of the invention (1n) 1 y Table 5 Example of the ratio of water supply ratio of plant residues of thermoplastic resin (resin / plant) Pressure foaming rate Surface hardness residue name Particle size water content β%% weight% kg / cm2 times D type 65 Polystyrene wheat bran 50 12,0-60/40 70 about 5.0 about 25 ~ 35 66. plant stem powder m — 鼸 about 30 ~ 40 67 Μ tofu residue ¥ — ¥ 50 about 4.0 mol 68 % non-fat tofu residue Miscellaneous m-m 80 Approx. 4.5 Approx. 15 to 25 69 • Coffee grounds ¥-• 40 Approx. 3.5 Approx. 25 to 35 70 0 Rice bran brewed M-50 Approx. 4.0 71 Μ Degreased rice bran 0 — • _ 70 Approx. 4 5 Approx. 15 ~ 25 72 Ρ 壤 酒 土 M — It 60 Huan Approx. 25 ~ 35 Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs This paper is printed in accordance with Chinese National Standard (CNS) A4 (210X297 mm) 22 Ministry of Economic Affairs Printed by the Consumer Standards Cooperative of the Central Bureau of Standards §? Δΐ63 at Β7 V. Description of the Invention (2 ()) Example 7 3 is a polycaprolactone resin using a biodegradable resin, and plant residues are using plant stem powder. The blending weight ratio was set to 40:60. The mold of the extruder is a cylinder mold for PS foam molding. The highest temperature of the cylinder is 140 ° C, the lowest temperature is 90 ° C, the mold temperature is 125 ° C, and the temperature of the front end of the mold is It was 110 ° C, the temperature of the extruded mixture was 145 ° C, and the pressure was 1000 kg / cm2, and then a sheet was formed. The formed composite foam has a foaming ratio of about 35 times, and a thin skin layer is formed on the surface, which has cushioning properties, reducing properties, softness, and air permeability. It is suitable as a cushioning material and foamed sheet. It is also biodegradable, and it will decompose 95% in about 4 months after being buried in the soil. In Example 74, polypropylene and polyethylene resins were used, and plant residues were plant stem powders, and calcium carbonate was used as the nucleating agent for foaming. The compounding weight ratio of these is set to 40% by weight of polypropylene, 5% by weight of polyethylene, 50% by weight of wheat bran, and 5% by weight of calcium carbonate. »The mold of the extruder uses a cylindrical mold for PS foam molding. The maximum temperature of the cylinder is 150 ° C, the lowest temperature is 90 ° C, the temperature of the mold is 14 5 ° C, and the temperature of the front end of the mold is 140 ° C. The temperature of the extruded mixture is 1 8 At 0 ° C, the pressure is 120 kg / c m2, and then a flaky body is formed. The formed composite foam has a foaming ratio of about 40 times, a thin skin layer is formed on the surface, and it has cushioning properties, reducing properties, softness, and air permeability. It is suitable as a cushioning material. [Effects of the invention] According to the present invention Resin and water-containing plant residues are stirred and mixed in a heating and melting state, and the plant residues will not agglomerate and become homogeneous -.- _ This paper size applies to China National Standard (CNS) A4 (210X297 mm) (谛 Read the precautions on the back before filling this page) " ° -23-Your thing A7 __ ^ _ B7 _ V. Description of the invention (21) Dispersed in the molten resin, then water can be dispersed in the molten resin slightly in. That is, the water contained in the plant residue is used as a foaming agent, and the plant residue is a vehicle for finely dispersing water in the molten resin. Therefore, the conventional manufacturing method using water as a foaming agent is not required, and the complicated steps of forming porous aggregates in advance in order to retain the moisture are not required, but only a simple, inexpensive and safe formation of a composite foam having an independent cell structure is required. Plant residues originally contain a lot of water, so drying plant residues makes it easy to adjust moisture. Therefore, more water can be dispersed in the resin than the conventional manufacturing method using water as a foaming agent, and a composite foam with a very high foaming ratio can be formed. The entire raw material can also be adjusted by changing the mixing ratio of plant residues. Moisture content to form a composite foam with various physical properties. Plant residues are water-absorptive. Therefore, water is added during heating and melting with a molding machine. The water will be absorbed by the plant residues and the added water will be finely dispersed in the molten resin, which will increase the expansion ratio. The amount of water can be adjusted at the same time by changing the blending ratio of resin and plant residues, so the adjustment of raw materials can be easily performed. Printed by the Consumer Cooperatives of the Central Standards Bureau of the Ministry of Economic Affairs (please read the precautions on the back before filling this page) Using plant residues can further reduce manufacturing costs and provide a cheap composite foam. Most of the plant residues are treated as waste, and the use of it as a composite foam is helpful for the reuse of resources and waste disposal. Moreover, the composite foam produced has biodegradability and shrinks in volume when buried in soil. It is small and has low heat generation during incineration, which can suppress the damage of the incinerator, so it is easier to dispose of it than in the past. The resulting composite foam has almost no continuous bubbles, and is a finely divided independent foam with a uniformly distributed foam structure. It has almost the same mechanical properties as conventional resin foams, so it can be used as a substitute. The copy size with high foaming magnification is applicable to China's national standard (CNS > A4 size (210X297mm) ~~ -24-8 ^^ 169 A7 __ _________B7 ___; __ 5. Description of the invention (22) Because of its cushioning, reducing, and softness, the foam can be used as a buffering material for packing. Especially it is breathable, so it is very suitable for packing materials such as fruits and vegetables. It can prevent these fruits and vegetables for a long time. Corruption. A composite foam with a low expansion ratio has considerable surface hardness and strength, which can be used as a substitute for wood.-[Simplified description of the drawing] [Fig. 1] It is used in the embodiments of the present invention. Sectional view of an extruder—example. [Symbols] 1 Extruder 2. Cylinder 3 Mould (cover, mold) 4 Spiral 5 Heater Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs (Please read first Note on the back, please fill in this page again) 6 Feed hopper W Raw material M Melted mixture The paper size applies to China National Standard (CNS) A4 specification (210 × 297 mm) -25-
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW85115941A TW379169B (en) | 1996-12-24 | 1996-12-24 | Method of making compound resin foaming agents |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW85115941A TW379169B (en) | 1996-12-24 | 1996-12-24 | Method of making compound resin foaming agents |
Publications (1)
Publication Number | Publication Date |
---|---|
TW379169B true TW379169B (en) | 2000-01-11 |
Family
ID=21625635
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW85115941A TW379169B (en) | 1996-12-24 | 1996-12-24 | Method of making compound resin foaming agents |
Country Status (1)
Country | Link |
---|---|
TW (1) | TW379169B (en) |
-
1996
- 1996-12-24 TW TW85115941A patent/TW379169B/en not_active IP Right Cessation
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR0135603B1 (en) | Pressed polymer foam product and method of preparation | |
KR101344471B1 (en) | Bio plastic using coffee residual products and method making the same | |
KR100570550B1 (en) | Process for producing foarmed article and the foamed article | |
JP4640814B2 (en) | Thermoplastic resin foam | |
JP2729936B2 (en) | Method for producing composite resin foam | |
US20240124659A1 (en) | Method for producing resin composite material, and resin composite material | |
TW379169B (en) | Method of making compound resin foaming agents | |
CN109679307A (en) | A kind of biodegradable pearl cotton and preparation method thereof | |
JPH1112379A (en) | Biodegradable resin foam | |
JP3878623B2 (en) | Rice-blended polyolefin resin composition, production method thereof, film molded product thereof, and molding method of this molded product | |
JP2000025852A (en) | Heat insulation container | |
JP2002371153A (en) | Biodegradable foamed molded body and method for manufacturing the same | |
JP2001002838A (en) | Nonstatic or conductive foaming member | |
JP2000103893A (en) | Expansion molding looking as if made of ice and its manufacture | |
JPH0971677A (en) | Biodegradable cushioning material and its production | |
JP2002249666A (en) | Buffer sheet composition, method for preparing buffer sheet, and buffer sheet | |
US20040075194A1 (en) | Process for the use of polymeric materials to produce molded foam products | |
JP2000108153A (en) | Manufacture of rigid-surface loose buffer material | |
JP2003138063A (en) | Water-resistant starch composition and its foam | |
JP2000143869A (en) | Preparation of foamed material using plastic-laminated paper waste | |
JP7058822B1 (en) | Manufacturing method and manufacturing system for biodegradable plastic products | |
JP2010132295A (en) | Assembly type shock-absorbing heat insulating material | |
JP3009261B2 (en) | Moisture-proof starch molding | |
TW201741526A (en) | Synthetic paper and application thereof | |
JP2001302834A (en) | Method for producing foamed material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GD4A | Issue of patent certificate for granted invention patent | ||
MM4A | Annulment or lapse of patent due to non-payment of fees |