JPH10195232A - Continuous production for carrying out recycling of expanded polystyrene by precipitation - Google Patents
Continuous production for carrying out recycling of expanded polystyrene by precipitationInfo
- Publication number
- JPH10195232A JPH10195232A JP3253297A JP3253297A JPH10195232A JP H10195232 A JPH10195232 A JP H10195232A JP 3253297 A JP3253297 A JP 3253297A JP 3253297 A JP3253297 A JP 3253297A JP H10195232 A JPH10195232 A JP H10195232A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- polystyrene
- expanded polystyrene
- mass
- white
- 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
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明では発泡スチロールの
リサイクルにピネンを主成分とする生松脂の水蒸気蒸溜
又は減圧蒸溜によって得た無色透明な松精油(ターペン
タインオイル)を用いる。之にはリモネンは含まない。BACKGROUND OF THE INVENTION In the present invention, colorless and transparent pine essential oil (tarpentine oil) obtained by steam distillation or vacuum distillation of raw pine resin containing pinene as a main component is used for recycling styrene foam. This does not include limonene.
【0002】[0002]
【従来の技術】従来溶解法による発泡スチロールのリサ
イクルが中々実施されなかったのは再製品のポリスチレ
ンより溶剤が高価であり、高価な溶剤は回収しなければ
ならないが真空蒸溜にせよ水蒸気蒸溜にしても沸点に達
するまで加熱し冷却して製品にする過程に5%〜10%
程の目減りは公算され又蒸溜する為に一釜毎の加熱は酸
化重合され溶剤の劣化はまぬがれない、一度酸化させる
と自動的に劣化が進む。特に鉄と反応し有機炭化水素で
有効なものはほとんど鉄のドラム缶に入れて置くだけで
半年で墨汁様に加色し使用出来なくなる。特に一釜度の
加熱蒸溜は禁物である、そこで油を加熱せずに常温で蒸
溜もしないで製品を得る様にしなければ採算が成り立た
ない。そこで本発明の沈澱法の出現が期待される。本発
明ではステンレス製の容器かアルミかジェラルミン製や
又はホーロー引きの容器を用い底には木製のスノコ板を
用意し之で製品を取出せる様に設置する。2. Description of the Related Art Conventionally, recycling of polystyrene foam by the dissolving method has not been carried out frequently because the solvent is more expensive than recycled polystyrene, and the expensive solvent must be recovered. 5% to 10% in the process of heating and cooling to the product to reach the boiling point
The degree of reduction is likely to be expected, and the heating of each pot is oxidatively polymerized to distill, and the deterioration of the solvent cannot be avoided. Once oxidized, the deterioration proceeds automatically. In particular, most of the organic hydrocarbons that react with iron and are effective will be colored like ink and become unusable in six months just by being placed in an iron drum. In particular, heating distillation at a pot temperature is a prohibited matter. Therefore, unless the oil is heated and the product is not distilled at room temperature, the profit cannot be established. Therefore, the appearance of the precipitation method of the present invention is expected. In the present invention, a wooden container is prepared at the bottom using a stainless steel container, an aluminum container, a duralumin container or an enameled container, and is installed so that the product can be taken out.
【0003】[0003]
【発明が解決しようとする課題】本発明は松精油と組合
わせて発泡スチロールを全く溶解しない油脂例えば石油
系の高精製軽質油や軽重質の溜分を15%〜25%の割
合で松精油に混合する事により之をリサイクルの基油と
し之を用いて火を用いず常温で連続的に原料を仕込み基
油の底部に溶解沈澱させてガム状の塊とし之を取出して
又直ちに仕込み又製品を取出すと言った絶妙な連続生産
を可能にする新規の方法に依る製造方法である。SUMMARY OF THE INVENTION The present invention relates to an oil and fat which does not dissolve styrofoam at all in combination with pine essential oil, such as a petroleum-based highly refined light oil or light heavy fraction at a ratio of 15% to 25% to pine essential oil. By mixing, this is used as the base oil for recycling, and the raw material is continuously used at room temperature without using fire, and dissolved and settled at the bottom of the base oil to form a gum-like mass. It is a manufacturing method based on a new method that enables exquisite continuous production, which is to say that it takes out.
【0004】[0004]
【課題を解決するための手段】本発明の方法は一釜度の
蒸溜はせずあくまで製品を基油の底にポリスチレンとし
て沈澱させガム状か餅状の塊とし取出し製品のポリスチ
レンを得る。この様な現象はピネンの溶解力の限度で溶
融した液が発泡スチロールを溶融しないが松精油とは溶
融する油脂例えば石油系軽質油や軽重質油等を混入する
事により臨界を破られたポリスチレンは比重の差から下
に沈澱するもので、基油に微粒子となって溶融したもの
が溶融の臨界を破られたポリスチレンの粒子は下に集っ
て塊をつくるものである。従って粒子の間にわずか数%
しか製品中の基油の混入していないのでガム状の塊とな
るものである。加熱蒸溜しない為に油の劣化がなく時々
油を補充しただけで一回に2〜3時間度に製品を取出し
持続的に連続生産が可能である。他方に比べ基油のロス
は飛躍的に少しですむわけである。一例をあげれば植物
油のフライオイルは15回も使うと熱で酸化重合し劣化
が初まるのが分りやすい例である。発泡スチロールは細
片にし油と接触する様T型の棒で時々かき廻す必要があ
る。之で沈澱を早める。沈澱を促す油は発泡スチロール
を溶解出来ない油で、成るべく松精油の沸点150℃と
沸点の近いものを選んだ方が都合がよい。あまり沸点の
高い重質油や植物油などは高価な割に製品の中に残り易
いので成るべく之を避け石油系のベンゾール、商品名
(ベンジン)等やホワイトスピンドル油やホワイト流動
パラフイン、ミネラルスピリットの無色のもの、ホワイ
トオイル等の中から選び例えばベンジンの様な沸点80
゜〜150゜の様なものが製品のポリスチレン中のわず
かに残った油を熱風等に掛け完成品とする折都合がよ
い。本発明では火を仕込中は用いないので油の寿命が長
く時々不足分を補充するだけで連続使用出来る、また油
が汚染し着色する事は殆んどない。容器から取出した製
品のポリスチレンはガム状や出来たての餅の様で取出し
た後、板の上で延ばしても手などに粘着しない、粘土の
様に手やロールで延す事が出来刃物で切る事も出来る。
製品中のわずかに残った油は熱風で完成させる。ステン
レスの大皿盤の上で5耗程度に延して熱風に掛け熱風は
冷却され僅かな油も回収する。製品はカッターで細片と
し再生に廻す。再製品100%でも新しいものと同様で
あり新品と混ぜても質を落す事はない。According to the method of the present invention, the product is precipitated as polystyrene at the bottom of the base oil without distillation at a pot temperature to obtain a gum-like or rice cake-like mass to obtain the product polystyrene. Such a phenomenon is that the liquid melted at the limit of the solvency of pinene does not melt the styrofoam, but the pine essential oil is melted by mixing fats and oils such as petroleum light oil and light heavy oil. The polystyrene particles which precipitate downward due to the difference in specific gravity, and which have been broken down into fine particles in the base oil and whose melting criticality has been broken, are collected below to form a lump. So only a few percent between particles
However, since only the base oil in the product is mixed, the product becomes a gum-like mass. Since there is no heat distillation, there is no deterioration of the oil, and the product is taken out at a time of about 2 to 3 hours at a time and the continuous production is possible only by replenishing the oil occasionally. Compared to the other, base oil losses are significantly smaller. To give an example, it is easy to see that vegetable oil frying oil is oxidatively polymerized by heat and deteriorates after 15 uses. Styrofoam needs to be broken into pieces and stirred occasionally with a T-shaped rod to make contact with the oil. This speeds up the precipitation. The oil that promotes precipitation is an oil that cannot dissolve styrene foam, and it is more convenient to select an oil that has a boiling point as close as possible to 150 ° C. of pine essential oil. Heavy oils and vegetable oils with a very high boiling point tend to remain in the product despite being expensive, so avoid them as much as possible. Choose from colorless, white oil, etc., with a boiling point of 80
It is convenient to use a small amount of oil in the polystyrene of the product such as {-150} by applying hot air or the like to the finished product. In the present invention, since the fire is not used during charging, the life of the oil is long and the oil can be continuously used only by replenishing the shortage occasionally, and there is almost no contamination and coloring of the oil. Polystyrene of the product taken out of the container is taken out as a gum or freshly made rice cake, and it does not stick to hands etc. even if it is extended on a plate, it can be extended with hands or rolls like clay You can also cut with.
The slight residual oil in the product is completed with hot air. It is spread on a stainless steel platen for about 5 wears and then blasted with hot air to cool the hot air and recover even a small amount of oil. The product is cut into small pieces with a cutter and recycled. Even 100% remanufactured products are the same as new ones and do not lose quality when mixed with new ones.
【0005】[0005]
【表1】 [Table 1]
【0006】第1表は沈澱した製品の品評である。重い
溜分程沸点が高いので後の処理に留意する必要がある。
本法ではロスが少ないので沈澱を促す油は少し高くても
沸点の低い方が有利である。Table 1 shows the qualities of the precipitated products. Since the boiling point is higher for a heavy distillate, it is necessary to pay attention to the subsequent treatment.
In this method, since the loss is small, it is advantageous that the oil that promotes precipitation has a low boiling point even if it is slightly high.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B29K 105:04 105:26 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI B29K 105: 04 105: 26
Claims (1)
石油系軽質油又は軽重油によって発泡スチロールを油底
に沈澱させてリサイクルを常温で連続して行う製造方
法。1. A production method wherein styrene foam is precipitated on an oil bottom with oils and fats, especially petroleum-based light oil or light and heavy oil, in which pinene is used in combination, and recycling is continuously performed at room temperature.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3253297A JPH10195232A (en) | 1997-01-09 | 1997-01-09 | Continuous production for carrying out recycling of expanded polystyrene by precipitation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3253297A JPH10195232A (en) | 1997-01-09 | 1997-01-09 | Continuous production for carrying out recycling of expanded polystyrene by precipitation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10195232A true JPH10195232A (en) | 1998-07-28 |
Family
ID=12361562
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3253297A Pending JPH10195232A (en) | 1997-01-09 | 1997-01-09 | Continuous production for carrying out recycling of expanded polystyrene by precipitation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10195232A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11407877B2 (en) | 2018-10-26 | 2022-08-09 | Polystvert Inc. | Processes for recycling polystyrene waste and/or polystyrene copolymer waste |
US11407878B2 (en) | 2014-10-03 | 2022-08-09 | Polystyvert Inc. | Processes for recycling polystyrene waste |
US11680149B2 (en) | 2017-11-20 | 2023-06-20 | Polystyvert Inc. | Processes for recycling polystyrene waste |
-
1997
- 1997-01-09 JP JP3253297A patent/JPH10195232A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11407878B2 (en) | 2014-10-03 | 2022-08-09 | Polystyvert Inc. | Processes for recycling polystyrene waste |
US11680149B2 (en) | 2017-11-20 | 2023-06-20 | Polystyvert Inc. | Processes for recycling polystyrene waste |
US11407877B2 (en) | 2018-10-26 | 2022-08-09 | Polystvert Inc. | Processes for recycling polystyrene waste and/or polystyrene copolymer waste |
US12018132B2 (en) | 2018-10-26 | 2024-06-25 | Polystyvert Inc. | Processes for recycling polystyrene waste and/or polystyrene copolymer waste |
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