JP2010270243A - Polypropylene-based resin in-mold foam molded product - Google Patents

Polypropylene-based resin in-mold foam molded product Download PDF

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JP2010270243A
JP2010270243A JP2009123980A JP2009123980A JP2010270243A JP 2010270243 A JP2010270243 A JP 2010270243A JP 2009123980 A JP2009123980 A JP 2009123980A JP 2009123980 A JP2009123980 A JP 2009123980A JP 2010270243 A JP2010270243 A JP 2010270243A
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polypropylene resin
polypropylene
mold foam
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based resin
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JP5410157B2 (en
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Yoshimi Yoneda
祥美 米田
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Kaneka Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a polypropylene-based resin in-mold foam molded product having improved flame retardancy in a black polypropylene-based resin in-mold foam molded product containing carbon black. <P>SOLUTION: The polypropylene-based resin in-mold foam molded product comprises polypropylene-based resin foamed particles containing 0.1-10 wt.% of carbon black and a 3-6C polyhydric alcohol having ≥3 hydroxy groups. The polypropylene-based resin in-mold foam molded product exhibits self-extinguishability or slow combustibleness in a combustion testing method stipulated by FMVSS302. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、ポリプロピレン系樹脂発泡粒子からなる難燃性を有するポリプロピレン系樹脂型内発泡成形体に関する。   TECHNICAL FIELD The present invention relates to a polypropylene resin in-mold foam-molded article having flame retardancy composed of polypropylene resin foam particles.

ポリプロピレン系樹脂を発泡せしめたポリプロピレン系樹脂発泡粒子を型内発泡成形用の金型内に充填した後、これらを加熱融着させることによって得られるポリプロピレン系樹脂型内発泡成形体は、すでに包装材、緩衝材、断熱材、建築資材、自動車用部品等の広範な用途に供されている。このような用途の中でも、建築資材や自動車部品等の分野においては、難燃性を有することが求められており、必要に応じて難燃剤や難燃助剤を樹脂中に含有させたポリプロピレン系樹脂発泡粒子やこのポリプロピレン系樹脂発泡粒子を使用した型内発泡成形体が提案されている(例えば、特許文献1、2)。しかしながら、これらの難燃剤や難燃助剤を含有させたポリプロピレン系樹脂型内発泡成形体は、機械的強度の低下や、樹脂からブリードすることによる金型の汚染など問題を抱えており、また、ハロゲン系難燃剤やリン系難燃剤は環境適合性の問題をも抱えていると言われており、これらの難燃剤や難燃助剤を用いずに難燃性を発現できることが好ましい。   Polypropylene resin foam-in-mold molded product obtained by filling polypropylene resin foamed polypropylene resin foam into a mold for in-mold foam molding and then heat-sealing them is already a packaging material. It is used for a wide range of applications such as cushioning materials, heat insulating materials, building materials, and automotive parts. Among these uses, in the field of building materials and automobile parts, it is required to have flame retardancy, and a polypropylene system containing a flame retardant and a flame retardant aid in the resin as necessary. In-mold foam moldings using resin foam particles and polypropylene resin foam particles have been proposed (for example, Patent Documents 1 and 2). However, the polypropylene resin-in-mold foam-molded products containing these flame retardants and flame retardant aids have problems such as a decrease in mechanical strength and contamination of the mold caused by bleeding from the resin. Halogen flame retardants and phosphorus flame retardants are also said to have environmental compatibility problems, and it is preferable that flame retardancy can be expressed without using these flame retardants and flame retardant aids.

また、外観の点から着色したポリプロピレン系樹脂発泡粒子や該ポリプロピレン系樹脂発泡粒子を使用したポリプロピレン系樹脂型内発泡成形体が要求される場合があり、特に自動車部品等の分野では黒色化したポリプロピレン系樹脂発泡粒子や型内発泡成形体が要求されることから、カーボンブラックを用いて黒色化したポリプロピレン系樹脂発泡粒子および該型内発泡成形体が提案されている(例えば、特許文献3)。しかし、カーボンブラックは難燃性を低下させることから、カーボンブラックを添加しない場合に比べて多量の難燃剤や難燃助剤を必要とすることになり、機械的強度の低下などの問題が顕在化することになる。   In addition, polypropylene resin foam particles colored from the viewpoint of appearance and polypropylene resin in-mold foam moldings using the polypropylene resin foam particles may be required. In particular, blackened polypropylene in the field of automobile parts and the like. Therefore, polypropylene resin foam particles that have been blackened with carbon black and the in-mold foam molding have been proposed (for example, Patent Document 3). However, since carbon black lowers the flame retardancy, it requires a larger amount of flame retardant and flame retardant aid than when carbon black is not added, and problems such as a decrease in mechanical strength are apparent. It will become.

一方、特許文献4には、土木、建築、園芸等の排水資材等に用いられる、親水性に優れ水濡れが速やかで、水が成型体に接触した当初から良好な通水性を呈する連通した空隙を有する通水性発泡成形体を提供することを目的として、発泡成形体に親水性付与剤を含有または塗布させる技術が開示されている。親水性付与剤としては、エチレングリコール、グリセリン、ポリエチレングリコール等の親水性液体や界面活性剤が例示されている。   On the other hand, Patent Document 4 discloses a void that is used for drainage materials for civil engineering, architecture, horticulture, etc., has excellent hydrophilicity, has quick water wetting, and exhibits good water permeability from the beginning when the water contacts the molded body. For the purpose of providing a water-permeable foamed molded article having the above, a technique for incorporating or applying a hydrophilicity imparting agent to the foamed molded article is disclosed. Examples of the hydrophilicity-imparting agent include hydrophilic liquids and surfactants such as ethylene glycol, glycerin, and polyethylene glycol.

特開平7−309967号公報JP-A-7-309967 特開平10−147661号公報JP-A-10-147661 特開平7−300537号公報JP-A-7-300537 特開平8−59875号公報Japanese Patent Laid-Open No. 8-59875

本発明は、カーボンブラックを含有している黒色のポリプロピレン系樹脂型内発泡成形体において、難燃性が改善されたポリプロピレン系樹脂型内発泡成形体を提供することを目的とする。   An object of the present invention is to provide a polypropylene resin-in-mold foam-molded product having improved flame retardancy in a black polypropylene-based resin mold-in-mold foam-molded product containing carbon black.

本発明者らは鋭意検討の結果、カーボンブラックを含んでなるポリプロピレン系樹脂発泡粒子に、通常は添加することで難燃性が低下すると考えられているグリセリンに代表される炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを所定量添加することにより、意想外にも難燃性が向上することを見出し、本発明の完成に至った。   As a result of intensive investigations, the present inventors have made 3 to 6 carbon atoms typified by glycerin, which is considered to have reduced flame retardancy when added to polypropylene resin expanded particles containing carbon black. Moreover, by adding a predetermined amount of polyhydric alcohol having 3 or more hydroxyl groups, it was found that the flame retardancy is unexpectedly improved, and the present invention has been completed.

すなわち本発明は、以下の構成よりなる。
〔1〕 カーボンブラック0.1重量%以上10重量%以下、および炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを含有するポリプロピレン系樹脂発泡粒子からなるポリプロピレン系樹脂型内発泡成形体であって、該ポリプロピレン系樹脂型内発泡成形体がFMVSS302に定められる燃焼試験法にて自己消火性または遅燃性を示すことを特徴とするポリプロピレン系樹脂型内発泡成形体。
〔2〕 成形体密度が5g/L以上200g/L未満である〔1〕記載のポリプロピレン系樹脂型内発泡成形体。
〔3〕 炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを0.05重量%以上3重量%以下含んでなる、〔1〕または〔2〕に記載のポリプロピレン系樹脂型内発泡成形体。
〔4〕 炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールが、グリセリンである〔1〕〜〔3〕何れかに記載のポリプロピレン系樹脂型内発泡成形体。
That is, this invention consists of the following structures.
[1] Polypropylene resin in-mold foam composed of polypropylene resin foam particles containing 0.1 to 10% by weight of carbon black and a polyhydric alcohol having 3 to 6 carbon atoms and having 3 or more hydroxyl groups A polypropylene-based resin-mold-in-mold foam-molded article, wherein the polypropylene-series resin-mold-in-mold foam-molded article exhibits self-extinguishing properties or slow-flammability by a combustion test method defined in FMVSS302.
[2] The polypropylene resin in-mold foam molded product according to [1], wherein the molded product density is 5 g / L or more and less than 200 g / L.
[3] The polypropylene resin mold according to [1] or [2], comprising 0.05 to 3% by weight of a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups. Foam molded body.
[4] The polypropylene resin in-mold foam molded article according to any one of [1] to [3], wherein the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups is glycerin.

本発明のカーボンブラックおよび炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを含有するポリプロピレン系樹脂発泡粒子からなるポリプロピレン系樹脂型内発泡成形体は、FMVSS302試験法において、同じ量のカーボンブラックのみを添加したポリプロピレン系樹脂型内発泡成形体と比較して難燃性が向上する。   In the FMVSS302 test method, the same amount of the polypropylene resin-in-mold foam-molded article comprising the carbon black of the present invention and the polypropylene resin foamed particles containing polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups. The flame retardancy is improved as compared with the polypropylene resin in-mold foam-molded product to which only carbon black is added.

本発明において用いるポリプロピレン系樹脂とは、単量体成分としてプロピレンを60重量%以上、好ましくは、80重量%以上含んでなる樹脂をいい、プロピレンと共重合可能な単量体を含んでいてもかまわない。具体的にはプロピレン単独重合体、エチレン−プロピレンブロック共重合体、エチレン−プロピレンランダム共重合体、ブテン−プロピレンランダム共重合体、ブテン−プロピレンブロック共重合体、エチレン−ブテン−プロピレンランダム共重合体が例示することが出来る。この中でも、エチレン含有量が0.1重量%以上10重量%以下のエチレン−プロピレンランダム共重合体、あるいは、エチレンと1−ブテンを合計0.1重量%以上、10重量%以下含有し、かつ1−ブテンが0.5重量%以上含まれるエチレン−ブテン−プロピレンランダム共重合体が成形性や機械的強度の観点からより好ましい。   The polypropylene-based resin used in the present invention refers to a resin containing 60% by weight or more, preferably 80% by weight or more of propylene as a monomer component, and may contain a monomer copolymerizable with propylene. It doesn't matter. Specifically, propylene homopolymer, ethylene-propylene block copolymer, ethylene-propylene random copolymer, butene-propylene random copolymer, butene-propylene block copolymer, ethylene-butene-propylene random copolymer Can be illustrated. Among these, ethylene-propylene random copolymer having an ethylene content of 0.1 wt% to 10 wt%, or a total of 0.1 wt% and 10 wt% of ethylene and 1-butene, and An ethylene-butene-propylene random copolymer containing 0.5% by weight or more of 1-butene is more preferable from the viewpoints of moldability and mechanical strength.

これらポリプロピレン系樹脂は無架橋のものであっても架橋したものであっても良いが、リサイクルの点からいえば無架橋のものであるのが好ましい。   These polypropylene resins may be non-cross-linked or cross-linked, but are preferably non-cross-linked from the viewpoint of recycling.

本発明で用いることのできるポリプロピレン系樹脂の融点は、130℃以上165℃以下であることが好ましく、更には135℃以上155℃以下のものが好ましい。融点が130℃未満の場合、耐熱性、機械的強度が十分でない傾向がある。また、融点が165℃を超える場合、型内発泡成形時の融着を確保することが難しくなる傾向がある。ここで、前記融点とは、示差走査熱量計によってポリプロピレン系樹脂1mg以上10mg以下を40℃から220℃まで10℃/分の速度で昇温し、その後40℃まで10℃/分の速度で冷却し、再度220℃まで10℃/分の速度で昇温した時に得られるDSC曲線における吸熱ピークのピーク温度をいう。   The melting point of the polypropylene resin that can be used in the present invention is preferably 130 ° C. or higher and 165 ° C. or lower, and more preferably 135 ° C. or higher and 155 ° C. or lower. When the melting point is less than 130 ° C., heat resistance and mechanical strength tend to be insufficient. Moreover, when melting | fusing point exceeds 165 degreeC, there exists a tendency for it to become difficult to ensure the melt | fusion at the time of in-mold foam molding. Here, the melting point refers to a temperature of 10 to 10 mg of polypropylene-based resin raised from 40 ° C. to 220 ° C. at a rate of 10 ° C./min by a differential scanning calorimeter, and then cooled to 40 ° C. at a rate of 10 ° C./min. The peak temperature of the endothermic peak in the DSC curve obtained when the temperature is increased again to 220 ° C. at a rate of 10 ° C./min.

本発明で用いることが出来るポリプロピレン系樹脂のメルトインデックス(以下、MI値)は0.5g/10分以上30g/10分以下であることが好ましく、より好ましくは2g/10分以上20g/以下、さらに好ましくは5g/10分以上10g/10分以下である。   The melt index (hereinafter referred to as MI value) of the polypropylene resin that can be used in the present invention is preferably 0.5 g / 10 min to 30 g / 10 min, more preferably 2 g / 10 min to 20 g / min, More preferably, it is 5 g / 10 min or more and 10 g / 10 min or less.

MI値が0.5g/10分未満の場合、高発泡倍率のポリプロピレン系樹脂発泡粒子が得られにくく、30g/10分を超える場合、ポリプロピレン系樹脂発泡粒子の気泡が破泡し易く、ポリプロピレン系樹脂発泡粒子の連泡率が高くなる傾向にある。   When the MI value is less than 0.5 g / 10 minutes, it is difficult to obtain polypropylene-based resin expanded particles with a high expansion ratio. When the MI value exceeds 30 g / 10 minutes, the bubbles of the polypropylene-based resin expanded particles easily break, The open cell ratio of the resin foam particles tends to increase.

なお、本発明において、MI値とはJIS K7210に準拠し、温度230℃、荷重2.16kgで測定した値である。   In the present invention, the MI value is a value measured at a temperature of 230 ° C. and a load of 2.16 kg in accordance with JIS K7210.

また、融点、MI値が異なるポリプロピレン系樹脂を2種以上混合して、前記の範囲としても良い。   Further, two or more types of polypropylene resins having different melting points and MI values may be mixed to obtain the above range.

本発明におけるカーボンブラックは、ポリプロピレン系樹脂発泡粒子中、0.1重量%以上10重量%以下であり、好ましくは1重量%以上7重量%以下、さらに好ましくは3重量%以上5重量%以下である。カーボンブラックが0.1重量%未満の場合、ポリプロピレン系樹脂型内発泡成形体にした時に、黒色度合いが薄く、10重量%を超える場合、燃焼速度が速くなり、FMVSS302燃焼試験をクリアしない。   Carbon black in the present invention is 0.1 wt% or more and 10 wt% or less, preferably 1 wt% or more and 7 wt% or less, more preferably 3 wt% or more and 5 wt% or less in the expanded polypropylene resin particles. is there. When the carbon black is less than 0.1% by weight, the degree of blackness is thin when it is made into a polypropylene resin-molded in-mold foam, and when it exceeds 10% by weight, the combustion speed is increased and the FMVSS302 combustion test is not cleared.

本発明に用いるカーボンブラックの種類について制限はなく、ケッチェンブラック、サーマルブラック、ファーネスブラック、チャンネルブラック、ランプブラック、ガスブラック、ローラーブラック、アセチレンブラックなどを用いることができる。   There is no restriction | limiting about the kind of carbon black used for this invention, Ketjen black, thermal black, furnace black, channel black, lamp black, gas black, roller black, acetylene black, etc. can be used.

本発明に用いるカーボンブラックの粒径にも特に制限はないが、粒径としては0.1nm以上10000nm以下が好ましい。0.1nm未満ではハンドリングしにくくなる傾向があり、10000nmを超えると樹脂への分散性が悪くなり色むらの原因になる傾向がある。また、粒子が凝集したストラクチャーの大きさとしてはおおむね数十nm以上数百nm以下のものを用いればよい。   The particle size of carbon black used in the present invention is not particularly limited, but the particle size is preferably 0.1 nm or more and 10,000 nm or less. If it is less than 0.1 nm, it tends to be difficult to handle, and if it exceeds 10,000 nm, the dispersibility in the resin tends to be poor and color unevenness tends to be caused. In addition, the size of the structure in which the particles are aggregated may be approximately several tens nm to several hundreds nm.

本発明で使用する炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールとしては、具体的には、グリセリン、1,2,4−ブタントリオール、ジグリセリン、ペンタエリスリトール、トリメチロールプロパン、ソルビトール、D−マンニトール、エリスリトール、ヘキサントリオール、キシリトール、D−キシロース、イノシトール、フルクトース、ガラクトース、グルコース、マンノース等が挙げられる。中でも、グリセリン、ジグリセリン、ペンタエリスリトール、トリメチロールプロパン、ソルビトール、D−マンニトールから選ばれる1種以上であることが好ましく、より好ましくは、グリセリンである。グリセリンは、製造中に排水中へ溶出した場合においても易分解性を示すことから環境影響が小さい特徴も有する。一般に入手し易く、安価な点でも好適である。   Specific examples of the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups used in the present invention include glycerin, 1,2,4-butanetriol, diglycerin, pentaerythritol, and trimethylolpropane. Sorbitol, D-mannitol, erythritol, hexanetriol, xylitol, D-xylose, inositol, fructose, galactose, glucose, mannose and the like. Especially, it is preferable that it is 1 or more types chosen from glycerol, diglycerol, pentaerythritol, a trimethylol propane, sorbitol, and D-mannitol, More preferably, it is glycerol. Glycerin also has a feature that it has a small environmental impact because it exhibits easy degradability even when it is eluted into wastewater during production. In general, it is easy to obtain and inexpensive, which is preferable.

一般に分子内に水酸基を多く持ついわゆる親水性物質はポリプロピレン系樹脂への相溶性にやや劣る特性があるが、本発明で使用する炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールであれば、ポリプロピレン系樹脂にブレンド後、押出機にて混練、ストランドカット法にてポリプロピレン系樹脂粒子を作製する工程においても比較的良好に分散するためストランド切れの発生や、溶融樹脂の送り不安定などのトラブルの発生が少ない傾向がある。さらに均一な気泡で倍率バラツキが小さいポリプロピレン系樹脂発泡粒子が得られる傾向がある。該ポリプロピレン系樹脂発泡粒子を用いて型内発泡成形して得られたポリプロピレン系樹脂型内発泡成形体は良好な難燃性を示す。   In general, so-called hydrophilic substances having a large number of hydroxyl groups in the molecule are slightly inferior in compatibility with polypropylene resins. However, polyhydric alcohols having 3 to 6 carbon atoms and 3 or more hydroxyl groups used in the present invention. Then, after blending with a polypropylene resin, kneading with an extruder and dispersion in the process of producing polypropylene resin particles by a strand cutting method results in relatively good dispersion, so that strand breakage and molten resin feed are not possible. There is a tendency for troubles such as stability to occur less frequently. Furthermore, there is a tendency that polypropylene-based resin expanded particles having uniform bubbles and small variation in magnification are obtained. A polypropylene resin in-mold foam molded article obtained by in-mold foam molding using the polypropylene resin foam particles exhibits good flame retardancy.

炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールの添加量は、0.05重量%以上3重量%以下であることが好ましく、より好ましくは0.07重量%以上1重量%以下であり、更に好ましくは0.1重量%以上0.7重量%以下である。 炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールの添加量が0.05重量%より少ないと、ポリプロピレン系樹脂発泡粒子の難燃性を向上させることが難しい場合がある。添加量が3重量%を超えては、難燃性が低下する傾向がある。   The addition amount of the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups is preferably 0.05 to 3% by weight, more preferably 0.07 to 1% by weight. Or less, more preferably 0.1 wt% or more and 0.7 wt% or less. If the addition amount of the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups is less than 0.05% by weight, it may be difficult to improve the flame retardancy of the polypropylene resin expanded particles. When the addition amount exceeds 3% by weight, the flame retardancy tends to decrease.

炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールとして、グリセリンを使用する場合、その添加量は、0.05重量%以上0.8重量%以下であることが好ましい。より好ましくは0.05重量%以上0.5重量%以下であり、最も好ましくは0.05重量%以上0.3重量%以下である。   When glycerin is used as the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups, the amount added is preferably 0.05% by weight or more and 0.8% by weight or less. More preferably, it is 0.05 weight% or more and 0.5 weight% or less, Most preferably, it is 0.05 weight% or more and 0.3 weight% or less.

ここで、ポリプロピレン系樹脂粒子、およびポリプロピレン系樹脂発泡粒子中の炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールの含有量は、ELSD(エバポレート光散乱)を検出器とするHPLC装置(例えば、島津製作所製高速液体クロマトグラフ:プロミネンス高圧グラジエントシステム)を用いて定量することができる。   Here, the content of the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups in the polypropylene resin particles and the polypropylene resin expanded particles is determined by HPLC using ELSD (evaporation light scattering) as a detector. It can be quantified using an apparatus (for example, a high performance liquid chromatograph manufactured by Shimadzu Corporation: Prominence High Pressure Gradient System).

本発明のポリプロピレン系樹脂発泡粒子には、カーボンブラック、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコール以外に必要に応じて、発泡核剤、親水性物質、相溶化剤、帯電防止剤、着色剤、安定剤、耐候剤、難燃剤などの各種添加剤を使用することが出来る。   In addition to carbon black, a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups, the foamed polypropylene resin particles of the present invention include, as necessary, a foam nucleating agent, a hydrophilic substance, a compatibilizing agent, Various additives such as antistatic agents, colorants, stabilizers, weathering agents, flame retardants and the like can be used.

発泡核剤は、発泡の時に気泡核の形成を促す物質をいい、たとえば、タルク、炭酸カルシウム、シリカ、カオリン、硫酸バリウム、水酸化カルシウム、水酸化アルミニウム、酸化アルミニウム、酸化チタン、ゼオライト等の無機物質、ステアリン酸カルシウム、ステアリン酸バリウムなどの脂肪酸金属塩などが挙げられ、これらを単独、或いは、2種以上を併用することが出来る。これらの中でも、タルク、炭酸カルシウム、ステアリン酸カルシウムが好ましい。更に粒径分布がシャープであることが望ましい。   Foam nucleating agent refers to a substance that promotes the formation of cell nuclei during foaming. For example, inorganic substances such as talc, calcium carbonate, silica, kaolin, barium sulfate, calcium hydroxide, aluminum hydroxide, aluminum oxide, titanium oxide, and zeolite Substances, fatty acid metal salts such as calcium stearate and barium stearate can be mentioned, and these can be used alone or in combination of two or more. Among these, talc, calcium carbonate, and calcium stearate are preferable. Further, it is desirable that the particle size distribution is sharp.

また、ポリプロピレン系樹脂発泡粒子の発泡倍率を向上させるために、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコール以外の親水性物質を使用することも可能である。親水性物質とは、発泡粒子を製造する際に、樹脂中の含浸水分量を増加させる物質であり、具体例として、塩化ナトリウム、塩化カルシウム、塩化マグネシウム、ホウ砂、ホウ酸カルシウム、ホウ酸亜鉛等の水溶性無機物;メラミン、イソシアヌル酸、メラミン・イソシアヌル酸縮合物等の吸水性有機物;ポリエチレングリコール、およびセチルアルコール、ステアリルアルコールといった炭素数12以上18以下の脂肪アルコール類、等の親水性重合体が挙げられる。中でも、ポリエチレングリコール、メラミンが好適である。   Moreover, in order to improve the expansion ratio of the polypropylene resin expanded particles, it is also possible to use a hydrophilic substance other than polyhydric alcohol having 3 to 6 carbon atoms and having 3 or more hydroxyl groups. A hydrophilic substance is a substance that increases the amount of water impregnated in a resin when producing expanded particles. Specific examples include sodium chloride, calcium chloride, magnesium chloride, borax, calcium borate, and zinc borate. Water-soluble inorganic substances such as melamine, isocyanuric acid, water-absorbing organic substances such as melamine / isocyanuric acid condensate, etc .; hydrophilic polymers such as polyethylene glycol and fatty alcohols having 12 to 18 carbon atoms such as cetyl alcohol and stearyl alcohol Is mentioned. Of these, polyethylene glycol and melamine are preferred.

ポリプロピレン系樹脂は、通常、発泡に利用しやすいようにあらかじめ押出機、ニーダー、バンバリミキサー、ロール等を用いて溶融し、円柱状、楕円状、球状、立方体状、直方体上等のような所望の粒子形状のポリプロピレン系樹脂粒子とする。ポリプロピレン系樹脂粒子の平均粒重量は、0.5〜3.0mgが好ましく、より好ましくは0.5〜2.0mg、更に好ましくは0.5〜1.5mgである。この際に、カーボンブラック、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコール、その他必要に応じて添加する添加剤を一緒に溶融混練し、ポリプロピレン系樹脂粒子とすることが好ましい。カーボンブラック、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコール、その他必要に応じて添加する添加剤は、そのまま添加してもよいし、予め10%以上60%以下の濃度のマスターバッチにして添加してもよい。   Polypropylene resin is usually melted beforehand using an extruder, kneader, Banbury mixer, roll, etc. so that it can be easily used for foaming, and has a desired shape such as a cylinder, ellipse, sphere, cube, cuboid, etc. Particle-shaped polypropylene resin particles are used. The average particle weight of the polypropylene resin particles is preferably 0.5 to 3.0 mg, more preferably 0.5 to 2.0 mg, and still more preferably 0.5 to 1.5 mg. At this time, it is preferable to melt and knead together carbon black, a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups, and other additives to be added as necessary to obtain polypropylene resin particles. . Carbon black, a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups, and other additives that are added as necessary may be added as they are or may have a concentration of 10% to 60% in advance. A master batch may be added.

上記のようにして得たポリプロピレン系樹脂発泡粒子を密閉圧力容器において発泡剤とともに内容物を攪拌流動させながら水等の分散媒に分散させ、ポリプロピレン系樹脂の軟化温度以上、具体的にはポリプロピレン系樹脂の融点−10℃〜融点+10℃に加熱し、当該温度(以下、発泡温度と称す場合がある)にて一定時間保持して、しかる後、容器の一端を開放し、容器内圧力を発泡剤の蒸気圧以上の圧力に保持しながらポリプロピレン系樹脂粒子と分散媒とを容器内よりも低圧の雰囲気下(通常は大気圧下)に放出してポリプロピレン系樹脂粒子を発泡させ、ポリプロピレン系樹脂発泡粒子を得ることができる。   The polypropylene resin expanded particles obtained as described above are dispersed in a dispersion medium such as water while stirring and flowing the contents together with the foaming agent in a sealed pressure vessel, and more than the softening temperature of the polypropylene resin. Heat to the melting point of the resin from −10 ° C. to the melting point + 10 ° C., hold at that temperature (hereinafter sometimes referred to as the foaming temperature) for a certain period of time, then open one end of the container and foam the pressure inside the container. While maintaining the pressure higher than the vapor pressure of the agent, the polypropylene resin particles and the dispersion medium are released into a lower pressure atmosphere (usually under atmospheric pressure) than inside the container to expand the polypropylene resin particles, and the polypropylene resin Expanded particles can be obtained.

発泡剤としては、例えば、ブタン、プロパン、ペンタン、ヘキサン、ヘプタン、シクロブタン、シクロペンタンなどの脂肪族炭化水素、空気、窒素、二酸化炭素、ヘリウム、ネオン、アルゴン、水などの無機物質などを用いることができ、これらの中から2つ以上を併用しても用いても良い。なお、水を発泡剤として用いる場合は、発泡剤を得る際に用いる分散媒の水を利用できる。   Examples of the blowing agent include aliphatic hydrocarbons such as butane, propane, pentane, hexane, heptane, cyclobutane, and cyclopentane, and inorganic substances such as air, nitrogen, carbon dioxide, helium, neon, argon, and water. Two or more of these may be used in combination. In addition, when using water as a foaming agent, the water of the dispersion medium used when obtaining a foaming agent can be utilized.

発泡剤の使用量は、得ようとする発泡粒子の発泡倍率や発泡温度との関係で適宜調節されるものであるが、加熱中、又は加熱後に発泡温度で1.5〜7MPa(G)の圧力範囲となるように容器内に圧入する、あるいは発泡温度にて該圧力を示すような量を予め加熱前に仕込んでおくことが好ましい。   The amount of the foaming agent used is appropriately adjusted in relation to the expansion ratio and expansion temperature of the expanded particles to be obtained. The expansion temperature is 1.5 to 7 MPa (G) during or after heating. It is preferable to press-fit into the container so as to be in the pressure range, or to prepare in advance an amount that indicates the pressure at the foaming temperature before heating.

ポリプロピレン系樹脂粒子を分散媒に分散させ、発泡温度に加熱する場合の樹脂粒子相互の融着を防止するために分散剤を用いることができる。このような分散剤としては、例えば、リン酸カルシウム、酸化アルミニウム、酸化チタン、水酸化アルミニウム、カオリン、タルク、マイカ、硫酸バリウムなどが挙げられる。分散剤の平均粒径に特に制限はないが、0.001以上50μm以下が好ましく、より好ましくは0.01μm以上20μm以下である。0.001μm未満の場合ハンドリングしにくくなる場合があり、50μmを超えると分散剤としての性能が低下する傾向にある。   A dispersant can be used to prevent fusion of the resin particles when the polypropylene resin particles are dispersed in the dispersion medium and heated to the foaming temperature. Examples of such a dispersant include calcium phosphate, aluminum oxide, titanium oxide, aluminum hydroxide, kaolin, talc, mica, and barium sulfate. Although there is no restriction | limiting in particular in the average particle diameter of a dispersing agent, 0.001 or more and 50 micrometers or less are preferable, More preferably, they are 0.01 micrometer or more and 20 micrometers or less. When it is less than 0.001 μm, it may be difficult to handle, and when it exceeds 50 μm, the performance as a dispersant tends to decrease.

分散剤の添加量は、発泡温度、発泡剤の添加量、発泡剤の種類によりポリプロピレン系樹脂粒子相互の融着を防止するよう適宜調整されるものであるが、一般的にはポリプロピレン系樹脂粒子100重量部に対し、0.01重量部以上5重量部以下が好ましい。0.01重量部未満では分散剤としての性能が低下しポリプロピレン系樹脂粒子同士の融着が見られる場合があり、5重量部を超えても融着防止性能の大きな向上は見られない。   The addition amount of the dispersant is appropriately adjusted so as to prevent the fusion of the polypropylene resin particles depending on the foaming temperature, the addition amount of the foaming agent, and the type of the foaming agent. The amount is preferably 0.01 parts by weight or more and 5 parts by weight or less with respect to 100 parts by weight. If the amount is less than 0.01 part by weight, the performance as a dispersant may be reduced, and fusion between polypropylene resin particles may be observed. If the amount exceeds 5 parts by weight, no significant improvement in the anti-fusing performance is observed.

また、分散剤とともに、分散助剤を併用することが出来る。分散助剤としては、アルキルベンゼンスルホン酸ナトリウム、アルキル硫酸ナトリウム、n−パラフィンスルホン酸ナトリウム、オレイン酸ナトリウム、ポリオキシエチレンアルキルフェニルエーテル、ラウリルトリメチルアンモニウムクロライド、脂肪酸ジエタノールアミドなどの界面活性剤などが挙げられ、これらの1種または2種以上を好適に使用することができる。   A dispersing aid can be used in combination with the dispersing agent. Examples of the dispersion aid include surfactants such as sodium alkylbenzene sulfonate, sodium alkyl sulfate, sodium n-paraffin sulfonate, sodium oleate, polyoxyethylene alkylphenyl ether, lauryltrimethylammonium chloride, and fatty acid diethanolamide. These 1 type (s) or 2 or more types can be used conveniently.

このような分散助剤の添加量は、発泡温度、発泡剤の添加量、発泡剤の種類、分散剤の種類や添加量により適宜調節されるものであるが、一般的にはポリプロピレン系樹脂粒子100重量部に対し、0.001重量部以上2重量部以下が好ましい。0.001重量部未満では分散助剤としての性能が低下し樹脂粒子の融着が見られる場合があり、2重量部を超えても融着防止性能の大きな向上は見られない。   The amount of such a dispersion aid added is appropriately adjusted depending on the foaming temperature, the amount of foaming agent added, the type of foaming agent, the type of dispersant, and the amount added. 0.001 to 2 parts by weight is preferable with respect to 100 parts by weight. If the amount is less than 0.001 part by weight, the performance as a dispersion aid may be reduced and the resin particles may be fused. If the amount exceeds 2 parts by weight, no significant improvement in the anti-fusing performance is observed.

本発明のポリプロピレン系樹脂発泡粒子の作製方法に特に制限はないが、次のような公知の方法により作製することができる。すなわち、ポリプロピレン系樹脂、カーボンブラック、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールと必要に応じて各種添加剤とを溶融混練することによって得られる。ポリプロピレン系樹脂粒子を、必要に応じて分散剤、分散助剤とともに、密閉容器内にて発泡剤とともに分散媒に、分散せしめ、密閉容器の温度を上昇させ、該ポリプロピレン系樹脂粒子をポリプロピレン系樹脂粒子の軟化温度以上の温度とするが、必要に応じて昇温前、昇温中、昇温後のいずれかの少なくとも1つの段階で発泡剤を圧入する。ポリプロピレン系樹脂粒子の軟化温度以上の温度で分散媒とともにポリプロピレン系樹脂粒子を上記密閉容器内より低圧の雰囲気下(通常は大気圧下)に放出し、ポリプロピレン系樹脂発泡粒子を得ることができる。   Although there is no restriction | limiting in particular in the production method of the polypropylene resin expanded particle of this invention, It can produce by the following well-known methods. That is, it can be obtained by melt-kneading a polypropylene resin, carbon black, a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups and various additives as required. If necessary, the polypropylene resin particles are dispersed in a dispersion medium together with a foaming agent in a closed container together with a dispersant and a dispersion aid, and the temperature of the sealed container is increased, and the polypropylene resin particles are converted into a polypropylene resin. Although the temperature is equal to or higher than the softening temperature of the particles, the foaming agent is press-fitted in at least one stage before, during, or after the temperature rise as necessary. Polypropylene resin foam particles can be obtained by releasing the polypropylene resin particles together with the dispersion medium at a temperature equal to or higher than the softening temperature of the polypropylene resin particles in a low-pressure atmosphere (usually under atmospheric pressure) from the inside of the closed container.

なお、上記密閉容器内より低圧の雰囲気下(通常は大気圧下)に放出する際は、密閉容器内の圧力が低下しないように、例えば、窒素、空気、二酸化炭素などの無機ガスにより保圧することが好ましい。   In addition, when releasing in a low-pressure atmosphere (usually under atmospheric pressure) from the inside of the above-mentioned sealed container, the pressure in the sealed container is maintained, for example, with an inorganic gas such as nitrogen, air, carbon dioxide, etc. so as not to decrease. It is preferable.

以上のようにして得られたポリプロピレン系樹脂発泡粒子は、そのまま型内発泡成形に供することもできるが、空気、窒素等の無機ガスにてポリプロピレン系樹脂内に内圧を付与し、加熱することによって、更に発泡倍率を大きくするいわゆる二段発泡法を行ってもよい。   The polypropylene resin foam particles obtained as described above can be used for in-mold foam molding as they are, but by applying an internal pressure in the polypropylene resin with an inorganic gas such as air or nitrogen, and heating. Further, a so-called two-stage foaming method for further increasing the foaming ratio may be performed.

本発明のポリプロピレン系樹脂発泡粒子からなるポリプロピレン系樹脂型内発泡成形体は、ポリプロピレン系樹脂発泡粒子を、必要に応じて空気、酸素、窒素、二酸化炭素、あるいはこれらの中から選んだ複数の混合ガスである無機ガスにより加圧熟成して粒子内に所定の内圧を付与した後、閉鎖し得るが密閉し得ない成形用の型内に該ポリプロピレン系樹脂発泡粒子をそのまま、もしくは加圧圧縮状態で充填し、おおむねポリプロピレン系樹脂の融点付近の温度の水蒸気によりポリプロピレン系樹脂発泡粒子を加熱して粒子相互を融着せしめ、しかる後冷却することによって成形体を得る、型内発泡成形法によって得ることができる。   The polypropylene resin-in-mold foam-molded article comprising the polypropylene resin foam particles of the present invention is made of polypropylene resin foam particles, air, oxygen, nitrogen, carbon dioxide, or a mixture selected from these as required. After applying a predetermined internal pressure within the particles by pressure aging with an inorganic gas that is a gas, the polypropylene-based resin foamed particles are left as they are in a mold for molding that can be closed but cannot be sealed, or in a pressure-compressed state Filled with, generally heated polypropylene resin foam particles with water vapor at a temperature near the melting point of the polypropylene resin, the particles are fused together, and then cooled to obtain a molded product, obtained by an in-mold foam molding method be able to.

得られるポリプロピレン系樹脂型内発泡成形体の密度は、5g/L以上200g/L以下であることが好ましく、より好ましくは、10g/L以上150g/L以下である。当該範囲であると、気泡の破裂による機械的強度の低下が起きずに軽量化できるため、好ましい。   The density of the obtained polypropylene resin in-mold foam molding is preferably 5 g / L or more and 200 g / L or less, and more preferably 10 g / L or more and 150 g / L or less. This range is preferable because the mechanical strength is not reduced by the bursting of bubbles, and the weight can be reduced.

本発明のポリプロピレン系樹脂発泡粒子からなる型内発泡成形体は難燃性に優れる。具体的には、本発明のポリプロピレン系樹脂型内発泡成形体はFMVSS302に定められる燃焼試験法にて自己消火性または遅燃性を示す。FMVSS302に定められる燃焼試験法は以下のようにして行う。   The in-mold foam molded article comprising the polypropylene resin foamed particles of the present invention is excellent in flame retardancy. Specifically, the polypropylene resin in-mold foam-molded article of the present invention exhibits self-extinguishing properties or slow-flammability by a combustion test method defined in FMVSS302. The combustion test method defined in FMVSS 302 is performed as follows.

ポリプロピレン系樹脂型内発泡成形体から365mm×102mm×12mmの試験片を切り出し、試験片の長手方向の一端側(a側)から、38mmをA標線、A標線から254mmをB標線とし、他端側をクランプ等で試験片が水平になるように保持する。バーナーの口が試験片下面の下19mm、炎の高さが38mmとし、試験片の一端(a側)端部に炎を15秒間あてた後バーナーの炎を消し、炎がA標線に達したときストップウオッチで時間の測定を開始し、炎がA標線に達する前に、あるいはA標線を通過後60秒後以内、50mm以内で消火する場合を、自己消火性があるとし、A標線を超えB標線に至るまで、あるいはB標線に至らない場合はA標線を越え消火するまでの燃焼速度が100mm/分以下である場合を遅燃性とする。   A test piece of 365 mm × 102 mm × 12 mm is cut out from the foamed molded product in the polypropylene resin mold, and from one end side (a side) in the longitudinal direction of the test piece, 38 mm is an A marked line, and 254 mm from the A marked line is a B marked line. The other end is held with a clamp or the like so that the test piece is horizontal. The burner's mouth is 19 mm below the lower surface of the test piece and the flame height is 38 mm. The flame is applied to one end (a side) of the test piece for 15 seconds, and then the burner's flame is extinguished. The time measurement is started with a stopwatch, and if the fire extinguishes within 50 mm before the flame reaches the A mark or within 60 seconds after passing the A mark, When the combustion speed is 100 mm / min or less until exceeding the line B and reaching the mark B, or when the mark B is not reached, the mark A exceeds the mark A and extinguishes the fire.

また、本発明のポリプロピレン系樹脂型内発泡成形体は、軽量で熱変化が小さいことから、包装材、緩衝材、断熱材、建築資材、自動車用部品等の広範な用途に用いることができる。   In addition, since the polypropylene-based resin-molded foam-molded article of the present invention is lightweight and has little thermal change, it can be used in a wide range of applications such as packaging materials, cushioning materials, heat insulating materials, building materials, and automotive parts.

次に、本発明のポリプロピレン系樹脂発泡粒子、および該ポリプロピレン系樹脂粒子からなるポリプロピレン系樹脂型内発泡成形体に関して、実施例を挙げて更に詳細に説明する。なお、「部」「%」は特に断りのない限り、重量基準である。   Next, the polypropylene resin foamed particles of the present invention and the polypropylene resin in-mold foam-molded product made of the polypropylene resin particles will be described in more detail with reference to examples. “Parts” and “%” are based on weight unless otherwise specified.

<発泡倍率>
200mlのメスシリンダーにエタノールを入れ、その後重量を精秤したポリプロピレン系樹脂発泡粒子を投入し、体積の増分をメスシリンダーで読み取り、ポリプロピレン系樹脂発泡粒子の密度を算出する。ポリプロピレン系樹脂の密度を0.9g/mlとして、ポリプロピレン系樹脂粒子の密度をポリプロピレン系樹脂発泡粒子の密度で割り、発泡倍率とした。
<Foaming ratio>
Ethanol is placed in a 200 ml graduated cylinder, and then the expanded polypropylene resin particles are precisely weighed. The volume increment is read with the graduated cylinder, and the density of the expanded polypropylene resin particles is calculated. The density of the polypropylene resin was 0.9 g / ml, and the density of the polypropylene resin particles was divided by the density of the polypropylene resin foam particles to obtain the expansion ratio.

<成形体密度>
成形体の縦、横、厚みの寸法を測定し、重量を測定して密度を算出した。
<Molded body density>
The vertical, horizontal and thickness dimensions of the molded body were measured, and the weight was measured to calculate the density.

<難燃性>
成形体から365mm×102mm×12mmの試験片を切り出し、FMVSS302に定められる燃焼試験を行った。即ち、試験片の長手方向の一端側(a側)から、38mmをA標線、A標線から254mmをB標線とし、他端側をクランプ等で試験片が水平になるように保持した。バーナーの口が試験片下面の下19mm、炎の高さが38mmとし、試験片の一端(a側)端部に炎を15秒間あてた後バーナーの炎を消し、炎がA標線に達したときストップウオッチで時間の測定を開始し、次の基準で評価した。
◎:炎がA標線に達する前に、あるいはA標線を通過後60秒後以内、50mm以内で消火する(自己消火)
○:A標線を超えB標線に至るまで、あるいはB標線に至らない場合はA標線を越え消火するまでの燃焼速度が100mm/分以下である
×:A標線を超えB標線に至るまで、あるいはB標線に至らない場合はA標線を越え消火するまでの燃焼速度が100mm/分を超える
<Flame retardance>
A test piece of 365 mm × 102 mm × 12 mm was cut out from the molded body, and a combustion test defined in FMVSS 302 was performed. That is, from one end side (a side) in the longitudinal direction of the test piece, 38 mm was set as an A mark line, 254 mm from the A mark line was set as a B mark line, and the other end side was held by a clamp or the like so that the test piece was horizontal. . The burner's mouth is 19 mm below the lower surface of the test piece and the height of the flame is 38 mm. The flame is applied to one end (a side) end of the test piece for 15 seconds, and then the burner's flame is extinguished. Then, the time measurement was started with a stopwatch and evaluated according to the following criteria.
A: Fire extinguished within 50 mm before the flame reaches the A mark or within 60 seconds after passing the A mark (self-extinguishing)
○: Exceeds the A mark and reaches the B mark, or if it does not reach the B mark, the burning speed until exceeding the A mark and extinguishes is 100 mm / min or less. If it does not reach the B mark line, or if it does not reach the B mark line, the burning rate to exceed the A mark line and extinguish the fire exceeds 100 mm / min.

(実施例1〜12)
<ポリプロピレン系樹脂粒子の作製>
ポリプロピレン系樹脂、カーボンブラック、炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコール、および樹脂添加剤を表1記載の量となるように混合した。この混合物を50mmφの押出機にて投入し、溶融混練するとともに、ストランド状に吐出させ、水冷した後ペレタイザーでカッティングし、ポリプロピレン系樹脂粒子を得た。なお、カッティングの際に、このポリプロピレン系樹脂粒子の粒子重量が1.2mg/粒となるように調節した。
(Examples 1-12)
<Preparation of polypropylene resin particles>
Polypropylene resin, carbon black, polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups, and a resin additive were mixed so as to have the amounts shown in Table 1. This mixture was charged with an extruder of 50 mmφ, melted and kneaded, discharged into a strand, cooled with water, and then cut with a pelletizer to obtain polypropylene resin particles. In addition, at the time of cutting, it adjusted so that the particle weight of this polypropylene resin particle might be 1.2 mg / grain.

<ポリプロピレン系樹脂発泡粒子の作製>
上記記載の方法で作製したポリプロピレン系樹脂粒子100重量部を表1記載の量の分散媒、分散剤、分散助剤とともに10リットル圧力容器に仕込み、その後所定温度に加熱した。この際、加熱前から所定温度に達するまでの間、また、必要に応じて所定温度に達した後に、発泡剤を表1記載の圧力となるように仕込んだ。その後、容器内圧力を窒素ガスで保持しつつ、圧力容器下のバルブを開いて圧力容器の内容物を大気下に放出し、ポリプロピレン系樹脂発泡粒子を得た。得られたポリプロピレン系樹脂発泡粒子の発泡倍率を表1に示す。その後、ポリプロピレン系樹脂発泡粒子を別の圧力容器に仕込み、空気を圧入してポリプロピレン系樹脂発泡粒子に所定の量の空気内圧を付与し、その後攪拌機能を備えた圧力容器に投入した後、攪拌しながら所定圧力の水蒸気を吹き込み、元のポリプロピレン系樹脂発泡粒子よりも発泡倍率が大なるポリプロピレン系樹脂発泡粒子を得た。この二段発泡したポリプロピレン系樹脂発泡粒子の発泡倍率を表1に示す。
<Preparation of expanded polypropylene resin particles>
100 parts by weight of the polypropylene resin particles produced by the method described above were charged into a 10 liter pressure vessel together with the dispersion medium, dispersant, and dispersion aid shown in Table 1, and then heated to a predetermined temperature. At this time, the foaming agent was charged so that the pressure shown in Table 1 was reached before heating until reaching the predetermined temperature, and after reaching the predetermined temperature as necessary. Thereafter, while maintaining the internal pressure of the container with nitrogen gas, the valve under the pressure container was opened to release the contents of the pressure container into the atmosphere to obtain polypropylene-based resin expanded particles. Table 1 shows the expansion ratio of the obtained polypropylene resin expanded particles. Thereafter, the polypropylene resin expanded particles are charged into another pressure vessel, air is injected to give a predetermined amount of air internal pressure to the polypropylene resin expanded particles, and then the mixture is introduced into a pressure vessel having a stirring function, and then stirred. Then, water vapor of a predetermined pressure was blown to obtain expanded polypropylene resin particles having a larger expansion ratio than the original expanded polypropylene resin particles. Table 1 shows the expansion ratio of the two-stage expanded polypropylene resin expanded particles.

<ポリプロピレン系樹脂型内発泡成形体作製工程>
次に得られたポリプロピレン系樹脂発泡粒子を別の圧力容器に仕込み、空気を圧入して該ポリプロピレン系樹脂発泡粒子に0.2MPaの内圧を付与した。
<Process for producing foamed molded product in polypropylene resin mold>
Next, the obtained polypropylene resin expanded particles were charged into another pressure vessel, and air was injected to apply an internal pressure of 0.2 MPa to the polypropylene resin expanded particles.

内圧を付与したポリプロピレン系樹脂発泡粒子を400mm×300mm×120mmの金型に充填し、0.3MPaの水蒸気で10秒間加熱し、融着させて型内発泡成形体を得た。得られた型内発泡成形体の特性を表1に示す。   The polypropylene resin expanded particles to which the internal pressure was applied were filled in a 400 mm × 300 mm × 120 mm mold, heated with 0.3 MPa water vapor for 10 seconds, and fused to obtain an in-mold expanded molded body. Table 1 shows the characteristics of the obtained in-mold foam molded article.

Figure 2010270243
Figure 2010270243

(比較例1〜3)
実施例1〜11と同様にして、表1記載の内容で型内発泡成形体を得た。得られた型内発泡成形体を表1に示す。
(Comparative Examples 1-3)
In the same manner as in Examples 1 to 11, in-mold foam molded articles were obtained with the contents described in Table 1. The obtained in-mold foam molded article is shown in Table 1.

Claims (4)

カーボンブラック0.1重量%以上10重量%以下、および炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを含有するポリプロピレン系樹脂発泡粒子からなるポリプロピレン系樹脂型内発泡成形体であって、該ポリプロピレン系樹脂型内発泡成形体がFMVSS302に定められる燃焼試験法にて自己消火性または遅燃性を示すことを特徴とするポリプロピレン系樹脂型内発泡成形体。   A polypropylene resin-in-mold foam-molded article composed of polypropylene resin foam particles containing 0.1 to 10% by weight of carbon black and a polyhydric alcohol having 3 to 6 carbon atoms and having 3 or more hydroxyl groups. A polypropylene-based resin-in-mold foam-molded product, wherein the polypropylene-based resin-mold-in-mold foam-molded product exhibits self-extinguishing properties or slow-flammability by a combustion test method defined in FMVSS302. 成形体密度が5g/L以上200g/L未満である請求項1記載のポリプロピレン系樹脂型内発泡成形体。   The polypropylene resin in-mold foam molded article according to claim 1, wherein the density of the molded article is 5 g / L or more and less than 200 g / L. 炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールを0.05重量%以上3重量%以下含んでなる、請求項1または2に記載のポリプロピレン系樹脂型内発泡成形体。   The polypropylene resin internal foam molded article according to claim 1 or 2, comprising 0.05 to 3% by weight of a polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups. 炭素数3以上6以下でかつ水酸基を3個以上有する多価アルコールが、グリセリンである請求項1〜3何れか一項に記載のポリプロピレン系樹脂型内発泡成形体。   The polypropylene resin in-mold foam-molded article according to any one of claims 1 to 3, wherein the polyhydric alcohol having 3 to 6 carbon atoms and 3 or more hydroxyl groups is glycerin.
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