JPH0363123A - Mixed resin low density foam and manufacture thereof - Google Patents
Mixed resin low density foam and manufacture thereofInfo
- Publication number
- JPH0363123A JPH0363123A JP1199832A JP19983289A JPH0363123A JP H0363123 A JPH0363123 A JP H0363123A JP 1199832 A JP1199832 A JP 1199832A JP 19983289 A JP19983289 A JP 19983289A JP H0363123 A JPH0363123 A JP H0363123A
- Authority
- JP
- Japan
- Prior art keywords
- foam
- density polyethylene
- low
- balloon
- weight
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 229920005989 resin Polymers 0.000 title claims abstract description 23
- 239000011347 resin Substances 0.000 title claims abstract description 23
- 239000004620 low density foam Substances 0.000 title claims description 9
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 239000006260 foam Substances 0.000 claims abstract description 47
- 229920001684 low density polyethylene Polymers 0.000 claims abstract description 19
- 239000004702 low-density polyethylene Substances 0.000 claims abstract description 19
- 229920001903 high density polyethylene Polymers 0.000 claims abstract description 16
- 239000004700 high-density polyethylene Substances 0.000 claims abstract description 16
- 238000009835 boiling Methods 0.000 claims abstract description 5
- 239000000155 melt Substances 0.000 claims abstract 2
- 229920005990 polystyrene resin Polymers 0.000 claims description 20
- 239000004604 Blowing Agent Substances 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 6
- 238000004898 kneading Methods 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 238000003825 pressing Methods 0.000 claims description 2
- 239000004088 foaming agent Substances 0.000 abstract description 11
- 238000005452 bending Methods 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 6
- 239000000203 mixture Substances 0.000 abstract description 6
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 abstract description 6
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000001273 butane Substances 0.000 abstract description 4
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 abstract description 4
- 239000004793 Polystyrene Substances 0.000 abstract description 2
- 229920002223 polystyrene Polymers 0.000 abstract description 2
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000002253 acid Substances 0.000 description 10
- 125000005456 glyceride group Chemical group 0.000 description 10
- 239000005022 packaging material Substances 0.000 description 10
- -1 polyethylene Polymers 0.000 description 8
- 230000006835 compression Effects 0.000 description 7
- 238000007906 compression Methods 0.000 description 7
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 229920001577 copolymer Polymers 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 4
- 239000005977 Ethylene Substances 0.000 description 4
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 3
- 150000008282 halocarbons Chemical class 0.000 description 3
- 239000002667 nucleating agent Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- XPDWGBQVDMORPB-UHFFFAOYSA-N Fluoroform Chemical compound FC(F)F XPDWGBQVDMORPB-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- 239000012753 anti-shrinkage agent Substances 0.000 description 2
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- QWTDNUCVQCZILF-UHFFFAOYSA-N isopentane Chemical compound CCC(C)C QWTDNUCVQCZILF-UHFFFAOYSA-N 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229920013716 polyethylene resin Polymers 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 description 1
- BOUGCJDAQLKBQH-UHFFFAOYSA-N 1-chloro-1,2,2,2-tetrafluoroethane Chemical compound FC(Cl)C(F)(F)F BOUGCJDAQLKBQH-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical group [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 230000037396 body weight Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Chemical group BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Chemical group 0.000 description 1
- 125000001246 bromo group Chemical group Br* 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000002666 chemical blowing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- AFABGHUZZDYHJO-UHFFFAOYSA-N dimethyl butane Natural products CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006248 expandable polystyrene Polymers 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 150000002734 metacrylic acid derivatives Chemical class 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- CYRMSUTZVYGINF-UHFFFAOYSA-N trichlorofluoromethane Chemical compound FC(Cl)(Cl)Cl CYRMSUTZVYGINF-UHFFFAOYSA-N 0.000 description 1
- 229940029284 trichlorofluoromethane Drugs 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Molding Of Porous Articles (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ポリオレフィン系樹脂とポリスチレン系樹脂
からなる混合樹脂低密度発泡体及びその製造方法に関し
、特に傷の付き易い果物等の緩衝包装材として有用な発
泡体及びその製造方法に関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a mixed resin low-density foam made of a polyolefin resin and a polystyrene resin and a method for producing the same, and in particular to a cushioning packaging material for easily damaged fruits, etc. The present invention relates to a foam useful as a foam and a method for producing the same.
従来、傷の付き易い果物等の緩衝包装材として、サーキ
ュラ−ダイから発泡剤と共に押出すことにより製造され
る低密度ポリエチレン発泡体が広く用いられてきた。し
かし、この種低密度ポリエチレン発泡体は、曲げ剛性が
低く保形性に劣るため。BACKGROUND ART Conventionally, low-density polyethylene foam produced by extruding a foam together with a foaming agent from a circular die has been widely used as a cushioning packaging material for fruits and the like that are easily damaged. However, this type of low-density polyethylene foam has low bending rigidity and poor shape retention.
包装作業時に扱いにくいという欠点を有する。この原因
は、製造工程上、厚みが最大6m程度のものしか製造で
きないこと及び曲げ弾性率が低いことにある。It has the disadvantage of being difficult to handle during packaging work. The reason for this is that due to the manufacturing process, it is only possible to manufacture products with a maximum thickness of about 6 m, and the flexural modulus is low.
厚いシートを得る方法としては、サーキュラ−ダイから
発泡剤と共に押出される発泡体をバルーンに形成し、ロ
ール間を通してバルーン内面を圧着する方法が一般的で
ある。低密度ポリエチレン発泡体は、結晶化速度が遅い
ため、上記方法によるとバルーン内面が圧着し、一応は
厚いシートが得られるものの、厚みムラやコルゲートが
発生し易く、均一な厚みを有する厚いシートは得られな
かった。A common method for obtaining a thick sheet is to form a balloon from a foam extruded from a circular die together with a foaming agent, and then pass the foam between rolls and press the inner surface of the balloon. Since low-density polyethylene foam has a slow crystallization speed, the above method allows the inner surface of the balloon to be crimped and a thick sheet can be obtained, but uneven thickness and corrugation are likely to occur, and a thick sheet with a uniform thickness cannot be obtained. I couldn't get it.
そこで、優れた緩衝性と曲げ剛性を有する緩衝包装材と
して、二次加工によって低密度発泡体同士又はダンボー
ルや発泡ポリスチレンシート等の高い曲げ剛性を有する
材料と低密度ポリエチレン発泡体とを貼り合わせた包装
材が用いられている。Therefore, in order to create a cushioning packaging material with excellent cushioning properties and bending rigidity, we used secondary processing to bond low-density foams together or to materials with high bending rigidity such as cardboard or foamed polystyrene sheets and low-density polyethylene foam. Packaging material is used.
しかし、このような包装材は、二次加工によって製造さ
れるため、コストが高いという欠点がある。However, since such packaging materials are manufactured through secondary processing, they have the drawback of high cost.
また、高密度ポリエチレン単独の発泡体も知られている
が、発泡剤としてフロンガスを使用しなければ良好なも
のが得られないため、フロンガスによるオゾン層破壊の
問題を有している。Foamed products made of high-density polyethylene alone are also known, but good results cannot be obtained unless fluorocarbon gas is used as a foaming agent, which poses the problem of ozone layer depletion due to fluorocarbon gas.
なお、低密度ポリエチレン100重量部に対して、ポリ
スチレン系樹脂と高密度ポリエチレンとをその合計量が
10〜60重量部となる割合で、且つポリスチレン系樹
脂がポリスチレン系樹脂と高密度ポリエチレンとの合剖
量に対して6〜40重量2になる割合で、発泡剤と共に
加圧下において溶融混練した後、低圧帯域に移して発泡
体とする方法も知られている(特公昭51−41149
号公報)。In addition, the polystyrene resin and high density polyethylene should be used in a ratio such that the total amount thereof is 10 to 60 parts by weight with respect to 100 parts by weight of the low density polyethylene, and the polystyrene resin should be a combination of the polystyrene resin and the high density polyethylene. It is also known to melt and knead together with a foaming agent under pressure at a ratio of 6 to 40 weight 2 based on the body weight, and then transfer the mixture to a low pressure zone to form a foam (Japanese Patent Publication No. 51-41149
Publication No.).
この方法により得られる混合樹脂発泡体は、高密度ポリ
エチレン及びポリスチレン系樹脂が混入されているため
、低密度ポリエチレン発泡体よりは、優れた曲げ弾性率
を示す、しかし、上記配合でも、やはり厚みムラやコル
ゲート等が発生し、均一な厚みを有する厚いシートが得
られないため。Since the mixed resin foam obtained by this method contains high-density polyethylene and polystyrene resin, it exhibits a better flexural modulus than low-density polyethylene foam.However, even with the above composition, the thickness is still uneven. This is because thick sheets with uniform thickness cannot be obtained due to the occurrence of corrugations, etc.
充分な曲げ剛性を有する緩衝包装材は得られない。A cushioning packaging material with sufficient bending rigidity cannot be obtained.
本発明は、前記従来の緩衝包装材に見られる欠点を克服
し、好適な厚みと曲げ弾性率とにより、良好な曲げ剛性
を有する安価な緩衝包装材として好適な発泡体及びその
製造方法を提供することをその課題とする。The present invention overcomes the drawbacks seen in the conventional cushioning packaging materials and provides a foam suitable as an inexpensive cushioning packaging material that has good bending rigidity due to suitable thickness and flexural modulus, and a method for producing the same. The task is to do so.
本発明者らは、前記課題を解決すべく鋭意研究を重ねた
結果、高密度ポリエチレンと低密度ポリエチレンと特定
のメルトフローレート(以下MFRと略記する)の範囲
のポリスチレン系樹脂とを、特定割合で配合した混合樹
脂を用いる時には、低沸点の発泡剤と共に加圧下で溶融
混練した後、サーキュラ−ダイよりバルーンを形成させ
て低圧帯域に移し、ロール間を通してバルーン内面を圧
着させることにより、好適な厚み(6−以上)と好適な
曲げ弾性率を有する、緩衝包装材として好ましい発泡体
が得られることを見出し、本発明を完成するに至った。As a result of extensive research to solve the above problems, the present inventors have discovered that high density polyethylene, low density polyethylene, and polystyrene resin having a specific melt flow rate (hereinafter abbreviated as MFR) are combined in a specific ratio. When using a mixed resin blended with , it is melt-kneaded together with a low boiling point blowing agent under pressure, then formed into a balloon using a circular die, transferred to a low-pressure zone, and passed between rolls and crimped on the inner surface of the balloon. The present inventors have discovered that a foam suitable for use as a cushioning packaging material can be obtained, having a thickness (6 mm or more) and a suitable flexural modulus, and has completed the present invention.
即ち、本発明によれば、高密度ポリエチレン20〜60
重量%、低密度ポリエチレンzO〜40重量算及びポリ
スチレン系樹脂20〜60重量%からなる混合樹脂発泡
体であって、しかも該発泡体はバルーン状発泡体を内面
圧着させてなる0、05g/cm3未満の密度を有する
ものであることを特徴とする混合樹脂低密度発泡体が提
供される。That is, according to the present invention, high density polyethylene 20 to 60
A mixed resin foam consisting of 20 to 60% by weight of low-density polyethylene zO and 20 to 60% by weight of low-density polyethylene zO, and the foam is formed by internally pressing a balloon-shaped foam to 0.05 g/cm3. There is provided a mixed resin low density foam characterized in that it has a density of less than or equal to.
また、本発明によれば、高密度ポリエチレン、低密度ポ
リエチレン及びMFR5g/10分以上のポリスチレン
系樹脂を、夫々20〜60重量S、20〜40重量2及
び20〜40重量2の割合で、低沸点の発泡剤と共に加
圧下で溶融混練した後、サーキュラ−ダイよりバルーン
を形成させて低圧帯域に移し、ロール間を通してバルー
ン内面を圧着させて、密度0.05g/ad未溝の発泡
体を得ることを特徴とする混合樹脂低密度発泡体の製造
方法が提供される。Further, according to the present invention, high density polyethylene, low density polyethylene, and polystyrene resin having an MFR of 5 g/10 minutes or more are mixed in a proportion of 20 to 60 weight S, 20 to 40 weight 2, and 20 to 40 weight 2, respectively. After melting and kneading under pressure with a foaming agent at a boiling point, a balloon is formed from a circular die, transferred to a low pressure zone, and the inner surface of the balloon is pressed between rolls to obtain an ungrooved foam with a density of 0.05 g/ad. A method for producing a mixed resin low density foam is provided.
本発明における高密度ポリエチレンとは、常温常圧にお
ける密度が0.941〜0.970g/cm3であるエ
チレンを主体とする重合体であって、酢酸ビニル。The high-density polyethylene in the present invention is a polymer mainly composed of ethylene and has a density of 0.941 to 0.970 g/cm3 at room temperature and normal pressure, and is vinyl acetate.
メタアクリレート、アクリレートあるいはプロピレンそ
の他のエチレンと共重合し得るビニル系単量体との共重
合体も含まれる。なお、本発明で用いる高密度ポリエチ
レンとしては、通常MFRが0.03〜10g/lo分
の範囲のものが好ましい。Also included are methacrylates, acrylates, and copolymers with propylene and other vinyl monomers that can be copolymerized with ethylene. The high-density polyethylene used in the present invention is usually preferably one having an MFR of 0.03 to 10 g/lo min.
本発明における低密度ポリエチレンとは、常温常圧にお
ける密度が0.910〜0.930g/cjであるエチ
レンを主体とする重合体であって、前記した如きエチレ
ンと共重合し得る各種のビニル系単量体との共重合体も
含まれる。なお、本発明で用いる低密度ポリエチレンと
しては1通常MFRが0.1−Log/10分の範囲の
ものが好ましい。The low-density polyethylene in the present invention is a polymer mainly composed of ethylene and having a density of 0.910 to 0.930 g/cj at normal temperature and normal pressure, and includes various vinyl-based polymers that can be copolymerized with ethylene as described above. Copolymers with monomers are also included. The low-density polyethylene used in the present invention preferably has a normal MFR of 0.1-Log/10 minutes.
本発明におけるポリスチレン系樹脂とは、スチレンを主
体とする重合体で、スチレン単独重合体及びその他のス
チレンと共重合し得るビニル系単量体との共重合体、更
には一般に耐衝撃性ポリスチレン樹脂と呼ばれているポ
リスチレンを主体とするゴム系ポリマーとの共重合物又
は混合物、あるいは、ジエン系単量体との共重合体も本
発明のポリスチレン系樹脂の範囲に含まれるものである
。The polystyrene resin in the present invention refers to a polymer mainly composed of styrene, including styrene homopolymers and copolymers with other vinyl monomers that can be copolymerized with styrene, and generally impact-resistant polystyrene resins. Also included in the scope of the polystyrene resin of the present invention are copolymers or mixtures with rubber-based polymers mainly composed of polystyrene, or copolymers with diene monomers.
なお1本発明において、ポリスチレン系樹脂として、耐
衝撃性ポリスチレン樹脂を使用した場合には、得られる
発泡体の柔軟性、弾性を向上させることができる。たf
、本発明においては、ポリスチレン系樹脂として、 M
FRが5g/10分以上のものが用いられる。 MFR
が5g/ 10分未満のものを用いた場合には、バルー
ン状発泡体内面の圧着が困難になる。Note that in the present invention, when an impact-resistant polystyrene resin is used as the polystyrene resin, the flexibility and elasticity of the resulting foam can be improved. ta f
, in the present invention, as the polystyrene resin, M
A material with an FR of 5 g/10 minutes or more is used. MFR
If less than 5 g/10 minutes is used, it will be difficult to press the inner surface of the balloon-shaped foam.
なお、本明細書中でいうMFRとは、JIS K721
0に記載の方法により測定されるものであり、ポリスチ
レン系樹脂の場合条件8が、またポリエチレン系樹脂の
場合条件4が採用される。In addition, MFR referred to in this specification is JIS K721
Condition 8 is used for polystyrene resin, and Condition 4 is used for polyethylene resin.
本発明で用いる発泡剤としては、脂肪族炭化水素やハロ
ゲン化炭化水素あるいはフロンガスが単独で又は混合し
て用いられる。脂肪族炭化水素の具体例として、例えば
、プロパン、ブタン、イソブタン、ペンタン、イソペン
タン等が挙げられ、ハロゲン化炭化水素としては、それ
ら脂肪族炭化水素の塩素又は臭素置換体が挙げられる。As the blowing agent used in the present invention, aliphatic hydrocarbons, halogenated hydrocarbons, or chlorofluorocarbon gas may be used alone or in combination. Specific examples of aliphatic hydrocarbons include propane, butane, isobutane, pentane, isopentane, etc., and examples of halogenated hydrocarbons include chlorine or bromine substituted products of these aliphatic hydrocarbons.
また、フロンガスとしては、クロルジフルオロメタン、
トリフルオロメタン、1,2,2.2−テトラフルオロ
エタン、l−クロル−1,1−ジフルオロエタン、1.
1−ジフルオロエタン、1−クロル−1,2,2,2−
テトラフルオロエタン、トリクロルフルオロメタン、ジ
クロルジフルオロメタン、1,2−ジクロル−1,2,
2,2−テトラフルオロエタン等が挙げられる。上記発
泡剤を使用するに当たり、沸点範囲が一20〜20℃の
ものを主成分とした発泡剤を選択することが望ましい。In addition, as chlorofluorocarbon gas, chlordifluoromethane,
Trifluoromethane, 1,2,2,2-tetrafluoroethane, l-chloro-1,1-difluoroethane, 1.
1-difluoroethane, 1-chloro-1,2,2,2-
Tetrafluoroethane, trichlorofluoromethane, dichlorodifluoromethane, 1,2-dichloro-1,2,
Examples include 2,2-tetrafluoroethane. When using the above blowing agent, it is desirable to select a blowing agent whose main component has a boiling point range of 120 to 20°C.
また、発泡剤として、脂肪族炭化水素やハロゲン化炭化
水素に、少量(40重量%以下)のフロンガスを混合す
ることは、低密度の発泡体を得る点からは、有効な方法
である。Further, mixing a small amount (40% by weight or less) of fluorocarbon gas with an aliphatic hydrocarbon or halogenated hydrocarbon as a foaming agent is an effective method from the viewpoint of obtaining a low-density foam.
本発明における混合樹脂中、高密度ポリエチレンの割合
は、20〜60重量2、好ましくは25〜405〜40
重量部ポリエチレンの割合は20〜40重量2、好まし
くは25〜40重量2及びポリスチレン系樹脂の割合は
20〜400〜40重量部くは25〜40重量ぶである
。高密度ポリエチレンの割合が前記範囲より少なくなる
と、低密度ポリエチレン及びポリスチレン系樹脂との混
合が悪くなり、逆に前記範囲より多くなると、得られる
発泡体に大きな収縮が見られるようになると共に、反撥
弾性も損なわれるようになる。The proportion of high density polyethylene in the mixed resin in the present invention is 20 to 60% by weight2, preferably 25 to 405 to 40% by weight.
The proportion of polyethylene in parts by weight is 20 to 40 parts by weight2, preferably 25 to 40 parts by weight2, and the proportion of polystyrene resin is 20 to 400 to 40 parts by weight, or 25 to 40 parts by weight. If the proportion of high-density polyethylene is less than the above range, mixing with low-density polyethylene and polystyrene resin will be poor, and if it exceeds the above range, the resulting foam will show significant shrinkage and will have poor rebound. Elasticity also becomes impaired.
低密度ポリエチレンの割合が前記範囲より少なくなると
、得られる発泡体の圧縮後の回復性が損なわれるように
なり、逆に、前記範囲より多くなると、サージング現象
が起り、樹脂と発泡剤とがうまく混合しなくなり、低密
度発泡体を得ることが困難になる。ポリスチレン系樹脂
の割合が前記範囲より少なくなると、発泡体の収縮が大
きくなり、またバルーン状発泡体内面の圧着が困難にな
る。逆に前記範囲より多くなると、溶融混線時のポリエ
チレン系樹脂との相溶性が劣り、また得られる発泡体の
剛性が高すぎてもろくなると共に、圧縮後の回復性にも
劣るようになる。If the proportion of low-density polyethylene is less than the above range, the recovery properties of the resulting foam after compression will be impaired; on the other hand, if it exceeds the above range, a surging phenomenon will occur, making it difficult for the resin and blowing agent to interact properly. It will not mix and it will be difficult to obtain a low density foam. If the proportion of the polystyrene resin is less than the above range, the shrinkage of the foam will increase and it will be difficult to press the inner surface of the balloon-shaped foam. On the other hand, if the amount exceeds the above range, the compatibility with the polyethylene resin during melt mixing will be poor, and the resulting foam will have too high rigidity and become brittle, and will also have poor recovery properties after compression.
本発明において用いる発泡剤の使用割合は、混合樹脂1
00重量部に対し、1〜40重量部、好ましくは10〜
25重量部であり、所望する発泡体の密度に応じて適当
に定める1発泡剤としてブタン(ノルマル:イソ=7:
3)を主成分とするものを用いる場合には、密度0.0
5g/cm3未満の発泡体を得るために必要な混入量は
、通常混合樹脂100重量部に対して10〜20重量部
でよい。The proportion of the blowing agent used in the present invention is 1:1 for the mixed resin.
00 parts by weight, 1 to 40 parts by weight, preferably 10 to 40 parts by weight
Butane (normal:iso=7:
When using a material containing 3) as the main component, the density is 0.0.
The amount necessary to obtain a foam with a weight of less than 5 g/cm3 may be generally 10 to 20 parts by weight per 100 parts by weight of the mixed resin.
本発明においては、必要に応じて、一般に使用されてい
る気泡核生成剤を用いてもよい、この気泡核生成剤とし
ては、例えば、タルクの如き無機物質、あるいは押出機
内の温度で分解してガスを発生する如き化学発泡剤、又
は該温度で反応して炭酸ガスを発生する酸−アルカリの
組合わせ、例えば、クエン酸と重炭酸ソーダ、クエン酸
のアルカリ塩と重炭酸ソーダの如きものである。これら
の気泡植生成剤を添加することにより、得られる発泡体
の気泡の大きさを任意に1111することができると共
に、発泡体の柔軟性、感触等も向上させることができる
。更に1本発明においては、混合樹脂に対して、必要に
応じ、発泡に際しての発泡剤の樹脂透過を防いで発泡体
の収縮を抑制するために、収縮防止剤を添加することも
できる。このようなものとしては1例えば、ポリオキシ
エチレンモノミリステート、ポリオキシプロピレンモノ
ミリステート、ポリオキシエチレンモノパルミテート、
ポリオキシプロピレンモノパルミテート、ポリオキシエ
チレンモノステアレート、ポリオキシプロピレンモノス
テアレート、ポリオキシエチレンジステアレート、モノ
ラウリン酸グリセライド、モノミリスチン酸グリセライ
ド、モノパルミチン酸グリセライド、モノステアリン酸
グリセライド、モノアラキン酸グリセライド、ジラウリ
ン酸グリセライド、シバルミチン酸グリセライド、ジス
テアリン酸グリセライド、1−パルミト−2−ステアリ
ン酸グリセライド、1−ステアロ−2−ミリスチン酸グ
リセライド、トリステアリン酸グリセライド等の各種脂
肪族エステルが挙げられる。その他発泡核剤や無機充填
材等も用いることができる。In the present invention, a commonly used cell nucleating agent may be used as necessary. Examples of this cell nucleating agent include an inorganic substance such as talc, or a cell that is decomposed at the temperature inside the extruder. A chemical blowing agent that generates gas, or an acid-alkali combination that reacts at the temperature to generate carbon dioxide, such as citric acid and sodium bicarbonate, or an alkali salt of citric acid and sodium bicarbonate. By adding these cell-planting agents, the size of the cells in the obtained foam can be arbitrarily set to 1111, and the flexibility, feel, etc. of the foam can also be improved. Furthermore, in the present invention, an anti-shrinkage agent may be added to the mixed resin, if necessary, in order to prevent the foaming agent from permeating the resin during foaming and suppress shrinkage of the foam. Examples of such substances include 1, for example, polyoxyethylene monomyristate, polyoxypropylene monomyristate, polyoxyethylene monopalmitate,
Polyoxypropylene monopalmitate, polyoxyethylene monostearate, polyoxypropylene monostearate, polyoxyethylene distearate, monolauric acid glyceride, monomyristic acid glyceride, monopalmitic acid glyceride, monostearic acid glyceride, monoarachic acid glyceride , dilauric acid glyceride, cybalmitic acid glyceride, distearic acid glyceride, 1-palmito-2-stearic acid glyceride, 1-stearo-2-myristic acid glyceride, and tristearic acid glyceride. Other foam nucleating agents, inorganic fillers, etc. can also be used.
本発明の発泡体は、慣用の押出発泡成形機を用いて製造
することができる。即ち、押出機の加圧シリンダー内に
おいて混合樹脂と発泡剤とを溶融混練し、この混線物を
押出機のサーキュラ−°ダイからバルーンを形成させて
大気中に押出し、ロール間を通してバルーン内面を圧着
させて、板状発泡体を得ることができる。The foam of the present invention can be manufactured using a conventional extrusion foam molding machine. That is, the mixed resin and foaming agent are melted and kneaded in a pressurized cylinder of an extruder, and this mixture is extruded into the atmosphere through a circular die of the extruder to form a balloon, and then passed between rolls and crimped on the inner surface of the balloon. In this way, a plate-shaped foam can be obtained.
本発明の発泡体は、 0.05g/−未満の密度を有す
るものであり、好ましい発泡体は、0.015〜0.0
25g/cm3の密度を有する0発泡倍率で表現すると
、本発明の発泡体は少なくとも18倍以上という発泡倍
率を示すものである。The foam of the present invention has a density of less than 0.05 g/-, and preferred foams have a density of 0.015 to 0.0
When expressed in zero expansion ratio having a density of 25 g/cm 3 , the foam of the present invention exhibits an expansion ratio of at least 18 times or more.
本発明の発泡体は、好適な厚みと曲げ弾性率により、良
好な曲げ剛性を持つ安価な緩衝包装材として好ましいも
のである。The foam of the present invention has a suitable thickness and flexural modulus, and is therefore preferable as an inexpensive cushioning packaging material with good flexural rigidity.
本発明の発泡体は、このような特性を活かして、農産物
、家電製品、ガラス等の包装用あるいは輸送用緩衝材や
クツション材等として有利に利用される。By taking advantage of these characteristics, the foam of the present invention can be advantageously used for packaging agricultural products, home appliances, glass, etc., or as cushioning materials, cushioning materials, etc. for transportation.
次に、本発明を実施例により更に詳細に説明する。 Next, the present invention will be explained in more detail with reference to Examples.
実施例1〜3.比較例1〜6
密度0.958g/aj、 MFRo、3の高密度ポリ
エチレン(HOPE)、密度0.923g/cm3、阿
FR0,26iの低密度ポリエチレン(LDPfり及び
密度1.05g/aJ、表−1に示す値のMFRのポリ
スチレン樹脂(ps)を、表−1に示した割合で用いる
とともに、これらの樹脂約100重量部に収縮防止剤と
してモノステアリン酸グリセライド1.0重量部を配合
し、この配合物に発泡剤ブタン(ノルマル:イソ=7:
3)を表−1に示す割合で添加し、吐出量18kg/h
rの押出機中で、圧力200kg/aJGで溶融混練し
た後、押出機先端に設けたサーキュラ−ダイから表−1
に示した温度(発泡温度)で大気圧下に押出してバルー
ンを形成させ、ロール間を通して、バルーン内面を圧着
させて、板状発泡体を得た。Examples 1-3. Comparative Examples 1 to 6 High-density polyethylene (HOPE) with a density of 0.958 g/aj and MFRo of 3, low-density polyethylene (HOPE) with a density of 0.923 g/cm3 and AFR of 0.26i (LDP and density of 1.05 g/aJ, Table Polystyrene resins (ps) with MFR values shown in Table 1 were used in the proportions shown in Table 1, and 1.0 parts by weight of monostearic acid glyceride was added as an anti-shrinkage agent to about 100 parts by weight of these resins. , the blowing agent butane (normal:iso=7:
3) was added at the rate shown in Table 1, and the discharge amount was 18 kg/h.
After melt-kneading at a pressure of 200 kg/aJG in an extruder of
A balloon was formed by extrusion at the temperature shown in (foaming temperature) under atmospheric pressure, and the inner surface of the balloon was pressed between rolls to obtain a plate-shaped foam.
このようにして得られた発泡体について、その7日後の
常温における密度と厚さを測定すると共に、曲げ弾性率
及び圧縮残留歪を測定した。その結果を表−1に示す。Seven days later, the density and thickness of the foam thus obtained at room temperature were measured, as well as the flexural modulus and compressive residual strain. The results are shown in Table-1.
なお1曲げ弾性率及び圧縮残留歪の測定は次の方法に従
って行なった。Note that the bending elastic modulus and compressive residual strain were measured according to the following method.
(1)曲げ弾性率
JIS K7203に準拠し、試験速度10 m /分
、サンプル形状150 X 25mm、スパン100m
、治具半径5mで行なった。(1) Flexural modulus: Based on JIS K7203, test speed: 10 m/min, sample size: 150 x 25 mm, span: 100 m
, with a jig radius of 5 m.
(2) 50%圧縮残留歪
サンプル(サイズ50X50+w+s)を全厚(A)の
5部まで圧縮(圧縮速度10 wxa /分)した後、
直ちに圧縮と同速度で圧縮を取り除き、応力が0になっ
た厚み(B)と元の厚み(A)から算出した。(2) After compressing the 50% compression residual strain sample (size 50X50+w+s) to 5 parts of the total thickness (A) (compression speed 10 wxa/min),
The compression was immediately removed at the same speed as the compression, and the thickness was calculated from the thickness (B) at which the stress became zero and the original thickness (A).
−8
50%圧縮残留歪(%)= X 100表−1の結
果から、本発明の発泡体は、密度が極めて小さく(低密
度)且つ好適な厚みを有するものでありながら、優れた
曲げ弾性及び圧縮後の回復性を有するものであることが
判る。-8 50% compressive residual strain (%) = It can be seen that it has recovery properties after compression.
Claims (2)
リエチレン20〜40重量%及びポリスチレン系樹脂2
0〜40重量%からなる混合樹脂発泡体であって、しか
も該発泡体はバルーン状発泡体を内面圧着させてなる0
.05g/cm^3未満の密度を有するものであること
を特徴とする混合樹脂低密度発泡体。(1) 20-60% by weight of high-density polyethylene, 20-40% by weight of low-density polyethylene and polystyrene resin 2
A mixed resin foam consisting of 0 to 40% by weight, and the foam is formed by pressing a balloon-shaped foam on the inner surface.
.. A mixed resin low-density foam having a density of less than 0.05 g/cm^3.
ルトフローレート5g/10分以上のポリスチレン系樹
脂を、夫々20〜60重量%、20〜40重量%及び2
0〜40重量%の割合で、低沸点の発泡剤と共に加圧下
で溶融混練した後、サーキュラーダイよりバルーンを形
成させて低圧帯域に移し、ロール間を通してバルーン内
面を圧着させて、密度0.05g/cm^3未満の発泡
体を得ることを特徴とする混合樹脂低密度発泡体の製造
方法。(2) High-density polyethylene, low-density polyethylene, and polystyrene resin with a melt flow rate of 5 g/10 minutes or more, 20 to 60% by weight, 20 to 40% by weight, and 2% by weight, respectively.
After melting and kneading under pressure with a low boiling point blowing agent at a ratio of 0 to 40% by weight, a balloon is formed using a circular die, transferred to a low pressure zone, and the inner surface of the balloon is pressed between rolls to obtain a material with a density of 0.05 g. 1. A method for producing a mixed resin low-density foam, characterized in that a foam with a density of less than /cm^3 is obtained.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1199832A JP2717579B2 (en) | 1989-08-01 | 1989-08-01 | Mixed resin low density foam and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1199832A JP2717579B2 (en) | 1989-08-01 | 1989-08-01 | Mixed resin low density foam and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0363123A true JPH0363123A (en) | 1991-03-19 |
JP2717579B2 JP2717579B2 (en) | 1998-02-18 |
Family
ID=16414385
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1199832A Expired - Fee Related JP2717579B2 (en) | 1989-08-01 | 1989-08-01 | Mixed resin low density foam and method for producing the same |
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Country | Link |
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JP (1) | JP2717579B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6225363B1 (en) | 1998-04-07 | 2001-05-01 | Pactiv Corporation | Foamable composition using high density polyethylene |
US7045556B2 (en) | 2002-07-02 | 2006-05-16 | Pactiv Corporation | Polyolefin foams made with isopentane-based blowing agents |
US7166248B2 (en) | 2003-01-03 | 2007-01-23 | Pactiv Corporation | Reduced VOC emission alkenyl aromatic polymer foams and processes |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02232240A (en) * | 1989-03-03 | 1990-09-14 | Jsp Corp | Low-density foam of mixed resin and its production |
-
1989
- 1989-08-01 JP JP1199832A patent/JP2717579B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02232240A (en) * | 1989-03-03 | 1990-09-14 | Jsp Corp | Low-density foam of mixed resin and its production |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6225363B1 (en) | 1998-04-07 | 2001-05-01 | Pactiv Corporation | Foamable composition using high density polyethylene |
WO2001051550A1 (en) * | 2000-01-11 | 2001-07-19 | Pactiv Corporation | Foamable composition using high density polyethylene |
US7045556B2 (en) | 2002-07-02 | 2006-05-16 | Pactiv Corporation | Polyolefin foams made with isopentane-based blowing agents |
US7166248B2 (en) | 2003-01-03 | 2007-01-23 | Pactiv Corporation | Reduced VOC emission alkenyl aromatic polymer foams and processes |
Also Published As
Publication number | Publication date |
---|---|
JP2717579B2 (en) | 1998-02-18 |
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