TW201012649A - Polyolefin resin-laminated foam - Google Patents

Polyolefin resin-laminated foam Download PDF

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Publication number
TW201012649A
TW201012649A TW098125699A TW98125699A TW201012649A TW 201012649 A TW201012649 A TW 201012649A TW 098125699 A TW098125699 A TW 098125699A TW 98125699 A TW98125699 A TW 98125699A TW 201012649 A TW201012649 A TW 201012649A
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Taiwan
Prior art keywords
polyolefin
foam
resin
layer
based resin
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Application number
TW098125699A
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Chinese (zh)
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TWI461296B (en
Inventor
Koichi Ishikawa
Takeshi Aoki
Takashi Nishimoto
Takashi Muroi
Satoshi Iwasaki
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Jsp Corp
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Publication of TWI461296B publication Critical patent/TWI461296B/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/22Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by the presence of two or more layers which are next to each other and are fibrous, filamentary, formed of particles or foamed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/06Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/065Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of foam
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2266/00Composition of foam
    • B32B2266/02Organic
    • B32B2266/0214Materials belonging to B32B27/00
    • B32B2266/025Polyolefin
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/18Layered products comprising a layer of synthetic resin characterised by the use of special additives

Landscapes

  • Laminated Bodies (AREA)
  • Buffer Packaging (AREA)
  • Packaging Frangible Articles (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

This objective of the invention relates to a polyolefin resin-laminated foam capable of being applied to a packaging material that is suitable for precision electronic equipment like electronic appliances, precision machines, circuit base plates, silicon semi-conductors, and glass substrates for display and capable of providing excellent washing performance to contaminant transferred on the precision electronic equipment while using water or a cloth containing water to wipe and rinse the contaminant on the surface of the precision electronic equipment. The characteristics of the polyolefin resin-laminated foam are that: the polyolefin resin-laminated foam formed by the polyolefin resin layer is laminated on at least one surface of the polyolefin resin foam layer; more than one hydrophilic compound is selected from a poly epoxide and a surfactant which the HLB (hydrophilic lipophilic balance) value is above 8, and for 100 percent by weight of polyolefin resin that forms the resin layer in the polyolefin resin layer, the aforementioned hydrophilic compound is not actually added into the aforementioned polyolefin resin-laminated foam while simultaneously adding under a ratio between 0.5 and 20 weight percentage.

Description

201012649 六、發明說明: 【發明所屬之技術領域】 本發明係關於聚烯烴系樹脂層合發泡體,詳細爲可作 爲電子製品、精密機器、電路基盤、矽半導體、顯示器用 玻璃基板等電子精密機器之緩衝材、包裝材適用之聚烯烴 系樹脂層合發泡體。 ©【先前技術】 過去的聚烯烴系樹脂壓出發泡薄片爲富有柔軟性及緩 衝性,因可防止被包裝物之損傷、刮傷,故廣泛使用於家 電製品、玻璃器具、陶器等包裝材料。且,近年來隨著薄 型電視之開發、需求之擴大,因聚烯烴系樹脂壓出發泡薄 片成爲作爲顯示器用玻璃基板之包裝材料使用,新技術課 題被創出,對於該壓出發泡薄片進行種種技術改良。作爲 如此發泡薄片,例如專利文獻1所記載之玻璃基板用間紙 ❹ [專利文獻1]特開2007_262409號公報 【發明內容】 [發明所要解決的課題] 前述顯示器用玻璃基板等電子精密機器被要求非常高 水準之表面清淨性。然而,作爲該玻璃基板之包裝材料使 用前述壓出發泡薄片時,使用於壓出發泡薄片製造之添加 劑或原材料所引起的滲漏物質會於壓出發泡薄片表面上滲 -5- 201012649 漏,該滲漏物質會轉印至電子精密機器,有著污染到電子 精密機器表面之疑慮。又’因壓出發泡薄片容易蓄積靜電 而帶電,故有著將空氣中之塵埃吸引至壓出發泡薄片表面 之性質,以壓出發泡薄片包裝電子精密機器時,該吸引之 塵埃議會轉印製電子精密機器,有著污染到電子精密機器 表面之疑慮。 另一方面,電子精密機器之情況時,欲提高其表面清 淨性,取出壓出發泡薄片等包裝材料後的表面洗淨步驟爲 不可欠缺,該表面洗淨步驟中,將電子精密機器表面以水 洗淨、或以含有水之薄片擦拭時,可除去附著之塵、埃、 滲漏物質等污染物。因此,即使於電子精密機器附著前述 污染物,僅以水洗淨等即可除去,可保持電子精密機器表 面之清淨性。然而,依污染物之種類、洗淨方法,污染物 之除去有時並不充分,此爲造成電子精密機器之製品不良 的原因。 藉由如此發泡薄片所造成之電子精密機器等的表面污 染之課題並未充分地被解決。 本發明係以提供一種可作爲電子製品、精密機器、電 路基盤、矽半導體、顯示器用玻璃基板等精密電子機器之 包裝材料適用者,即使於精密電子機器轉印污染物,於水 洗、或含有水之布擦拭等精密電子機器表面的污染物質洗 淨時可賦予優良洗淨性能之聚烯烴系樹脂層合發泡體爲目 的。 201012649 [解決課題之手段] 本發明者等發現將親水親油平衡(HLB値)8〜20的 親水性化合物含於聚烯烴系樹脂發泡體時,於後步驟不可 欠缺的洗淨步驟中,對於精密電子機器之藉由水等洗淨性 會提高,即使轉印電子精密機器於過去以簡易洗淨難以洗 淨之污染物,僅以水等進行洗淨即可容易地除去》然而, 因同時該親水性化合物與聚烯烴系樹脂之相溶性不佳,故 雖可製造發泡體,但發泡性降低使得製造難度提高,產生 新課題,且親水性化合物一般爲低分子量,故依該添加量 發泡體本身的機械性強度亦會有降低之新課題產生。 特別爲發泡體作爲液晶顯示器用之玻璃基板的間紙使 用時,因要求充分之韌性強度,故於發泡體添加親水性化 合物時,欲補足韌性強度,必須進行需提高外觀密度等等 處理。 另一方面,欲提高藉由親水性化合物之洗淨性,親水 性化合物無須含於發泡體全體,接觸於被包裝物之發泡體 表面附近,含有可發揮洗淨性之程度的量之親水性化合物 即足夠。因此,本發明者等於發泡體表面設置非發泡樹脂 層,於該樹脂層嘗試添加親水性化合物,完成本發明。 本發明爲提供以下所示聚烯烴系樹脂層合發泡體。 [1] 一種聚烯烴系樹脂層合發泡體,其爲於聚烯烴系樹 脂發泡體層之至少一面上,層合聚烯烴系樹脂層所成之聚 烯烴系樹脂層合發泡體,其特徵爲將選自聚環氧化物及親 水親油平衡(HLB値)8以上之界面活性劑的1種以上之 201012649 親水性化合物,於前述聚烯烴系樹脂層中對於構成該樹脂 層之聚烯烴系樹脂1〇〇重量份而言,以0.5〜20重量份之 比率下添加之同時, 實質於前述聚烯烴系樹脂發泡體層未添加前述親水性 化合物。 [2] 如前述1所記載的聚烯烴系樹脂層合發泡體,其中 前述聚環氧化物爲聚環氧乙烷。 [3] 如前述1或2所記載的聚烯烴系樹脂層合發泡體, 其中前述聚環氧化物於溫度20°C爲液狀。 [4] 如前述1〜3中任一項所記載的聚烯烴系樹脂層合 發泡體,其中前述親水性化合物之數平均分子量爲100 0 以下。 [5] 如前述1〜4中任一項所記載的聚烯烴系樹脂層合 發泡體,其中於前述聚烯烴系樹脂層添加聚烯烴系樹脂與 前述親水性化合物之相溶化劑。 [6] 如前述1〜5中任一項所記載的聚烯烴系樹脂層合 發泡體,其中對聚烯烴系樹脂層合發泡體之前述親水性化 合物的添加量,對該層合發泡體100重量份而言爲2重量 份以下。 [7] 如前述1〜6中任一項所記載的聚烯烴系樹脂層合 發泡體,其中前述聚烯烴系樹脂發泡體層爲壓出發泡體, 外觀密度爲10〜200g/L,厚度爲0.2〜2mm。 [8] 如前述7所記載的聚烯烴系樹脂層合發泡體,其中 前述聚烯烴樹脂層藉由共壓出於聚烯烴系樹脂發泡體層進 -8- 201012649 行層合者。 [9] 如前述1〜8中任一項所記載的聚烯烴系樹脂層合 發泡體,其中於前述聚烯烴系樹脂層,將高分子型防帶電 劑對於聚烯烴系樹脂100重量份以2〜30重量份的比率添 加,該樹脂層之表面電阻率爲lxlO8〜1χ1014(Ω)。 [10] 如前述9所記載的聚烯烴系樹脂層合發泡體,其 中前述高分子型防帶電劑係以聚醚與聚烯烴之嵌段共聚物 作爲主成分的防帶電劑。 [發明效果] 本發明的聚烯烴系樹脂層合發泡體因以特定量添加選 自環氧化物及親水親油平衡(HLB値)8以上的界面活性 劑之1種以上的親水性化合物,藉由層合發泡體,即使塵 、埃、滲漏物質等污染物轉印至電子製品、精密機器、電 路基盤、矽半導體、顯示器用玻璃基板等電子精密機器表 面時,藉由該化合物與污染物同時轉印至電子精密機器表 面,僅將電子精密機器經水洗淨、或以含有水之薄片擦拭 等簡易洗淨,即可容易將污染物與該親水性化合物同時除 去。特別爲轉印至電子精密機器表面時,即使鈉離子等金 屬離子或寡聚物質等洗淨困難的污染物由層合發泡體轉印 至電子精密機器表面,僅存在該親水性化合物即可藉由簡 易洗淨由電子精密機器表面容易地除去。 且,本發明的聚烯烴系樹脂層合發泡體中,親水性化 合物雖添加於樹脂層,但實質上未添加於發泡體層,故親 -9- 201012649 水性化合物不會阻礙發泡性,故所得之層合發泡體具有優 良之機械性強度。 [實施發明的最佳型態] 以下對於本發明之聚烯烴系樹脂層合發泡體作詳細說 明。 本發明的聚烯烴系樹脂層合發泡體(以下亦可僅稱爲 層合發泡體)爲,聚烯烴系樹脂發泡體層(以下亦可僅稱 爲發泡體層)、與該發泡體層的至少一面上經層合之聚烯 烴系樹脂層(以下亦僅稱爲樹脂層)所成之層合體。 本發明之構成層合發泡體的發泡體層係將聚烯烴系樹 脂作爲基材樹脂之發泡體。 該聚烯烴系樹脂爲烯烴成分單位爲50莫耳%以上之樹 脂。作爲該聚烯烴系樹脂,可舉出聚乙烯系樹脂、聚丙烯 系樹脂等。聚烯烴系樹脂因表面硬度低,柔軟性優良,於 被包裝體之表面保護上爲優良故較佳,特別爲聚乙烯系樹 脂更具有優良之柔軟性,於被包裝體之表面保護性更優良 故較佳。 作爲前述聚乙烯系樹脂,例如爲乙烯成分單位爲50 莫耳%以上之樹脂,可舉出高密度聚乙烯、低密度聚乙烯 、直鏈狀低密度聚乙烯、乙烯-乙酸乙烯共聚物、乙烯-丙 烯共聚物、乙烯-丙烯-丁烯-1共聚物、乙烯-丁烯-1共聚 物、乙烯-己烯-1共聚物、乙烯-4-甲基戊烯-1共聚物、乙 烯-辛烯-1共聚物,進一步可舉出彼等2種以上之混合物 -10- 201012649 等。 這些聚乙烯系樹脂中,若考慮到發泡性,以密度爲 93 5 g/L以下之聚乙烯系樹脂作爲主成分者爲佳。具體而言 使用低密度聚乙烯、直鏈狀低密度聚乙烯等爲佳,發泡性 特良好的低密度聚乙烯爲較佳。 且,將密度爲93 5 g/L以下之聚乙烯系樹脂作爲「主 成分」時,該聚乙烯樹脂之含有量爲發泡體層全重量的50[Technical Field] The present invention relates to a polyolefin-based resin laminated foam, which is specifically capable of being used as an electronic product, a precision machine, a circuit substrate, a germanium semiconductor, a glass substrate for a display, and the like. A polyolefin-based resin laminated foam suitable for cushioning materials and packaging materials for machines. © [Prior Art] Conventional polyolefin-based resin extruded foamed sheets are widely used for packaging materials such as household electrical appliances, glassware, and ceramics because they are flexible and cushioned, and can prevent damage or scratches of the packaged articles. In addition, in recent years, with the development of thin-type televisions and the increase in demand, the foamed sheet of polyolefin-based resin has been used as a packaging material for a glass substrate for display, and new technical issues have been created. Various techniques for the extruded foamed sheet have been made. Improvement. In the case of the above-mentioned foamed sheet, for example, the glass substrate for a glass substrate is disclosed in the above-mentioned Japanese Patent Application Laid-Open Publication No. 2007-262409. A very high level of surface cleanliness is required. However, when the above-mentioned extruded foamed sheet is used as the packaging material of the glass substrate, the leakage material caused by the additive or the raw material used for the extrusion of the foamed sheet may leak on the surface of the extruded foamed sheet, which is leaked to the surface of the foamed sheet. The leaking material is transferred to an electronic precision machine, which has the concern of contaminating the surface of the electronic precision machine. In addition, since it is easy to accumulate static electricity and is charged by the extruded foam sheet, it has the property of attracting dust in the air to the surface of the foamed sheet, and when the foamed sheet is pressed to package an electronic precision machine, the attracted dust is printed by the assembly board. Precision machines have the suspicion of contaminating the surface of electronic precision machines. On the other hand, in the case of an electronic precision machine, in order to improve the surface cleansing property, the surface cleaning step after taking out a packaging material such as a foamed sheet is indispensable, and in the surface cleaning step, the surface of the electronic precision machine is made of water. When it is washed or wiped with a sheet containing water, it can remove contaminants such as dust, worms, and leaking substances. Therefore, even if the contaminant adheres to the electronic precision machine, it can be removed only by washing with water or the like, and the surface of the electronic precision machine can be cleaned. However, depending on the type of the contaminant and the cleaning method, the removal of the contaminant is sometimes insufficient, which is a cause of defective products of the electronic precision machine. The problem of surface contamination of an electronic precision machine or the like caused by such a foamed sheet is not sufficiently solved. The present invention provides a packaging material which can be used as a packaging material for a precision electronic device such as an electronic product, a precision machine, a circuit substrate, a germanium semiconductor, or a glass substrate for a display, and even if it is transferred to a precision electronic device, it is washed with water or contains water. It is intended to provide a polyolefin-based resin laminated foam which is excellent in cleaning performance when the contaminant on the surface of a precision electronic device is cleaned by wiping the cloth. 201012649 [Means for Solving the Problems] The present inventors have found that when a hydrophilic compound having a hydrophilic-lipophilic balance (HLB値) of 8 to 20 is contained in a polyolefin-based resin foam, in the washing step which is indispensable in the subsequent step, In the case of a precision electronic device, the water-repellent property is improved, and even if the transfer-precision precision machine has been used to clean the difficult-to-clean contaminants in the past, it can be easily removed by washing with water or the like. At the same time, since the hydrophilic compound and the polyolefin resin have poor compatibility, the foam can be produced, but the foaming property is lowered to make the production difficult, and a new problem arises, and the hydrophilic compound generally has a low molecular weight. A new problem in which the mechanical strength of the foam itself is also reduced is also reduced. In particular, when the foam is used as a paper for a glass substrate for a liquid crystal display, since sufficient toughness is required, when a hydrophilic compound is added to the foam, it is necessary to increase the toughness strength, and it is necessary to increase the appearance density and the like. . On the other hand, in order to improve the detergency of the hydrophilic compound, the hydrophilic compound does not need to be contained in the entire foam, and is in contact with the vicinity of the surface of the foam of the packaged product, and contains an amount capable of exhibiting detergency. A hydrophilic compound is sufficient. Therefore, the inventors of the present invention have set a non-foamed resin layer on the surface of the foam, and attempted to add a hydrophilic compound to the resin layer to complete the present invention. The present invention provides the polyolefin-based resin laminated foam shown below. [1] A polyolefin-based resin laminated foam which is obtained by laminating a polyolefin-based resin layer on at least one surface of a polyolefin-based resin foam layer, One or more of the 201012649 hydrophilic compounds selected from the group consisting of a polyepoxide and a surfactant having a hydrophilic-lipophilic balance (HLB値) of 8 or more, and a polyolefin constituting the resin layer in the polyolefin-based resin layer The 1 part by weight of the resin is added in a ratio of 0.5 to 20 parts by weight, and the hydrophilic compound is not added to the polyolefin-based resin foam layer. [2] The polyolefin-based resin laminated foam according to the above 1, wherein the polyepoxide is polyethylene oxide. [3] The polyolefin-based resin laminated foam according to the above 1 or 2, wherein the polyepoxide is in a liquid state at a temperature of 20 °C. [4] The polyolefin-based resin laminated foam according to any one of the above-mentioned, wherein the hydrophilic compound has a number average molecular weight of 100 or less. [5] The polyolefin-based resin laminated foam according to any one of the above-mentioned first aspect, wherein a polyolefin-based resin and a compatibilizing agent of the hydrophilic compound are added to the polyolefin-based resin layer. [6] The polyolefin-based resin laminated foam according to any one of the above-mentioned 1 to 5, wherein the amount of the hydrophilic compound added to the polyolefin-based resin laminated foam is The foam is 2 parts by weight or less in terms of 100 parts by weight. The polyolefin-based resin laminated foam according to any one of the above-mentioned, wherein the polyolefin-based resin foam layer is an extruded foam having an apparent density of 10 to 200 g/L. It is 0.2~2mm. [8] The polyolefin-based resin laminated foam according to the above-mentioned item 7, wherein the polyolefin resin layer is laminated by a pressure-bonding of the polyolefin-based resin foam layer to -8 to 201012649. The polyolefin-based resin laminated foam according to any one of the above-mentioned first aspect, wherein the polymer-based antistatic agent is 100 parts by weight of the polyolefin-based resin. When the ratio is 2 to 30 parts by weight, the surface resistivity of the resin layer is 1 x 10 8 to 1 χ 1014 (Ω). [10] The polyolefin-based resin laminated foam according to the above-mentioned item 9, wherein the polymer type antistatic agent is an antistatic agent containing a block copolymer of a polyether and a polyolefin as a main component. [Effect of the Invention] The polyolefin-based resin laminated foam of the present invention is one or more kinds of hydrophilic compounds selected from the group consisting of an epoxide and a surfactant having a hydrophilic-lipophilic balance (HLB値) of 8 or more, in a specific amount. By laminating the foam, even if contaminants such as dust, worms, and leaking substances are transferred to the surface of an electronic precision machine such as an electronic product, a precision machine, a circuit substrate, a semiconductor, or a glass substrate for display, The contaminants are simultaneously transferred to the surface of the electronic precision machine, and the electronic precision machine can be easily removed by simultaneously washing the water or washing it with a sheet containing water to easily remove the contaminants and the hydrophilic compound. In particular, when transferring to the surface of an electronic precision machine, even if a contaminant that is difficult to clean such as metal ions or oligomers such as sodium ions is transferred from the laminated foam to the surface of the electronic precision machine, only the hydrophilic compound can be present. It is easily removed by the surface of the electronic precision machine by simple cleaning. Further, in the polyolefin-based resin laminated foam of the present invention, the hydrophilic compound is added to the resin layer, but is not substantially added to the foam layer. Therefore, the aqueous compound of the parent--9-201012649 does not inhibit the foaming property. Therefore, the obtained laminated foam has excellent mechanical strength. [Best Mode of Carrying Out the Invention] The polyolefin-based resin laminated foam of the present invention will be described in detail below. The polyolefin-based resin laminated foam of the present invention (hereinafter may be simply referred to as a laminated foam) is a polyolefin-based resin foam layer (hereinafter may be simply referred to as a foam layer), and the foaming A laminate of a polyolefin resin layer (hereinafter also referred to simply as a resin layer) laminated on at least one surface of the bulk layer. In the foam layer constituting the laminated foam of the present invention, a polyolefin resin is used as a foam of a base resin. The polyolefin resin is a resin having an olefin component of 50 mol% or more. Examples of the polyolefin resin include a polyethylene resin and a polypropylene resin. The polyolefin resin is excellent in surface hardness and excellent in flexibility, and is excellent in surface protection of the packaged body. In particular, the polyethylene resin has excellent flexibility and is excellent in surface protection of the packaged body. Therefore, it is better. The polyethylene-based resin is, for example, a resin having an ethylene component of 50 mol% or more, and examples thereof include high-density polyethylene, low-density polyethylene, linear low-density polyethylene, ethylene-vinyl acetate copolymer, and ethylene. - propylene copolymer, ethylene-propylene-butene-1 copolymer, ethylene-butene-1 copolymer, ethylene-hexene-1 copolymer, ethylene-4-methylpentene-1 copolymer, ethylene-octane Further, the ene-1 copolymer may be a mixture of two or more thereof, such as -10-201012649. Among these polyethylene resins, a polyethylene resin having a density of 93 5 g/L or less is preferably used as a main component in consideration of foamability. Specifically, a low-density polyethylene or a linear low-density polyethylene is preferred, and a low-density polyethylene having excellent foaming properties is preferred. When the polyethylene resin having a density of 93 5 g/L or less is used as the "main component", the content of the polyethylene resin is 50% of the total weight of the foam layer.

0 重量%以上。又,聚乙烯系樹脂之密度下限大約爲890g/L 〇 又,作爲前述聚丙烯系樹脂,可舉出丙烯單獨聚合物 、或與可與丙烯共聚合之其他烯烴等成分的共聚物。作爲 可與丙嫌共聚合之其他烯烴,例如可舉出乙烯、或1-丁烯 、異丁烯、1-戊烯、3-甲基-1-丁烯、1-己烯、3,4-二甲基-1-丁烯、1-庚烯、3-甲基-1-己烯等碳數4〜10之α-烯烴。 又,前述共聚物可爲無規共聚物或嵌段共聚物等,且不僅 φ 爲二元共聚物亦可爲三元共聚物。且,前述共聚物中之與 丙烯可共聚合之其他成分以25重量%以下,特別以1 5重 量%以下的比率下含有爲佳。且,作爲該可共聚合之其他 成分的含有量之下限値,考慮到選則共聚物之理由等大槪 爲0.3重量%。又,這些聚丙烯系樹脂可混合、2種以上 使用。 又,前述聚烯烴系樹脂之融點大槪爲100〜170°c。該 聚烯烴系樹脂之融點可依據JIS K7 121-1987之方法進行測 定。即,藉由JIS K7121-1987中之試驗片的狀態調節(2 -11 - 201012649 )之條件(但,冷卻速度爲10°C /分鐘)進行前處理,藉 由以l〇C /分鐘進行昇溫’得到融解波峰。所得之融解波 峰頂點的溫度作爲融點。且’融解波峰出現2個以上時, 將主融解波峰(面積最大的波峰)頂點溫度作爲融點。且 ’具有對於具有最大面積之波峰的波峰面積之8〇 %以上的 波峰面積之波峰另外存在時’該波峰之頂點溫度與最大面 積之波峰頂點的溫度之相加平均値作爲融點。 本發明中之聚烯烴系樹脂中,以不阻礙本發明中之發 泡體層的目的及效果之範圍下,可添加聚苯乙烯等苯乙烯 系樹脂、乙烯丙烯橡膠等彈性體、聚丁烯等丁烯系樹脂等 。此時的添加量以40重量%以下爲佳,以25重量%以下 爲較佳,以1 0重量%以下爲特佳。 又,聚烯烴系樹脂中以不阻礙本發明之目的效果的範 圍下,例如可含有氣泡調整劑、造核劑、抗氧化劑、熱安 定劑、耐候劑、紫外線吸收劑、難燃劑、抗菌劑、收縮防 止劑等功能性添加劑、無機塡充劑等添加劑。 本發明的層合發泡體之厚度並無特別限制,但發泡體 層爲壓出發泡體時,其厚度大槪爲0·2〜l〇〇mm,若爲薄 片狀時大槪爲0.2〜20mm。且,薄片狀壓出發泡體之厚度 過薄時,對於電子精密機器之緩衝性、表面保護性會不足 ’厚度過厚時,對電子精密機器之積載量會有損失。由此 觀點來看,薄片狀壓出發泡體之厚度爲0.2〜2.0mm,以 0.2〜1.5mm爲佳,較佳爲 0.3〜1 · 0mm,特佳爲 0.3〜 0.7mm 〇 -12- 201012649 本發明的層合發泡體之外觀密度較佳爲10〜200g/L。 發泡體層爲壓出發泡體時的層合發泡體外觀密度較佳爲10 〜200g/L,更佳爲15〜180g/L,特佳爲20〜100g/L。層合 發泡體之外觀密度過高時,有著表面保護性降低之疑慮。 另一方面,該外觀密度過低時,於層合發泡體所望保形性 或壓縮強度等機械性強度會有降低之疑慮。特別爲層合發 泡體爲薄片狀時,與下垂関連之韌性強度有著降低之疑慮 φ 。且,由前述表面保護性之觀點來看,層合發泡體之外觀 密度爲150g/L以下爲佳,較佳爲120g/L以下,更佳爲 100g/L以下。又,韌性強之發泡薄片以單方固定之樑支持 時的下垂最小者,由如此觀點來看,該外觀密度以20g/L 以上爲佳,較佳爲30g/L以上,更佳爲40g/L以上。 又,發泡體層爲薄片狀壓出發泡體時,層合發泡體的 秤量以10〜80g/m2爲佳,較佳爲12〜60g/m2,更佳爲15 〜5 0g/m2,特佳爲20〜40g/m2。該坪量僅爲1 Og/m2以上 φ ,即可確保韌性強度,僅爲80g/m2以下不會造成過度提 高成本。 本發明中之層合發泡體全體之厚度,於層合發泡體全 寬度下,於寬方向以1cm間隔進行測定所得之厚度(mm )的算術平均値。 本發明中之層合發泡體的外觀密度爲,由層合發泡體 所切出之試驗片的重量(g)除以由該試驗片之外形尺寸 求得之體積(cm3)所得値作爲單位換算(g/L)。 又,前述發泡體層爲壓出發泡體時,該平均氣泡徑由 -13- 201012649 發泡體層之伸縮等機械性物性、外觀、表面平滑性、被包 裝物之表面保護性等觀點來看,壓出方向及寬方向之平均 氣泡徑同時爲0.2〜0.8 mm爲佳,較佳爲0.3〜0.7mm,更 佳爲0.4〜0.6mm» 前述發泡體層之平均氣泡徑爲,將發泡體層於寬方向 、及與寬方向呈垂直的壓出方向進行切斷,依據所出現的 截面進行測定。具體而言,於發泡體層之寬方向截面擴大 照片,拉出將發泡體層之厚度分爲2等分之長度30mm( 考慮到擴大照片之擴大率,3 0mm乘上擴大率的長度線分 )的中心線,求得與該線分交叉的氣泡數(η)。依據線 分之長度30mm與所求之氣泡數(η),將寬方向之氣泡 徑平均値由30/(η-1)之計算式求得。將同樣操作於發泡 體層的其他寬方向截面,重複計算5處之寬方向氣泡徑並 求得其平均値,將這些算術平均値作爲發泡體層之寬方向 中之平均氣泡徑。又,依據發泡體層的壓出方向截面擴大 照片進行測定以外,與寬方向之平均氣泡徑的測定方法同 樣求得之値,作爲發泡體層的壓出方向中之平均氣泡徑。 本發明的聚烯烴系樹脂層合發泡體中,於前述發泡體 層之至少一面層合聚烯烴系樹脂層。 本發明中構成樹脂層之聚烯烴系樹脂、添加於此的其 他樹脂或添加劑等與前述對於發泡體層所述者同様。但, 發泡體層與樹脂層之構成並非必須相同,兩者僅可層合即 可,前述聚烯烴系樹脂之範疇中可採用相異構成。 該樹脂層之秤量爲每一面〇.5g/m2以上爲佳,較佳爲 201012649 0.7g/m2以上,更佳爲lg/m2以上。該樹脂層之秤量僅爲 前述範圍內,可充分地發揮所望洗淨性。由洗淨性觀點來 看,秤量上限並未受到限制,但由緩衝性或輕量性的觀點 來看,該上限以l〇〇g/m2以下爲佳,較佳爲60g/m2,更佳 爲50g/m2以下。特別爲樹脂層藉由共壓出形成時,因可 使樹脂層的厚度變薄,故樹脂層之秤量以0.5〜10g/m2爲 佳,較佳爲0.7〜5g/m2,更佳爲1〜3g/m2。 φ 又,樹脂層之厚度均勻爲佳,但僅可達到本發明之目 的、效果的範圍內即可,厚度不均亦可。本發明中,前述 樹脂層之秤量可由以下2種方法之任一而求得。 秤量測定的第1方法中,將層合發泡體之垂直截面以 顯微鏡等作適宜擴大,將樹脂層厚度於等間隔下,於寬方 向測定10點,所得之算術平均値作爲樹脂層之平均厚度 ,該平均厚度乘上構成樹脂層之基材樹脂的密度,以單位 換算下求得樹脂層之秤量[g/m2]。但,該方法僅限定於樹 φ 脂層與發泡層之界面爲明確之情況。 秤量測定之第2方法中,層合發泡體藉由共壓出而製 造時,製造層合發泡體時,壓出發泡條件內,由樹脂層之 吐出量X[kg/時]、與所得之層合發泡體的幅W[m]、層合 發泡體每單位時間的長度L[m/時],以以下(1 )式可求得 樹脂層之秤量[g/m2]。且,於發泡體層之雙面’層合樹脂 層時,由各樹脂層之吐出量可求得各樹脂層之秤量。 秤量4/1112] = [1000又/(1>'^)]..*(1) 本發明的層合發泡體中,因前述樹脂層含有特定親水 -15- 201012649 性化合物,故將樹脂層側面向被包裝體進行包裝時’即使 由樹脂層將塵、埃、滲漏物質等污染物轉印至電子製品、 精密機器、電路基盤、矽半導體、顯示器用玻璃基板等電 子精密機器表面時,藉由該親水性化合物與污染物同時轉 印至電子精密機器表面,僅將電子精密機器藉由水洗淨、 或以含有水之薄片擦拭等簡易洗淨,即可將污染物與該親 水性化合物同時容易地除去。特別爲鈉離子等金屬離子或 寡聚物質等洗淨困難,必須進行嚴密洗淨始能除去的污染 物,即使由樹脂層轉印至電子精密機器表面,因該親水性 化合物的存在下僅進行簡易洗淨,即可將這些污染物由電 子精密機器表面容易地除去。 添加於樹脂層之親水性化合物係選自聚環氧化物及 HLB値爲8以上的界面活性劑之1種以上化合物。 且,對於本發明的樹脂層可添加如後述之高分子型防 帶電劑,該高分子型防帶電劑有時含有聚環氧化物等。但 含於高分子型防帶電劑之聚環氧化物等爲作爲共聚物成分 等而少量含於高分子型防帶電劑,其爲使用於提高防帶電 性。該高分子型防帶電劑中之聚環氧化物等於本發明中, 與作爲親水性化合物添加於樹脂層的聚環氧化物等添加量 相比較極微量,並非可影響到本發明所特定之該親水性化 合物的添加量範圍之量,無法期待可達到本發明目的、效 果之被包裝物的洗淨性之提高效果。 作爲構成前述聚環氧化物(poly alkylene oxide)之 環氧化物爲碳數2〜6之環氧化物,例如可舉出環氧乙烷 -16- 201012649 (乙二醇)、環氧丙烷(丙二醇)、1,2-環氧丁烷、1,4· 環氧丁烷、2,3-環氧丁烷、1,3-環氧丁烷、環氧丁烷(丁 二醇)、環氧戊烷(戊二醇)、環氧己烷(己二醇)等。 作爲聚環氧化物可倂用2種以上之環氧化物。 聚環氧化物中由容易獲得、容易處理之觀點來看’以 聚環氧乙烷(聚乙二醇)爲佳。 本發明中之HLB値可配合該親水性化合物之型態, φ 如下述,以周知方法之Atlas法、或Griffin’s法求得。0% by weight or more. In addition, the lower limit of the density of the polyethylene-based resin is approximately 890 g/L. Further, the polypropylene-based resin may be a copolymer of a propylene single polymer or a component other than a olefin copolymerizable with propylene. Examples of other olefins copolymerizable with propylene include ethylene, or 1-butene, isobutylene, 1-pentene, 3-methyl-1-butene, 1-hexene, and 3,4-di. An α-olefin having 4 to 10 carbon atoms such as methyl-1-butene, 1-heptene or 3-methyl-1-hexene. Further, the copolymer may be a random copolymer or a block copolymer, and not only φ may be a binary copolymer or a ternary copolymer. Further, it is preferred that the other component copolymerizable with propylene in the copolymer is contained in an amount of 25% by weight or less, particularly preferably 15% by weight or less. Further, the lower limit of the content of the other component which can be copolymerized is about 0.3% by weight in consideration of the reason for selecting the copolymer. Further, these polypropylene resins may be used in combination of two or more kinds. Further, the polyolefin resin has a melting point of 100 to 170 ° C. The melting point of the polyolefin resin can be measured in accordance with the method of JIS K7 121-1987. Namely, pretreatment was carried out by the condition adjustment of the test piece (2-11 - 201012649) in JIS K7121-1987 (however, the cooling rate was 10 ° C / min), and the temperature was raised by l 〇 C / min. 'Get the melting peak. The temperature of the resulting peak of the melting peak is used as the melting point. When there are two or more melting peaks, the peak temperature of the main melting peak (the peak with the largest area) is used as the melting point. And the sum of the peaks of the peak areas of the peak area of 8 〇 % or more with respect to the peak area having the largest area is the sum ’ of the peak apex temperature of the peak and the peak apex of the maximum area as a melting point. In the polyolefin-based resin of the present invention, a styrene resin such as polystyrene, an elastomer such as ethylene propylene rubber, or polybutene may be added to the extent that the purpose and effect of the foam layer in the present invention are not inhibited. Butylene resin, etc. The amount of addition at this time is preferably 40% by weight or less, more preferably 25% by weight or less, and particularly preferably 10% by weight or less. Further, the polyolefin resin may contain, for example, a bubble regulator, a nucleating agent, an antioxidant, a heat stabilizer, a weathering agent, an ultraviolet absorber, a flame retardant, and an antibacterial agent in a range that does not inhibit the effects of the object of the present invention. Additives such as functional additives such as shrinkage preventive agents and inorganic chelating agents. The thickness of the laminated foam of the present invention is not particularly limited, but when the foam layer is an extruded foam, the thickness is as large as 0·2 to 1 mm, and in the case of a sheet, it is 0.2 to 0.2. 20mm. Further, when the thickness of the sheet-like extruded foam is too small, the cushioning property and the surface protective property of the electronic precision machine may be insufficient. When the thickness is too thick, the amount of load on the electronic precision machine may be lost. From this point of view, the thickness of the flaky extruded foam is 0.2 to 2.0 mm, preferably 0.2 to 1.5 mm, preferably 0.3 to 1 mm, and particularly preferably 0.3 to 0.7 mm 〇-12- 201012649 The laminated foam of the invention preferably has an apparent density of 10 to 200 g/L. The foamed body layer preferably has a density of the laminated foam when the foam is extruded, and is preferably from 10 to 200 g/L, more preferably from 15 to 180 g/L, particularly preferably from 20 to 100 g/L. When the appearance density of the laminated foam is too high, there is a fear that surface protection is lowered. On the other hand, when the apparent density is too low, there is a fear that the mechanical strength such as conformality or compressive strength of the laminated foam is lowered. In particular, when the laminated foam is in the form of a sheet, the strength of the toughness associated with sagging is lowered. Further, from the viewpoint of the surface protective property, the laminated foam preferably has an appearance density of 150 g/L or less, preferably 120 g/L or less, more preferably 100 g/L or less. Further, the foaming sheet having high toughness is minimized when supported by a single-fixed beam. From this viewpoint, the apparent density is preferably 20 g/L or more, preferably 30 g/L or more, more preferably 40 g/ L or more. Further, when the foam layer is a sheet-like extruded foam, the laminated foam is preferably weighed at 10 to 80 g/m2, more preferably 12 to 60 g/m2, still more preferably 15 to 50 g/m2. Good for 20~40g/m2. The flatness is only 1 Og/m2 or more φ, which ensures the toughness strength, and only 80g/m2 or less does not cause excessive cost increase. The thickness of the entire laminated foam in the present invention is an arithmetic mean 厚度 of the thickness (mm) measured at intervals of 1 cm in the width direction over the entire width of the laminated foam. The apparent density of the laminated foam in the present invention is obtained by dividing the weight (g) of the test piece cut out from the laminated foam by the volume (cm3) obtained from the outer shape of the test piece. Unit conversion (g/L). Further, when the foam layer is a pressure-extracted foam, the average cell diameter is from the viewpoints of mechanical properties such as stretching of the foam layer of -13 to 201012649, appearance, surface smoothness, and surface protection of the packaged article. The average bubble diameter in the extrusion direction and the width direction is preferably 0.2 to 0.8 mm, preferably 0.3 to 0.7 mm, more preferably 0.4 to 0.6 mm. The average bubble diameter of the foam layer is such that the foam layer is The width direction and the extrusion direction perpendicular to the width direction are cut, and the measurement is performed according to the cross section that appears. Specifically, the photograph is enlarged in the width direction of the foam layer, and the length of the foam layer is divided into two equal parts and a length of 30 mm (in consideration of the enlargement ratio of the enlarged photograph, the length line of the enlargement ratio of 30 mm by the enlargement ratio) The center line of the line finds the number of bubbles (η) that intersect the line. The average diameter of the bubble diameter in the width direction is determined by the calculation formula of 30/(η-1) according to the length of the line of 30 mm and the number of bubbles (η) sought. The other wide-direction cross-sections of the foam layer were similarly operated, and the wide-direction bubble diameters at five places were repeatedly calculated to obtain the average enthalpy, and these arithmetic mean enthalpies were used as the average bubble diameter in the width direction of the foam layer. Further, the measurement was carried out in the same manner as in the measurement method of the average cell diameter in the width direction, in addition to the measurement of the cross-sectional area in the extrusion direction of the foam layer, and the average cell diameter in the extrusion direction of the foam layer. In the polyolefin-based resin laminated foam of the present invention, a polyolefin-based resin layer is laminated on at least one surface of the foam layer. The polyolefin-based resin constituting the resin layer in the present invention, the other resin or the additive added thereto, and the like are the same as those described above for the foam layer. However, the structure of the foam layer and the resin layer are not necessarily the same, and the two may be laminated only, and the polyolefin resin may be of a different composition. The amount of the resin layer is preferably 55 g/m2 or more per side, preferably 201012649 0.7 g/m2 or more, more preferably lg/m2 or more. The amount of the resin layer to be weighed is within the above range, and the desired detergency can be sufficiently exhibited. From the viewpoint of detergency, the upper limit of the weighing amount is not limited, but from the viewpoint of cushioning property or lightness, the upper limit is preferably 1 g/m 2 or less, preferably 60 g/m 2 , more preferably It is 50 g/m2 or less. In particular, when the resin layer is formed by co-extrusion, since the thickness of the resin layer can be made thin, the amount of the resin layer is preferably 0.5 to 10 g/m2, preferably 0.7 to 5 g/m2, more preferably 1 to 1. 3g/m2. φ Further, the thickness of the resin layer is preferably uniform, but it may be within the range of the object and effect of the present invention, and the thickness may be uneven. In the present invention, the weighing amount of the resin layer can be determined by any of the following two methods. In the first method of weighing measurement, the vertical cross section of the laminated foam is appropriately enlarged by a microscope or the like, and the thickness of the resin layer is measured at 10 points in the width direction at equal intervals, and the arithmetic mean enthalpy obtained is used as the average of the resin layer. The thickness is multiplied by the density of the base resin constituting the resin layer, and the weight of the resin layer [g/m2] is obtained in units of conversion. However, this method is limited only to the case where the interface between the tree φ lipid layer and the foam layer is clear. In the second method of measuring the amount of the laminated foam, when the laminated foam is produced by co-extrusion, when the laminated foam is produced, the amount of discharge from the resin layer X [kg/hour] and The width W [m] of the obtained laminated foam and the length L [m/hr] of the laminated foam per unit time can be determined by the following formula (1) [g/m2]. Further, when the resin layer is laminated on both sides of the foam layer, the amount of each resin layer can be determined by the amount of discharge of each resin layer. Weighing 4/1112] = [1000 again / (1 > '^)]..* (1) In the laminated foam of the present invention, since the resin layer contains a specific hydrophilic -15-201012649 compound, the resin is used. When the side of the layer is packaged on the packaged body, even when the contaminants such as dust, worms, and leaking substances are transferred from the resin layer to the surface of an electronic precision machine such as an electronic product, a precision machine, a circuit board, a semiconductor, or a glass substrate for a display. By transferring the hydrophilic compound and the contaminant to the surface of the electronic precision machine at the same time, the electronic precision machine can be cleaned by water alone or wiped with a sheet containing water to clean the contaminant and the hydrophilic substance. The compound is easily removed at the same time. In particular, it is difficult to wash metal ions or oligomers such as sodium ions, and it is necessary to carry out the cleaning to remove the contaminants which can be removed, even if the resin layer is transferred to the surface of the electronic precision machine, only the hydrophilic compound is present. These contaminants can be easily removed from the surface of an electronic precision machine by simple washing. The hydrophilic compound to be added to the resin layer is one or more compounds selected from the group consisting of polyepoxides and surfactants having 8 or more HLB値. Further, a polymer type antistatic agent to be described later may be added to the resin layer of the present invention, and the polymer type antistatic agent may contain a polyepoxide or the like. However, the polyepoxide or the like contained in the polymer type antistatic agent is contained in a small amount as a copolymer component or the like in a polymer type antistatic agent, and is used for improving the antistatic property. The polyepoxide in the polymer type antistatic agent is equal to the amount of the polyepoxide added to the resin layer as a hydrophilic compound in the present invention, and does not affect the specificity of the present invention. When the amount of the hydrophilic compound added is in the range of the amount, the effect of improving the detergency of the packaged article which can achieve the object and effect of the present invention cannot be expected. Examples of the epoxide having a carbon number of 2 to 6 as the epoxide constituting the polyalkylene oxide include, for example, ethylene oxide-16-201012649 (ethylene glycol) and propylene oxide (propylene glycol). ), 1,2-butylene oxide, 1,4·butylene oxide, 2,3-butylene oxide, 1,3-butylene oxide, butylene oxide (butanediol), epoxy Pentane (pentanediol), hexylene oxide (hexanediol), and the like. Two or more kinds of epoxides can be used as the polyepoxide. Among the polyepoxides, polyethylene oxide (polyethylene glycol) is preferred from the viewpoint of easy availability and easy handling. The HLB(R) in the present invention can be blended with the type of the hydrophilic compound, and φ is obtained by the Atlas method or the Griffin's method known in the art as described below.

Atlas法(親水性化合物型態爲酯系界面活性劑之情 況) HLB = 20 ( 1 -S/A ) S:皂化價 A:構成親水性化合物之脂肪酸的酸價 Griffin’s法(親水性化合物的型態爲酯系界面活性劑 以外的情況) HLB = 2〇x親水基部分之分子量/親水性化合物全體之分 φ 子量 前述HLB値未達8時,洗淨性會不足、或有著附著 於顯示器用玻璃基板等電子精密機器表面的污染物無法容 易除去之疑慮。由該觀點得知,HLB値以10以上爲佳, 15以上爲較佳。且界面活性劑之HLB値的上限爲未達20 〇 本說明書中,對於聚環氧化物之HLB値以Griffin’s 法求得。具體而言,例如聚環氧化物由聚環氧乙烷與以外 的聚環氧化物之共聚物所成時,將聚環氧乙烷視爲親水基 -17- 201012649 部分,對於此以外之聚環氧化物,考慮到其親油親水性, 決定爲親水基部分或疏水基部分,藉由Griffin’s法求得 HLB値。且,聚環氧乙烷的情況爲所有皆爲親水基部分, 故聚環氧化物之HLB値的上限爲20。 作爲前述HLB値爲8以上之界面活性劑,僅HLB値 爲8以上,可使用任何種類之界面活性劑,其中亦以非離 子系界面活性劑的聚環氧化物系界面活性劑爲佳。作爲聚 環氧化物系界面活性劑,以前述聚環氧化物爲主,使用環 氧化物加成型非離子界面活性劑爲佳,作爲該具體例,可 舉出氧化烯烷基醚(例如辛醇環氧乙烷加成物、月桂醇環 氧乙烷加成物、硬脂醇環氧乙烷加成物、油醇環氧乙烷加 成物、月桂醇環氧乙烷環氧丙烷嵌段加成物等);聚氧化 烯高級脂肪酸酯(例如硬脂酸環氧乙烷加成物、月桂酸環 氧乙烷加成物等):聚氧化烯多元醇高級脂肪酸酯(例如 聚乙二醇之月桂酸二酯、聚乙二醇之油酸二酯、聚乙二醇 之硬脂酸二酯等);聚氧化烯烷基苯基醚(例如壬基酚環 氧乙烷加成物、壬基酚環氧乙烷環氧丙烷嵌段加成物、辛 基酚環氧乙烷加成物、雙酚A環氧乙烷加成物、二壬基酚 環氧乙烷加成物、苯乙烯化酚環氧乙烷加成物等);聚氧 化烯烷基胺醚及(例如月桂胺環氧乙烷加成物、硬脂醯胺 環氧乙烷加成物等):聚氧化烯烷基烷醇醯胺(例如羥基 乙基月桂酸醯胺之環氧乙烷加成物、羥基丙基油酸醯胺之 環氧乙烷加成物、二羥基乙基月桂酸醯胺之環氧乙烷加成 物等)。 -18- 201012649 前述親水性化合物中,選自聚環氧化物及HLB値爲8 以上之聚環氧化物系界面活性劑的1種以上之合物爲佳, 以聚環氧化物爲較佳。 本發明中之聚環氧化物爲,溫度20°C下爲液狀者爲佳 。20°C下爲固體的聚環氧化物等可發揮將寡聚物或金屬離 子可藉由水除去時之優良洗淨性,於2(TC爲液狀之聚環氧 化物等由樹脂層更容易滲漏,更容易溶解於水等,故對於 0 難以水等洗淨之寡聚物或金屬離子等污染物可發揮優良之 洗淨性。由該觀點得知,1 〇°c爲液狀者爲佳,於o°c爲液 狀者爲較佳,於-10°c爲液狀者爲更佳,於-20°c爲液狀者 爲特佳。 由相同理由得知,聚環氧化物或前述界面活性劑之數 平均分子量以1 000以下爲佳,較佳爲600以下。又,其 下限大槪爲150。 且,聚環氧化物之數平均分子量可由以酸基價算出之 ❹ 周知方法求得。又,聚環氧化物等數平均分子量難由該羥 基價算出時,使用高溫凝膠滲透層析法求得。 對該樹脂層之親水性化合物的添加量,對於構成該樹 脂層之聚烯烴系樹脂100重量份而言,其爲0.5〜20重量 份之比率。該親水性化合物之添加量未達0.5重量時,其 洗淨性會不足、或有著附著於顯示器用玻璃基板等電子精 密機器表面之污染物不容易除去之疑慮。另一方面,該添 加量超過2 0重量份時,雖由洗淨性來看並無問題,添加 量不僅會影響到洗淨性,添加量過多時,形成樹脂層時親 -19- 201012649 水性化合物會由樹脂層分離,有著無法形成樹脂層自體之 疑慮。由該觀點得知,對於樹脂層之親水性化合物的添加 量,對於構成該樹脂層之聚烯烴系樹脂〖〇〇重量份而言, 1〜15重量份爲佳,較佳1.5〜12重量份,更佳爲2〜10 重量份,特佳爲3〜7重量份之比率。 本發明中之樹脂層中,欲使聚烯烴系樹脂與親水性化 合物融合變佳,且抑制兩者之分離,添加相溶化劑爲佳。 作爲該相溶化劑,可舉出聚烯烴與親水性聚合物之共 聚物等,具體可舉出聚烯烴與聚醚之共聚物等,可使用後 述之高分子型防帶電劑。 本發明中,於前述聚烯烴系樹脂發泡體層中實質上未 添加親水性化合物。實質上未添加表示於發泡層完全未添 加親水性化合物、或即使添加亦不會阻礙發泡性,與無添 加時相比較不會降低機械性強度之添加量,該添加量對於 構成前述發泡體層之聚烯烴系樹脂100重量份而言,其爲 0.4重量份以下(但含有0),較佳爲0.3重量份以下(但 含有〇),更佳爲0.1重量份以下(但含有0),無添加 爲特佳。 且,作爲於發泡層添加親水性化合物之可能性,即使 不用刻意添加,使用回收原料時,結果會有違反本意之添 加情況。 本發明的聚烯烴系樹脂層合發泡體(層合發泡體)如 前述’具有由聚烯烴系樹脂發泡體層(發泡體層)、與層 合於該表面之聚烯烴系樹脂層(樹脂層)所成之多層結構 -20- 201012649 者。進一步樹脂層中,因添加特定量的親水性化合物,故 可發揮優良之洗淨性。另一方面’於發泡體層因實質上未 添加親水性化合物,發泡體層製造時並無因親水性化合物 所引起的發泡性阻礙,可成爲具有優良機械性強度之層合 發泡體。且,添加於樹脂層之親水性化合物因不會阻礙發 泡性,故可增加其添加量濃度,洗淨性與單層發泡體相比 較時更爲提高。且,層合發泡體全體中之親水性化合物的 Φ 添加量即使爲高濃度,因比僅發泡體層的單層結構中之親 水性化合物的添加量還少,故該層合發泡體於同秤量、同 厚度之條件下,與單層發泡體相比較具有同等以上之機械 性強度。 本發明的層合發泡體含有僅於發泡體層單面上層合樹 脂層者、與於兩面層合樹脂層者雙方的形態。於雙面層合 樹脂層時,配合使用用途,親水性化合物可僅添加於單面 、或亦可添加於雙面。本發明的層合發泡體作爲玻璃基板 φ 之間紙使用時,添加親水性化合物之樹脂層係以層合於發 泡體層雙面者爲佳。 由不使層合發泡體之機械性強度降低的觀點來看,層 合發泡體全體中之親水性化合物的添加量對於該層合發泡 體100重量份而言,以2重量份以下者爲佳,較佳爲1.5 重量份以下,更佳爲1重量份以下。 又,本發明之層合發泡體爲,發泡體層中實質上未添 加親水性化合物,故與於發泡體層添加親水性化合物時相 比,層合發泡體之獨立氣泡率可容易維持較高。作爲層合 -21 - 201012649 發泡體之獨立氣泡率,由兼具被包裝物之表面保護性與機 械性強度的觀點來看,以40%以上爲佳,以50%以上爲更 佳。 前述層合發泡體之獨立氣泡率依據 AS TM-D2 8 5 6-7 0 之步驟C,由使用東芝Beckman股份有限公司之空氣比較 式比重計 930型所測定(將由層合發泡體切出 2 5 mm X 2 5mm X 2 0mm之樣品切片放入樣品杯內進行測定。 且,若層合發泡體過薄而無法切出前述尺寸之樣品切片時 ,切出複數片之25mmx25mmX層合發泡體厚度之樣品,藉 由重疊使其成爲25mmx25mmx約20mm之測定用樣品切片 )之層合發泡體(樣品切片)的真體積Vx,經下述(1) 式計算出獨立氣泡率S ( % )。 S(%) = (Vx-W/p)x 100/(Va-W/p) (1)Atlas method (in the case where the hydrophilic compound type is an ester-based surfactant) HLB = 20 ( 1 -S/A ) S: saponification A: acid value of the fatty acid constituting the hydrophilic compound Griffin's method (type of hydrophilic compound) When the state is other than the ester-based surfactant, HLB = 2〇x The molecular weight of the hydrophilic group portion/the total amount of the hydrophilic compound is φ. When the HLB is less than 8, the detergency may be insufficient or may be attached to the display. Contaminants on the surface of electronic precision machines such as glass substrates cannot be easily removed. From this point of view, it is preferable that HLB is preferably 10 or more, and 15 or more is preferable. Further, the upper limit of the HLB of the surfactant is less than 20 〇 In the present specification, the HLB of the polyepoxide is determined by the Griffin's method. Specifically, for example, when the polyepoxide is formed of a copolymer of polyethylene oxide and a polyepoxide other than the polyethylene oxide, the polyethylene oxide is regarded as a hydrophilic group-17-201012649 portion, and the polymerization is further The epoxide, which is determined to be a hydrophilic group or a hydrophobic group in consideration of its hydrophilicity to hydrophilicity, is obtained by Griffin's method. Further, in the case of polyethylene oxide, all of them are hydrophilic groups, so the upper limit of the HLB of the polyepoxide is 20. As the surfactant having an HLB of 8 or more, only HLB値 is 8 or more, and any type of surfactant can be used. Among them, a polyepoxide-based surfactant which is also a nonionic surfactant is preferable. The polyepoxide-based surfactant is preferably a polyepoxide, and an epoxide-added nonionic surfactant is preferred. Specific examples of the polyepoxide-based surfactant include an oxyalkylene alkyl ether (for example, octanol). Ethylene oxide adduct, lauryl alcohol ethylene oxide adduct, stearyl alcohol ethylene oxide adduct, oleyl alcohol ethylene oxide adduct, lauryl alcohol oxide propylene oxide block Adducts, etc.); polyoxyalkylene higher fatty acid esters (such as ethylene glycol adducts of stearic acid, ethylene oxide adducts of lauric acid, etc.): polyoxyalkylene polyols higher fatty acid esters (eg poly Ethylene glycol lauric acid diester, polyethylene glycol oleic acid diester, polyethylene glycol stearic acid diester, etc.; polyoxyalkylene alkylphenyl ether (such as nonylphenol ethylene oxide plus Compound, nonylphenol ethylene oxide propylene oxide block adduct, octylphenol ethylene oxide adduct, bisphenol A ethylene oxide adduct, dinonyl phenol ethylene oxide a product, a styrenated phenol ethylene oxide adduct, etc.; a polyoxyalkylene alkylamine ether and (for example, a laurylamine ethylene oxide adduct, a stearylamine ring) Ethane adduct, etc.): polyoxyalkylene alkyl alkanoate (for example, ethylene oxide adduct of hydroxyethyl laurate decylamine, ethylene oxide adduct of hydroxypropyl oleate decylamine) , an ethylene oxide adduct of dihydroxyethyl lauric acid decylamine, etc.). -18-201012649 Among the above hydrophilic compounds, one or more kinds of polyepoxide-based surfactants having a polyepoxide and an HLB値 of 8 or more are preferable, and a polyepoxide is preferable. The polyepoxide in the present invention is preferably a liquid at a temperature of 20 ° C. A polyepoxide which is solid at 20 ° C can exhibit excellent detergency when an oligomer or a metal ion can be removed by water, and 2 (TC is a liquid polyepoxide or the like by a resin layer. It is easy to leak, and it is more easily dissolved in water. Therefore, it is excellent in the detergency of impurities such as oligomers or metal ions which are difficult to wash by water, etc. From this point of view, 1 〇 °c is liquid. It is preferred that it is liquid at o °c, preferably liquid at -10 °c, and liquid at -20 °c. For the same reason, poly ring The number average molecular weight of the oxide or the above surfactant is preferably 1,000 or less, preferably 600 or less. Further, the lower limit is greater than 150. Further, the number average molecular weight of the polyepoxide can be calculated from the acid base price. Further, when the number average molecular weight of polyepoxide is difficult to be calculated from the hydroxyl value, it is determined by high temperature gel permeation chromatography. The amount of the hydrophilic compound added to the resin layer is The 100% by weight of the polyolefin resin of the resin layer is a ratio of 0.5 to 20 parts by weight. When the amount of the compound added is less than 0.5%, the detergency may be insufficient, or contaminants adhering to the surface of an electronic precision machine such as a glass substrate for a display may not be easily removed. On the other hand, the added amount exceeds 20% by weight. In the case of the detergent, there is no problem in terms of detergency, and the amount of addition not only affects the detergency, but when the amount of addition is too large, when the resin layer is formed, the aqueous compound is separated from the resin layer, and the resin cannot be formed. From the viewpoint of the layer, it is preferable that the amount of the hydrophilic compound added to the resin layer is preferably from 1 to 15 parts by weight based on the weight of the polyolefin resin constituting the resin layer. It is preferably from 1.5 to 12 parts by weight, more preferably from 2 to 10 parts by weight, particularly preferably from 3 to 7 parts by weight. In the resin layer of the present invention, it is preferred to fuse the polyolefin-based resin with a hydrophilic compound, and In order to suppress the separation of the two, it is preferable to add a compatibilizing agent. Examples of the compatibilizing agent include a copolymer of a polyolefin and a hydrophilic polymer, and specific examples thereof include a copolymer of a polyolefin and a polyether, and the like. Rear In the present invention, substantially no hydrophilic compound is added to the polyolefin resin foam layer. Substantially no addition means that no hydrophilic compound is added to the foamed layer, or even if it is added. The foaming property is not impaired, and the amount of mechanical strength is not reduced as compared with the case of no addition. The amount of addition is 0.4 parts by weight or less based on 100 parts by weight of the polyolefin resin constituting the foam layer. However, it contains 0), preferably 0.3 part by weight or less (but contains ruthenium), more preferably 0.1 part by weight or less (but contains 0), and no addition is particularly preferable. Moreover, as a possibility of adding a hydrophilic compound to the foamed layer The use of the recycled raw material may result in a violation of the intention, even if it is not intentionally added. The polyolefin-based resin laminated foam (laminated foam) of the present invention has the above-mentioned 'having a polyolefin-based resin. A multilayer structure of a foam layer (foam layer) and a polyolefin resin layer (resin layer) laminated on the surface -20-201012649. Further, in the resin layer, since a specific amount of the hydrophilic compound is added, excellent detergency can be exhibited. On the other hand, since the foam layer is substantially free of a hydrophilic compound, the foam layer is not hindered by the foaming property due to the hydrophilic compound, and can be a laminated foam having excellent mechanical strength. Further, since the hydrophilic compound added to the resin layer does not inhibit the foaming property, the concentration of the hydrophilic compound can be increased, and the detergency is higher than that of the single-layer foam. Further, even if the amount of addition of the hydrophilic compound in the entire laminated foam is high, the amount of the hydrophilic compound added in the single layer structure of the foam layer is small, so the laminated foam is small. Under the same conditions and the same thickness, it has the same mechanical strength as the single-layer foam. The laminated foam of the present invention contains a form in which both the resin layer is laminated on one side of the foam layer and the resin layer is laminated on both sides. When the resin layer is laminated on both sides, the hydrophilic compound may be added to only one side or may be added to both sides. When the laminated foam of the present invention is used as a paper between glass substrates φ, it is preferred that the resin layer to which the hydrophilic compound is added is laminated on both sides of the foam layer. The amount of the hydrophilic compound added to the entire laminated foam is not more than 2 parts by weight based on 100 parts by weight of the laminated foam, from the viewpoint of not lowering the mechanical strength of the laminated foam. Preferably, it is preferably 1.5 parts by weight or less, more preferably 1 part by weight or less. Further, in the laminated foam of the present invention, since the hydrophilic compound is not substantially added to the foam layer, the closed cell ratio of the laminated foam can be easily maintained as compared with the case where the hydrophilic compound is added to the foam layer. Higher. As a laminate, the closed cell ratio of the foam is preferably 40% or more, and more preferably 50% or more, from the viewpoint of the surface protective properties and the mechanical strength of the packaged article. The independent bubble ratio of the above laminated foam is determined according to ASTM-D2 8 5 6-7 0, step C, using an air comparison type hydrometer 930 type of Toshiba Beckman Co., Ltd. (will be cut by laminated foam) A sample piece of 2 5 mm X 2 5 mm X 2 0 mm was placed in a sample cup for measurement. Further, if the laminated foam was too thin to cut a sample piece of the above size, a 25 mm x 25 mm X laminate of a plurality of pieces was cut out. The sample of the thickness of the foam was superimposed to have a true volume Vx of the laminated foam (sample piece) of the sample for measurement of 25 mm x 25 mm x about 20 mm, and the independent bubble ratio S was calculated by the following formula (1). (%). S(%) = (Vx-W/p)x 100/(Va-W/p) (1)

Vx :前述方法所測定之樣品切片的真體積(cm3 ), 相當於構成樣品切片之樹脂的容積、與樣品切片內之獨立 氣泡部分的氣泡全容積之和。Vx: The true volume (cm3) of the sample slice measured by the above method corresponds to the sum of the volume of the resin constituting the sample slice and the total volume of the bubble of the individual bubble portion in the sample slice.

Va :由測定所使用之樣品切片的外寸所計算之樣品切 片的外觀體積(cm3)。 W :測定所使用之樣品切片全重量(g )。 P :將層合發泡體經脫泡後所求得之樹脂組成物的密 度(g/cm3 ) 本發明之樹脂層中添加高分子型防帶電劑,可將樹脂 層之表面電阻率設定爲lxio8〜1χ1014(Ω)。 -22- 201012649 該表面電阻率過大時,防帶電特性會不足,或於樹脂 層表面會蓄積靜電荷,容易附著塵埃。欲使塵埃不容易附 著,該表面電阻率以5χ1013Ω以下爲佳,以1χ1013Ω以下 爲更佳。另一方面,表面電阻率過小時,雖於防帶電性能 並無問題,但包裝材上所要求之防帶電性能會過剩而有著 成本過高之疑慮。 本說明書中之表面電阻率爲進行下述試驗片的狀態調 φ 節後,依據JIS Κ6271 ( 2001 )進行測定。即,由測定對 象物之層合發泡體所切出之試驗片(縱 lOOmmx橫 lOOmmx厚度:試驗片厚度)於溫度3(TC,相對濕度30% 之環境下放置36小時後,進行試驗片之狀態調節,再依 據JIS K6271 ( 2001 )以外加電壓500kV之條件下開始進 行電壓外加,求得1分鐘後之表面電阻率。 欲使樹脂層之表面電阻率成爲ΙχΙΟ8〜1χ1〇14Ω,於聚 烯烴系樹脂層添加對於聚烯烴系樹脂100重量份而言爲2 φ 〜30重量份比率之高分子型防帶電劑爲佳。該添加量過少 時,有著無法發揮所望防帶電特性之疑慮。另一方面,該 添加量過多時,雖由防帶電性能來看並無問題,但防帶電 性能會到達極限,故成本表現不佳。由該觀點來看,防帶 電劑之添加量以4〜30重量份爲佳,以6〜25重量份爲較 佳。 該防帶電劑之數平均分子量以2000以上爲佳,較佳 爲 2,000 〜100,000,更佳爲 5,000 〜60,000,特佳爲 8,000 〜40,000。因此,該防帶電劑係爲可與由界面活性劑所成 -23- 201012649 之防帶電劑作區別之高分子型防帶電劑。且,該高分子型 之防帶電劑的數平均分子量之上限大槪爲1,〇〇〇,000。高 分子型防帶電劑之數平均分子量於前述範圍時,被包裝體 中放入防帶電劑,不會污染被包裝體表面。 且,前述數平均分子量可使用高溫凝膠滲透層析法求 得。例如高分子型防帶電劑爲將聚醚酯醯胺或聚醚作爲主 成分的親水性樹脂時,將鄰二氯苯作爲溶劑使試料濃度爲 3mg/ml,將聚苯乙烯作爲基準物質以管柱溫度135°C之條 件下進行測定所得之値。且前述溶劑之種類、管柱溫度可 配合高分子型防帶電劑之種類作適宜變更。 作爲本發明所使用之高分子型防帶電劑,可舉出體積 電阻率爲1〇5〜1〇ηΩ· cm之親水性樹脂、及與聚烯烴之 共聚物。 作爲該親水性樹脂,可使用聚醚二醇、聚醚二胺、及 彼等變性物等聚醚,作爲聚醚鏈段形成成分可使用具有聚 醚二醇之鏈段的聚醚酯醯胺,作爲聚醚鏈段形成成分可使 用具有聚醚二醇之鏈段的聚醚醯胺亞胺,作爲聚醚鏈段形 成成分可使用具有聚醚二醇之鏈段的聚醚酯,作爲聚醚鏈 段形成成分可使用具有聚醚二胺之鏈段的聚醚醯胺,作爲 聚醚鏈段形成成分可使用具有聚醚二醇或聚醚二胺之鏈段 的聚醚尿烷等聚醚含有親水性樹脂、分子內具有以非離子 性分子鏈相隔之2〜80個,較佳爲3〜60個之陽離子性基 的陽離子性聚合物、及具有磺醯基之二羧酸與以二醇或聚 醚作爲須構成單位,且分子內具有2〜80個、較佳爲3〜 -24- 201012649 60個之磺醯基的陰離子性聚合物。 又,高分子型防帶電劑中欲得到提高與聚烧烴系樹脂 之相溶性,賦予防帶電效果之同時,藉由添加防帶電劑可 抑制物性降低的效果,與聚烯烴系樹脂爲同種或相溶性高 之聚烯烴系樹脂經嵌段共聚合者爲佳,例如可舉出具有聚 烯烴的嵌段物、與體積電阻率爲105〜ΐ〇1ΐΩ· cm之前述 親水性樹脂的嵌段物經重複交互結合的結構之數平均分子 φ 量(Μη)爲2000〜60000之嵌段共聚物。彼等中亦以聚醚 與聚烯烴之嵌段共聚物(嵌段共聚物)比前述相溶性更優 故較佳。 且,前述聚烯烴之嵌段物與親水性樹脂的嵌段物爲, 具有介著選自酯鍵、醯胺鍵、醚鍵、尿烷鍵、亞胺鍵之至 少1種鍵結經重複交互結合的結構者。 又,作爲高分子型防帶電劑較佳所使用的前述嵌段聚 合物的聚烯烴之嵌段物,聚合物兩末端具有羧基的聚烯烴 • 、聚合物的單末端具有羰基之聚烯烴爲佳。 更詳細爲,作爲如前述之高分子型防帶電劑,可舉出 特開平3-103466號公報、特開2001 -2 78985號公報所記載 的組成物。特開平3 - 103466號公報記載之組成物爲含有 (I) 熱可塑性樹脂、(Π)聚環氧乙烷或50重量%以上 之聚環氧乙烷嵌段物成分的嵌段共聚物、及(III)與前述 (II) 中之聚環氧乙烷嵌段物成分爲固溶的金屬鹽所成者 ,特開200 1 -278985號公報所記載之組成物爲,具有聚烯 cm 烴(a)的嵌段物、與體積電阻率爲ΙχΙΟ5〜ΙχΙΟ^Ω. -25- 201012649 之親水性樹脂(b)的嵌段物,經重複交互結合的結構之 數平均分子量(Μη)爲2000〜60000之嵌段共聚物。前述 (a)的嵌段物與(b)之嵌段物爲,具有介著選自酯鍵、 醯胺鍵、醚鍵、尿烷鍵、亞胺鍵的至少1種的鍵結以重複 交互結合的結構者。作爲如此高分子型防帶電劑,例如可 購得三井· DU PONT POLYCHEMICALS 股份有限公司製 「SD100」、三洋化成工業股份有限公司製 「 PELESTAT300」等商品名。 前述高分子型防帶電劑各可單獨使用,亦可複數組合 後使用。 又,高分子型防帶電劑之融點較佳爲70〜270 °C,更 較佳爲80〜230 °C,特佳爲80〜200 °C,但由防帶電功能表 現性之觀點來看爲佳。 高分子型防帶電劑之融點可由以下JIS K7121(1987 )爲準的方法所測定。即藉由JIS K7121 ( 1987)中之試 驗片的狀態調節(2 )之條件(但,冷卻速度爲1 0°C /分鐘 )進行前處理,藉由1(TC/分鐘之昇溫,得到融解波峰。 將所得之融解波峰的頂點溫度作爲融點。且,融解波峰出 現2個以上時,以最大面積之融解波峰頂點的溫度作爲融 點。 欲達到所期待之表面電阻率,發泡體層中無須添加前 述高分子型防帶電劑,但將層合發泡體之回收原料作爲發 泡體層用原料使用時,添加高分子型防帶電劑時,會使發 泡體層含有高分子型防帶電劑。即使爲此狀況,欲不會阻 -26- 201012649 礙發泡體層之發泡性,高分子型防帶電劑之含有量爲對於 構成發泡體層之聚烯烴系樹脂100重量份而言,以15重 量份以下之比率者爲佳。且,欲維持層合發泡體之機械性 強度,對於構成發泡體層之聚烯烴系樹脂100重量份而言 以5重量份以下爲佳,較佳爲3重量份以下。 其次,對於本發明之聚烯烴系樹脂層合發泡體的製造 方法作說明。 φ 本發明的構成層合發泡體之發泡體層,僅由壓出發泡 所製造者即可,可由將發泡粒子以金屬模具內進行加熱並 融著的模型內成形方法而製造。且,作爲將樹脂層層合於 發泡體層之方法,可由於預先製造之發泡體層表面上,添 加親水性化合物的薄膜,藉由熱層壓進行層合之方法、或 藉由壓出層壓進行層合之方法來製造。又亦可由將發泡體 層與樹脂層由一塑模壓出之共壓出法而製造。藉由模型內 成形方法時,將含有預先製造之親水性化合物的薄膜以金 ❹ 屬模具內可融著於發泡粒子成形體。發泡體層爲壓出發泡 體時,藉由共壓出法,將添加防帶電劑之樹脂層層合於發 泡體層而進行壓出發泡,可使樹脂層厚度變薄,同時可得 到樹脂層與發泡體層之間的接著力較高的層合發泡體故較 佳。 藉由共壓出法製造薄片狀層合發泡體的方法中,有著 使用共壓出用平模以薄片狀既行共壓出發泡並層合之方法 、與使用共壓出用環狀塑模與圓柱狀冷卻裝置,將筒狀層 合發泡體進行共壓出發泡,再將筒狀層合發泡體切開使其 -27- 201012649 成爲薄片狀層合發泡體之方法等。彼等中,使用共壓出用 環狀塑模之方法可抑制稱爲corrugate之波狀模様的產生 、或容易製造寬度爲1000mm以上之幅度廣的層合發泡體 ,故爲較佳方法。 對於使用前述共壓出用環狀塑模進行共壓出的情況, 詳紐說明如下。如圖1所示,首先將聚烯烴系樹脂(A1 ) 、親水性化合物(B )與視必要所添加的高分子型防帶電 劑(C)供給於樹脂層形成用壓出機11,經加熱熔融並混 煉後,視必要添加揮發性可塑劑(D ),經熔融混煉後成 爲聚烯烴系樹脂層形成用樹脂熔融物(E1)。同時,將聚 烯烴系樹脂(A2 )與視必要添加的氣泡調整劑等添加劑( G)供給於發泡體層形成用壓出機12,經加熱熔融並混煉 後壓入物理發泡劑(F ),再進行混煉後成爲聚烯烴系樹 脂發泡體層形成用樹脂熔融物(E2 )。 且,親水性化合物(B )爲液狀親水性化合物(B 1 ) 時,可與揮發性可塑劑(D)同様地藉由壓入而添加,親 水性化合物(B )爲固體狀親水性化合物(B2 )時,作爲 使用聚烯烴系樹脂之母料,可與聚烯烴系樹脂(A1)同時 添加、或可加熱固體狀親水性化合物(B2)成爲液狀後藉 由壓入而添加。 且’對於共壓出方法,僅可於環狀塑模內層合樹脂層 形成用樹脂熔融物(E1)與發泡體層形成用樹脂熔融物( E2) ’亦可將壓出之前述熔融物彼此於塑模出口外進行層 合。又,前述環狀塑模、壓出機、圓柱狀冷卻裝置、切開 -28- 201012649 筒狀層合發泡體之裝置等可使用於自過去的壓出發泡領域 中所使用的公知者。 於聚烯烴系樹脂層形成用樹脂熔融物(E1)添加揮發 性可塑劑時,作爲揮發性可塑劑(D),具有可降低樹脂 熔融物(E1)之熔融黏度的功能之同時,使用於聚烯烴系 樹脂層(J )形成後,比該聚烯烴系樹脂層更容易揮發而 不存在於樹脂層中者。藉由將揮發性可塑劑(D)添加於 φ 樹脂熔融物(E1)中,共壓出層合發泡體時,將樹脂層形 成用樹脂熔融物(E1)之壓出溫度接近發泡體層形成用樹 脂用物(E2)之壓出溫度的同時,可顯著提高熔融狀態樹 脂層(J)之熔融延伸的提高。因此,發泡時樹脂層藉由 熱之發泡體層的氣泡結構難遭到破壞,且該樹脂層(J) 之延伸會追隨聚烯烴系樹脂發泡體層(I)之發泡時的延 伸,故藉由樹脂層(J)之延伸不足可防止龜裂產生。 作爲揮發性可塑劑(D),使用選自碳數2〜7的脂肪 族烴、碳數1〜4的脂肪族醇、或碳數2〜8的脂肪族醚之 1種、或2種以上者爲佳。將如滑劑一般揮發性較低者作 爲可塑劑使用時,滑劑等殘存於樹脂層(J),會污染到 被包裝體表面。相對於此揮發性可塑劑(D)可將樹脂層 (J)的樹脂有效率地可塑化,於所得之樹脂層(J),揮 發性可塑劑本身難以殘留故較佳。 作爲前述碳數2〜7的脂肪族烴,例如可舉出乙烷、 丙烷、正丁烷、異丁烷、正戊烷、異戊烷、新戊烷、環戊 烷、正己烷、異己烷、環己烷、正庚烷等。 -29- 201012649 作爲前述碳數1〜4的脂肪族醇,例如可舉出甲醇、 乙醇、丙醇、丁醇、異丙基醇、異丁基醇、正丁基醇、 sec-丁 基醇、tert-丁 基醇。 作爲前述碳數2〜8的脂肪族醚,例如可舉出二甲基 酸、二乙基酸、丙基酸、異丙基酸、甲基乙基醚、甲基丙 基醚、甲基異丙基醚、甲基丁基醚、甲基異丁基醚、甲基 戊基醚、甲基異戊基醚、乙基丙基醚、乙基異丙基醚、乙 基丁基醚、乙基異丁基醚、乙基戊基醚、乙基異戊基醚、 乙烯醚、烯丙基醚、甲基乙烯醚、甲基烯丙基醚、乙基乙 烯醚、乙基烯丙基醚。 揮發性可塑劑(D)之沸點因可由樹脂層(J)容易揮 發,故以120°C以下爲佳,較佳爲80°C以下。揮發性可塑 劑(D)的沸點僅於該範圍時,經共壓出後,僅放置所得 之層合發泡體(H),藉由共壓出後之熱,進一步藉由於 後的室溫下的氣體透過,揮發性可塑劑(D)由層合發泡 體的樹脂層(J)自然揮散,自然地除去。該沸點的下限 値大槪爲-50T:。 揮發性可塑劑(D)的添加量爲,對於聚烯烴系樹脂 (A1)與親水性化合物(B)與視必要所添加的高分子型 防帶電劑(C)之混煉物100重量份而言,以5重量份〜 50重量份爲佳。揮發性可塑劑(D)的添加量僅爲5重量 份以上,可抑制藉由構成樹脂層(J)之聚烯烴系樹脂等 混煉時的剪斷所引起之發熱,層合樹脂層(J)之發泡體 層(I)所成之發泡體層形成用樹脂熔融物(E2)的樹脂 -30- 201012649 溫度之上昇受到抑制(溫度降低效果)。因此,發泡體層 形成用樹脂熔融物(E2)於發泡時,可防止氣泡被破壞等 害處。且揮發性可塑劑(D)可提高樹脂層形成用樹脂熔 融物(E1)的發泡體層形成用樹脂熔融物(E2)於發泡時 所追隨之延伸性(伸張性改善效果),亦具有使樹脂層( J)的厚度均勻地薄薄形成之效果。由該觀點得知,揮發 性可塑劑(D )之添加量以7重量份以上爲佳,1 0重量份 φ 以上爲較佳。 另一方面,揮發性可塑劑(D)的添加量對於聚烯烴 系樹脂(A1) 100重量份而言,僅爲50重量份以下,不 會引起樹脂層(J)本身的物性降低,揮發性可塑劑(D) 會浸透於樹脂層形成用樹脂熔融物(E1)中,可充分地混 煉,故不會由模唇噴出揮發性可塑劑,沒有於樹脂層(J )會開洞、或表面產生凹凸狀而使表面平滑性降低的疑慮 。由該觀點得知,揮發性可塑劑(D)的添加量以40重量 # 份以下爲佳,以3 0重量份以下爲較佳,以2 5重量份以下 爲更佳。使揮發性可塑劑(D)的添加量於前述範圍時, 可確保共壓出時的樹脂層形成用樹脂熔融物之溫度降低效 果與伸張性改善效果。 又,樹脂層形成用樹脂熔融物(E1)中,於不阻礙本 發明之目的的範圍下可添加各種添加劑。作爲各種添加劑 ’例如可舉出抗氧化劑、熱安定劑、耐候劑、紫外線吸收 劑、難燃劑、塡充劑、抗菌劑等。此時的添加量,對於形 成前述熔融物(E1)之聚烯烴系樹脂(A1) 100重量份以 -31 - 201012649 1 0重量份以下爲佳,5重量份以下爲較佳,以3重量份以 下爲特佳。下限大槪爲〇·〇1重量份。 作爲物理發泡劑(F),例如可舉出丙烷、正丁烷、 異丁烷、正戊烷、異戊烷、正己烷、異己烷等脂肪族烴、 環戊烷、環己烷等脂環式烴、氯化甲烷、氯化乙烷等氯化 烴、1,1,1,2-四氟乙烷、1,1-二氟乙烷等氟化烴等有機系物 理發泡劑、氧、氮、二氧化碳、空氣等無機系發泡劑、偶 氮二碳醯胺等分解型發泡劑。前述物理發泡劑可混合2種 以上使用。彼等中,特別由與聚乙烯系樹脂之相溶性、發 泡性的觀點來看以有機系發泡劑爲佳,其中亦以正丁烷、 異丁烷、或彼等混合物作爲主成分者爲佳。 作爲主要添加劑(G),一般添加氣泡調整劑。作爲 氣泡調整劑,可使用有機系、或無機系中任一種。作爲無 機系氣泡調整劑,可舉出硼酸鋅、硼酸鎂、硼砂等硼酸金 屬鹽、氯化鈉、氫氧化鋁、滑石、沸石、二氧化矽、碳酸 鈣、重碳酸鈉等。又,作爲有機系氣泡調整劑,可舉出磷 酸-2,2-伸甲基雙(4,6-tert-丁基苯基)鈉、安息香酸鈉、 安息香酸鈣、安息香酸鋁、硬脂酸鈉等。又,檸檬酸與重 碳酸鈉、檸檬酸與鹼金屬鹽與重碳酸鈉等組合等亦可作爲 氣泡調整劑使用。這些氣泡調整劑可混合2種以上使用。 物理發泡劑(F)之添加量可配合發泡劑之種類、目 的之外觀密度作調整。又氣泡調整劑的添加量可配合作爲 目的之氣泡徑作調節。例如作爲發泡劑使用異丁烷3 0重 量%與正丁烷70重量%之丁烷混合物,欲得到前述密度範 201012649 圍之層合發泡體時’丁烷混合物的添加量對於聚烯烴系樹 脂(A2) 100重量份爲3〜3〇重量份,較佳爲4〜2〇重量 份’更佳爲6〜18重量份。又,氣泡調整劑之添加量對於 聚烯烴系樹脂(A2) 100重量份而言爲〇.〇1〜1〇重量份, 較佳爲0.03〜8重量份。 聚烯烴系樹脂發泡體層形成用樹脂熔融物(E2 )中, 如前述以不阻礙本發明的目的及效果之範圍下,可添加苯 φ 乙稀系樹脂或彈性體等其他樹脂、或熱安定劑之添加劑。 如前述’將層合發泡體藉由共壓出製造時,使用壓出 機Π形成樹脂層形成用樹脂熔融物(E1),使用壓出機 12形成發泡體層形成用樹脂熔融物(E2),於壓出機12 內將樹脂熔融物(E2)調整爲可發泡之溫度,於壓出機 11內將樹脂熔融物(E1)調整爲可共壓出之溫度後,將 樹脂層形成用樹脂熔融物(E 1 )與發泡體層形成用樹脂熔 融物(E2)導入於共壓出用環狀塑模13使兩者層合,進 • —步於大氣中共壓出,使發泡體層形成用樹脂熔融物(E2 )發泡,形成於發泡體層層合樹脂層之筒狀層合發泡體, 將該筒狀層合發泡體之內面沿著圓柱狀冷卻裝置一邊冷卻 —邊吸引切開,得到層合發泡體(H)。 但,樹脂層形成用樹脂熔融物(E1)與發泡體層形成 用樹脂熔融物(E2)之層合爲,僅以環狀塑模13的內部 進行層合即可,可於出口附近、或塑模出口外進行層合。 【實施方式】 -33- 201012649 [實施例] 以下依據實施例對本發明作更詳細說明。但,本發明 未受到實施例之限定。 作爲氣泡調整劑,使用對於聚乙烯系樹脂80重量%添 加20%之滑石(松村產業股份有限公司製商品名「High filler#12」)所成之氣泡調整劑母料。 作爲發泡體層形成用及樹脂層形成用之聚烯烴系樹脂 ,使用股份有限公司日本Unicar製的低密度聚乙烯「 NUC8321」(密度 922g/L,MFR : 2.4g/10 分鐘)。 作爲高分子型防帶電劑,使用將三洋化成工業股份有 限公司製之聚醚-聚丙烯嵌段共聚物作爲主成分之「 Pelestat3 00」(融點 136°C,數平均分子量 14000,密度 990g/L )。 作爲物理發泡劑,使用由正丁烷70重量%與異丁烷 30重量%所成之混合丁烷。 使用之親水性化合物如表1所示。 -34- 201012649 [表1] 化合物名 HLB 性狀(20〇C ) 數平均分子量 化雜1 聚乙二醇 20 mk 300 化雜2 聚乙二醇 20 固體 2000 化合物3 聚環氧乙烷聚環氧丙院嵌段共聚物 (polyoxyethylene polyoxypropylene block copolymer) 16 固體 8750 化合物4 聚乙二醇 20 職 600 化合物5 硬脂酸聚乙二醇酯 11.9 固體 670 化雜6 十甘油硬脂酸酯 12 固體 1000 化合物7 甘油單硬脂酸酯 4.3 「固體 350 化合物8 四甘油硬脂酸酯 5.6 固體 570 化合物9 丙二醇單月桂酸酯 4.2 猶 240 且,化合物3爲作爲該構成成分具有20質量%之聚環 氧丙烷成分。聚環氧丙烷於低分子量時顯示親水性,但隨 著分子量提高,會顯示疏水性。化合物3中,聚環氧丙院 成分之數平均分子量因比1750大,故聚環氧丙烷成分顯 示疏水性。將聚環氧丙院部分視爲疏水基部分而計算出 HLB 値。 實施例1〜9、比較例1〜5 作爲聚烯烴系樹脂發泡體層形成用之壓出機(12), 使用由直徑115mm的第一壓出機與直徑150mm第二壓出 機所成之雙座壓出機,作爲聚烯烴系樹脂層形成用之壓出 機(11)使用直徑65mm,L/D = 5 0之第三壓出機。且於共 壓出用環狀塑模連結第二壓出機與第三壓出機之各出口, 將各熔融樹脂於環狀塑模中可層合。 -35- 201012649 將作爲聚烯烴系樹脂之低密度聚乙烯「NUC832 1」、 與表2所示種類、量之親水性化合物供給於第三壓出機之 原料投入口,經加熱混煉,作爲揮發性可塑劑壓入如表2 所示量之前述混合丁烷,進一步進行混煉,調節爲表2所 示壓出樹脂溫度,作爲樹脂層形成用樹脂熔融物,將該樹 脂層形成用樹脂熔融物以如表2所示吐出量導入於共壓出 用環狀塑模。且實施例1、3、9及比較例5中,作爲高分 子型防帶電劑將「PELESTAT300」以表2所示量的比率添 加。 但,液狀親水性化合物與物理發泡劑同樣地以直接壓 入方式添加,製作出固體狀親水性化合物以低密度聚乙烯 「NUC83 2 1」作爲基質樹脂的濃度10重量%之母料,添加 至如所定量。 同時將作爲聚烯烴系樹脂之低密度聚乙烯「NUC 8 32 1 」、與表3所示量之氣泡調整劑母料,供給於雙座壓出機 之第一壓出機的原料投入口,加熱混煉,作爲調整爲約 200 °C之熔融樹脂混合物。其次,於該熔融樹脂混合物中 壓入如表3所示量的物理發泡劑,其次供給於連接前述第 一壓出機的下游側的第二壓出機,溫度調節至如表3所示 壓出樹脂溫度作爲發泡體層形成用樹脂熔融物,將該發泡 體層形成用樹脂熔融物以表3所示吐出量導入共壓出用環 狀塑模。 於導入於共壓出用環狀塑模並以環狀流動的發泡體層 形成用樹脂熔融物之外側與內側,層合導入於共壓出用環 -36- 201012649 狀塑模以環狀流動的樹脂層形成用樹脂熔融物,將熔融物 之層合體自塑模壓出於大氣中,形成由樹脂層/發泡體層/ 樹脂層所成之3層構成的筒狀層合發泡體。將經壓出的筒 狀層合發泡體沿著冷卻的圓柱狀冷卻裝置(心軸),以表 3所示拉取速度一邊進行拉取一邊切開得到層合發泡體。 參考例1 g 作爲聚烯烴系樹脂發泡體層形成用之壓出機,使用由Va: The apparent volume (cm3) of the sample slice calculated from the outer dimensions of the sample slice used for the measurement. W: The total weight (g) of the sample slice used was determined. P: density of the resin composition obtained by defoaming the laminated foam (g/cm3) The surface resistivity of the resin layer can be set by adding a polymer type antistatic agent to the resin layer of the present invention. Lxio8~1χ1014(Ω). -22- 201012649 When the surface resistivity is too large, the antistatic property will be insufficient, or an electrostatic charge will accumulate on the surface of the resin layer, and dust will easily adhere. In order to prevent dust from adhering, the surface resistivity is preferably 5 χ 1013 Ω or less, and more preferably 1 χ 1013 Ω or less. On the other hand, when the surface resistivity is too small, there is no problem in the antistatic property, but the antistatic property required on the packaging material is excessive and there is a concern that the cost is too high. The surface resistivity in the present specification is measured in accordance with JIS Κ 6271 (2001) after the state of the following test piece is adjusted. In other words, the test piece cut out from the laminated foam of the object to be measured (length 100 mm×100 mm×thickness: thickness of the test piece) was placed in an environment of temperature 3 (TC, relative humidity of 30% for 36 hours, and then test piece was taken. The state is adjusted, and the voltage is applied in accordance with JIS K6271 (2001) with a voltage of 500 kV, and the surface resistivity after 1 minute is obtained. To make the surface resistivity of the resin layer ΙχΙΟ8~1χ1〇14Ω, The olefin-based resin layer is preferably a polymer type antistatic agent having a ratio of 2 φ to 30 parts by weight based on 100 parts by weight of the polyolefin resin. When the amount is too small, there is a fear that the antistatic property may not be exhibited. On the one hand, when the amount of addition is too large, there is no problem in terms of antistatic property, but the antistatic property reaches the limit, so the cost performance is poor. From this point of view, the antistatic agent is added in an amount of 4 to 30. The parts by weight are preferably 6 to 25 parts by weight. The number average molecular weight of the antistatic agent is preferably 2,000 or more, preferably 2,000 to 100,000, more preferably 5,000 to 60,000, particularly preferably 8,000 to 40.千. Therefore, the antistatic agent is a polymer type antistatic agent which can be distinguished from the antistatic agent formed by the surfactant -23-201012649. Moreover, the number average of the antistatic agent of the polymer type When the number average molecular weight of the polymer type antistatic agent is within the above range, the antistatic agent is placed in the package, and the surface of the package is not contaminated. The number average molecular weight can be obtained by high temperature gel permeation chromatography. For example, when the polymer type antistatic agent is a hydrophilic resin containing a polyether ester decylamine or a polyether as a main component, o-dichlorobenzene is used as a solvent to prepare a sample. The concentration is 3 mg/ml, and the polystyrene is used as a reference material at a column temperature of 135 ° C. The type of the solvent and the column temperature can be matched with the type of the polymer antistatic agent. The polymer type antistatic agent used in the present invention is a hydrophilic resin having a volume resistivity of 1 〇 5 to 1 〇 η·cm and a copolymer with a polyolefin. Can use polyether two a polyether such as a polyether diamine or a denature thereof, and a polyether ester decylamine having a segment of a polyether diol as a polyether segment forming component, and a polyether segment forming component can be used as a poly As the polyether segment forming component, a polyether ester having a segment of a polyether diol can be used as a polyether segment forming component, and a polyether diamine can be used as a polyether segment forming component. As the polyether oxime in the segment, a polyether such as a polyether urethane having a segment of a polyether diol or a polyether diamine may be used as a polyether sulfonate-containing polyether having a hydrophilic resin and having a nonionic ion in the molecule. a cationic polymer having 2 to 80, preferably 3 to 60 cationic groups, a dicarboxylic acid having a sulfonyl group, and a diol or a polyether as a constituent unit, and a molecule An anionic polymer having 2 to 80, preferably 3 to -24 to 201012649, 60 sulfonyl groups. In addition, in the polymer type antistatic agent, it is desired to improve the compatibility with the polyalkylene-based resin, and to provide an antistatic effect, and to suppress the decrease in physical properties by adding an antistatic agent, the same type as the polyolefin resin or The polyolefin-based resin having a high compatibility is preferably a block copolymerization, and examples thereof include a block having a polyolefin and a block of the hydrophilic resin having a volume resistivity of 105 to 1 ΐ Ω·cm. The number average molecular φ (?η) of the structure which is repeatedly cross-linked is 2000 to 60,000 block copolymer. Among them, block copolymers of polyether and polyolefin (block copolymer) are more preferable than the above-mentioned compatibility. Further, the block of the polyolefin and the block of the hydrophilic resin have a repeated interaction via at least one bond selected from the group consisting of an ester bond, a guanamine bond, an ether bond, a urethane bond, and an imine bond. Combined structure. Further, a block of a polyolefin of the above-mentioned block polymer which is preferably used as a polymer type antistatic agent, a polyolefin having a carboxyl group at both terminals of the polymer, and a polyolefin having a carbonyl group at one end of the polymer are preferred. . More specifically, the polymer type antistatic agent as described above is a composition described in JP-A No. 3-103466 and JP-A No. 2001-2780985. The composition described in JP-A-3-103466 is a block copolymer containing (I) a thermoplastic resin, (poly)polyethylene oxide or a polyethylene oxide block component of 50% by weight or more, and (III) The metal salt of the polyethylene oxide block component in the above (II) is a solid solution, and the composition described in JP-A No. 2001-278985 has a polyalkylene hydrocarbon ( The block of a) and the block of the hydrophilic resin (b) having a volume resistivity of ΙχΙΟ5~ΙχΙΟ^Ω. -25- 201012649, the number average molecular weight (Μη) of the structure which is repeatedly cross-linked is 2000~ Block copolymer of 60000. The block of the above (a) and the block of (b) have a bond interposed by at least one selected from the group consisting of an ester bond, a guanamine bond, an ether bond, a urethane bond, and an imine bond. Combined structure. As such a polymer type antistatic agent, for example, "SD100" manufactured by Mitsui, DU PONT POLYCHEMICALS Co., Ltd., and "PELESTAT300" manufactured by Sanyo Chemical Industries Co., Ltd., are commercially available. Each of the above-mentioned polymer type antistatic agents may be used singly or in combination of plural kinds. Further, the melting point of the polymer type antistatic agent is preferably 70 to 270 ° C, more preferably 80 to 230 ° C, and particularly preferably 80 to 200 ° C, but from the viewpoint of the performance of the antistatic function It is better. The melting point of the polymeric antistatic agent can be measured by the following method in accordance with JIS K7121 (1987). That is, pretreatment was carried out by the condition adjustment (2) of the test piece in JIS K7121 (1987) (however, the cooling rate was 10 ° C /min), and the melting peak was obtained by 1 (TC/min heating). The peak temperature of the obtained melting peak is used as the melting point. When two or more melting peaks appear, the temperature of the peak of the melting peak of the largest area is used as the melting point. To achieve the desired surface resistivity, the foam layer is not required. When the polymer-based antistatic agent is added, when the recovered material of the laminated foam is used as a raw material for the foam layer, when the polymer antistatic agent is added, the foam layer contains a polymer antistatic agent. Even in this case, the content of the polymer type antistatic agent is 15 parts by weight of the polyolefin resin constituting the foam layer, and 15 The mechanical strength of the laminated foam is preferably 5 parts by weight or less, preferably 3 parts by weight based on 100 parts by weight of the polyolefin resin constituting the foam layer. Below the weight Next, a method for producing the polyolefin-based resin laminated foam of the present invention will be described. φ The foam layer constituting the laminated foam of the present invention may be produced only by extrusion foaming, and may be produced. The foam particles are produced by an in-mold forming method in which heating and melting are performed in a metal mold. Further, as a method of laminating the resin layer to the foam layer, a hydrophilic compound may be added to the surface of the previously produced foam layer. The film is produced by lamination by thermal lamination or lamination by extrusion lamination, or by co-extrusion method in which a foam layer and a resin layer are extruded by a mold. When the in-mold forming method is used, a film containing a hydrophilic compound prepared in advance can be melted into a foamed particle molded body in a metal mold. When the foamed layer is a pressed foam, it is co-extruded. In the method, a resin layer to which an antistatic agent is added is laminated on a foam layer to carry out extrusion foaming, whereby the thickness of the resin layer can be reduced, and a laminate having a high adhesion between the resin layer and the foam layer can be obtained. Bubble body Preferably, the method for producing a sheet-like laminated foam by a co-extrusion method has a method in which a flat die for co-extrusion is used in a sheet form, and a method of co-extrusion foaming and lamination is used, and a method of co-extrusion is used. Ring-molded mold and cylindrical cooling device, method of co-extrusion foaming of cylindrical laminated foam, and slitting of cylindrical laminated foam to make -27-201012649 a lamellar laminated foam In the above, the method of using a ring-shaped mold for co-extrusion suppresses the generation of a corrugated mold called corrugate, or it is easy to produce a laminated foam having a wide width of 1000 mm or more, which is preferable. For the case of co-extrusion using the above-mentioned co-extrusion annular mold, the details are as follows. As shown in Fig. 1, first, the polyolefin resin (A1) and the hydrophilic compound (B) are necessary. The polymer type antistatic agent (C) to be added is supplied to the resin layer forming extruder 11, and after being heated and melted and kneaded, a volatile plasticizer (D) is added as necessary, and after melt-kneading, it becomes a polyolefin. A resin melt (E1) for forming a resin layer. At the same time, an additive (G) such as a polyolefin-based resin (A2) and a bubble adjusting agent to be added as needed is supplied to the foam layer forming extruder 12, and is heated and melted, kneaded, and then pressed into a physical foaming agent (F). After the kneading, the resin-formed resin melt (E2) is formed into a polyolefin-based resin foam layer. Further, when the hydrophilic compound (B) is a liquid hydrophilic compound (B 1 ), it can be added by indentation together with the volatile plasticizer (D), and the hydrophilic compound (B) is a solid hydrophilic compound. In the case of (B2), the base material using the polyolefin resin may be added simultaneously with the polyolefin resin (A1), or the solid hydrophilic compound (B2) may be heated to be liquid, and then added by press-fitting. In the case of the co-extrusion method, only the resin melt (E1) for forming the resin layer in the annular mold and the resin melt (E2) for forming the foam layer can be used. Lamination is performed outside each other outside the mold exit. Further, the above-mentioned annular mold, extruder, cylindrical cooling device, and apparatus for cutting a cylindrical laminated foam of -28-201012649 can be used for a person who has been used in the field of extrusion foaming in the past. When a volatile plasticizer is added to the resin-based resin layer (E1) for forming a polyolefin resin layer, the volatile plasticizer (D) has a function of lowering the melt viscosity of the resin melt (E1) and is used for polymerization. After the olefin-based resin layer (J) is formed, it is more likely to volatilize than the polyolefin-based resin layer and is not present in the resin layer. When the volatile plasticizer (D) is added to the φ resin melt (E1) and the laminated foam is pressed together, the extrusion temperature of the resin layer-forming resin melt (E1) is close to the foam layer. When the extrusion temperature of the resin (E2) for forming is formed, the improvement of the melt extension of the resin layer (J) in the molten state can be remarkably improved. Therefore, the foam layer is hardly broken by the foam structure of the hot foam layer at the time of foaming, and the elongation of the resin layer (J) follows the elongation at the time of foaming of the polyolefin resin foam layer (I). Therefore, cracking can be prevented by the insufficient extension of the resin layer (J). As the volatile plasticizer (D), one type or two or more types selected from the group consisting of aliphatic hydrocarbons having 2 to 7 carbon atoms, aliphatic alcohols having 1 to 4 carbon atoms, and aliphatic ethers having 2 to 8 carbon atoms are used. It is better. When the volatile agent is generally used as a plasticizer, a lubricant or the like remains on the resin layer (J), which may contaminate the surface of the package. The resin of the resin layer (J) can be plasticized efficiently with respect to the volatile plasticizer (D), and it is preferable that the volatile plasticizer itself is hard to remain in the obtained resin layer (J). Examples of the aliphatic hydrocarbon having 2 to 7 carbon atoms include ethane, propane, n-butane, isobutane, n-pentane, isopentane, neopentane, cyclopentane, n-hexane, and isohexane. , cyclohexane, n-heptane, and the like. -29- 201012649 Examples of the aliphatic alcohol having 1 to 4 carbon atoms include methanol, ethanol, propanol, butanol, isopropyl alcohol, isobutyl alcohol, n-butyl alcohol, and sec-butyl alcohol. , tert-butyl alcohol. Examples of the aliphatic ether having 2 to 8 carbon atoms include dimethyl acid, diethyl acid, propyl acid, isopropyl acid, methyl ethyl ether, methyl propyl ether, and methyl group. Propyl ether, methyl butyl ether, methyl isobutyl ether, methyl amyl ether, methyl isoamyl ether, ethyl propyl ether, ethyl isopropyl ether, ethyl butyl ether, B Isobutyl ether, ethyl amyl ether, ethyl isoamyl ether, vinyl ether, allyl ether, methyl vinyl ether, methyl allyl ether, ethyl vinyl ether, ethyl allyl ether . Since the boiling point of the volatile plasticizer (D) can be easily volatilized by the resin layer (J), it is preferably 120 ° C or lower, preferably 80 ° C or lower. When the boiling point of the volatile plasticizer (D) is only in this range, after the co-extrusion, only the obtained laminated foam (H) is placed, and the heat after co-extrusion is further used to further the room temperature. The lower gas is transmitted, and the volatile plasticizer (D) is naturally volatilized by the resin layer (J) of the laminated foam, and is naturally removed. The lower limit of the boiling point is -50T槪-50T:. The amount of the volatile plasticizer (D) to be added is 100 parts by weight of the kneaded product of the polyolefin-based resin (A1) and the hydrophilic compound (B) and, if necessary, the polymer-based antistatic agent (C). In other words, it is preferably 5 parts by weight to 50 parts by weight. The addition amount of the volatile plasticizer (D) is only 5 parts by weight or more, and heat generation due to shearing during kneading of the polyolefin resin constituting the resin layer (J) can be suppressed, and the laminated resin layer (J) The resin -30-201012649 of the resin layer-forming resin melt (E2) formed by the foam layer (I) is suppressed in temperature (temperature reduction effect). Therefore, when the resin layer-forming resin melt (E2) is foamed, it is possible to prevent the bubbles from being damaged or the like. In addition, the volatile plasticizer (D) can improve the elongation (stretching property improvement effect) of the resin layer-forming resin melt (E2) for foam layer formation of the resin layer-forming resin melt (E1) during foaming, and also has The effect of uniformly forming the thickness of the resin layer (J) is thin. From this viewpoint, the amount of the volatile plasticizer (D) to be added is preferably 7 parts by weight or more, and more preferably 10 parts by weight or more. On the other hand, the addition amount of the volatile plasticizer (D) is only 50 parts by weight or less based on 100 parts by weight of the polyolefin-based resin (A1), and does not cause deterioration in physical properties of the resin layer (J) itself, and is volatile. The plasticizer (D) is impregnated into the resin layer-forming resin melt (E1), and can be sufficiently kneaded. Therefore, the volatile plasticizer is not ejected from the lip, and the resin layer (J) is not opened, or The surface has irregularities and the surface smoothness is lowered. From this viewpoint, the amount of the volatile plasticizer (D) to be added is preferably 40 parts by weight or less, more preferably 30 parts by weight or less, still more preferably 25 parts by weight or less. When the amount of the volatile plasticizer (D) to be added is in the above range, the temperature-reducing effect and the stretchability-improving effect of the resin layer-forming resin melt at the time of co-extrusion can be ensured. Further, in the resin layer-forming resin melt (E1), various additives may be added in a range not inhibiting the object of the present invention. Examples of the various additives include an antioxidant, a heat stabilizer, a weather resistance agent, an ultraviolet absorber, a flame retardant, a chelating agent, and an antibacterial agent. The amount of the polyolefin resin (A1) forming the melt (E1) is preferably -31 to 201012649 by weight or less, more preferably 5 parts by weight or less, and preferably 3 parts by weight or less. The following is especially good. The lower limit is 重量·〇1 parts by weight. Examples of the physical foaming agent (F) include aliphatic hydrocarbons such as propane, n-butane, isobutane, n-pentane, isopentane, n-hexane, and isohexane, and lipids such as cyclopentane and cyclohexane. Organic physical foaming agents such as chlorinated hydrocarbons such as cyclic hydrocarbons, methyl chloride and chlorinated ethane, and fluorinated hydrocarbons such as 1,1,1,2-tetrafluoroethane and 1,1-difluoroethane; An inorganic foaming agent such as oxygen, nitrogen, carbon dioxide or air, or a decomposable foaming agent such as azobiscarbonamide. The above physical foaming agent may be used in combination of two or more kinds. Among them, an organic foaming agent is preferred from the viewpoint of compatibility with a polyethylene resin and foaming property, and n-butane, isobutane, or a mixture thereof as a main component is also preferable. It is better. As the main additive (G), a bubble regulator is generally added. As the bubble adjusting agent, any of an organic type or an inorganic type can be used. Examples of the inorganic bubble adjusting agent include boric acid metal salts such as zinc borate, magnesium borate, and borax, sodium chloride, aluminum hydroxide, talc, zeolite, ceria, calcium carbonate, and sodium bicarbonate. Further, examples of the organic bubble adjusting agent include phosphoric acid-2,2-extended methylbis(4,6-tert-butylphenyl)sodium, sodium benzoate, calcium benzoate, aluminum benzoate, and stearic acid. Sodium and so on. Further, a combination of citric acid, sodium bicarbonate, citric acid, an alkali metal salt, sodium bicarbonate or the like may be used as the bubble regulator. These bubble modifiers can be used in mixture of 2 or more types. The amount of the physical foaming agent (F) to be added can be adjusted in accordance with the type of the foaming agent and the apparent density of the object. Further, the amount of the bubble adjusting agent added can be adjusted in accordance with the purpose of the bubble diameter. For example, as a foaming agent, a butane mixture of 30% by weight of isobutane and 70% by weight of n-butane is used, and when the laminated foam having the density of 201012649 is obtained, the amount of the butane mixture added is for the polyolefin system. The resin (A2) is 100 parts by weight, preferably 3 to 3 parts by weight, preferably 4 to 2 parts by weight, more preferably 6 to 18 parts by weight. In addition, the amount of the air-conditioner to be added is 0.1 to 1 part by weight, preferably 0.03 to 8 parts by weight, per 100 parts by weight of the polyolefin-based resin (A2). In the resin melt (E2) for forming a polyolefin resin foam layer, other resins such as benzene φ ethylene resin or elastomer, or thermal stability may be added as long as the object and effect of the present invention are not inhibited. Additive for the agent. When the laminated foam is produced by co-extrusion, the resin layer-forming resin melt (E1) is formed using an extruder, and the foam layer-forming resin melt is formed using the extruder 12 (E2). The resin melt (E2) is adjusted to a foamable temperature in the extruder 12, and the resin melt (E1) is adjusted to a temperature which can be co-pressed in the extruder 11, and then the resin layer is formed. The resin melt (E1) and the resin layer-forming resin melt (E2) are introduced into the co-extrusion annular mold 13 to laminate the two, and are simultaneously pressed in the atmosphere to cause foaming. The resin layer-forming resin melt (E2) is foamed, and is formed into a cylindrical laminated foam of the foam layer laminated resin layer, and the inner surface of the cylindrical laminated foam is cooled along the cylindrical cooling device. - At the same time, the slit is opened to obtain a laminated foam (H). However, the resin layer-forming resin melt (E1) and the foam layer-forming resin melt (E2) are laminated so as to be laminated only inside the ring mold 13, and may be in the vicinity of the outlet, or Lamination is carried out outside the mold exit. [Embodiment] - 33 - 201012649 [Examples] Hereinafter, the present invention will be described in more detail based on examples. However, the invention is not limited by the examples. As the bubble adjusting agent, a bubble conditioner masterbatch prepared by adding 20% of talc (trade name "High filler #12" manufactured by Matsumura Co., Ltd.) to 80% by weight of the polyethylene resin was used. As a polyolefin resin for forming a foam layer and a resin layer, a low density polyethylene "NUC8321" (density: 922 g/L, MFR: 2.4 g/10 min) manufactured by Unicar Co., Ltd., Japan was used. As a polymer type antistatic agent, a polyether-polypropylene block copolymer manufactured by Sanyo Chemical Industries Co., Ltd. was used as a main component of "Pelestat 3 00" (melting point 136 ° C, number average molecular weight 14000, density 990 g / L). As the physical foaming agent, a mixed butane of 70% by weight of n-butane and 30% by weight of isobutane was used. The hydrophilic compounds used are shown in Table 1. -34- 201012649 [Table 1] Compound name HLB Properties (20〇C) Number average molecular weight impurity 1 Polyethylene glycol 20 mk 300 Chemically mixed 2 Polyethylene glycol 20 Solid 2000 Compound 3 Polyethylene oxide polyepoxy Polyoxyethylene polyoxypropylene block copolymer 16 solid 8750 compound 4 polyethylene glycol 20 occupation 600 compound 5 stearic acid polyethylene glycol ester 11.9 solid 670 chemical 6 glyceryl stearate 12 solid 1000 compound 7 Glycerol monostearate 4.3 "Solid 350 compound 8 Tetraglyceryl stearate 5.6 Solid 570 Compound 9 Propylene glycol monolaurate 4.2 Juru 240 and Compound 3 is 20% by mass of polypropylene oxide as the constituent component The polypropylene oxide exhibits hydrophilicity at a low molecular weight, but exhibits hydrophobicity as the molecular weight increases. In the compound 3, the number average molecular weight of the polyacrylic acid compound component is larger than 1750, so the polypropylene oxide component Hydrophobicity was observed. HLB 値 was calculated by considering the polypropylene oxide-based portion as a hydrophobic group portion. Examples 1 to 9 and Comparative Examples 1 to 5 were formed as a polyolefin-based resin foam layer. The extruder (12) is a two-seat extruder made of a first extruder having a diameter of 115 mm and a second extruder having a diameter of 150 mm, and is used as an extruder for forming a polyolefin resin layer (11). A third extruder having a diameter of 65 mm and an L/D = 50 is used, and each of the outlets of the second extruder and the third extruder is connected by a ring-shaped mold for co-extrusion, and each molten resin is ring-shaped. The mold can be laminated in the mold. -35- 201012649 The low-density polyethylene "NUC832 1" which is a polyolefin resin and the hydrophilic compound of the type and amount shown in Table 2 are supplied to the raw material input port of the third extruder. The mixture was heated and kneaded, and the mixed butane in an amount shown in Table 2 was injected as a volatile plasticizer, and kneaded further to adjust the temperature of the extruded resin shown in Table 2 as a resin melt for resin layer formation. The resin layer-forming resin melt was introduced into a ring-shaped mold for co-extrusion at a discharge amount as shown in Table 2. Further, in Examples 1, 3, and 9 and Comparative Example 5, "PELESTAT300" was added as a high molecular type antistatic agent in a ratio shown in Table 2. However, the liquid hydrophilic compound was added in the same manner as the physical foaming agent, and a solid hydrophilic compound was prepared using a low-density polyethylene "NUC83 2 1" as a masterbatch of a matrix resin concentration of 10% by weight. Add to as quantified as. At the same time, the low-density polyethylene "NUC 8 32 1 " which is a polyolefin resin and the bubble conditioner masterbatch of the amount shown in Table 3 are supplied to the raw material input port of the first extruder of the two-seat extruder. The mixture was heated and kneaded as a molten resin mixture adjusted to about 200 °C. Next, a physical foaming agent in an amount as shown in Table 3 was injected into the molten resin mixture, and secondarily supplied to a second extruder connected to the downstream side of the first extruder, and the temperature was adjusted as shown in Table 3. The temperature of the resin to be extruded is used as a resin melt for foam layer formation, and the resin melt for foam layer formation is introduced into the annular mold for coextrusion in the discharge amount shown in Table 3. The outer side and the inner side of the resin melt for forming a foam layer which is introduced into the annular mold for coextrusion and introduced in a ring shape are laminated and introduced into the common extrusion ring-36-201012649. In the resin layer-forming resin melt, the laminate of the melt is molded into the atmosphere by molding, and a cylindrical laminate foam composed of three layers of a resin layer/foam layer/resin layer is formed. The extruded cylindrical laminated foam was cut along the cooled cylindrical cooling device (mandrel) at a drawing speed shown in Table 3 to obtain a laminated foam. Reference Example 1 g As an extruder for forming a polyolefin resin foam layer, use

W 直徑115mm的第一壓出機與直徑150mm的第二壓出機所 成的雙座壓出機,於第二壓出機的出口連結環狀塑模。 將作爲聚烯烴系樹脂的低密度聚乙烯「NUC 832 1」、 與表2所示量之氣泡調整劑母料,供給於雙座壓出機之第 一壓出機的原料投入口,經加熱混煉,經調整至約200°C 作爲熔融樹脂混合物。其次,於該熔融樹脂混合物作爲親 水性化合物將表1記載之「化合物1」以對聚烯烴系樹脂 φ 100重量份爲3.1重量份之比率進行壓入,壓入表2所示 量的物理發泡劑,其次供給於連接第一壓出機的下游側之 第二壓出機,調溫至如表2所示壓出樹脂溫度,作爲發泡 體層形成用樹脂熔融物,將該發泡體層形成用樹脂熔融物 以表3所示吐出量導入於環狀塑模。將該熔融物由塑模壓 出於大氣中,形成僅由發泡體層所成之筒狀發泡體。將壓 出之筒狀發泡體沿著冷卻心軸一邊拉取一邊切開,得到發 泡體。 -37- 201012649A two-seat extruder of a first extruder having a diameter of 115 mm and a second extruder having a diameter of 150 mm is connected to the annular mold at the outlet of the second extruder. The low-density polyethylene "NUC 832 1" which is a polyolefin resin and the bubble conditioner masterbatch of the amount shown in Table 2 are supplied to the raw material input port of the first extruder of the two-seat extruder, and are heated. The mixture was adjusted to about 200 ° C as a molten resin mixture. Then, the "Compound 1" described in Table 1 was pressed as a hydrophilic compound in a ratio of 3.1 parts by weight to 100 parts by weight of the polyolefin resin φ, and the physical amount shown in Table 2 was pressed. The foaming agent is supplied to the second extruder connected to the downstream side of the first extruder, and the temperature is adjusted to the temperature of the resin extruded as shown in Table 2, and the foam layer is formed as a resin layer for foam layer formation. The resin melt for formation was introduced into the annular mold in the amount of discharge shown in Table 3. The melt is pressed out of the atmosphere by a mold to form a cylindrical foam formed only of the foam layer. The extruded cylindrical foam was cut while being pulled along the cooling mandrel to obtain a foamed body. -37- 201012649

【S 樹脂層 Π出量(kg/時) S面側 κη vd κη vd in V) ν〇 \ό •«Η 'd νη 'Ο ^0 m 'Ο 1 Μ面側 \ό \Τ) 'Ο vd ir> F—Η V) V£) »r> m νο •-Η iTi v〇 ιρ^ v-i iTi SO 層合面 1兩面1 陌 膣 兩面 1兩面1 1兩面! 1兩面1 兩面 1兩面1 1 mm 1 兩面 1兩面1 1兩面| 1兩面 兩面 壓出溫度 (°C ) VO ν〇 ν〇 *-Η Ό ^-Η VO \〇 «-Η ν〇 Τ"*Η V〇 ^-Η ν〇 Η \〇 SO 揮發性 可塑劑 (重量份) <N <N <Ν CN (Μ (N cs (N 异 fN (N CN CN 异 <s CS 高肝型帶 電防止劑 (重量份) 1 I 1 1 1 1 1 I 1 1 τ—Η 親水性化合物 添加方式 1直接壓入1 |直接壓入| 1直接壓入I 母料 母料 1直接壓入1 母料 母料 母料 母料 母料 |直接壓入| |直接壓入I 1直接壓入1 添加量 (重量份) — 〇 CN ο 卜 — 卜 — — Ο CN 卜 寸· C^; — 〇 〇 m 〇 〇 (S m •ΤΝΤΝ itmll m 丨化合物lj 1化合物1| 丨化合物ι| 丨化合物2| 丨化合物3j 丨化合物4」 丨化合物5| 丨化合物ό| 丨化合物6| 丨化合物7j 丨化合物8 ! 丨化合物9| 丨化合物11 丨化合物lj 聚嫌烴系樹脂 _ £ in iW riJ ώπΐ] jsn ψΠι Ο 〇 〇 〇 Ο ο 〇 ο 〇 Ο 〇 〇 〇 〇 種類 1 NUC8321 1 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 丨實施例1 I |實施例2 I j實施例3 1 |實施例4 ] 1實施例5 I 1實施例6 1 |實施例7 I 實施例8 |實施例9 I 比較例1 丨比較例2 |比較例3 I |比較例4 I 比較例5 參考例1 。1}瞄^総令丑莛脃8二|}瞄^§^^鯽菊餾啪幽濉1}闽2^_93±1* 。1_葙?^__001^_味«獎跋§^製_长«「^__」旮谳* -38- 201012649 【ε® 拉取速度 (m/分) (N cK (N & iT) Os cs a; iTi <N iTi CN o; V) Ό (N (N a: m (N σ; (N cK (N 〇< CN cK m Os (Ν m 赛 發泡體層 吐出量 (kg/時) in ON 〇\ 〇\ in as iT) On in ON ir> 〇\ κη as y/Ί On m as m a\ ON U^i Os ο 2 壓出溫度 L (°〇) CN 1 H CN CN «—1 04 oj rj OJ <Ν 寸 Μ Μ 爾_ 芻w r4 (N r"H <N 卜 o f-H r4 卜 o CN CN ψ^< oi (N (N CN c〇 ^Η 氣泡調節劑母料 (重量份) κη <n r*^ in U-i in ν£> ^Η 聚烯烴系樹脂 配合量(重量份) 〇 o o o o o o o o o 〇 o o o o o 〇 o O 2 o 〇 o o Ο ο Ο Ο Ο ι~Η 種類 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 | NUC8321 1 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 1 NUC8321 實施例1 實施例2 實施例3 實施例4 實施例5 實施例6 實施例7 I實施例8] 實施例9 比較例1 1比較例2 I 1比較例3 1 1比較例4] 比較例5 丨參考例1 。蠢_3- f - φδοο- i^l^siiiil" -- _oIM}siNI_0QIlgl議-N1 義 i「甶__」旮漱 * -39- 201012649 將實施例、比較例及參考例所得之層合發泡體的厚度 、外觀密度、秤量、平均氣泡徑、表面電阻率、洗淨性等 評估如表4所示。[S resin layer extraction amount (kg/hour) S surface side κη vd κη vd in V) ν〇\ό •«Η 'd νη 'Ο ^0 m 'Ο 1 Μ面侧\ό \Τ) 'Ο Vd ir> F—Η V) V£) »r> m νο •-Η iTi v〇ιρ^ vi iTi SO Laminated surface 1 on both sides 1 膣 2 sides 1 2 sides 1 1 2 sides! 1 2 sides 1 2 sides 1 2 sides 1 1 Mm 1 two sides 1 two sides 1 1 two sides | 1 two sides and two sides of the extrusion temperature (°C) VO ν〇ν〇*-Η Ό ^-Η VO \〇«-Η ν〇Τ"*Η V〇^-Η ν〇 Η \〇SO Volatile plasticizer (parts by weight) <N <N <Ν CN (Μ (N cs (N CN n) <s CS high liver type antistatic agent (parts by weight) 1 I 1 1 1 1 1 I 1 1 τ—Η Hydrophilic compound addition method 1 Direct press 1 | Direct press in | 1 Direct press in I Masterbatch masterbatch 1 Direct press in 1 Masterbatch masterbatch masterbatch Masterbatch|Direct press in | | Direct press in I 1 Direct press in 1 Add amount (parts by weight) — 〇CN ο 卜 — 卜 — — Ο CN 卜 寸 · C^; — 〇〇m 〇〇 (S m • ΤΝΤΝ itmll m 丨 compound lj 1 compound 1| 丨 compound ι| 丨 compound 2| 丨 compound 3j 丨 compound 4" 丨 compound 5| 丨 compound ό | 丨 compound 6| 丨 compound 7j 丨 compound 8 ! 丨 compound 9| 丨 compound 11 丨 compound lj poly olefin resin _ £ i i i ο ο 〇ο 〇Ο 〇〇〇〇 Category 1 NUC8321 1 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 丨 Example 1 I | Example 2 I j Example 3 1 | Example 4 ] 1 Example 5 I 1 Example 6 1 | Example 7 I Example 8 | Example 9 I Comparative Example 1 丨 Comparative Example 2 | Comparative Example 3 I | Comparative Example 4 I Comparative Example 5 Reference Example 1 1}総令莛脃8二|} aiming ^§^^鲫菊啪啪啪濉1}闽2^_93±1* .1_葙?^__001^_味«奖跋§^制_长«"^ __"旮谳* -38- 201012649 [ε® Pulling speed (m/min) (N cK (N & iT) Os cs a; iTi <N iTi CN o; V) Ό (N (N a: m N ( Y/Ί On m as ma\ ON U^i Os ο 2 Pressure Temperature L (°〇) CN 1 H CN CN «—1 04 oj rj OJ <Ν inchΜ Μ尔_ 刍w r4 (N r"H <N 卜o fH r4 卜o CN CN ψ^< oi (N (N CN c〇^Η bubble modifier masterbatch (parts by weight) κη <nr*^ in Ui in ν£> ^Η Polyolefin resin blending amount (parts by weight) 〇ooooooooo 〇ooooo 〇o O 2 o 〇oo Ο ο Ο Ο Ο ι~Η Type NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 | NUC8321 1 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 NUC8321 1 NUC8321 Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Implementation Example 7 I Example 8] Example 9 Comparative Example 1 1 Comparative Example 2 I 1 Comparative Example 3 1 1 Comparative Example 4] Comparative Example 5 丨 Reference Example 1. Stupid _3- f - φδοο- i^l^siiiil" -- _oIM}siNI_0QIlgl-N1 义i "甶__"旮漱* -39- 201012649 The laminated results obtained from the examples, comparative examples and reference examples The evaluation of the thickness, appearance density, weighing, average cell diameter, surface resistivity, and detergency of the foam body is shown in Table 4.

-40- 201012649 【寸漱】 洗淨性 ◎ ◎ 〇 〇 〇 ◎ 〇 〇 〇 X X X X ※ ng #( ◎ 垂下量 (mm) 〇 CN (Ν κη »-Η cn CN m (N OO CSI 表面電阻率 (Ω ) | 8xl010 I 1 2χ1010 1 1 1 1 1 ο X 00 1 1 1 1 1 平均氣泡徑(mm) 寬方向 L〇.43一丨 1 0.42 I I 0.45 I L〇:4lJ I 0.40 1 1 0.44 1 | 0.40 1 1 0.44 1 1 0.44 1 0.42 | 0.42 1 1 0.42 1 0.40 | 1 0.42 | 壓出方向 L___ 0.53 0.48 0.40 0.55 | 0.52 | 0.54 0.40 1 0.52 1 0.52 1 L 0.49 0.58 0.51 1 0.41 0.50 外觀密度 (g/L) m cn VO m Ϊ—H m v〇 m m \〇 m vo 〇 m m 班 m m v〇 寸 o 厚度 (mm) 寸 ο 寸 ο Ο 1 < | 0.35 ! yn ci 寸 卜 o 寸 〇 寸 o | 0.35 j 寸 c5 O Ϊ _ 發泡層 1 21.4 1 丨 21.4 1 1 25.6 1 1 21.4 I 1 21.4 | 21-4 | 1 42.8 I 1 21.4 1 Γ21.4 1 Γ21.4Π 1 21.4 I 121.4 1 25.6 | r4 樹脂層 I s面側I 00 00 (Ν CN 00 oo OO i-H \D rn OO 00 00 OO f—^ 00 <N <N 1 I Μ面側| 00 〇〇 (Ν (Ν 00 oo OO v〇 cn oo i-H 00 00 00 00 <N CN 1 全體 (Ν CN (N <N U^i CN IT) (N (Ν cs iT) (N in (N (N 1實施例ϊ 1 1實施例2 1 1實施例3 1 1實施例4 1 實施例5 實施例6 實施例7 實施例8 實施例9 1比較例ϊ 1 丨比較例2 1 1比較例3 1 |比較例4 1比較例5 1 參考例1 。1— <鯽裝網妲^&賊忉鬆仞^劫爷骼龌尔它襄^^翅联嵌钮届^—旮^田劉鹚:们匡%#※ -41 - 201012649 表4中之洗淨性評估如以下進行。 <洗淨性之評估方法> 於平均表面租度〇·2μιη的鏡面之不銹鋼板將經硬質鍍 鉻處理的鋼板,以層合發泡體挾持,自該上面加上 50g/cm2的荷重,於60°C之環境下放置48小時。其後將鋼 板於純水中浸漬、洗淨。洗淨乾燥後’於鋼板表面吹氣並 以目視法觀察污垢(雲霧)狀況’依據以下基準進行評估 〇 ◎:完全無污垢(雲霧)。 〇:稍有點狀污垢(雲霧)存在。 X:存在多數污垢(雲霧)。 層合發泡體中之表面電阻率的測定如下進行。 <表面電阻率之測定> 將由層合發泡體所切出的3片試驗片(縱lOOmmx橫 lOOmmx厚度:試驗片厚度)作爲樣品。 表中的表面電阻率爲,將試驗片於相對濕度3 0%,溫 度30°C之環境下放置36小時,完成試驗片之狀態調整後 ,馬上於23°C,5 0%RH環境下測定表面電阻。此時,依 據前述JIS K6 271 ( 2001)的方法,採用以外加電壓500V 加壓至1分鐘後的表面電阻値,由所得之測定値的平均値 求得表面電阻率。測定裝置使用Takera理硏工業股份有 限公司製「TR8 601」。且’對於樹脂層未添加高分子型防 -42- 201012649 帶電劑之層合發泡體,並未進行表面電阻率之測定。 <垂下量(韌性之強度)的測定> 表4中的韌性強度測定如以下進行。 將寬度100mm、長度200mm、厚度:「層合發泡體厚 度」之試驗片將自實施例、比較例及參考例所得之層合發 泡體切成如層合發泡體的寬方向與試驗片之長度方向爲一 φ 致,將該試驗片於水平支持台上,使心軸面側爲上,將長 度200mm中之50mm部分由支持台端部漏出下支持,測定 試驗片漏出的部先端的垂下量[mm],評估層合發泡體之韌 性強度。且,因比壓出方向,寬方向下垂量較爲大,故僅 測定寬方向之垂下量。 【圖式簡單說明】 [圖1]表示本發明發泡薄片之製造方法的1例說明圖 【主要元件符號說明】 11 :樹脂層形成用壓出機 12:發泡體層形成用壓出機 13:共壓出用環狀塑模 Al、A2 :聚烯烴系樹脂 B :親水性化合物 B 1 :液狀的親水性化合物 -43 - 201012649 B2 :固體的親水性化合物 D :揮發性可塑劑 E 1 :聚烯烴系樹脂層形成用樹脂熔融物 E2 :聚烯烴系樹脂發泡體層形成用樹脂熔融物 F :物理發泡劑 G :添加劑 Η :層合發泡體 I :發泡體層 J :樹脂層 -44--40- 201012649 [Inch 漱] Washability ◎ ◎ 〇〇〇 ◎ 〇〇〇XXXX ※ ng #( ◎ Drop amount (mm) 〇CN (Ν κη »-Η cn CN m (N OO CSI surface resistivity ( Ω ) | 8xl010 I 1 2χ1010 1 1 1 1 1 ο X 00 1 1 1 1 1 Average bubble diameter (mm) Width direction L〇.43 丨1 0.42 II 0.45 IL〇:4lJ I 0.40 1 1 0.44 1 | 0.40 1 1 0.44 1 1 0.44 1 0.42 | 0.42 1 1 0.42 1 0.40 | 1 0.42 | Extrusion direction L___ 0.53 0.48 0.40 0.55 | 0.52 | 0.54 0.40 1 0.52 1 0.52 1 L 0.49 0.58 0.51 1 0.41 0.50 Appearance density (g/L m cn VO m Ϊ—H mv〇mm \〇m vo 〇mm class mmv〇 inch o thickness (mm) inch ο inch ο Ο 1 < | 0.35 ! yn ci inch inch o inch inch inch o | 0.35 j inch C5 O Ϊ _ foam layer 1 21.4 1 丨 21.4 1 1 25.6 1 1 21.4 I 1 21.4 | 21-4 | 1 42.8 I 1 21.4 1 Γ 21.4 1 Γ 21.4 Π 1 21.4 I 121.4 1 25.6 | r4 Resin layer I s face side I 00 00 (Ν CN 00 oo OO iH \D rn OO 00 00 OO f-^ 00 <N <N 1 I Μ 侧 side | 00 〇〇(Ν (Ν 00 oo OO v〇cn oo iH 00 00 00 00 <N CN 1 All (Ν CN (N < NU^i CN IT) (N (Ν cs iT) (N in (N 1 embodiment ϊ 1 1 embodiment 2 1 1 embodiment 3 1 1 embodiment 4 1 embodiment 5 embodiment 6 embodiment 7 implementation Example 8 Example 9 1 Comparative Example 丨 1 丨 Comparative Example 2 1 1 Comparative Example 3 1 | Comparative Example 4 1 Comparative Example 5 1 Reference Example 1 1 - <鲫装网妲^& thief 忉松仞^龌 龌 龌 襄 襄 ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ <Evaluation method of detergency> The hard-chrome-plated steel sheet was held in a laminated foam on a mirror-shaped stainless steel plate having an average surface rent of 〇·2 μm, and a load of 50 g/cm 2 was applied thereto. It was allowed to stand at 60 ° C for 48 hours. Thereafter, the steel sheet was immersed and washed in pure water. After washing and drying, 'blowing on the surface of the steel sheet and visually observing the condition of the dirt (cloud)' was evaluated according to the following criteria 〇 ◎: completely free of dirt (clouds). 〇: A little bit of dirt (clouds) is present. X: Most of the dirt (clouds) is present. The measurement of the surface resistivity in the laminated foam was carried out as follows. <Measurement of Surface Resistivity> Three test pieces (length 100 mm x width 100 mm x thickness: test piece thickness) cut out from the laminated foam were used as samples. The surface resistivity in the table was measured by placing the test piece at a relative humidity of 30% and a temperature of 30 ° C for 36 hours. After the state of the test piece was adjusted, it was immediately measured at 23 ° C and 50% RH. Surface resistance. At this time, according to the method of JIS K6 271 (2001), the surface resistivity after pressurization to a voltage of 500 V for 1 minute was used, and the surface resistivity of the obtained enthalpy was measured. The measuring device uses "TR8 601" manufactured by Takera Lai Industrial Co., Ltd. Further, the surface resistivity of the laminated foam in which the polymer layer was not added with the polymer type anti-42-201012649 was not measured. <Measurement of the amount of drooping (strength of toughness)> The measurement of the toughness in Table 4 was carried out as follows. A test piece having a width of 100 mm, a length of 200 mm, and a thickness of "laminate foam thickness" was cut into the width direction and test of the laminated foam obtained from the examples, the comparative examples, and the reference examples. The length direction of the sheet is φ, the test piece is placed on the horizontal support table, the mandrel surface side is upward, and the 50 mm part of the length 200 mm is supported by the end of the support table, and the tip end of the test piece leaking is measured. The amount of dangling [mm] was evaluated to evaluate the toughness of the laminated foam. Further, since the amount of sag in the width direction is larger than the direction of extrusion, only the amount of drooping in the width direction is measured. [Brief Description of the Drawings] Fig. 1 is a view showing an example of a method for producing a foamed sheet of the present invention. [Description of main elements and symbols] 11: Presser for forming a resin layer 12: Extruder 13 for forming a foam layer : cyclic molding die A, A2: polyolefin resin B: hydrophilic compound B 1 : liquid hydrophilic compound - 43 - 201012649 B2 : solid hydrophilic compound D : volatile plasticizer E 1 Resin melt E2 for polyolefin resin layer formation: Resin melt for forming polyolefin resin foam layer F: Physical foaming agent G: Additive Η: Laminated foam I: Foam layer J: Resin layer -44-

Claims (1)

201012649 七、申請專利範圍: 1·—種聚烯烴系樹脂層合發泡體,其爲於聚烯烴系樹 脂發泡體層之至少一面上層合聚烯烴系樹脂層所成之聚烯 烴系樹脂層合發泡體,其特徵爲將選自聚環氧化物及親水 親油平衡(HLB値)8以上的界面活性劑之1種以上的親 水性化合物,於前述聚烯烴系樹脂層中對於構成該樹脂層 之聚稀烴系樹脂100重量份而言,以0.5〜20重量份之比 φ 率下添加的同時, 前述親水性化合物實質上並未添加於前述聚烯烴系樹 脂發泡體層。 、 2. 如申請專利範圍第1項之聚烯烴系樹脂層合發泡體 ,其中前述聚環氧化物爲聚環氧乙烷。 3. 如申請專利範圍第1項或第2項之聚烯烴系樹脂層 合發泡體,其中前述聚環氧化物於溫度2(TC爲液狀。 4. 如申請專利範圍第1項至第3項中任一項之聚烯烴 φ 系樹脂層合發泡體’其中前述親水性化合物之數平均分子 量爲1 000以下。 5. 如申請專利範圍第1項至第4項中任一項之聚烯烴 系樹脂層合發泡體’其中於前述聚烯烴系樹脂層中’添加 聚烯烴系樹脂與前述親水性化合物之相溶化劑。 6. 如申請專利範圍第1項至第5項中任一項之聚烯烴 系樹脂層合發泡體’其中於聚嫌烴系樹脂層合發泡體之前 述親水性化合物的添加量,對於該層合發泡體100重量份 而言爲2重量份以下。 -45- 201012649 7. 如申請專利範圍第1項至第6項中任一項之聚烯烴 系樹脂層合發泡體,其中前述聚燒烴系樹脂發泡體層爲壓 出發泡體,聚烯烴系樹脂層合發泡體之外觀密度爲10〜 200g/L,厚度爲 0.2 〜2mm。 8. 如申請專利範圍第7項之聚嫌烴系樹脂層合發泡體 ,其中前述聚烯烴系樹脂層爲藉由共壓出於聚烯烴系樹脂 發泡體層進行層合者。 9. 如申請專利範圍第1項至第8項中任一項之聚烯烴 系樹脂層合發泡體,其中於前述聚烯烴系樹脂層’高分子 型防帶電劑以對於聚烯烴系樹脂100重量份爲2〜30重量 份之比率添加,該樹脂層之表面電阻率爲lxl〇8〜1x1014 (Ω)。 10. 如申請專利範圍第9項之聚烯烴系樹脂層合發泡 體,其中前述高分子型防帶電劑係以聚醚與聚烯烴之嵌段 共聚物作爲主成分的防帶電劑。 -46-201012649 VII. Patent application scope: A polyolefin resin laminated foam which is a polyolefin resin laminated layer formed by laminating a polyolefin resin layer on at least one surface of a polyolefin resin foam layer. The foam is characterized in that one or more hydrophilic compounds selected from the group consisting of a polyepoxide and a hydrophilic-lipophilic balance (HLB値) 8 or more are used to form the resin in the polyolefin-based resin layer. 100 parts by weight of the layer of the polyolefin resin is added at a ratio of 0.5 to 20 parts by weight, and the hydrophilic compound is not substantially added to the polyolefin resin foam layer. 2. The polyolefin-based resin laminated foam according to claim 1, wherein the polyepoxide is polyethylene oxide. 3. The polyolefin-based resin laminated foam according to claim 1 or 2, wherein the polyepoxide is at a temperature of 2 (TC is a liquid. 4. If the patent application is in the first to the first The polyolefin φ-based resin laminated foam of any one of the above-mentioned, wherein the number average molecular weight of the hydrophilic compound is 1 000 or less. 5. The method according to any one of claims 1 to 4 A polyolefin-based resin laminated foamed body in which a polyolefin-based resin and a hydrophilic compound are added to the polyolefin-based resin layer. 6. In the first to fifth aspects of the patent application scope In the polyolefin-based resin laminated foamed body, the amount of the hydrophilic compound added to the polyether-based resin laminated foam is 2 parts by weight based on 100 parts by weight of the laminated foam. The polyolefin-based resin laminated foam according to any one of the above-mentioned items, wherein the polyalkylene-based resin foam layer is an extruded foam, The polyolefin resin laminated foam has an apparent density of 10 to 200 g/L, and is thick. 8. The polyether-based resin laminated foam of the seventh aspect of the invention, wherein the polyolefin-based resin layer is laminated by co-pressing a polyolefin-based resin foam layer The polyolefin-based resin laminated foam according to any one of the first to eighth aspects of the invention, wherein the polyolefin-based resin layer is a polymer-based antistatic agent for a polyolefin system. 100 parts by weight of the resin is added in a ratio of 2 to 30 parts by weight, and the surface resistivity of the resin layer is lxl 〇 8 to 1 x 1014 (Ω). 10. Polyolefin-based resin laminated foam according to claim 9 The polymer type antistatic agent is an antistatic agent containing a block copolymer of a polyether and a polyolefin as a main component.
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