JPH0277436A - Polyolefin based resin foamed particle having gas adsorbing ability, molded article and production of above-mentioned foamed particle - Google Patents
Polyolefin based resin foamed particle having gas adsorbing ability, molded article and production of above-mentioned foamed particleInfo
- Publication number
- JPH0277436A JPH0277436A JP23105288A JP23105288A JPH0277436A JP H0277436 A JPH0277436 A JP H0277436A JP 23105288 A JP23105288 A JP 23105288A JP 23105288 A JP23105288 A JP 23105288A JP H0277436 A JPH0277436 A JP H0277436A
- Authority
- JP
- Japan
- Prior art keywords
- zeolite
- foamed particle
- pressure
- based resin
- particles
- 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
- 239000002245 particle Substances 0.000 title claims abstract description 49
- 229920005672 polyolefin resin Polymers 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- 239000010457 zeolite Substances 0.000 claims abstract description 27
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000002270 dispersing agent Substances 0.000 claims abstract description 8
- 239000006260 foam Substances 0.000 claims abstract description 7
- 238000001179 sorption measurement Methods 0.000 claims description 14
- 239000004604 Blowing Agent Substances 0.000 claims description 7
- 238000007664 blowing Methods 0.000 claims 1
- 230000001877 deodorizing effect Effects 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 239000005022 packaging material Substances 0.000 abstract description 5
- 239000003795 chemical substances by application Substances 0.000 abstract description 3
- 239000004088 foaming agent Substances 0.000 abstract description 3
- 239000006185 dispersion Substances 0.000 abstract 2
- 238000002156 mixing Methods 0.000 abstract 1
- 229920005989 resin Polymers 0.000 description 11
- 239000011347 resin Substances 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 10
- 238000005187 foaming Methods 0.000 description 6
- 239000003463 adsorbent Substances 0.000 description 4
- 229920000092 linear low density polyethylene Polymers 0.000 description 4
- 239000004707 linear low-density polyethylene Substances 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 238000004332 deodorization Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- NEHMKBQYUWJMIP-UHFFFAOYSA-N chloromethane Chemical compound ClC NEHMKBQYUWJMIP-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 2
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- -1 polypropylene Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 2
- BOSAWIQFTJIYIS-UHFFFAOYSA-N 1,1,1-trichloro-2,2,2-trifluoroethane Chemical compound FC(F)(F)C(Cl)(Cl)Cl BOSAWIQFTJIYIS-UHFFFAOYSA-N 0.000 description 1
- DDMOUSALMHHKOS-UHFFFAOYSA-N 1,2-dichloro-1,1,2,2-tetrafluoroethane Chemical compound FC(F)(Cl)C(F)(F)Cl DDMOUSALMHHKOS-UHFFFAOYSA-N 0.000 description 1
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910001579 aluminosilicate mineral Inorganic materials 0.000 description 1
- JYIBXUUINYLWLR-UHFFFAOYSA-N aluminum;calcium;potassium;silicon;sodium;trihydrate Chemical compound O.O.O.[Na].[Al].[Si].[K].[Ca] JYIBXUUINYLWLR-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- HRYZWHHZPQKTII-UHFFFAOYSA-N chloroethane Chemical compound CCCl HRYZWHHZPQKTII-UHFFFAOYSA-N 0.000 description 1
- AFYPFACVUDMOHA-UHFFFAOYSA-N chlorotrifluoromethane Chemical compound FC(F)(F)Cl AFYPFACVUDMOHA-UHFFFAOYSA-N 0.000 description 1
- 229910001603 clinoptilolite Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229940087091 dichlorotetrafluoroethane Drugs 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920005680 ethylene-methyl methacrylate copolymer Polymers 0.000 description 1
- 229920005677 ethylene-propylene-butene terpolymer Polymers 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 210000000744 eyelid Anatomy 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 1
- 239000001095 magnesium carbonate Substances 0.000 description 1
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 229910052680 mordenite Inorganic materials 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- UOURRHZRLGCVDA-UHFFFAOYSA-D pentazinc;dicarbonate;hexahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Zn+2].[Zn+2].[Zn+2].[Zn+2].[Zn+2].[O-]C([O-])=O.[O-]C([O-])=O UOURRHZRLGCVDA-UHFFFAOYSA-D 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 230000008569 process Effects 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
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 229910000391 tricalcium phosphate Inorganic materials 0.000 description 1
- 235000019731 tricalcium phosphate Nutrition 0.000 description 1
- 229940078499 tricalcium phosphate Drugs 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
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野〕
本発明は各種ガス吸着剤として用いることができるガス
吸着能を有するポリオレフィン系樹脂発泡粒子、その成
形体および前記発泡粒子の製法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to expanded polyolefin resin particles having gas adsorption ability that can be used as various gas adsorbents, molded articles thereof, and a method for producing the expanded particles.
[従来の技術・発明が解決しようとする課題]ゼオライ
トはその特異な結晶構造およびイオン的性質により、吸
着剤、分離剤、イオン交換剤、触媒などとして広く用い
られている。とくにその吸着能を利用して、乾燥、精製
、回収などの用途に好適に用いられている。[Prior Art/Problems to be Solved by the Invention] Zeolites are widely used as adsorbents, separation agents, ion exchange agents, catalysts, etc. due to their unique crystal structure and ionic properties. In particular, by taking advantage of its adsorption ability, it is suitably used for purposes such as drying, purification, and recovery.
包装分野においてもゼオライトを添加したフィルム包装
材は生鮮食料品の鮮度保持や脱臭に使用されている。In the packaging field, zeolite-added film packaging materials are used to maintain freshness and deodorize perishable foods.
しかし、前記フィルム包装材では脱臭性が充分でない、
被包装物の形態によっては効率的な脱臭ができない、ま
た緩衝包装材としての効果は期待できないなどの問題が
ある。However, the film packaging material does not have sufficient deodorizing properties.
Depending on the form of the packaged item, there are problems such as it is not possible to deodorize efficiently, and it cannot be expected to be effective as a cushioning packaging material.
[課題を解決するための手段]
本発明者らは前記のごとき問題を改善するために鋭意に
研究を重ねた結果、ゼオライトを含む特定の樹脂粒子を
発泡させ、えられた発泡粒子から成形体を製造し、包装
容器に使用すると、緩衝性を有しながら生鮮食料品の鮮
度保持性や脱臭性に優れた効果を示すことを見出すに至
った。またゼオライトを添加した特定の樹脂粒子は、該
樹脂粒子に揮発性発泡剤を含浸させて水蒸気などの加熱
媒体で加熱・発泡させる方法では高い発泡倍率をうろこ
とが難しいが、分散剤の存在下で揮発性発泡剤とともに
耐圧容器中に水に分散させ、高温・高圧の状態にしてか
ら低圧域に放出して発泡させる方法により、発泡倍率の
高いゼオライト含有ポリオレフィン系樹脂発泡粒子かえ
られることを併せて見出し、本発明を完成するに至った
。[Means for Solving the Problems] As a result of intensive research in order to improve the above-mentioned problems, the present inventors foamed specific resin particles containing zeolite, and created a molded article from the obtained expanded particles. The inventors have discovered that when produced and used in packaging containers, it exhibits excellent effects on freshness retention and deodorization of perishable foods while having buffering properties. In addition, it is difficult to achieve a high expansion ratio with certain resin particles to which zeolite has been added by impregnating the resin particles with a volatile blowing agent and heating and foaming them with a heating medium such as water vapor, but in the presence of a dispersant. In addition, foamed particles of zeolite-containing polyolefin resin with a high expansion ratio can be obtained by dispersing them in water together with a volatile foaming agent in a pressure-resistant container, bringing them to a high temperature and high pressure state, and then releasing them into a low pressure region to foam them. This discovery led to the completion of the present invention.
本発明は、
ゼオライトを5〜50%(重量%、以下同様)含有し、
ガス吸着能を有するポリオレフィン系樹脂発泡粒子、
前記ポリオレフィン系樹脂発泡粒子から成形された成形
体および
ゼオライトを5〜50%含有するポリオレフィン系樹脂
粒子と揮発性発泡剤とを耐圧容器中、分散剤の存在下で
水に分散させ、加熱・昇温して高温・高圧の状態にし、
耐圧容器下部に設けた放出口から低圧域に放出して発泡
させることを特徴とするガス吸着能を有するポリオレフ
ィン系樹脂発泡粒子の製法
に関する。The present invention contains 5 to 50% (weight%, the same applies hereinafter) of zeolite,
Expanded polyolefin resin particles having gas adsorption ability, a molded article formed from the expanded polyolefin resin particles, polyolefin resin particles containing 5 to 50% of zeolite, and a volatile blowing agent are placed in a pressure-resistant container, and a dispersant is added to the foamed particles. Dispersed in water in the presence of a substance, heated and raised to a high temperature and high pressure state,
The present invention relates to a method for producing foamed polyolefin resin particles having gas adsorption ability, which is characterized by foaming by discharging into a low pressure region from a discharge port provided at the bottom of a pressure-resistant container.
[実施例]
本発明の発泡粒子はゼオライトを含有するポリオレフィ
ン系樹脂からの発泡粒子である。[Example] The foamed particles of the present invention are foamed particles made of a polyolefin resin containing zeolite.
前記発泡粒子の大きさ、発泡倍率、発泡粒子の密度など
にはとくに限定はないが、通常直径1〜20+em程度
の大きさで、発泡倍率が5〜100倍程度のものが使用
される。Although there are no particular limitations on the size, expansion ratio, density, etc. of the foamed particles, those having a diameter of about 1 to 20+em and an expansion ratio of about 5 to 100 times are usually used.
前記ゼオライトには天然ゼオライトおよび合成ゼオライ
トがあり、主要成分は5I02、/V2O3、CaO、
Na2O、K2O,820である。天然ゼオライトは沸
石として総称される鉱物であり、比較的低温の加熱によ
りガラス化し、この過程で多量に含まれる水分の放出に
よって発泡状態となり、3次元網目構造を有する結晶性
含水アルミノケイ酸鉱物である。主としてクリノプチロ
ライト、モルデナイトとして産する。合成ゼオライトは
モレキュラーシーブとして知られており、構造は天然ゼ
オライトと類似している。The zeolite includes natural zeolite and synthetic zeolite, and the main components are 5I02, /V2O3, CaO,
Na2O, K2O, 820. Natural zeolite is a mineral collectively known as zeolite, and is a crystalline hydrated aluminosilicate mineral that vitrifies by heating at a relatively low temperature and becomes foamed by releasing a large amount of water during this process, and has a three-dimensional network structure. . It mainly occurs as clinoptilolite and mordenite. Synthetic zeolites are known as molecular sieves and are similar in structure to natural zeolites.
いずれのゼオライトも特異な結晶構造に基づく分子レベ
ルの細孔(2〜15人)を有する。ゼオライトの吸着材
としての特徴は
(1)ゼオライト結晶の分子ふるい作用により分子の形
状、大きさに応じて吸着分離ができること、(a結晶格
子内に存在する陽イオンがつくる電場の効果によって、
極性の高い分子などを選択的に強く吸着できること
にある。All zeolites have molecular-level pores (2 to 15 pores) based on their unique crystal structure. The characteristics of zeolite as an adsorbent are (1) the ability to adsorb and separate molecules according to their shape and size due to the molecular sieving action of zeolite crystals;
The reason is that it can selectively and strongly adsorb highly polar molecules.
ゼオライトの形態としては、粉末状、顆粒状のものがあ
り、粒系は1μから1CI11ぐらいまで種々のものが
ある。Zeolite can be in the form of powder or granules, and the grain size varies from 1μ to about 1CI11.
本発明に用いられるポリオレフィン系樹脂としては、た
とえば高密度ポリエチレン、中密度ポリエチレン、低密
度ポリエチレン、直鎖状低密度ポリエチレン、エチレン
−酢酸ビニルコポリマー、エチレン−メチルメタクリレ
ートコポリマーなどのエチレン系樹脂、ポリプロピレン
、エチレン−プロピレンコポリマー、エチレン−プロピ
レン−ブテンターポリマー、ブテン−プロピレンコポリ
マーなどのプロピレン系樹脂、ポリブテン−11ポリペ
ンテンなどがあげられるが、これらに限定されるもので
はない。またポリオレフィン系樹脂を50%以上含む他
の樹脂とのブレンド物も使用しうる。Examples of the polyolefin resin used in the present invention include ethylene resins such as high density polyethylene, medium density polyethylene, low density polyethylene, linear low density polyethylene, ethylene-vinyl acetate copolymer, and ethylene-methyl methacrylate copolymer, polypropylene, Examples include, but are not limited to, propylene resins such as ethylene-propylene copolymer, ethylene-propylene-butene terpolymer, butene-propylene copolymer, polybutene-11 polypentene, and the like. Blends with other resins containing 50% or more of polyolefin resin may also be used.
ポリオレフィン系樹脂は他の樹脂に比べてガスバリアー
性が低く、これが−膜内には欠点として考えられている
が、本発明のごときガス吸着材としての目的にはポリオ
レフィン系樹脂のようにガス透過性が大きいことが好ま
しく、このような樹脂を用いるためガス分子が樹脂中を
容易に拡散してゼオライトに到達して吸着され、吸着性
能が高くなる。それゆえ発泡粒子の基材樹脂としてポリ
オレフィン系樹脂を用いることが必須である。Polyolefin resins have low gas barrier properties compared to other resins, and this is considered a drawback when used in membranes, but for purposes of gas adsorption materials such as the present invention, gas permeability is low compared to polyolefin resins. It is preferable that the zeolite has high properties, and since such a resin is used, gas molecules easily diffuse through the resin, reach the zeolite, and are adsorbed, resulting in high adsorption performance. Therefore, it is essential to use a polyolefin resin as the base resin of the expanded particles.
本発明の発泡粒子中のゼオライトの含有率は5〜50%
、好ましくは10〜50%である。該含有率が5%未満
ではガス吸着材としての効果が充分でなく、50%をこ
えると発泡させることが困難になる。The content of zeolite in the expanded particles of the present invention is 5 to 50%
, preferably 10 to 50%. If the content is less than 5%, the effect as a gas adsorbent is insufficient, and if it exceeds 50%, it becomes difficult to foam.
前記のごとき本発明のポリオレフィン系樹脂発泡粒子は
このまま緩衝材などの用途に用いてもよいが、通常の予
備発泡粒子の成形と同様の方法で成形体にすることがで
きる。The polyolefin resin foamed particles of the present invention as described above may be used as is for purposes such as cushioning materials, but they can also be made into molded articles in the same manner as in the molding of ordinary pre-expanded particles.
このようにしてえられる成形体は通常の予備発泡粒子か
らの成形体と同様の機械的強度などの物性を有するうえ
に、優れた吸着能を有するため、通常の予備発泡粒子か
らの成形体と同様の用途に使用することができる。とく
に生鮮食品などのように脱臭性のごときガス吸着性が要
求される用途に用いたばあいには、脱臭性や鮮度保持性
などに優れた成形体かえられる。The molded product obtained in this way has physical properties such as mechanical strength similar to molded products made from normal pre-expanded particles, and also has excellent adsorption ability, so it is better than molded products made from normal pre-expanded particles. Can be used for similar purposes. In particular, when used in applications such as fresh foods that require gas adsorption properties such as deodorizing properties, molded products with excellent deodorizing properties and freshness retention properties can be used.
つぎに本発明の発泡粒子の製法について説明する。Next, the method for producing expanded particles of the present invention will be explained.
本発明の発泡粒子は、ゼオライトを5〜50%含有する
ポリオレフィン系樹脂粒子と揮発性発泡剤とを耐圧容器
中、分散剤の存在下で水に分散させ、加熱・昇温して高
温・高圧の状態にしたのち、耐圧容器下部に設けた放出
口から低圧域に放出して製造される。低圧域として通常
は大気圧が用いられる。The foamed particles of the present invention are produced by dispersing polyolefin resin particles containing 5 to 50% zeolite and a volatile blowing agent in water in the presence of a dispersant in a pressure-resistant container, and then heating and raising the temperature to achieve high temperature and high pressure. After the pressure is brought to this state, it is released into a low-pressure area from an outlet provided at the bottom of the pressure-resistant container. Atmospheric pressure is usually used as the low pressure region.
前記揮発性発泡剤としては、たとえばプロパン、ブタン
、ペンタン、ヘキサンなどの炭化水素類、トリクロロモ
ノフルオロメタン、ジクロロジフルオロメタン、モノク
ロロトリフルオロメタン、モノクロロジフルオロメタン
、トリクロロトリフルオロエタン、ジクロロテトラフル
オロエタン、モノクロロメタン、ジクロロメタン、モノ
クロロエタンなどのハロゲン化炭化水素類などがあげら
れるが、これらに限定されるものではない。これらの揮
発性発泡剤は単独で用いてもよく、2種以上混合して使
用してもよい。Examples of the volatile blowing agent include hydrocarbons such as propane, butane, pentane, and hexane, trichloromonofluoromethane, dichlorodifluoromethane, monochlorotrifluoromethane, monochlorodifluoromethane, trichlorotrifluoroethane, dichlorotetrafluoroethane, and monochloromethane. Examples include, but are not limited to, halogenated hydrocarbons such as lomethane, dichloromethane, and monochloroethane. These volatile foaming agents may be used alone or in combination of two or more.
前記分散剤としては、たとえば塩基性第3リン酸カルシ
ウム、塩基性炭酸マグネシウム、塩基性炭酸亜鉛、炭酸
カルシウム、ビロリン酸マグネシウムなどの難水溶性無
機粉末があげられ、その使用量としては通常たとえば水
100部(重量部、以下同様)に対し0.1〜5部程度
使用される。Examples of the dispersant include poorly water-soluble inorganic powders such as basic tricalcium phosphate, basic magnesium carbonate, basic zinc carbonate, calcium carbonate, and magnesium birophosphate, and the amount used is usually, for example, 100 parts of water. (parts by weight, the same applies hereinafter) is used in an amount of about 0.1 to 5 parts.
前記分散剤とともに、さらに少量の界面活性剤、たとえ
ばドデシルベンゼンスルホン酸ソーダ、n−パラフィン
スルホン酸ソーダ、α−オレフィンスルホン酸ソーダな
どを添加し、分散性を向上させてもよい。In addition to the dispersant, a small amount of a surfactant such as sodium dodecylbenzenesulfonate, sodium n-paraffin sulfonate, sodium α-olefin sulfonate, etc. may be added to improve dispersibility.
前記高温・高圧の状態とは、用いるポリオレフィン系樹
脂の種類、揮発性発泡剤の種類、量などによっても異な
るが、通常90〜180℃、5〜50kg4 (ゲージ
圧)の範囲である。The above-mentioned high temperature and high pressure state varies depending on the type of polyolefin resin used, the type and amount of volatile blowing agent, etc., but is usually in the range of 90 to 180°C and 5 to 50 kg4 (gauge pressure).
つぎに本発明を実施例に基づき説明する。Next, the present invention will be explained based on examples.
実施例1
撹拌機を宵する内容積4gの耐圧容器中で、平均粒子径
5μの天然産ゼオライト(日東粉化工業■製、活性化ゼ
オライ) 5PII2300)を30%含有する直鎖状
低密度ポリエチレン(以下、LLDPEという)ペレッ
ト(メルトフローインデックス(旧) 0.8g710
分、密度1.10g/cj、ベレット粒子径約3 mm
)100部を、水300部に分散剤として塩基性第3リ
ン酸カルシウム1.2部、n−パラフィンスルホン酸ソ
ーダo、ooe部を用いて分散させた。撹拌下、発泡剤
としてジクロロジフルオロメタン40部を入れ、昇温し
な。耐圧容器の内温ILB、5℃、内圧27.5しη(
ゲージ圧)で容器下部に設けたボール弁を開放し、直径
151Ilolの放出口より内容物を大気圧下に放出し
、発泡させた。えられた発泡粒子は、発泡倍率40倍(
高倍率)で気泡径が50〜ioo Jlのものであった
。Example 1 Linear low-density polyethylene containing 30% of naturally produced zeolite (manufactured by Nitto Funka Kogyo ■, activated zeolite 5PII2300) with an average particle size of 5 μm was placed in a pressure-resistant container with an internal volume of 4 g and equipped with a stirrer. (hereinafter referred to as LLDPE) pellets (melt flow index (old) 0.8g710
minute, density 1.10g/cj, pellet particle size approximately 3mm
) was dispersed in 300 parts of water using 1.2 parts of basic tertiary calcium phosphate and o, oe parts of sodium n-paraffin sulfonate as dispersants. While stirring, add 40 parts of dichlorodifluoromethane as a blowing agent, and do not raise the temperature. The internal temperature ILB of the pressure vessel is 5℃, the internal pressure is 27.5, and η(
A ball valve provided at the bottom of the container was opened under pressure (gauge pressure), and the contents were discharged to atmospheric pressure through a discharge port with a diameter of 151 Ilol to cause foaming. The obtained expanded particles have an expansion ratio of 40 times (
(high magnification) and the bubble diameter was 50 to ioo Jl.
えられた発泡粒子を60℃で24時間乾燥後、東洋機械
金属■製の5C−10B成形機を用いて、1kg4 (
ゲージ圧)の蒸気で加熱し、融着成形した。冷却後、金
型からとり出し、ただちに75℃で18時間乾燥し、室
温にとり出した。After drying the obtained expanded particles at 60°C for 24 hours, 1 kg4 (
The material was heated with steam at a pressure of 1.25 mm (gauge pressure) and fusion-molded. After cooling, it was taken out from the mold, immediately dried at 75°C for 18 hours, and then taken out to room temperature.
なお、前記金型の外寸は巾150■、長さ300II1
1高さ150■、内寸は巾100[fiffi、長さ2
50■、高さ25IllIIの箱型であった。The outside dimensions of the mold are width 150cm and length 300mm.
1 height 150cm, inner dimensions width 100cm, length 2
It was box-shaped, measuring 50cm and 25IllII in height.
えられた成形体は、内部融着性、表面性が良好で、やや
アイポリ−色で、発泡倍率が30倍であった。The obtained molded product had good internal fusion properties and surface properties, had a slightly eyelid color, and had an expansion ratio of 30 times.
比較例1
実施例1と同じ4IIの耐圧容器を用いて、基材樹脂と
してタルク0.01部を含有するDSC法融点117℃
、密度0.920g/cj、旧0.8g710分、球換
算直径2■のLLDPEベレットを用いた以外は、はぼ
実施例1と同じ条件で発泡させ、発泡倍率40倍(高倍
率)で気泡径が210〜250 jJnの発泡粒子をえ
た。Comparative Example 1 Using the same 4II pressure container as in Example 1, the DSC method containing 0.01 part of talc as the base resin had a melting point of 117°C.
Foaming was carried out under the same conditions as in Example 1, except that an LLDPE pellet with a density of 0.920 g/cj, a former weight of 0.8 g, 710 minutes, and a sphere equivalent diameter of 2 cm was used, and the foaming was carried out at a foaming ratio of 40 times (high magnification). Expanded particles with a diameter of 210 to 250 jJn were obtained.
えられた発泡粒子を実施例1と同様の方法で成形、乾燥
し、内部融着性、表面性の良好な発泡倍率30倍の成形
体をえた。The obtained expanded particles were molded and dried in the same manner as in Example 1 to obtain a molded product with an expansion ratio of 30 times and good internal fusion properties and surface properties.
実施例2〜4および比較例2〜4
実施例1および比較例1で・えられた発泡粒子を用いて
下記方法により、アンモニアガス(実施例2および比較
例2)、エチレンガス(実施例3および比較例3)、ト
リメチルアミンガス(実施例4および比較例4)に対す
るガス吸着性を評価した。結果を第1図に示す。Examples 2 to 4 and Comparative Examples 2 to 4 Using the expanded particles obtained in Example 1 and Comparative Example 1, ammonia gas (Example 2 and Comparative Example 2) and ethylene gas (Example 3) were prepared by the following method. and Comparative Example 3), and the gas adsorption properties for trimethylamine gas (Example 4 and Comparative Example 4) were evaluated. The results are shown in Figure 1.
(ガス吸着性評価方法)
温度25℃、湿度50%、1000ccの中栓付広口ビ
ンを用意し、ビン内を所定ガスで飽和状態に保持する。(Gas adsorption evaluation method) A 1000 cc wide mouth bottle with an inner stopper is prepared at a temperature of 25° C. and a humidity of 50%, and the inside of the bottle is kept saturated with a predetermined gas.
飽和状態の確認は、所定ガスを広口ビンに少量注入し、
広口ビン内のガスを約3cc抜きとってガス濃度をガス
クロマトグラフ法により測定する。ガス濃度の変化がな
くなったら、飽和状態とみなす。つぎに中栓を開き、発
泡粒子10gをすばやく入れて蓋をし、中栓に突きさし
た注射器の注射針よりガスを約3cc抜きとりガスクロ
マトグラフ法により濃度を測定する。To check the saturation state, inject a small amount of the specified gas into a wide mouth bottle,
Approximately 3 cc of the gas in the wide-mouthed bottle is removed and the gas concentration is measured by gas chromatography. When there is no change in gas concentration, it is considered to be saturated. Next, open the inner stopper, quickly add 10 g of foam particles, close the lid, draw out about 3 cc of gas from the needle of the syringe inserted into the inner stopper, and measure the concentration using gas chromatography.
飽和状態の濃度を100とし、時間の経過にしたがって
濃度がどのように変化するかを求める。Assuming that the concentration in the saturated state is 100, how the concentration changes over time is determined.
経過時間0分は、発泡粒子を広口ビンに入れ、蓋をした
ときである。The elapsed time of 0 minutes is when the foamed particles are placed in a wide mouth bottle and the lid is placed on the bottle.
第1図から、実施例1の発泡粒子は比較例1の発泡粒子
に比して、吸着性に優れ、脱臭性に優れていることがわ
かる。From FIG. 1, it can be seen that the foamed particles of Example 1 have better adsorption and deodorization properties than the foamed particles of Comparative Example 1.
また、実施例1および比較例1でえられた型内発泡成形
体を用いて緩衝性を評価したところ、差がなかった。Furthermore, when the cushioning properties were evaluated using the in-mold foam molded products obtained in Example 1 and Comparative Example 1, there was no difference.
[発明の効果コ
本発明の発泡粒子は、脱臭性、鮮度保持性に優れた緩衝
材などとして、また、本発明の型内発泡成形体は、脱臭
性、鮮度保持性にすぐれた緩衝包装材などとして使用し
うる。[Effects of the invention] The foamed particles of the present invention can be used as a cushioning material with excellent deodorizing properties and freshness retention properties, and the in-mold foam molded product of the present invention can be used as a cushioning packaging material with excellent deodorization properties and freshness retention properties. It can be used as such.
また本発明の発泡粒子は本発明の方法により製造しうる
。The expanded particles of the present invention can also be produced by the method of the present invention.
第1図は、実施例1および比較例1でえられた発泡粒子
のアンモニアガス、エチレンガス、トリメチルアミンガ
スに対するガス吸着性能を評価した、実施例2〜4およ
び比較例2〜4の結果を示すグラフである。
第1図
経過時間 (分)Figure 1 shows the results of Examples 2 to 4 and Comparative Examples 2 to 4, in which the gas adsorption performance of the expanded particles obtained in Example 1 and Comparative Example 1 to ammonia gas, ethylene gas, and trimethylamine gas was evaluated. It is a graph. Figure 1 Elapsed time (minutes)
Claims (1)
有するポリオレフィン系樹脂発泡粒子。 2 請求項1記載の発泡粒子から成形された成形体。 3 ゼオライトを5〜50重量%含有するポリオレフィ
ン系樹脂粒子と揮発性発泡剤とを耐圧容器中、分散剤の
存在下で水に分散させ、加熱・昇温して高温・高圧の状
態にし、耐圧容器下部に設けた放出口から低圧域に放出
して発泡させることを特徴とするガス吸着能を有するポ
リオレフィン系樹脂発泡粒子の製法。[Scope of Claims] 1. Polyolefin resin foam particles containing 5 to 50% by weight of zeolite and having gas adsorption ability. 2. A molded article formed from the expanded particles according to claim 1. 3 Polyolefin resin particles containing 5 to 50% by weight of zeolite and a volatile blowing agent are dispersed in water in the presence of a dispersant in a pressure-resistant container, heated and heated to a high temperature and high pressure state, and then A method for producing foamed polyolefin resin particles having gas adsorption ability, which comprises blowing the particles into a low pressure region through a discharge port provided at the bottom of a container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63231052A JPH0633341B2 (en) | 1988-09-14 | 1988-09-14 | Polyolefin resin foamed particles having gas adsorption ability, molded body, and method for producing foamed particles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63231052A JPH0633341B2 (en) | 1988-09-14 | 1988-09-14 | Polyolefin resin foamed particles having gas adsorption ability, molded body, and method for producing foamed particles |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0277436A true JPH0277436A (en) | 1990-03-16 |
JPH0633341B2 JPH0633341B2 (en) | 1994-05-02 |
Family
ID=16917534
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63231052A Expired - Lifetime JPH0633341B2 (en) | 1988-09-14 | 1988-09-14 | Polyolefin resin foamed particles having gas adsorption ability, molded body, and method for producing foamed particles |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0633341B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008546876A (en) * | 2005-06-24 | 2008-12-25 | エジオ マーギオッタ, | Liquid impervious material |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4922547A (en) * | 1972-06-28 | 1974-02-28 | ||
JPS5230872A (en) * | 1975-09-04 | 1977-03-08 | Mitsubishi Plastics Ind | Process for manufacturing expandable polyolefin particles |
-
1988
- 1988-09-14 JP JP63231052A patent/JPH0633341B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4922547A (en) * | 1972-06-28 | 1974-02-28 | ||
JPS5230872A (en) * | 1975-09-04 | 1977-03-08 | Mitsubishi Plastics Ind | Process for manufacturing expandable polyolefin particles |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008546876A (en) * | 2005-06-24 | 2008-12-25 | エジオ マーギオッタ, | Liquid impervious material |
Also Published As
Publication number | Publication date |
---|---|
JPH0633341B2 (en) | 1994-05-02 |
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