JPH0543677A - Cooling of polyester made by solid-phase polymerization - Google Patents
Cooling of polyester made by solid-phase polymerizationInfo
- Publication number
- JPH0543677A JPH0543677A JP22854191A JP22854191A JPH0543677A JP H0543677 A JPH0543677 A JP H0543677A JP 22854191 A JP22854191 A JP 22854191A JP 22854191 A JP22854191 A JP 22854191A JP H0543677 A JPH0543677 A JP H0543677A
- Authority
- JP
- Japan
- Prior art keywords
- solid
- cooling
- phase polymerization
- chips
- polyester
- 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
Landscapes
- Polyesters Or Polycarbonates (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は固相重合されたポリエス
テルの冷却方法に関し、更に詳しくは液体冷媒により効
率良く冷却を行い、かつこれによりチップ密度の無用な
増加が避けられ、高[η]、高密度の粉末状チップも除
去できる為、結果として白化のない、透明性の優れた成
形品の得られる固相重合されたポリエステルの冷却方法
に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for cooling a solid-state polymerized polyester, and more specifically, it efficiently cools with a liquid refrigerant, thereby avoiding an unnecessary increase in chip density and increasing the high [η]. The present invention relates to a method for cooling a solid-state polymerized polyester, which is capable of removing a high-density powdery chip, resulting in a molded article having no transparency and having excellent transparency.
【0002】[0002]
【従来の技術及び問題点】従来よりポリエステル、特に
ポリエチレンテレフタレートは、抗張力、ヤング率、弾
性回復率、耐衝撃性、寸法安定性等々の物理的性質及び
耐薬品性、耐候性、耐水性等々の化学的性質が優れ、工
業的に大きな価値を有することはよく知られており、繊
維、フイルム、工業用樹脂、ボトル等に広く用いられて
いる。2. Description of the Related Art Polyesters, especially polyethylene terephthalate, have hitherto been used in physical properties such as tensile strength, Young's modulus, elastic recovery rate, impact resistance, dimensional stability, etc. and chemical resistance, weather resistance, water resistance, etc. It is well known that it has excellent chemical properties and has great industrial value, and is widely used in fibers, films, industrial resins, bottles and the like.
【0003】また特に高[η]、低アセトアルデヒド、
低オリゴマーなどの要求のある用途では、一度重合させ
たポリマーを更に固相重合させたものを用いる場合も多
くなっている。この固相重合は180℃〜融点という高
温で長時間窒素気流下或いは真空下でチップなどの固体
状態で重合反応させるものである為、反応終了後の冷却
工程は不可欠であり、従来技術では窒素などの不活性気
流下で空冷するのが一般的であった。In addition, particularly high [η], low acetaldehyde,
In applications where low oligomers and the like are required, a polymer that has been once polymerized and further solid-phase polymerized is often used. Since this solid-state polymerization is a polymerization reaction in a solid state such as a chip under a nitrogen stream or under vacuum at a high temperature of 180 ° C. to melting point for a long time, a cooling step after completion of the reaction is indispensable. It was common to air-cool under an inert gas stream such as.
【0004】しかし、この方法では冷却に比較的長い時
間を要する為好ましくなく、更に冷却が徐冷となる為こ
の冷却中でもチップの密度が結晶化して増加してしま
う。しかも、従来の空冷方法では、重合において生ずる
高[η]・高密度の粉末状のチップが十分に除けないと
いう欠点もあった。However, this method is not preferable because it requires a relatively long time for cooling, and the cooling is gradually cooled, so that the density of the chips is crystallized and increased even during this cooling. Moreover, the conventional air-cooling method has a drawback in that the powdery chips with high [η] and high density generated in the polymerization cannot be sufficiently removed.
【0005】高密度のチップや高[η]・高密度の粉末
状のチップは、フイルムなどに成形した場合、完全に溶
融できず白異物として残ったり、成形品とした場合に一
部溶融不十分を惹起こし、その結果流動ムラや成形歪を
生じたり、ボトルを成形し口部を結晶化させた場合に結
晶化ムラを生ずるなど、種々の問題を引き起こす。粉末
状チップに関しては振動篩などで除去する方法があるが
その効果は十分でない。High-density chips and high- [η] / high-density powdery chips cannot be completely melted when formed into a film or the like, and remain as white foreign matters, or partially melted when formed into a molded product. As a result, various problems such as flow unevenness and molding distortion are caused, and crystallization unevenness occurs when the bottle is molded and the mouth is crystallized. There is a method of removing powdery chips with a vibrating screen or the like, but the effect is not sufficient.
【0006】このため粉チップを効率的に除去する方法
及びチップの密度を無用に増加させない効率的な固相重
合チップの冷却方法の開発が強く望まれていた。Therefore, it has been strongly desired to develop a method for efficiently removing powder chips and an efficient cooling method for solid-state polymerized chips that does not unnecessarily increase the density of chips.
【0007】[0007]
【発明の目的】本発明の目的はかかる問題を解消し、液
体冷媒により効率良く冷却を行い、かつこれによりチッ
プ密度の無用な増加が避けられ、高[η]・高密度の粉
末状チップも除去できる為、結果として白化のない透明
性の優れた成形品を得ることのできる、連続固相重合さ
れたポリエステルの冷却方法を提供することにある。SUMMARY OF THE INVENTION The object of the present invention is to solve such problems, to efficiently cool the liquid refrigerant, and to avoid an unnecessary increase in the chip density. It is an object of the present invention to provide a method for cooling a continuous solid-phase polymerized polyester, which can be removed, and as a result, a molded article having no transparency and excellent in transparency can be obtained.
【0008】[0008]
【発明の構成】本発明は、固相重合を行った直後の高温
状態にあるポリエステルのチップ等を液体溶媒に直接接
触させることからなる固相重合されたポリエステルの冷
却方法である。The present invention is a method for cooling a solid-phase polymerized polyester, which comprises directly contacting a polyester chip or the like in a high temperature state immediately after solid-phase polymerization with a liquid solvent.
【0009】本発明のポリエステルは少なくとも1段の
固相重合工程で重縮合されたものであり、その固相重合
方法に関しては従来から蓄積された方法で製造すること
ができる。固相重合は高温状態(180℃〜融点)で長
時間かけて行われる為反応後冷却過程が不可欠である。
本発明によればこの冷却方法は液体冷媒を用いてチップ
に直接接触させることにより行われる。冷媒としては例
えば水、塩酸などの酸性水溶液、NH3 水などのアルカ
リ性水溶液、その他金属塩の水溶液、アルコール類、ア
セトンなどのケトン類、エステル類など常温で液体のも
のならばいずれでもよく、冷媒としての温度は100℃
以下、好ましくは50℃以下、更に好ましくは30℃以
下である。The polyester of the present invention is polycondensed in at least one solid phase polymerization step, and the solid phase polymerization method can be manufactured by a conventionally accumulated method. Since the solid phase polymerization is carried out at a high temperature (180 ° C to melting point) for a long time, a cooling process after the reaction is indispensable.
According to the invention, this cooling method is carried out by directly contacting the chip with a liquid coolant. The refrigerant may be, for example, water, an acidic aqueous solution such as hydrochloric acid, an alkaline aqueous solution such as NH 3 water, an aqueous solution of other metal salts, alcohols, ketones such as acetone, esters, etc. as long as they are liquid at room temperature. Temperature is 100 ℃
The temperature is preferably 50 ° C. or lower, more preferably 30 ° C. or lower.
【0010】冷却方法としては、液体と接触できるなら
バッチ式、連続式を問わずいずれでもよく、バッチ方式
の場合冷却装置に冷媒と固相重合されたチップを入れて
冷却する方法などが例示できる。また、連続式の場合連
続的に冷媒を向流或いは並流で供給し、チップを冷却さ
せる方法などが例示できる。これらの方法により冷却さ
せたチップは、乾燥させる必要があるが、通常用いられ
るポリエステルチップの乾燥処理方法を用いることがで
きる。The cooling method may be either batch type or continuous type as long as it can contact with a liquid, and in the case of batch method, a method of cooling by putting a refrigerant and a solid-state polymerized chip in a cooling device can be exemplified. .. Further, in the case of the continuous system, a method of continuously supplying a coolant in a countercurrent or a parallel flow to cool the chip can be exemplified. The chips cooled by these methods need to be dried, but a commonly used polyester chip drying treatment method can be used.
【0011】[0011]
【発明の効果】本発明は液体冷媒により効率良く冷却を
行う冷却方法に関するものであり、これによりチップ密
度の無用な増加が避けられ、高[η]・高密度の粉末状
チップも除去できる為結果として白化のない透明性の優
れた成形品が得られ、固相重合されたポリエステルの冷
却方法として極めて有効である。Industrial Applicability The present invention relates to a cooling method for efficiently cooling with a liquid refrigerant, whereby an unnecessary increase in chip density can be avoided and powder chips of high [η] / high density can be removed. As a result, a molded product with no whitening and excellent transparency is obtained, which is extremely effective as a method for cooling solid-state polymerized polyester.
【0012】以下実施例により本発明を補説する。The present invention will be supplemented by the following examples.
【0013】[0013]
【実施例1】220℃で10時間真空下で連続固相重合
されたポリエチレンテレフタレート(固有粘度0.75
dl/g)を常温の水50kgを入れた容積100リットル
の冷却装置に20kg入れて15分間冷却した。100℃
5時間真空下で乾燥したのちチップ密度を測定したとこ
ろ、1.402g/cm3 であり、粉末状チップ量は1.
6gであった。Example 1 Polyethylene terephthalate (intrinsic viscosity 0.75) continuously solid-phase polymerized under vacuum at 220 ° C. for 10 hours.
20 kg of dl / g) was placed in a cooling device having a volume of 100 liters containing 50 kg of water at room temperature and cooled for 15 minutes. 100 ° C
When the chip density was measured after drying under vacuum for 5 hours, it was 1.402 g / cm 3 , and the powdery chip amount was 1.
It was 6 g.
【0014】[0014]
【実施例2〜6】冷媒と時間を変えた以外は実施例1と
同じ処理を行った。冷媒については表1に示した。Examples 2 to 6 The same treatments as in Example 1 were carried out except that the refrigerant and the time were changed. The refrigerants are shown in Table 1.
【0015】[0015]
【比較例】500リットル/分の流量の常温の窒素気流
にて冷却し、乾燥工程を省略した以外は実施例と同様な
方法を用いた。チップの密度は1.408g/cm3 で、
粉末状チップ量は4.8gであった。[Comparative Example] The same method as in Example was used, except that cooling was carried out in a nitrogen stream at room temperature at a flow rate of 500 liters / minute and the drying step was omitted. The density of the chip is 1.408 g / cm 3 ,
The amount of powdery chips was 4.8 g.
【0016】以上の実施例1〜6及び比較例の結果を表
1に示した。The results of Examples 1 to 6 and Comparative Example are shown in Table 1.
【0017】[0017]
【表1】 [Table 1]
Claims (1)
を液体冷媒に直接接触させて冷却せしめることからなる
固相重合されたポリエステルの冷却方法。1. A method for cooling a solid-state polymerized polyester, which comprises directly contacting a liquid refrigerant with a solid-state polymerized polyester in a high temperature state to cool the polyester.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03228541A JP3121876B2 (en) | 1991-08-15 | 1991-08-15 | Cooling method of solid phase polymerized polyester |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03228541A JP3121876B2 (en) | 1991-08-15 | 1991-08-15 | Cooling method of solid phase polymerized polyester |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0543677A true JPH0543677A (en) | 1993-02-23 |
JP3121876B2 JP3121876B2 (en) | 2001-01-09 |
Family
ID=16878010
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP03228541A Expired - Lifetime JP3121876B2 (en) | 1991-08-15 | 1991-08-15 | Cooling method of solid phase polymerized polyester |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3121876B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001233954A (en) * | 2000-02-23 | 2001-08-28 | Toyobo Co Ltd | Polyester, and blow molded article, sheet-like article, and stretched film made thereof |
JP2007119644A (en) * | 2005-10-28 | 2007-05-17 | Toyo Seikan Kaisha Ltd | Polyester resin for low-temperature molding and preform |
USRE40571E1 (en) | 1998-12-25 | 2008-11-11 | Mitsui Chemicals, Inc. | Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester |
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JP5575671B2 (en) | 2010-01-18 | 2014-08-20 | 富士フイルム株式会社 | Polyester resin polymerization method, polyester resin composition and polyester film |
JP5734569B2 (en) | 2010-01-18 | 2015-06-17 | 富士フイルム株式会社 | SOLAR CELL BACK SHEET, MANUFACTURING METHOD THEREOF, AND SOLAR CELL MODULE |
JP2011165967A (en) | 2010-02-10 | 2011-08-25 | Fujifilm Corp | Solar cell backsheet and solar cell module |
JP5575680B2 (en) | 2010-03-09 | 2014-08-20 | 富士フイルム株式会社 | Polyester resin composition and method for producing the same, polyester film, and solar cell power generation module |
JP5623938B2 (en) | 2010-03-25 | 2014-11-12 | 富士フイルム株式会社 | Solar cell backsheet |
US20120048348A1 (en) | 2010-08-26 | 2012-03-01 | Fujifilm Corporation | Solar cell protective sheet and its production method, backsheet for solar cell, and solar cell module |
KR101625420B1 (en) | 2010-11-12 | 2016-05-30 | 후지필름 가부시키가이샤 | Back sheet for solar cells and process for production thereof, and solar cell module |
JP5753110B2 (en) | 2012-02-03 | 2015-07-22 | 富士フイルム株式会社 | Back surface protection sheet for solar cell module and solar cell module |
JP6200131B2 (en) | 2012-03-28 | 2017-09-20 | 富士フイルム株式会社 | Polymer sheet, back surface protection sheet for solar cell, and solar cell module |
JP5852626B2 (en) | 2012-11-06 | 2016-02-03 | 富士フイルム株式会社 | Ketene imine compound, polyester film, back sheet for solar cell module and solar cell module |
-
1991
- 1991-08-15 JP JP03228541A patent/JP3121876B2/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
USRE40571E1 (en) | 1998-12-25 | 2008-11-11 | Mitsui Chemicals, Inc. | Catalyst for polyester production, process for producing polyester using the catalyst, polyester obtained by the process, and uses of the polyester |
JP2001233954A (en) * | 2000-02-23 | 2001-08-28 | Toyobo Co Ltd | Polyester, and blow molded article, sheet-like article, and stretched film made thereof |
JP2007119644A (en) * | 2005-10-28 | 2007-05-17 | Toyo Seikan Kaisha Ltd | Polyester resin for low-temperature molding and preform |
Also Published As
Publication number | Publication date |
---|---|
JP3121876B2 (en) | 2001-01-09 |
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