JPH04108834A - Method for preparing molded product reclaimed from foamed polystyrene - Google Patents
Method for preparing molded product reclaimed from foamed polystyreneInfo
- Publication number
- JPH04108834A JPH04108834A JP2226968A JP22696890A JPH04108834A JP H04108834 A JPH04108834 A JP H04108834A JP 2226968 A JP2226968 A JP 2226968A JP 22696890 A JP22696890 A JP 22696890A JP H04108834 A JPH04108834 A JP H04108834A
- Authority
- JP
- Japan
- Prior art keywords
- molded product
- foamed polystyrene
- pieces
- cubes
- 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims description 18
- 229920006248 expandable polystyrene Polymers 0.000 title abstract description 13
- 239000002245 particle Substances 0.000 claims abstract description 25
- 229920005989 resin Polymers 0.000 claims abstract description 19
- 239000011347 resin Substances 0.000 claims abstract description 19
- 239000006260 foam Substances 0.000 claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 3
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 3
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 2
- -1 fluoro compound Chemical class 0.000 claims abstract 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 50
- 229920006328 Styrofoam Polymers 0.000 claims description 15
- 239000008261 styrofoam Substances 0.000 claims description 15
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000004064 recycling Methods 0.000 claims description 3
- 239000004793 Polystyrene Substances 0.000 claims description 2
- 229920002223 polystyrene Polymers 0.000 claims description 2
- 239000003570 air Substances 0.000 claims 1
- 238000000465 moulding Methods 0.000 abstract description 5
- 239000005022 packaging material Substances 0.000 abstract description 4
- 229910001120 nichrome Inorganic materials 0.000 abstract description 2
- 239000011810 insulating material Substances 0.000 abstract 1
- 238000005452 bending Methods 0.000 description 4
- 238000005187 foaming Methods 0.000 description 4
- 239000004604 Blowing Agent Substances 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920006327 polystyrene foam Polymers 0.000 description 2
- 229920001890 Novodur Polymers 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004794 expanded polystyrene Substances 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical class FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 238000010097 foam moulding Methods 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は発泡スチロール再生成形品の製造方法に関し、
とくに一度使用された発泡スチロール成形品を、再度、
梱包材、断熱材等として再使用するための方法に関する
。[Detailed Description of the Invention] (Industrial Application Field) The present invention relates to a method for manufacturing recycled foamed polystyrene molded products.
In particular, once used Styrofoam molded products are recycled.
This invention relates to a method for reusing packaging materials, insulation materials, etc.
(従来の技術)
一般に発泡スチロール成形品は1発泡性スチレン樹脂粒
子をスチーム等によって加熱し、予備発泡スチレン樹脂
粒子としたのち、熟成工程を経て。(Prior Art) Generally, expanded styrene molded products are produced by heating expandable styrene resin particles with steam or the like to form pre-expanded styrene resin particles, which are then subjected to an aging process.
小孔を有する金型に充填され再加熱され二次発泡し製造
されている。こうして得られた発泡スチロール成形品は
優れた経済性、軽量性、衛生性、断熱性等を示すため包
装材料、建材1食品容器等として多くの分野で使用され
ている。It is manufactured by filling a mold with small holes and reheating it to cause secondary foaming. The foamed polystyrene molded products thus obtained are used in many fields as packaging materials, building materials, food containers, etc. because they exhibit excellent economic efficiency, lightness, hygiene, heat insulation, etc.
しかしながら発泡スチロール成形品はカサ密度が低いこ
と及びワンウェイの用途が多いことよシ。However, styrofoam molded products have a low bulk density and are often used in one-way applications.
廃棄されたときの処理に難があった。There were difficulties in disposing of it when it was discarded.
本発明はかかる欠点に鑑み、使用済みの発泡スチロール
成形品を発泡体として有効に再利用すること全目的とす
る。更に詳しくは使用済みの発泡スチロール成形品を細
片状に切断し、これを原料として再度発泡性を付与した
のち、金形に充填。In view of these drawbacks, the entire purpose of the present invention is to effectively reuse a used expanded polystyrene molded product as a foam. More specifically, we cut used Styrofoam molded products into strips, use them as raw materials to give them foamability again, and then fill them into molds.
成形し発泡スチロール成形品として利用しようとするも
のである。The idea is to mold it and use it as a styrofoam molded product.
一度使用された発泡スチロール成形品を再利用とする試
みは過去何度か々されている。例えば特開昭50−88
185号及び特開昭50−88186号では発泡スチロ
ール成形品を細片としたのち。There have been many attempts in the past to recycle used Styrofoam molded products. For example, JP-A-50-88
No. 185 and JP-A No. 50-88186, after a styrofoam molded product is cut into strips.
ペンタン等の発泡剤により収縮9発泡剤の再含浸を行い
発泡性スチレン系樹脂粒子を得ようとする方法が示され
ている。また公知技術としては発泡スチロール成形品を
粉砕機で粉砕後、未便用の発泡スチロール粒子と混合成
形する方法などがある。A method of obtaining expandable styrenic resin particles by re-impregnating the shrinkage 9 blowing agent with a blowing agent such as pentane is disclosed. Further, as a known technique, there is a method of crushing a foamed polystyrene molded product using a crusher, and then mixing and molding the molded product with foamed polystyrene particles for non-consumption use.
(発明が解決しようとする課題) しかしながらこれらの方法は次の理由によシ。(Problem to be solved by the invention) However, these methods are difficult for the following reasons.
工業的に行われてはいなかった。前者は9発泡スチロー
ル成形品を細片状にしたのち、耐圧容器に充填されるわ
けでるるか1発泡体ゆえ容積効率が劣)、経済的でなか
った。一方、粉砕機で粉砕後発泡粒と混合成形する方法
は、その混入率が10%を越えることは9発泡体の気泡
構造を破壊し発泡スチロール成形品品質を著しく低下さ
せるため使用済み発泡スチロール成形品の処理方法とし
ては適切でなかった。It was not done industrially. The former method was not economical because the styrofoam molded product was cut into strips and then filled into a pressure container (because it was a foam product, the volumetric efficiency was poor). On the other hand, in the method of mixing and molding foam particles after crushing them in a crusher, if the mixing ratio exceeds 10%, the cell structure of the 9 foam will be destroyed and the quality of the foamed polystyrene molded product will deteriorate significantly. It was not an appropriate treatment method.
本発明は、これらの課題を解決し、有効な発泡スチロー
ル再生成形品の製造方法を提供するものである。The present invention solves these problems and provides an effective method for producing recycled foamed polystyrene molded products.
(課題を解決するための手段)
すなわち1本発明は一度使用した発泡スチロール成形品
を再生利用する方法であって、まず発泡スチロール成形
品を細片に切断し、該細片を加圧気体下に保持して発泡
性を付与し、必要に応じて未使用の予備発泡スチレン樹
脂粒子と混合し9次いで成形することを特徴とする発泡
スチロール再生成形品の製造方法に関する。(Means for Solving the Problems) That is, 1. The present invention is a method for recycling a once-used polystyrene foam molded product, which involves first cutting the polystyrene foam molding into strips, and holding the strips under pressurized gas. The present invention relates to a method for producing a recycled polystyrene molded product, which is characterized in that the foamed polystyrene resin particles are mixed with unused pre-expanded styrene resin particles as needed, and then molded.
一度使用した発泡スチロール成形品を細片に切断する方
法としては、特に限定はされないが、粉砕機等によって
独立気泡発泡体としての気泡構造までも破壊してしまう
方法よシも9例えばニゲロム線等の熱線により、気泡構
造を破壊することなく切断する方法が、得られる再生成
形品の特性の面からも好ましい。There are no particular limitations on the method of cutting a used Styrofoam molded product into small pieces, but there are also methods in which the cell structure of the closed-cell foam is destroyed using a crusher, etc. A method in which the cell structure is cut without destroying it using a hot wire is preferable from the viewpoint of the characteristics of the resulting recycled molded product.
細片の形状は、特に制限されるものではないが。The shape of the strip is not particularly limited.
均一な大きさであるのがよく、特に立方体(正六面体)
、直方体、長方体、それらに類似の形状等の角状細片で
あるのが好ましく、特に立方体でろるのが好ましい。It is best to have a uniform size, especially a cube (regular hexahedron)
, rectangular parallelepipeds, rectangular parallelepipeds, angular strips of shapes similar to these, etc. are preferred, and cubes are particularly preferred.
細片の大きさとしては、未使用の予備発泡スチレン樹脂
粒子と混合する場合には、未使用の予備発泡スチレン樹
脂粒子の粒子径との比較において。When mixing with unused pre-expanded styrene resin particles, the size of the pieces is compared to the particle size of the unused pre-expanded styrene resin particles.
スチレン樹脂粒子の平均粒子径/#lI片の大きさ(球
状の場合は直径、角状の場合は縦、横、高さの3辺の長
さの平均値)で0,01〜1.0であるのが成形品の外
観や、成形のしやすさの面で好ましい。体積比では、ス
チレン樹脂粒子/ニアfEU片で10−6〜1.0であ
るのが好ましい。Average particle diameter of styrene resin particles/size of #lI piece (diameter if spherical, average value of length, width, and height of 3 sides if angular) 0.01 to 1.0 It is preferable in terms of the appearance of the molded product and the ease of molding. The volume ratio of styrene resin particles/near fEU piece is preferably 10-6 to 1.0.
さらに具体的な大きさへは、5肺角〜10cm角の立方
体が好ましい。For a more specific size, a cube of 5 cm square to 10 cm square is preferable.
細片は、加圧気体下に保持して発泡性を付与するが9発
泡性を付与せしめる要因として加圧気体(以下9発泡剤
とする)の種類、加圧圧力、加圧時間、加圧温度等の諸
条件がある。The pieces are held under pressurized gas to impart foaming properties.9 Factors that impart foaming properties include the type of pressurized gas (hereinafter referred to as 9 foaming agent), pressurizing pressure, pressurizing time, and pressurization. There are various conditions such as temperature.
発泡剤としては、経済性、取扱いのし易さから空気、窒
素、炭化水素、フロン化合物、またはこれらの混合物の
中から選択されるのが好ましい。The blowing agent is preferably selected from air, nitrogen, hydrocarbons, fluorocarbon compounds, or mixtures thereof from the viewpoint of economy and ease of handling.
加圧圧力はゲージ圧力で0.1 kg/cm2以上10
に9/cm2以下であるのが好ましい。0−1kg/c
m2未満では長時間加圧下に置かなければならないばか
シでなく、高い発泡性を付与することが困難である。The pressurizing pressure is 0.1 kg/cm2 or more in gauge pressure10
It is preferable that it is 9/cm2 or less. 0-1kg/c
If it is less than m2, it is difficult to keep it under pressure for a long time, and it is difficult to provide high foaming properties.
一方、10kg/cm2を越えることは、その必要がな
いばかりでなく9発泡体の気泡構造を破壊し発泡成形体
としたときの物性を低下させる傾向にある。On the other hand, if it exceeds 10 kg/cm2, it is not only unnecessary, but also tends to destroy the cell structure of the foam and deteriorate the physical properties of the foam molded product.
発泡スチロール成形品細片に発泡性を付与せしめる為の
時間はその他の諸条件によって異な9゜特に限定される
ものでないが、おおよそ約30分以上要する。又、加圧
時の雰囲気温度は発泡スチロール成形品細片が軟化、凝
集する温度以下であればよい。The time required to impart foamability to the styrofoam molded strips varies depending on other conditions and is not particularly limited, but approximately 30 minutes or more is required. Further, the atmospheric temperature during pressurization may be below the temperature at which the styrofoam molded article pieces soften and coagulate.
得られる発泡性を付与された細片は1次いで必一
要に応じて未使用の予備発泡スチレン樹脂粒子と混合さ
れ、成形される。The resulting expandable strips are then optionally mixed with unused pre-expanded styrene resin particles and molded.
得られる再生成形品の強度の面から、未使用の予備発泡
スチレン樹脂粒子と混合する方が好ましいが、この場合
、細片の混合量としては、再生率の面から10体積チ以
上であるのが好ましく、また得られる発泡スチロール再
生成形品の物性の面からは70体積係以下であるのが好
ましい。From the viewpoint of the strength of the recycled molded product obtained, it is preferable to mix it with unused pre-expanded styrene resin particles, but in this case, from the viewpoint of recycling rate, the amount of mixed pieces should be 10 volume cm or more. is preferable, and from the viewpoint of the physical properties of the obtained recycled styrene molded product, it is preferable that the volume coefficient is 70 or less.
なお、細片のみ100チ使用しても特定の梱包材として
は十分使用に劇えうるものである。Note that even if only 100 strips are used, it can be used as a specific packaging material.
使用される未使用の予備発泡スチレン樹脂粒子の種類や
大きさ(粒子径)は、特に限定されるものではない。The type and size (particle diameter) of the unused pre-expanded styrene resin particles used are not particularly limited.
また、成形条件等は常法に従って行なうことができる。Moreover, the molding conditions etc. can be carried out according to conventional methods.
(実施例) つぎに実施例を示し本発明を更に詳しく説明する。(Example) Next, the present invention will be explained in more detail with reference to Examples.
実施例1
46倍(−46mf!、/ 9 )に発泡された発泡ス
チロール成形品をニクロム線で70角の立方体に切断し
、見かけ発泡倍数47倍の角状発泡スチレン樹脂細片を
得た。この発泡スチロール成形品細片をゲージ圧1.0
kg/ cm2の圧縮空気下に1時間おき。Example 1 A styrene foam molded product foamed to 46 times (-46 mf!, /9) was cut into 70 square cubes with a nichrome wire to obtain angular foamed styrene resin pieces with an apparent expansion ratio of 47 times. Gauge pressure 1.0
kg/cm2 of compressed air every hour.
発泡性を調べたところ加圧前の発泡性が1.2 vol
/vat (発泡スチロール成形品細片を沸騰水中に2
分装置いたときの体積比(例 1.2 vol/vol
=2096の体積増加))であったのに対し、1.5v
ol/volまで向上した。この発泡性スチロール成形
品細片を10100X100X45の長方体の内寸をも
つ金型に充填し1.2 kg/ cm2のスチーム圧で
15秒間加熱し発泡成形体を得た。成形品の発泡倍率と
曲げ強度を(JIS A9511による)全表IK示し
た。When the foamability was investigated, the foamability before pressurization was 1.2 vol.
/vat (Styrofoam molded product strips are placed in boiling water for 2
Volume ratio when using a separation device (Example 1.2 vol/vol
= 2096 volume increase)), whereas 1.5v
It improved to ol/vol. The pieces of the foamable styrene molded product were filled into a mold having rectangular inner dimensions of 10100 x 100 x 45, and heated for 15 seconds at a steam pressure of 1.2 kg/cm2 to obtain a foamed molded product. The expansion ratio and bending strength of the molded product are shown in Table IK (according to JIS A9511).
実施例2〜4
表1に実施例1と同様にして得られた発泡スチロール成
形品細片と52倍に予備発泡した平均粒子径が約2.0
旧である未使用の発泡スチレン樹脂粒子(日立化成工業
■製)・イビーズA3−T)’r混合し、実施例1と同
様に成形し、評価した。その結果を表1に示した。Examples 2 to 4 Table 1 shows the foamed polystyrene molded strips obtained in the same manner as in Example 1 and the average particle diameter of the pre-expanded 52 times that of about 2.0.
Old, unused expanded styrene resin particles (manufactured by Hitachi Chemical Co., Ltd.) and Ibis A3-T) were mixed, molded in the same manner as in Example 1, and evaluated. The results are shown in Table 1.
参考例1
実施例10発泡スチロール細片を使用せず、全て未使用
の発泡スチレン樹脂粒子として同様に成形し、評価した
。その結果を表1に示した。Reference Example 1 Example 10 No expanded styrene foam pieces were used, and all unused expanded styrene resin particles were similarly molded and evaluated. The results are shown in Table 1.
比較例1〜4
加圧未処理の発泡スチレン樹脂細片又は加圧未処理の粉
砕機による粉砕品を用いて表1に示す配合とし、実施例
1と同様に成形し、評価した。その結果を表1に示した
。Comparative Examples 1 to 4 The formulations shown in Table 1 were prepared using non-pressurized styrene foam resin pieces or non-pressurized pulverized products using a pulverizer, and molded and evaluated in the same manner as in Example 1. The results are shown in Table 1.
以上の例及びその他の例をまとめ、第1図に発泡スチロ
ール成形品細片混入量と成形品の曲げ強(発明の効果)
本発明の製造方法によれば、一度使用した発泡スチロー
ル成形品を、成形品の品質をあまシ低下させることなく
、経済的に再利用することができる。また、未使用の予
備発泡スチレン樹脂粒子と併用した場合には、未使用の
もののみより曲げ強度を向上せしめることもできる。The above examples and other examples are summarized and shown in Fig. 1 shows the amount of fine pieces mixed in a Styrofoam molded product and the bending strength of the molded product (effects of the invention). It can be economically reused without significantly reducing the quality of the product. Furthermore, when used in combination with unused pre-expanded styrene resin particles, the bending strength can be improved compared to unused particles alone.
第1図は1本発明の実施例及び比較飼において得られた
発泡成形品の、一度使用した発泡スチロール成形品の混
入量と曲げ強度の関係を示すグラフである。FIG. 1 is a graph showing the relationship between the amount of mixed styrene foam molded products used once and the bending strength of the foamed molded products obtained in Examples of the present invention and comparative feeding.
Claims (1)
方法であつて、まず発泡スチロール成形品を細片に切断
し、該細片を加圧気体下に保持して発泡性を付与し、成
形することを特徴とする発泡スチロール再生成形品の製
造方法。 2、細片に発泡性を付与した後、未使用の予備発泡スチ
レン樹脂粒子と混合し、成形する請求項1記載の発泡ス
チロール再生成形品の製造方法。 3、加圧気体が、空気、窒素、炭化水素、フロン化合物
またはこれらの混合物である請求項1または2記載の発
泡スチロール再生成形品の製造方法。 4、細片の量が、未使用の予備発泡スチレン樹脂粒子と
の合計に対して10体積%以上である請求項2又は3記
載の発泡スチロール再生成形品の製造方法。[Claims] 1. A method for recycling a once-used styrofoam molded product, in which the styrofoam molded product is first cut into thin pieces, and the thin pieces are held under pressurized gas to impart foamability. A method for manufacturing a recycled styrofoam molded product, the method comprising: 2. The method for manufacturing a recycled styrene molded product according to claim 1, wherein after imparting foamability to the strips, the strips are mixed with unused pre-expanded styrene resin particles and molded. 3. The method for producing a recycled polystyrene molded product according to claim 1 or 2, wherein the pressurized gas is air, nitrogen, hydrocarbon, a fluorocarbon compound, or a mixture thereof. 4. The method for producing a recycled styrene foam product according to claim 2 or 3, wherein the amount of the pieces is 10% by volume or more based on the total amount of the unused pre-expanded styrene resin particles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2226968A JPH04108834A (en) | 1990-08-29 | 1990-08-29 | Method for preparing molded product reclaimed from foamed polystyrene |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2226968A JPH04108834A (en) | 1990-08-29 | 1990-08-29 | Method for preparing molded product reclaimed from foamed polystyrene |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04108834A true JPH04108834A (en) | 1992-04-09 |
Family
ID=16853447
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2226968A Pending JPH04108834A (en) | 1990-08-29 | 1990-08-29 | Method for preparing molded product reclaimed from foamed polystyrene |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04108834A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06285859A (en) * | 1993-04-06 | 1994-10-11 | Hiroshima Pref Gov | Composite made of material of waste foamed plastics and manufacture thereof |
WO2006100517A1 (en) * | 2005-03-24 | 2006-09-28 | Zotefoams Plc | Process for introducing a gas into a polymer |
-
1990
- 1990-08-29 JP JP2226968A patent/JPH04108834A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06285859A (en) * | 1993-04-06 | 1994-10-11 | Hiroshima Pref Gov | Composite made of material of waste foamed plastics and manufacture thereof |
WO2006100517A1 (en) * | 2005-03-24 | 2006-09-28 | Zotefoams Plc | Process for introducing a gas into a polymer |
GB2439697A (en) * | 2005-03-24 | 2008-01-02 | Zotefoams Plc | Process for introducing a gas into a polymer |
GB2439697B (en) * | 2005-03-24 | 2009-11-04 | Zotefoams Plc | Process for introducing a gas into a polymer |
US8871823B2 (en) * | 2005-03-24 | 2014-10-28 | Zotefoams, PLC | Process for introducing a gas into a polymer |
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