JPH10324740A - Production of polybutylene terephthalate - Google Patents

Production of polybutylene terephthalate

Info

Publication number
JPH10324740A
JPH10324740A JP15052397A JP15052397A JPH10324740A JP H10324740 A JPH10324740 A JP H10324740A JP 15052397 A JP15052397 A JP 15052397A JP 15052397 A JP15052397 A JP 15052397A JP H10324740 A JPH10324740 A JP H10324740A
Authority
JP
Japan
Prior art keywords
butanediol
polybutylene terephthalate
sodium acetate
terephthalic acid
mmhg
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
Application number
JP15052397A
Other languages
Japanese (ja)
Inventor
Yoshinori Komatsu
善徳 小松
Kouichi Matano
孝一 又野
Sadakatsu Suzuki
貞勝 鈴木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tonen Chemical Corp
Original Assignee
Tonen Sekiyu Kagaku KK
Tonen Chemical Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tonen Sekiyu Kagaku KK, Tonen Chemical Corp filed Critical Tonen Sekiyu Kagaku KK
Priority to JP15052397A priority Critical patent/JPH10324740A/en
Publication of JPH10324740A publication Critical patent/JPH10324740A/en
Pending legal-status Critical Current

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  • Polyesters Or Polycarbonates (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the by-production of tetrahydrofuran and obtain the subject polymer improved in whiteness by polycondensing terephthalic acid with 1,4-butanediol in the presence of anhydrous sodium acetate. SOLUTION: This method for producing polybutylene terephthalate comprises esterifying (oligomerizing) (A) terephthalic acid with (B) 1,4-butanediol in the presence of anhydrous sodium acetate in an amount of preferably 0.1-50 ppm, more preferably 1-10 ppm, based on the weight of the component B at 200-250 deg.C at the atmospheric pressure to 100 mmHg for 1-5 hr and subsequently polymerizing the product at a vacuum of 0.1-10 mmHg for 1-5 hr. Known catalysts are preferably used in the esterification reaction and in the subsequent polymerization reaction. The catalysts are preferably a titanium compound, a tin compound, etc.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、テレフタル酸と1,4
‐ブタンジオールからポリブチレンテレフタレートを製
造する方法に関する。
The present invention relates to terephthalic acid and 1,4
A process for producing polybutylene terephthalate from butanediol.

【0002】[0002]

【従来の技術】テレフタル酸ジメチルと1,4‐ブタン
ジオールとのエステル交換反応により、あるいはテレフ
タル酸と1,4‐ブタンジオールとのエステル化反応に
よりポリブチレンテレフタレートを製造することは公知
である。その際に、100℃未満の低温の1,4‐ブタ
ンジオールを反応缶へ仕込むと反応缶の温度変化が大き
いので長期運転において歪が生じる。従って、1,4‐
ブタンジオールを100〜200℃に予め加温すること
が必要とされていた。ところが1,4‐ブタンジオール
は熱的に不安定であり、加熱下で環化してテトラヒドロ
フランと水に転化するという問題があったところ、加熱
される1,4‐ブタンジオールにアルカリ金属化合物を
添加存在させてテトラヒドロフランの生成を抑制すると
いう1,4‐ブタンジオールの熱安定化法が知られてい
る(特公昭55−33696号公報)。
2. Description of the Related Art It is known to produce polybutylene terephthalate by a transesterification reaction of dimethyl terephthalate with 1,4-butanediol or by an esterification reaction of terephthalic acid with 1,4-butanediol. At that time, if 1,4-butanediol having a low temperature of less than 100 ° C. is charged into the reaction vessel, the temperature of the reaction vessel changes greatly, so that distortion occurs in long-term operation. Therefore, 1,4-
It was necessary to preheat butanediol to 100-200 ° C. However, 1,4-butanediol was thermally unstable, and had the problem of cyclizing under heating and converting it to tetrahydrofuran and water. A thermal stabilization method of 1,4-butanediol, which suppresses the formation of tetrahydrofuran by being present, is known (Japanese Patent Publication No. 55-33696).

【0003】そこでは、アルカリ金属化合物として水酸
化アルカリ(土類)金属、酢酸アルカリ(土類)金属
塩、ヘキサアンミン白金塩が挙げられている。発明の詳
細な説明において、酢酸アルカリ(土類)金属塩として
総てのアルカリ金属およびアルカリ土類金属の塩が列挙
されているが、実施例においては含水塩のみ(酢酸リチ
ウム二水塩および酢酸カルシウム一水塩)が用いられて
いる。
In this case, alkali (earth) metal hydroxides, alkali (earth) metal acetates, and hexaammine platinum salts are mentioned as alkali metal compounds. In the detailed description of the invention, all alkali metal and alkaline earth metal salts are listed as alkali (earth) metal acetate salts, but in the examples only hydrated salts (lithium acetate dihydrate and acetic acid) Calcium monohydrate) is used.

【0004】1,4‐ブタンジオールの有機酸エステル
を、陽イオン交換樹脂触媒の存在下で加水分解すること
により得た1,4‐ブタンジオールを用いて、エステル
化反応によりポリブチレンテレフタレートを製造する方
法において、1,4‐ブタンジオールにアルカリ(土
類)金属の水酸化物を添加することが知られている(特
開平7−10981号公報)。
[0004] Polybutylene terephthalate is produced by an esterification reaction using 1,4-butanediol obtained by hydrolyzing an organic acid ester of 1,4-butanediol in the presence of a cation exchange resin catalyst. In this method, it is known to add an alkali (earth) metal hydroxide to 1,4-butanediol (JP-A-7-10981).

【0005】[0005]

【発明が解決しようとする課題】本発明は、テレフタル
酸と1,4‐ブタンジオールを重合反応させてポリブチ
レンテレフタレートを製造する方法において、テトラヒ
ドロフランの副生を抑制し、かつ生成されたポリブチレ
ンテレフタレートがより白色であるところの方法を提供
することを目的とする。
SUMMARY OF THE INVENTION The present invention relates to a method for producing polybutylene terephthalate by polymerizing terephthalic acid and 1,4-butanediol, suppressing the by-product of tetrahydrofuran and producing polybutylene terephthalate. It is an object to provide a method where terephthalate is more white.

【0006】[0006]

【課題を解決するための手段】本発明は、テレフタル酸
と1,4‐ブタンジオールを重合反応させてポリブチレ
ンテレフタレートを製造する方法において、酢酸ナトリ
ウム無水塩の存在下に重合反応を行うことを特徴とする
方法である。
SUMMARY OF THE INVENTION The present invention provides a method for producing polybutylene terephthalate by polymerizing terephthalic acid and 1,4-butanediol, wherein the polymerization reaction is carried out in the presence of anhydrous sodium acetate. Characteristic method.

【0007】本発明において、酢酸ナトリウムの無水塩
を用いることが必須である。代りに水酸化アルカリ(土
類)金属を用いると、効果が小さい。特に、水酸化アル
カリ(土類)金属と1,4‐ブタンジオール(又はテレ
フタル酸)とを予め混合して、後に重合反応に用いる場
合には、予め混合した後の保存中に水酸化アルカリ(土
類)金属が空気中の二酸化炭素と反応してたとえば炭酸
ナトリウムに転化すると、効果が著しく損われることが
判った。また代りに、酢酸ナトリウムの含水塩を用いる
と、得られるポリブチレンテレフタレートの重合度が比
較的小さいことが判った。本発明に従って酢酸ナトリウ
ムの無水塩を用いることによって、ポリブチレンテレフ
タレート(PBT)の重合反応中にテトラヒドロフラン
(THF)の副生を顕著に抑制でき、かつ得られたPB
Tがより白色である。
In the present invention, it is essential to use an anhydrous salt of sodium acetate. If an alkali (earth) metal hydroxide is used instead, the effect is small. In particular, when an alkali (earth) metal hydroxide and 1,4-butanediol (or terephthalic acid) are previously mixed and used for a polymerization reaction later, the alkali hydroxide ( It has been found that when the (earth) metal reacts with the carbon dioxide in the air to convert it to, for example, sodium carbonate, the effect is significantly impaired. It was also found that when a hydrate of sodium acetate was used instead, the degree of polymerization of the resulting polybutylene terephthalate was relatively small. By using an anhydrous salt of sodium acetate according to the present invention, by-product of tetrahydrofuran (THF) can be remarkably suppressed during the polymerization reaction of polybutylene terephthalate (PBT), and the obtained PB
T is more white.

【0008】好ましくは、出発の1,4‐ブタンジオー
ルの重量に対して0.1〜50ppm、より好ましくは
1〜10ppmの量の酢酸ナトリウム無水塩を重合反応
系に仕込む。この量が下限より少ないと、発明の効果が
不十分であり、一方、上限より多くしても発明の効果の
格別の増大はなく、しかもPBTが着色する傾向があ
る。
Preferably, anhydrous sodium acetate in an amount of 0.1 to 50 ppm, more preferably 1 to 10 ppm, based on the weight of the starting 1,4-butanediol is charged to the polymerization reaction system. If the amount is less than the lower limit, the effect of the invention is insufficient, while if it is more than the upper limit, the effect of the invention is not particularly increased and the PBT tends to be colored.

【0009】重合反応自体は、公知法に従って行うこと
ができ、たとえば200〜250℃の温度、常圧〜10
0mmHgでエステル化反応(オリゴマー化)を1〜5
時間行い、次に0.1〜10mmHg(たとえば1mm
Hg)へ減圧して1〜5時間更に重合を進行させて、目
的のPBTを得る。
The polymerization reaction itself can be carried out according to a known method, for example, at a temperature of 200 to 250 ° C. and a normal pressure to 10
Esterification reaction (oligomerization) at 0 mmHg
Time, then 0.1 to 10 mmHg (eg 1 mm
The pressure is reduced to Hg), and the polymerization is further advanced for 1 to 5 hours to obtain the desired PBT.

【0010】エステル化反応及び続く重合段階におい
て、自体公知の触媒を用いることが好ましい。触媒は、
たとえばチタン化合物、スズ化合物である。
In the esterification reaction and the subsequent polymerization step, it is preferable to use a catalyst known per se. The catalyst is
For example, a titanium compound and a tin compound.

【0011】以下で実施例により本発明を更に説明す
る。
Hereinafter, the present invention will be further described by way of examples.

【0012】[0012]

【実施例】冷却管、受器及び攪拌装置を装着した容量5
00mlのガラス製フラスコにテレフタル酸粉末16
6.2g(1.0mol)、1,4‐ブタンジオール1
80g(2.0mol)、触媒としてテトラ‐n‐ブチ
ルチタネート0.1g、及び表1に示す量(1,4‐ブ
タンジオールに対する重量ppm)の酢酸ナトリウム無
水塩を仕込んだ。系内を窒素置換後、200rpmで攪
拌しながら210℃まで約25分間で昇温し、常圧で
3.5時間エステル化反応を行った。反応中に副生した
THF、水及び留出した1,4‐ブタンジオールは冷却
管で冷却され、受器に貯められ、エステル化反応終了時
に回収された。
EXAMPLE Capacity 5 equipped with a cooling pipe, a receiver and a stirring device
Terephthalic acid powder 16 in a 00 ml glass flask
6.2 g (1.0 mol), 1,4-butanediol 1
80 g (2.0 mol), 0.1 g of tetra-n-butyl titanate as a catalyst, and anhydrous sodium acetate in the amount shown in Table 1 (weight ppm based on 1,4-butanediol) were charged. After replacing the inside of the system with nitrogen, the temperature was raised to 210 ° C. in about 25 minutes while stirring at 200 rpm, and the esterification reaction was carried out at normal pressure for 3.5 hours. THF, water, and 1,4-butanediol distilled off during the reaction were cooled in a cooling tube, stored in a receiver, and collected at the end of the esterification reaction.

【0013】その後、テトラ‐n‐ブチルチタネート
0.1gを追加し、系内を1mmHg以下の減圧とした
後、温度を230℃まで上昇し、重合反応を進行させ
た。反応は、副生した水や1,4‐ブタンジオールを留
出させながら行い、温度が230℃となってから約2時
間で終了した。
Thereafter, 0.1 g of tetra-n-butyl titanate was added, and the pressure inside the system was reduced to 1 mmHg or less, and then the temperature was raised to 230 ° C. to allow the polymerization reaction to proceed. The reaction was carried out while distilling off by-produced water and 1,4-butanediol, and was completed in about 2 hours after the temperature reached 230 ° C.

【0014】THF副生率および得たPBTの色を表1
に示す。
Table 1 shows the by-product THF ratio and the color of the obtained PBT.
Shown in

【0015】THF副生率は以下の式で求めた。The THF by-product rate was determined by the following equation.

【0016】THF副生率=副生したTHFのモル数/
使用した1,4‐ブタンジオールのモル数
THF by-product rate = mol number of by-produced THF /
Number of moles of 1,4-butanediol used

【0017】[0017]

【表1】 [Table 1]

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 テレフタル酸と1,4‐ブタンジオール
を重合反応させてポリブチレンテレフタレートを製造す
る方法において、酢酸ナトリウム無水塩の存在下に重合
反応を行うことを特徴とする方法。
1. A method for producing polybutylene terephthalate by polymerizing terephthalic acid and 1,4-butanediol, wherein the polymerization reaction is carried out in the presence of anhydrous sodium acetate.
【請求項2】 出発1,4‐ブタンジオールの重量に対
して1〜10ppmの量の酢酸ナトリウム無水塩を重合
反応系に仕込む請求項1の方法。
2. The process of claim 1 wherein sodium acetate anhydrous in an amount of 1 to 10 ppm based on the weight of the starting 1,4-butanediol is charged to the polymerization reaction system.
JP15052397A 1997-05-23 1997-05-23 Production of polybutylene terephthalate Pending JPH10324740A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15052397A JPH10324740A (en) 1997-05-23 1997-05-23 Production of polybutylene terephthalate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15052397A JPH10324740A (en) 1997-05-23 1997-05-23 Production of polybutylene terephthalate

Publications (1)

Publication Number Publication Date
JPH10324740A true JPH10324740A (en) 1998-12-08

Family

ID=15498735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15052397A Pending JPH10324740A (en) 1997-05-23 1997-05-23 Production of polybutylene terephthalate

Country Status (1)

Country Link
JP (1) JPH10324740A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001060888A1 (en) * 2000-02-17 2001-08-23 Shell Internationale Research Maatschappij B.V. Zero-heel polyester process
JP2015028141A (en) * 2013-07-02 2015-02-12 三菱化学株式会社 Method for producing polybutylene terephthalate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001060888A1 (en) * 2000-02-17 2001-08-23 Shell Internationale Research Maatschappij B.V. Zero-heel polyester process
JP2015028141A (en) * 2013-07-02 2015-02-12 三菱化学株式会社 Method for producing polybutylene terephthalate

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