JPS63182336A - Production of heat-resistant polycarbonate - Google Patents
Production of heat-resistant polycarbonateInfo
- Publication number
- JPS63182336A JPS63182336A JP1228287A JP1228287A JPS63182336A JP S63182336 A JPS63182336 A JP S63182336A JP 1228287 A JP1228287 A JP 1228287A JP 1228287 A JP1228287 A JP 1228287A JP S63182336 A JPS63182336 A JP S63182336A
- Authority
- JP
- Japan
- Prior art keywords
- hydroxyphenyl
- bis
- phosgene
- polycarbonate
- reaction
- 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
- 239000004417 polycarbonate Substances 0.000 title claims abstract description 22
- 229920000515 polycarbonate Polymers 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical class ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 claims abstract description 32
- YWFPGFJLYRKYJZ-UHFFFAOYSA-N 9,9-bis(4-hydroxyphenyl)fluorene Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC=CC=C2C2=CC=CC=C21 YWFPGFJLYRKYJZ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 150000002896 organic halogen compounds Chemical class 0.000 claims abstract description 12
- 239000000243 solution Substances 0.000 claims abstract description 12
- 239000004094 surface-active agent Substances 0.000 claims abstract description 11
- 238000012696 Interfacial polycondensation Methods 0.000 claims abstract description 9
- 239000007864 aqueous solution Substances 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims 1
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 abstract description 5
- 238000006116 polymerization reaction Methods 0.000 abstract description 5
- 239000012670 alkaline solution Substances 0.000 abstract description 4
- HCUYBXPSSCRKRF-UHFFFAOYSA-N diphosgene Chemical compound ClC(=O)OC(Cl)(Cl)Cl HCUYBXPSSCRKRF-UHFFFAOYSA-N 0.000 abstract description 4
- 230000009477 glass transition Effects 0.000 abstract description 3
- 238000000354 decomposition reaction Methods 0.000 abstract description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 abstract 1
- 150000001875 compounds Chemical class 0.000 abstract 1
- DZLFLBLQUQXARW-UHFFFAOYSA-N tetrabutylammonium Chemical compound CCCC[N+](CCCC)(CCCC)CCCC DZLFLBLQUQXARW-UHFFFAOYSA-N 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 22
- 238000000034 method Methods 0.000 description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 230000035484 reaction time Effects 0.000 description 9
- NIHNNTQXNPWCJQ-UHFFFAOYSA-N fluorene Chemical compound C1=CC=C2CC3=CC=CC=C3C2=C1 NIHNNTQXNPWCJQ-UHFFFAOYSA-N 0.000 description 8
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- NHGXDBSUJJNIRV-UHFFFAOYSA-M tetrabutylammonium chloride Chemical compound [Cl-].CCCC[N+](CCCC)(CCCC)CCCC NHGXDBSUJJNIRV-UHFFFAOYSA-M 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 4
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 4
- 239000000539 dimer Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 150000002220 fluorenes Chemical class 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 125000004203 4-hydroxyphenyl group Chemical group [H]OC1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 238000005809 transesterification reaction Methods 0.000 description 3
- -1 3-ethyl- (4-hydroxyphenyl)fluorene Chemical compound 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- 238000002411 thermogravimetry Methods 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- RYHBNJHYFVUHQT-UHFFFAOYSA-N 1,4-Dioxane Chemical compound C1COCCO1 RYHBNJHYFVUHQT-UHFFFAOYSA-N 0.000 description 1
- KZMAWJRXKGLWGS-UHFFFAOYSA-N 2-chloro-n-[4-(4-methoxyphenyl)-1,3-thiazol-2-yl]-n-(3-methoxypropyl)acetamide Chemical compound S1C(N(C(=O)CCl)CCCOC)=NC(C=2C=CC(OC)=CC=2)=C1 KZMAWJRXKGLWGS-UHFFFAOYSA-N 0.000 description 1
- 238000012695 Interfacial polymerization Methods 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- VJGNLOIQCWLBJR-UHFFFAOYSA-M benzyl(tributyl)azanium;chloride Chemical compound [Cl-].CCCC[N+](CCCC)(CCCC)CC1=CC=CC=C1 VJGNLOIQCWLBJR-UHFFFAOYSA-M 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007033 dehydrochlorination reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- ROORDVPLFPIABK-UHFFFAOYSA-N diphenyl carbonate Chemical compound C=1C=CC=CC=1OC(=O)OC1=CC=CC=C1 ROORDVPLFPIABK-UHFFFAOYSA-N 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 210000002784 stomach Anatomy 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、耐熱性ポリカーボネートの製造法、特に、9
,9−ビス(4−ヒドロキシフェニル)フルオレン類と
ホスゲンダイマーとから東合度が高<、P、+;折率が
大きく、透明性に潰れた耐熱性ポリカーボネートを製造
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for producing heat-resistant polycarbonate, particularly 9
, 9-bis(4-hydroxyphenyl) fluorenes and phosgene dimer. The present invention relates to a method for producing a heat-resistant polycarbonate having a high degree of oxidation, a high refractive index, and a crushed transparency from ,9-bis(4-hydroxyphenyl)fluorenes and phosgene dimer.
従来の技術
ポリカーボネートは、耐衝撃性及び引張強さ等の機械的
性質が優れていることから機械部品など、また絶縁性等
の電気的性質も優れているので、電気部品等の分解に多
用されている。Conventional technology Polycarbonate is often used in mechanical parts because of its excellent mechanical properties such as impact resistance and tensile strength, and for disassembling electrical parts etc. due to its excellent electrical properties such as insulation. ing.
ポリカーボネートの製造法としては、ホスゲンυ、とエ
ステル交換法の2つの方法が知られている。There are two known methods for producing polycarbonate: phosgene υ and transesterification.
ホスゲン法は、米国特許3,548,185(1970
年)に記載されているように下記式(υに示すようにビ
スフェノールAまたは9,9−ビス(4−ヒドロキシフ
ェニル)フルオレンのナトリウムli!のアルカリ水溶
液または懸濁液に溶媒としてジクロロメタンを加え、攪
拌しながらホスゲンを吹き込む方法である。The phosgene method is described in U.S. Pat. No. 3,548,185 (1970).
Add dichloromethane as a solvent to an alkaline aqueous solution or suspension of sodium li! of bisphenol A or 9,9-bis(4-hydroxyphenyl)fluorene as shown in the following formula (υ) as described in This method involves blowing in phosgene while stirring.
エステル交換法は、下記式(2)に示すようにビスフェ
ノールAとジフェニルカーボネートを混合し、溶媒を用
いず、加熱溶融し、高温減圧下、エステル交換反応によ
り重縮合する方法である。この方法で製造したポリカー
ボネートはホスゲン法に比べ分子量分布のよいものが得
られる特徴があるが、高分子量のものを製造することは
困難である。The transesterification method is a method in which bisphenol A and diphenyl carbonate are mixed as shown in the following formula (2), heated and melted without using a solvent, and polycondensed by transesterification at high temperature and reduced pressure. The polycarbonate produced by this method has a characteristic that a product with a better molecular weight distribution can be obtained compared to the phosgene method, but it is difficult to produce a polycarbonate with a high molecular weight.
式(2)
発明が解決しようとする問題点
前記した、従来技術のホスゲン法はth性を有するホス
ゲンを用いるものであり、エステル交換状は1°・Y酷
な条件により製造するものであるので1本発明はこれら
の問題のない新規な耐熱性ポリカーボネートの!IJ
n ’J)iを提供することを目的とする。Formula (2) Problems to be Solved by the Invention The prior art phosgene method described above uses phosgene having th properties, and transesterified products are produced under harsh conditions of 1°/Y. 1. The present invention is a new heat-resistant polycarbonate that does not have these problems! I.J.
The purpose is to provide n'J)i.
問題点を解決するための1段 本発明は、111N述の問題点を解決したもので。The first step to solving the problem The present invention solves the problems mentioned in 111N.
9.9−ビス(4−ヒドロキシフェニル)フルオし/類
のアルカリ水溶液とホスゲンダイマーの有機ハロゲン化
合物溶液とを、攪拌下に界面重縮合することを特徴とす
るものである。また9、9−ビス(4−ヒドロキシフェ
ニル)フルオレン類のアルカリ水溶液とホスゲンダイマ
ーの有機ハロゲン化合物溶液との界面重縮合の際に界面
活性剤を存在させるようにしたものである。9.9-Bis(4-hydroxyphenyl) fluoride is characterized by interfacial polycondensation of an aqueous alkaline solution of 9-bis(4-hydroxyphenyl) fluoride and an organic halogen compound solution of phosgene dimer while stirring. Further, a surfactant is present during the interfacial polycondensation of an alkaline aqueous solution of 9,9-bis(4-hydroxyphenyl)fluorenes and an organic halogen compound solution of phosgene dimer.
本発明は、9.9−ビス(4−ヒドロキシフェニル)フ
ルオレン類を原料としてポリカーボネートを製造する際
に、ホスゲンと反応性に相違はあるが同一の構造を与え
、かつ液状で取扱いが容易なホスゲンダイマーを用いる
ことによって、比較的低い温度の短時間反応により高収
率で耐熱性ポリカーボネートを得る方法である。The present invention uses phosgene, which has the same structure as phosgene but has a different reactivity when producing polycarbonate using 9,9-bis(4-hydroxyphenyl)fluorenes as a raw material, and which is liquid and easy to handle. This method uses a dimer to obtain heat-resistant polycarbonate in high yield through a short reaction time at a relatively low temperature.
以下さらに本発明の内容を詳しく説明する。The contents of the present invention will be further explained in detail below.
本発明は、9.9−ビス(4−ヒドロキシフェニル)フ
ルオレン類とホスゲンダイマーとを界面重縮合させる方
法である。The present invention is a method of interfacial polycondensation of 9,9-bis(4-hydroxyphenyl)fluorenes and phosgene dimer.
本発明で用いられる9、9−ビス(4−ヒドロキシフェ
ニル)フルオレン類は下記式(3)で示されるものであ
る0例えば、9,9−ビス(4−ヒドロキシフェニル)
フルオレン、9.9−ビス(3−メチル−4−ヒドロキ
シフェニル)フルオレン、9.9−ビス(3−エチル−
4−ヒドロキシフェニル)フルオレンが挙げられ、これ
らのナトリウム、カリウムなどとのアルカリ塩も使用で
きル。The 9,9-bis(4-hydroxyphenyl)fluorenes used in the present invention are those represented by the following formula (3). For example, 9,9-bis(4-hydroxyphenyl)
Fluorene, 9.9-bis(3-methyl-4-hydroxyphenyl)fluorene, 9.9-bis(3-ethyl-
(4-hydroxyphenyl)fluorene, and their alkali salts with sodium, potassium, etc. can also be used.
(但し1式中RはH,CH3’、C2H1のいずれかを
示す、)
また1本発明に用いられるホスゲンダイマーはトリクロ
ルメチルクロルホルメートで、下記式%式%
式(4)
6区
本発明において、9,9−ビス(4−ヒドロキシフェニ
ル)フルオレン′類とホスゲンダイマーとの割合は、前
者のフルオレン類1モルに対して、後者のホスゲンダイ
マーを0.5〜3.0倍モル、好ましくは0.7〜2.
0倍モル、最も好ましくは当モル付近とすることがよく
、この範囲内では反応が良好に進行する。(However, in formula 1, R represents either H, CH3', or C2H1.) In addition, the phosgene dimer used in the present invention is trichloromethyl chloroformate, and the following formula % formula % Formula (4) Section 6 This invention In the above, the ratio of the 9,9-bis(4-hydroxyphenyl)fluorenes and the phosgene dimer is 0.5 to 3.0 times the mole of the latter phosgene dimer, preferably 0.5 to 3.0 times the mole of the former fluorene. is 0.7-2.
The amount is preferably set to 0 times the molar amount, most preferably around the same molar value, and within this range, the reaction proceeds well.
また本発明に用いられる有機ハロゲン化合物は、ホスゲ
ンダイマーを溶解するものであればよく、具体例として
はl、2−ジクロルエタン、りロロホルム、トリクロル
エタン、ジクロルメタン等が挙げられる。Further, the organic halogen compound used in the present invention may be one that dissolves phosgene dimer, and specific examples thereof include 1,2-dichloroethane, lyloloform, trichloroethane, dichloromethane, and the like.
本発明の方法によってポリカーボネートを製造するには
、まず9,9−ビス(4−ヒドロキシフエニル)フルオ
レン類を、水酸化ナトリウム。To produce polycarbonate by the method of the present invention, 9,9-bis(4-hydroxyphenyl)fluorenes are first mixed with sodium hydroxide.
水酸化カリウムなどを添加した水溶液に溶解し、アルカ
リ水溶液とする。この際にアルカリ水溶液中にホスゲン
ダイマーの溶媒に用いたような有機ハロゲン化合物を少
に添加すると、界面重縮合反応の進行が容易となるので
好ましい、一方ホスゲンダイマーは有機ハロゲン化合物
に溶解し、ホスゲンダイマー有機ハロゲン化合物溶液と
する。Dissolve in an aqueous solution containing potassium hydroxide, etc. to make an alkaline aqueous solution. At this time, it is preferable to add a small amount of an organic halogen compound, such as that used as a solvent for phosgene dimer, to the alkaline aqueous solution, as this facilitates the progress of the interfacial polycondensation reaction. Prepare a dimer organic halogen compound solution.
次いで前記の9.9−ビス(4−ヒドロキシフェニル)
フルオレン類のアルカリ水溶液にホスゲンダイマーの有
機ハロゲン化合物溶液を添加する。この場合、前者のア
ルカリ水溶液中に後者のホスゲンダイマーの溶液を少量
ずつ撹拌しながら添加し、反応させることが好ましい、
なお9.9−ビス(4−ヒドロキシフェニル)フルオレ
ン類のアルカリ水′溶液とホスゲンダイマーの溶媒とな
る有機ハロゲン化合物とを混合攪拌し、そこにホスゲン
ダイマー自身を滴下することによっても反応は+i(能
である。Then the above 9,9-bis(4-hydroxyphenyl)
An organic halogen compound solution of phosgene dimer is added to an alkaline aqueous solution of fluorenes. In this case, it is preferable to add the latter solution of phosgene dimer little by little to the former alkaline aqueous solution while stirring and react.
The reaction can also be carried out by mixing and stirring an alkaline aqueous solution of 9.9-bis(4-hydroxyphenyl)fluorenes and an organic halogen compound serving as a solvent for the phosgene dimer, and adding the phosgene dimer itself dropwise thereto. It is Noh.
反応に際して攪拌を行なわない場合には、1;層はフル
オレン類のアルカリ水溶液、下層はホスゲンダイマーの
有機ハロゲン化合物溶液の二層状態となり、接触が上層
と下層の界面のみで行われ、反応の進行が遅くなる。When stirring is not performed during the reaction, 1; the layer is an aqueous alkaline solution of fluorenes, and the lower layer is a solution of an organic halogen compound of phosgene dimer. Contact occurs only at the interface between the upper layer and the lower layer, and the reaction progresses. is delayed.
本発明は1尾に混り合わない2つの溶媒に七ツマー成分
を溶解し界面で用台させる界面重縮合反応であるので、
反応系に界面活性剤を乳化しない程度のfl)を添加す
ると、Wl拌によって界面が拡がり反応が進むので界面
活性剤を夕晴添加することは反応効率をhげるうえで望
ましい。Since the present invention is an interfacial polycondensation reaction in which the heptamer component is dissolved in two solvents that are immiscible and used at the interface,
If fl) is added to the reaction system to the extent that it does not emulsify the surfactant, the interface will expand due to Wl stirring and the reaction will proceed, so it is desirable to add the surfactant in a small amount in order to increase the reaction efficiency.
界面活性剤としては特に制約はないが1反応に関tしな
いことが望ましく、一般的にはカチオン系を用いること
がよい0例えばテトラブチルアンモニウムクロリド、ト
リブチルベンジルアンモニウムクロリド等の使用が好ま
しい、界面活性剤の添加?はその種類にもよるが、水溶
液中に5%以F、好ましくは1%以下である。界面活性
剤の添加は、得られるポリカーボネートの重合度にはほ
とんど#響しない。There are no particular restrictions on the surfactant, but it is preferable that it not be involved in one reaction, and it is generally preferable to use a cationic type. For example, it is preferable to use tetrabutylammonium chloride, tributylbenzylammonium chloride, etc. Addition of agent? Although it depends on the type, the F content in the aqueous solution is 5% or more, preferably 1% or less. The addition of surfactants has little effect on the degree of polymerization of the polycarbonate obtained.
反応温度はθ〜30℃、好ましくは20〜30℃1反応
時間は滴下時間を含めて約20分〜80時間程度で反応
が終了する0反応時間が長くなると得られるポリカーボ
ネートの重合度が低下する傾向があるため、反応時間と
してはあまり長時間にならないようにすることがψしい
。The reaction temperature is θ to 30°C, preferably 20 to 30°C. 1. The reaction time is about 20 minutes to 80 hours, including the dropping time. The longer the reaction time, the lower the degree of polymerization of the resulting polycarbonate. Therefore, it is recommended that the reaction time not be too long.
以上のようにして製造することによりポリカーボネート
が高収率で得られ、その物性はガラス転移温度260℃
1分対温度465℃と高い耐熱性を示し、また透明性は
90%以上、屈折率は1.7近い大きな値を示し、かつ
高重合度のものである。By manufacturing as described above, polycarbonate can be obtained in high yield, and its physical properties include a glass transition temperature of 260°C.
It exhibits high heat resistance with a temperature of 465° C. for 1 minute, transparency of 90% or more, a refractive index of nearly 1.7, and a high degree of polymerization.
以下実施例により、さらに本発明の詳細な説明する。The present invention will be further explained in detail below with reference to Examples.
実施例
実施例1
9.9−ビス(4−ヒドロキシフェニル)フルオレン3
.5g (0,01モル)を水酸化ナトリウム2.28
g (0,057モル)、界面活性剤としてテトラブ
チルアンモニウムクロリド0.00175gとともに木
6〇−に溶解し、これに1.2−ジクロルエタン60−
を加えた。Examples Example 1 9.9-bis(4-hydroxyphenyl)fluorene 3
.. 5g (0.01 mol) of sodium hydroxide 2.28
g (0,057 mol), dissolved in wood 60- with 0.00175 g of tetrabutylammonium chloride as a surfactant, and 1,2-dichloroethane 60-
added.
準備した]−述の混合液に、l、2−ジクロルエタン1
5aQにホステンダイマー(トリクロルメチルクロルホ
ルメート)1.2m1(0,01モル)を溶解した溶液
を21”0の温度で攪拌しながら7分間かけて滴ドし、
さらに15分間攪拌して反応を行なった9反応絆了後1
.2−ジクロルエタン層を分離し、濃縮後へキサン中に
注いだ、析出物を濾過し、乾燥した後、クロロホルムに
溶解してからヘキサン中に再沈した。[prepared] - Add 1 1,2-dichloroethane to the above-mentioned mixture.
A solution of 1.2 ml (0.01 mol) of hosten dimer (trichloromethyl chloroformate) dissolved in 5aQ was added dropwise over 7 minutes with stirring at a temperature of 21"0.
The reaction was carried out by stirring for an additional 15 minutes.9 After the reaction was completed, 1
.. The 2-dichloroethane layer was separated, concentrated, and then poured into hexane. The precipitate was filtered, dried, dissolved in chloroform, and reprecipitated into hexane.
+1f度析出物を濾過し、乾燥してポリマーを得た。The +1f precipitate was filtered and dried to obtain a polymer.
反応条件及び結果を表1に示した。The reaction conditions and results are shown in Table 1.
表1中の略号は次のものを示す。The abbreviations in Table 1 indicate the following.
)IPF・・・9,9−ビス(4−ヒドロキシフェニル
)フルオレン
TBG・・・テトラブチルアンモニウムクロリド(界部
活性剤)
DCE・・・l、2−ジクロ、ルエタン、↑CMCF・
・・トリクロルメチルクロルホルメート(ホスゲンダイ
マー)
Mn、 14w・・・ゲルパーミエーシ電ンクロマトグ
ラフィー(GPC)による数平均分子量、重驕平均分子
暖
収率・・・固形分を測定
熱重量分析(TG)は、熱重量減少5%をもって示した
。) IPF...9,9-bis(4-hydroxyphenyl)fluoreneTBG...tetrabutylammonium chloride (surfactant) DCE...l, 2-dichloro, luethane, ↑CMCF・
... Trichloromethyl chloroformate (phosgene dimer) Mn, 14w ... Number average molecular weight by gel permeability electron chromatography (GPC), weight average molecular weight yield ... Measure solid content Thermogravimetric analysis (TG) showed a thermogravimetric loss of 5%.
実施例2〜14
反応条件を表1に示すように変えた以外は実施例1と同
様にして反応を行った。その結果を表1に示す。Examples 2 to 14 Reactions were carried out in the same manner as in Example 1 except that the reaction conditions were changed as shown in Table 1. The results are shown in Table 1.
なお実施例12はHPF 、 H2O、NaOHを50
℃に加熱した後冷却して用いた。In addition, in Example 12, HPF, H2O, and NaOH were mixed at 50%
It was heated to ℃ and then cooled before use.
表1から判るように実施例7は滴下時間35分。As can be seen from Table 1, in Example 7, the dropping time was 35 minutes.
滴下後の反応時間が70分の場合Mw/Mnは4.19
であり、実施例8は滴下時間80分、滴下後の反応時間
120分ノ場合H9I/ ii”nt* 1 、 Hト
t 4J、反応時nnb<r。When the reaction time after dropping is 70 minutes, Mw/Mn is 4.19
In Example 8, when the dropping time was 80 minutes and the reaction time after dropping was 120 minutes, H9I/ii"nt*1, Htot4J, and nnb<r during the reaction.
くなるとポリカーボネートの屯合度が低くなる傾向を示
す。When the temperature decreases, the degree of loading of the polycarbonate tends to decrease.
実施例5により得られたポリマーの分解温度465℃、
ガラス転移温度260℃、全光線透過−4t91.5%
、黄色度 1.7%、屈折率!、67であった。The decomposition temperature of the polymer obtained in Example 5 was 465°C,
Glass transition temperature 260℃, total light transmission -4t91.5%
, yellowness 1.7%, refractive index! , 67.
実施例15
界面活性剤を使用しない以外は実施例5と同様に反応を
行なったところ実施例5とはC同様の結果が得られた。Example 15 The reaction was carried out in the same manner as in Example 5 except that no surfactant was used, and results similar to Example 5 and C were obtained.
°表1に示した実施例1〜7は、ホスゲンダイマー溶液
の滴下時間と滴下後の反応時間の分子量及び分子−1誹
分布に及ぼす影響をみたものである。Examples 1 to 7 shown in Table 1 examine the effects of the dropwise addition time of the phosgene dimer solution and the reaction time after the dropwise addition on the molecular weight and molecule-1 distribution.
これらの中では、分子4)分布は実施例3が良好で、分
子・4」に関しては実施例5が最もよく、フィルム成形
についても良好であった。Among these, Example 3 had the best molecule 4) distribution, and Example 5 had the best molecule 4) distribution, and was also good in film forming.
反応の際の滴下時間を30分と一定にした場合の滴ド後
の反応時間のY#響は、実施例5,8.12゜13より
判断できるが1反応時間を60分を越えて、長時間とす
ることは、あまりメリットはなく、かえって分散度をま
ず傾向があることが判る。また、実施例8.9によりホ
スゲンダイマーの使用;1:の#胃、実施例9.lOに
よりアルカリ使用駿の#響が判る。The Y# effect of the reaction time after dropping when the dropping time during the reaction is kept constant at 30 minutes can be judged from Example 5, 8.12゜13, but if one reaction time exceeds 60 minutes, It can be seen that there is not much merit in using a long time, and on the contrary, it tends to reduce the degree of dispersion. Also, use of phosgene dimer according to Example 8.9; 1: #stomach, Example 9. The #echo of alkali usage can be determined by lO.
また実施例11は界面活性剤を多量に用いた場合で、得
、られたポリカーボネートの分子量分布が単分散のもの
であった。実施例14はジクロロエタンの使用脣を多量
にした場合であるが、これも特別な影πは認められなか
った。Further, in Example 11, a large amount of surfactant was used, and the molecular weight distribution of the obtained polycarbonate was monodisperse. In Example 14, a large amount of dichloroethane was used, but no special influence π was observed in this case either.
比較例
界面重合法でなく、均−溶液重合法によりポリカーボネ
ートの製造を行なった。Comparative Example A polycarbonate was produced by a homogeneous solution polymerization method instead of an interfacial polymerization method.
9.9−ビス(4−ヒドロキシフェニル)フルオレンと
ホスゲンダイヤ−を原料とし、溶剤としては、テトラヒ
ドロフラン(THF) 、ジオキサン。9.9-bis(4-hydroxyphenyl)fluorene and phosgene diamond are used as raw materials, and the solvents are tetrahydrofuran (THF) and dioxane.
ピリジン、クロロホルム、ベンゼン、トルエンを用い、
脱塩酸剤としてトリエチルアミン、ピリジンの塩基を用
いた場合と用いずに反応を行なった結果、数平均分子量
で約toooo程度の重合物が多かった。なかには数モ
均分子* 30000程度の重合物も得られたがフィル
ム成形はできなかった。Using pyridine, chloroform, benzene, and toluene,
As a result of conducting the reaction with and without using a base such as triethylamine or pyridine as a dehydrochlorination agent, there were many polymers having a number average molecular weight of about too much. Although some polymers with a molecular weight of about 30,000 were obtained, they could not be formed into films.
また、収率はいずれも約50%前後であり、満足しうる
ちのではなかった。Moreover, the yields were all around 50%, which was not satisfactory.
(以下余白)
発明の効果
本発明によれば、ホスゲンダイマーを使用することによ
り1反応に際しての安全性を向上するとともに液体であ
るので取扱いを容易にした。また穏和な条件で反応させ
ることができ、重合度が高く、耐熱性、透明性に優れ屈
折率の大きいポリカーボネートを収率よ<111ること
ができる。(The following is a blank space) Effects of the Invention According to the present invention, the use of phosgene dimer improves the safety in one reaction, and since it is a liquid, it is easy to handle. Further, the reaction can be carried out under mild conditions, and a polycarbonate having a high degree of polymerization, excellent heat resistance and transparency, and a large refractive index can be produced in a yield of <111.
本発明品は融点が高く切削却下によっても溶融すること
がないのでプラスチックレンズや各種成形品に適してい
る。また焼付温度にも耐えることができるので11(の
外板などにも利用可能であり。The product of the present invention has a high melting point and does not melt even when cut, so it is suitable for plastic lenses and various molded products. It can also withstand baking temperatures, so it can be used for exterior panels of 11.
従来使用困難であった分野に使用できる画期的なもので
ある。This is an epoch-making product that can be used in fields where it was previously difficult to use.
Claims (2)
ロキシフェニル)フルオレン類のアルカリ水溶液と、 ▲数式、化学式、表等があります▼(RはH、CH_3
、C_2H_5のいずれかである。) ホスゲンダイマーの有機ハロゲン化合物溶液とを、攪拌
下に界面重縮合することを特徴とする耐熱性ポリカーボ
ネートの製造法。(1) An alkaline aqueous solution of 9,9-bis(4-hydroxyphenyl)fluorenes represented by the general formula below, ▲There are mathematical formulas, chemical formulas, tables, etc.▼ (R is H, CH_3
, C_2H_5. ) A method for producing a heat-resistant polycarbonate, which comprises interfacial polycondensation of phosgene dimer and an organic halogen compound solution under stirring.
レン類のアルカリ水溶液と、ホスゲンダイマーの有機ハ
ロゲン化合物溶液との界面重縮合の際に、界面活性剤を
存在させる特許請求の範囲第1項記載の耐熱性ポリカー
ボネートの製造法。(2) Claim 1 in which a surfactant is present during the interfacial polycondensation of an alkaline aqueous solution of 9,9-bis(4-hydroxyphenyl)fluorenes and an organic halogen compound solution of phosgene dimer. Method for producing the heat-resistant polycarbonate described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1228287A JPS63182336A (en) | 1987-01-23 | 1987-01-23 | Production of heat-resistant polycarbonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1228287A JPS63182336A (en) | 1987-01-23 | 1987-01-23 | Production of heat-resistant polycarbonate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63182336A true JPS63182336A (en) | 1988-07-27 |
JPH0476373B2 JPH0476373B2 (en) | 1992-12-03 |
Family
ID=11801004
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1228287A Granted JPS63182336A (en) | 1987-01-23 | 1987-01-23 | Production of heat-resistant polycarbonate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63182336A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0591962A2 (en) * | 1992-10-09 | 1994-04-13 | Idemitsu Petrochemical Co., Ltd. | Polycarbonate copolymer and process for producing the same |
NL9401529A (en) * | 1993-09-22 | 1995-04-18 | Bayer Ag | Application of special polycarbonates for the manufacture of optical objects. |
US5434235A (en) * | 1992-10-14 | 1995-07-18 | Daicel Chemical Industries, Ltd. | Process for the preparation of (co)polycarbonate |
WO1995019380A1 (en) * | 1994-01-12 | 1995-07-20 | The Dow Chemical Company | Process for preparing polycarbonate from a bisphenoxy fluorene |
US5475786A (en) * | 1992-11-02 | 1995-12-12 | The Furukawa Electric Co., Ltd. | Aromatic polycarbonate copolymer, a process for producing the same, and a plastic optical waveguide using the same |
US5486577A (en) * | 1995-03-21 | 1996-01-23 | The Dow Chemical Company | Blends of diaryl fluorene carbonate polymers with bisphenol A carbonate polymers |
EP0708129A1 (en) | 1991-05-08 | 1996-04-24 | Daicel Chemical Industries, Ltd. | Process for producing polycarbonate |
US5516877A (en) * | 1994-08-16 | 1996-05-14 | The Dow Chemical Company | Crosslinkable carbonate polymers of dihydroxyaryl fluorene |
US5556904A (en) * | 1992-11-02 | 1996-09-17 | The Furukawa Electric Co. Ltd | Aromatic polycarbonate copolymer, a process for producing the same, and a plastic optical waveguide using the same |
-
1987
- 1987-01-23 JP JP1228287A patent/JPS63182336A/en active Granted
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0708129A1 (en) | 1991-05-08 | 1996-04-24 | Daicel Chemical Industries, Ltd. | Process for producing polycarbonate |
US5470939A (en) * | 1992-10-09 | 1995-11-28 | Idemitsu Petrochemical Co., Ltd. | Polycarbonate copolymer |
US5391693A (en) * | 1992-10-09 | 1995-02-21 | Idemitsu Petrochemical Co., Ltd. | Process for producing a polycarbonate copolymer |
EP0591962A2 (en) * | 1992-10-09 | 1994-04-13 | Idemitsu Petrochemical Co., Ltd. | Polycarbonate copolymer and process for producing the same |
EP0591962A3 (en) * | 1992-10-09 | 1994-09-21 | Idemitsu Petrochemical Co | Polycarbonate copolymer and process for producing the same |
US5434235A (en) * | 1992-10-14 | 1995-07-18 | Daicel Chemical Industries, Ltd. | Process for the preparation of (co)polycarbonate |
US5475786A (en) * | 1992-11-02 | 1995-12-12 | The Furukawa Electric Co., Ltd. | Aromatic polycarbonate copolymer, a process for producing the same, and a plastic optical waveguide using the same |
US5556904A (en) * | 1992-11-02 | 1996-09-17 | The Furukawa Electric Co. Ltd | Aromatic polycarbonate copolymer, a process for producing the same, and a plastic optical waveguide using the same |
NL9401529A (en) * | 1993-09-22 | 1995-04-18 | Bayer Ag | Application of special polycarbonates for the manufacture of optical objects. |
BE1009103A5 (en) * | 1993-09-22 | 1996-11-05 | Bayer Ag | Polycarbonates special and use for preparing optical articles. |
WO1995019380A1 (en) * | 1994-01-12 | 1995-07-20 | The Dow Chemical Company | Process for preparing polycarbonate from a bisphenoxy fluorene |
US5516877A (en) * | 1994-08-16 | 1996-05-14 | The Dow Chemical Company | Crosslinkable carbonate polymers of dihydroxyaryl fluorene |
US5486577A (en) * | 1995-03-21 | 1996-01-23 | The Dow Chemical Company | Blends of diaryl fluorene carbonate polymers with bisphenol A carbonate polymers |
Also Published As
Publication number | Publication date |
---|---|
JPH0476373B2 (en) | 1992-12-03 |
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