JPS5945107A - Storing of polyester grnule - Google Patents
Storing of polyester grnuleInfo
- Publication number
- JPS5945107A JPS5945107A JP15451382A JP15451382A JPS5945107A JP S5945107 A JPS5945107 A JP S5945107A JP 15451382 A JP15451382 A JP 15451382A JP 15451382 A JP15451382 A JP 15451382A JP S5945107 A JPS5945107 A JP S5945107A
- Authority
- JP
- Japan
- Prior art keywords
- pellets
- granules
- polyester
- powder
- storing
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/06—Conditioning or physical treatment of the material to be shaped by drying
- B29B13/065—Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はポリエステル粉粒体をバンカー等に貯蔵する際
に粉粒体の含有水分率上昇を極力少なくする貯蔵方法に
関するものである。ポリエステルは通常溶融重合後にペ
レット状、チップ状または粉状等の粉粒体としホッパー
あるいはバンカー等に長時間貯蔵され、必要に応じて取
り出され、糸、フィルム、ボトル等に成形される。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a storage method for minimizing the increase in moisture content of polyester powder when storing it in a bunker or the like. After melt polymerization, polyester is usually made into powder such as pellets, chips, or powder and stored in a hopper or bunker for a long time, taken out as needed, and formed into threads, films, bottles, etc.
ところで、ポリエステルは、水分を含有したまま溶融す
ると、エステル結合が加水分解を起して重合度が低下し
、紡糸又は成形して得られた製品の品質を著しく低下さ
せる原因となる。By the way, when polyester is melted while containing water, the ester bonds are hydrolyzed and the degree of polymerization decreases, causing a significant deterioration in the quality of products obtained by spinning or molding.
このため、ポリエステルの溶融紡糸又は溶融成形に際し
、溶融前に該ポリエステルを粉粒体の状態で十分加熱乾
燥し、水分をできるだけ除去しておくことが行なわれて
いる。For this reason, when polyester is melt-spun or melt-molded, the polyester is sufficiently heated and dried in the form of powder or granules to remove as much moisture as possible before melting.
この乾燥工程では、十分な温度と時間をかけて粉粒体を
加熱乾燥し、G融工程において水分による重合度低下が
起らなくな、るようにしているにもかかわらず、加熱乾
燥後の粉粒体に大幅な水分率の変動が生ずるのを防ぐこ
とができな℃飄。In this drying process, the powder and granules are heated and dried at a sufficient temperature and time to prevent the degree of polymerization from decreasing due to moisture in the G melting process. It is not possible to prevent large fluctuations in the moisture content of powder and granules.
本発明者等は、この原因について、種々調査検討を重ね
た結果、乾燥前の粉粒体が貯蔵中に水分を吸収すると乾
燥1稈で十分な乾燥が行なえなくなり、乾燥後の粉粒体
の水分率が上昇することを見出し、貯蔵中の粉粒体が水
分を吸収しないようにすればこの問題を解消しうろこと
を究明して本発明に到達した。As a result of various investigations into the cause of this, the present inventors found that if the powder or granule before drying absorbs moisture during storage, sufficient drying cannot be performed in one drying process. They discovered that the moisture content increases, and discovered that this problem could be solved by preventing the granular material during storage from absorbing moisture, leading to the present invention.
即ち、本発明は、アルキレンテレフタレートを主たる繰
返単位とするポリエステル粉粒体を貯蔵するに際し、重
合終了後のポリエステルを粉粒体となした後、l亘ち圧
、該粉粒体の少なくとも表層部を結晶化せしめて貯蔵す
ることを特徴とするポリエステル粉粒体の貯蔵方法であ
る。That is, in the present invention, when storing a polyester powder having alkylene terephthalate as a main repeating unit, after the polyester is made into a powder after completion of polymerization, at least the surface layer of the powder is compressed for one hour. This is a method for storing polyester powder, which is characterized by crystallizing and storing a portion of the polyester powder.
本発明におけるポリエステルは、アルキレンテレフタレ
ートを主たる繰返単位とするもので、特にエチレンテレ
フタレートを主たる繰返単位とするものが好ましい。第
3成分として、例えば、アジピン酸、セバシン酸、イソ
フタル酸。The polyester in the present invention has alkylene terephthalate as its main repeating unit, and particularly preferably has ethylene terephthalate as its main repeating unit. Examples of the third component include adipic acid, sebacic acid, and isophthalic acid.
5−ソジウムスルホイソフタル酸、ナフタレンジカルボ
ン酸1等の二塩基酸類、オキシ安息香酸の如きオキシ酸
類、及びジエチレングリコール、プロピレングリコール
、ネオペンチルグリコール、ペンタエリスリトール、ポ
リエチレングリフール、1.4−ブタンジオール、等の
グリコール類を10モルチ以下共重合させてもよく、ま
た、他のポリマーを10重量%以下ブレンドしたもので
もよい。Dibasic acids such as 5-sodium sulfoisophthalic acid and naphthalene dicarboxylic acid 1, oxyacids such as oxybenzoic acid, and diethylene glycol, propylene glycol, neopentyl glycol, pentaerythritol, polyethylene glyfur, 1,4-butanediol, 10% or less of glycols may be copolymerized, or other polymers may be blended with 10% by weight or less.
また該ポリエステルには酸化チタン等の艶消剤、難燃剤
、耐候、耐熱剤、リン化合物等の着色安定剤、滞電防止
剤、蛍光増白剤、ホウ素化合物等の公知の粘度安定剤等
が含まれてもよい。The polyester also contains matting agents such as titanium oxide, flame retardants, weather and heat resistant agents, coloring stabilizers such as phosphorus compounds, antistatic agents, optical brighteners, known viscosity stabilizers such as boron compounds, etc. May be included.
本発明におけるポリエステル粉粒体とは、チップ、ペレ
ット、フレーク、粉末状のポリエステルを意味する。The polyester powder in the present invention means chips, pellets, flakes, and powdered polyester.
溶融紡糸、成形に先だって、粉粒体の乾燥を行なうまで
の間は、該粉粒体は、少なくともその表層部を結晶化さ
せた状態で貯蔵する必要がある、少なくとも表層部を結
晶化させておくことによって、粉粒体内部に水分が吸収
されるのが防Iしされ、乾燥前の粉粒体の水分率が増大
するようなことがなく、従って、乾燥後の粉粒体の水分
率が上昇するようなことがない。粉粒体内部に水分が吸
収されるのを防1ヒするには、そのP曙部のみを結晶化
させておけば十分であり、表1傾部結晶化層の厚さは、
20μ以−ヒ、特忙40μ以上とするのが好ましい。粉
粒体の全体な完全に結晶化させてもよいことはいうまで
もない。Prior to melt spinning and molding, the powder and granule must be stored in a state where at least the surface layer thereof is crystallized until the powder and granule are dried. This prevents moisture from being absorbed into the powder and granules, and the moisture content of the powder before drying does not increase. Therefore, the moisture content of the powder and granules after drying does not increase. There is no such thing as rising. In order to prevent moisture from being absorbed into the inside of the powder, it is sufficient to crystallize only the P-shape part, and the thickness of the crystallized layer in the inclined part in Table 1 is as follows:
It is preferable that the thickness is 20μ or more, and the special thickness is 40μ or more. It goes without saying that the entire powder or granule may be completely crystallized.
粉粒体を結晶化させるには、110℃以上の加熱水蒸気
で処理するのが好適で詰り、この加熱水蒸気は、イ【和
水蒸気であっても、スーパーヒートされた水蒸気でAり
ってもよい。該粉粒体の水分含有率の増加を防止すると
いういみで、なるべく120℃ないし200℃のスーパ
ーヒートされた水蒸気が好ましい。また加熱水蒸気温度
は、なるべく高温が望ましいが、温度をあまり高くしす
ぎると該ポリエステルの分解反応が促進されることより
200℃以下程度で結晶化処理することが好ましい。In order to crystallize powder and granules, it is preferable to treat them with heated steam at a temperature of 110°C or higher. good. In order to prevent an increase in the moisture content of the granular material, superheated steam at 120° C. to 200° C. is preferable. Further, the heating steam temperature is preferably as high as possible, but if the temperature is too high, the decomposition reaction of the polyester will be accelerated, so it is preferable to perform the crystallization treatment at about 200° C. or lower.
更に、加熱水蒸気で結晶化する場合には、粉粒体長時間
にわたって、水蒸気雰囲気中に曝露 5−
しておくと、粉粒体の水分率が増加することになるので
、なるべく短時間で処理するのが好ましい。処理時間を
短縮させることは、省エネルギー及び生産効率の向上の
うえからも好ましい。Furthermore, when crystallizing with heated steam, if the powder or granules are exposed to a steam atmosphere for a long time, the moisture content of the powder or granules will increase, so the treatment should be done in as short a time as possible. is preferable. It is preferable to shorten the processing time from the viewpoint of energy saving and improvement of production efficiency.
更に、本発明においては、粉粒体の結晶化処理を、重合
終了後粉粒体を形成した直後に行なうことが必要である
。粉粒体形成後、時間が経過してかし結晶化処理を施し
たのでは、その間に粉粒体が水分を吸収してしまうので
効果が半減してしまう。Furthermore, in the present invention, it is necessary to perform the crystallization treatment of the granular material immediately after the completion of polymerization and the formation of the granular material. If the crystallization treatment is performed after a period of time has elapsed after the formation of the powder, the effect will be halved as the powder will absorb water during that time.
このように、本発明方法によれば、貯蔵中の粉粒体の水
分含有率増加を防止し、乾燥後の粉粒体の水分率上昇を
防ぐことができ、溶融紡糸、成形時に製品が加水分解に
よって劣化するのを阻止することができる。また、本発
明方法では、貯蔵中の粉粒体がすでに結晶化されている
から、従来行なわれているように、乾燥直前に粘着防止
のために粉粒体を結晶化させる必要もな、い。As described above, according to the method of the present invention, it is possible to prevent an increase in the moisture content of the powder or granular material during storage, prevent an increase in the moisture content of the powder or granular material after drying, and prevent the product from becoming hydrated during melt spinning or molding. Deterioration due to decomposition can be prevented. In addition, in the method of the present invention, since the powder or granules during storage are already crystallized, there is no need to crystallize the powder or granules immediately before drying to prevent sticking, as is conventionally done. .
以下、実施例により本発明方法を説明する。The method of the present invention will be explained below with reference to Examples.
6−
実施例1〜3.比較例1〜2
ジメチルテレフタレートとエチレンクリコールを溶融重
合して得た融点257℃、極限粘変しηJ0.64のポ
リエチレンテレフタフートを、吐出、急冷後、切断して
、直径3 m 、長さ4ml+の円柱状ペレットとなし
、これをそわぞれ300fづつとり、直ちに次表に示す
小作で加熱水蒸気による結晶化処理を施した。尚、吐出
、切断直後のベレットの水分率は0.05重を係であっ
た。6- Examples 1-3. Comparative Examples 1 to 2 A polyethylene terephthalate foot obtained by melt polymerizing dimethyl terephthalate and ethylene glycol and having a melting point of 257°C and an ultimate viscosity change of ηJ of 0.64 was discharged, rapidly cooled, and then cut into pieces with a diameter of 3 m and a length. The pellets were made into cylindrical pellets with a size of 4 ml+, each of which was taken in 300 f portions, and immediately subjected to a crystallization treatment using heated steam in the form shown in the following table. The moisture content of the pellet immediately after being discharged and cut was 0.05 weight.
次いで各サンプルを500cr:、のビーカーに入れ上
部を開放したまま相対湿度65%、温度23℃の室内に
所定時間放置して吸湿量を測定1.、更に7日間貯蔵し
たものについて150℃の熱風による流動床上で3時間
乾燥し、ペレットの水分率を測定した。Next, each sample was placed in a 500 cr beaker and left in a room at a relative humidity of 65% and a temperature of 23° C. for a predetermined period of time with the top open, and the amount of moisture absorbed was measured.1. After further storage for 7 days, the pellets were dried on a fluidized bed using hot air at 150° C. for 3 hours, and the moisture content of the pellets was measured.
尚、比較のために結晶化処理を施さないペレットについ
ても実施例と同様なテストを行った(比較例1)。但し
、比較例1においては、ベレットの乾燥直前に110℃
の加熱水蒸気で2秒間結晶化処理を施した。For comparison, the same test as in the example was also conducted on pellets that were not subjected to crystallization treatment (Comparative Example 1). However, in Comparative Example 1, the pellet was heated at 110°C immediately before drying.
A crystallization treatment was performed for 2 seconds using heated steam.
それらの結果を次表に示す。ベレットを結晶化させて貯
蔵する本発明方法によれば、貯蔵中のペレットの吸湿I
が少なく、乾燥後のベレット水分率も低くなることが明
らかである。The results are shown in the table below. According to the method of the present invention for crystallizing and storing pellets, the moisture absorption I of pellets during storage is
It is clear that the moisture content of the pellet after drying is also low.
9一
実施例4〜6.比較例3〜4
実施例1〜3、比較例1〜2において、ベレットを、相
対湿度95チ、温度23℃の芥囲気中に貯蔵するように
変更し、その他の壱件はそのままとして実験をくりかえ
した1、結果を次表に示す。この結果からも、不発明方
法によれば。91 Examples 4-6. Comparative Examples 3 to 4 In Examples 1 to 3 and Comparative Examples 1 to 2, the pellets were changed to be stored in an atmosphere with a relative humidity of 95 degrees and a temperature of 23 degrees Celsius, and the experiments were carried out with the other conditions unchanged. Repeat 1. The results are shown in the table below. From this result also, according to the uninvented method.
貯蔵中のベレットの吸湿量が少なく、乾燥後のペレット
の水分率も低くなることが明らかである。It is clear that the pellets absorb less moisture during storage and the moisture content of the pellets after drying is also lower.
特許出願人 帝人株式会社 代理人 弁理士 前 1) 純 博 10−Patent applicant Teijin Ltd. Agent Patent Attorney Former 1) Jun Hiroshi 10-
Claims (1)
ポリエステル粉粒体を貯蔵するに際し、重合終了後のポ
リエステルを粉粒体となした後、直ちに、該粉粒体の少
なくとも表層部を結晶化せしめて貯蔵することを特徴と
するポリエステル粉粒体の貯蔵方法。 2 粉粒体表層部の結晶化層の厚さが20μ以上である
特許請求の範囲第1項記載の方法。 3 結晶化を110℃以上の加熱水蒸気で行なう特許請
求の範囲第1項又は第2項記載の方法。[Scope of Claims] 1. When storing polyester powder containing alkylene terephthalate as a main repeating unit, immediately after the polyester is made into powder after completion of polymerization, at least the surface layer of the powder is stored. A method for storing polyester powder, which comprises crystallizing and storing it. 2. The method according to claim 1, wherein the thickness of the crystallized layer on the surface layer of the granular material is 20 μm or more. 3. The method according to claim 1 or 2, wherein the crystallization is carried out using heated steam at 110° C. or higher.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15451382A JPS5945107A (en) | 1982-09-07 | 1982-09-07 | Storing of polyester grnule |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15451382A JPS5945107A (en) | 1982-09-07 | 1982-09-07 | Storing of polyester grnule |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5945107A true JPS5945107A (en) | 1984-03-13 |
Family
ID=15585891
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15451382A Pending JPS5945107A (en) | 1982-09-07 | 1982-09-07 | Storing of polyester grnule |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5945107A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0361581U (en) * | 1989-10-19 | 1991-06-17 | ||
WO1997036736A1 (en) * | 1996-03-31 | 1997-10-09 | Bernhard Lipp | Process and device for steam-conditioning plastic articles |
US7192545B2 (en) | 2003-10-10 | 2007-03-20 | Eastman Chemical Company | Thermal crystallization of a molten polyester polymer in a fluid |
US7329723B2 (en) | 2003-09-18 | 2008-02-12 | Eastman Chemical Company | Thermal crystallization of polyester pellets in liquid |
JP2013518742A (en) * | 2010-02-08 | 2013-05-23 | オートマティック プラスティックス マシーナリー ゲーエムベーハー | Method for producing polyethylene terephthalate pellets |
-
1982
- 1982-09-07 JP JP15451382A patent/JPS5945107A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0361581U (en) * | 1989-10-19 | 1991-06-17 | ||
WO1997036736A1 (en) * | 1996-03-31 | 1997-10-09 | Bernhard Lipp | Process and device for steam-conditioning plastic articles |
US7329723B2 (en) | 2003-09-18 | 2008-02-12 | Eastman Chemical Company | Thermal crystallization of polyester pellets in liquid |
US7674877B2 (en) | 2003-09-18 | 2010-03-09 | Eastman Chemical Company | Thermal crystallization of polyester pellets in liquid |
US7192545B2 (en) | 2003-10-10 | 2007-03-20 | Eastman Chemical Company | Thermal crystallization of a molten polyester polymer in a fluid |
US8039581B2 (en) | 2003-10-10 | 2011-10-18 | Grupo Petrotemex, S.A. De C.V. | Thermal crystallization of a molten polyester polymer in a fluid |
US8309683B2 (en) | 2003-10-10 | 2012-11-13 | Grupo Petrotemex, S.A. De C.V. | Thermal crystallization of a molten polyester polymer in a fluid |
JP2013518742A (en) * | 2010-02-08 | 2013-05-23 | オートマティック プラスティックス マシーナリー ゲーエムベーハー | Method for producing polyethylene terephthalate pellets |
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