JPH04504546A - Molded objects from aromatic polyester - Google Patents
Molded objects from aromatic polyesterInfo
- Publication number
- JPH04504546A JPH04504546A JP3503625A JP50362591A JPH04504546A JP H04504546 A JPH04504546 A JP H04504546A JP 3503625 A JP3503625 A JP 3503625A JP 50362591 A JP50362591 A JP 50362591A JP H04504546 A JPH04504546 A JP H04504546A
- Authority
- JP
- Japan
- Prior art keywords
- sintered body
- polyester
- pressure
- item
- temperature
- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
- C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
- C08L67/03—Polyesters derived from dicarboxylic acids and dihydroxy compounds the dicarboxylic acids and dihydroxy compounds having the carboxyl- and the hydroxy groups directly linked to aromatic rings
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- 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
- B29B13/007—Treatment of sinter powders
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/003—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor characterised by the choice of material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C43/00—Compression moulding, i.e. applying external pressure to flow the moulding material; Apparatus therefor
- B29C43/006—Pressing and sintering powders, granules or fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C37/00—Component parts, details, accessories or auxiliary operations, not covered by group B29C33/00 or B29C35/00
- B29C2037/90—Measuring, controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 芳香族ポリエステルからの成形体 技術分野 本発明は、ジフェノールとフタル酸ハロゲニドから製造した、一種又は一種以上 の芳香族ポリエステルから成る成形体に関する。[Detailed description of the invention] Molded objects from aromatic polyester Technical field The present invention provides one or more phthalic acid halides produced from diphenols and phthalic acid halides. The present invention relates to a molded article made of aromatic polyester.
技術の現状 この種の成形体は、たとえば、ヨーロッパ特許明細書簡64971及び6497 2号により、ポリエステル溶液からの注型によって製造したフィルムの形態で、 公知である。しかしヨーロッパ特許第64972号記載のポリエステルは1,1 −ビス(4−ヒドロキシフェニル)−1−フェニルエタンに基づくものであり、 これは330〜400℃の高い加工温度を必要とするために押出し又は射出成形 によって加工することが困難であることが認められており、一方、ヨーロッパ特 許第64971号により公知の9.9−ビス(4−ヒドロキシフェニル)フルオ レンに基づくポリエステルは一般に融解範囲を有しておらず、約400℃の高い 温度において熱分解を開始することが知られている。Current state of technology Moldings of this type are known, for example, from European Patent Specification Letters 64971 and 6497. No. 2, in the form of a film produced by casting from a polyester solution, It is publicly known. However, the polyester described in European Patent No. 64972 is 1,1 - based on bis(4-hydroxyphenyl)-1-phenylethane, This requires extrusion or injection molding as it requires high processing temperatures of 330-400℃. It is recognized that it is difficult to process by 9,9-bis(4-hydroxyphenyl)fluoro, known from Japanese Patent Application No. 64971. Ren-based polyesters generally have no melting range, with temperatures as high as about 400°C. It is known that thermal decomposition begins at a certain temperature.
発明の説明 本発明は、フィルムとは対照的に、広(任意の形態をとることができる、冒頭に 記した種類の成形体を提供することを課題とする。Description of the invention The present invention, as opposed to a film, is a wide (can take any form, The object is to provide a molded article of the type described above.
このような課題は、DSCによって測定するときに220〜400℃の範囲の一 つ又は一つ以上のガラス転移点及び4ON/mm”よりも高く、好ましくは6O N/mm”よりも高いDIN53455による引張強さを有する焼結体から成る ことを特徴とする本発明による成形体により解決することができる。この場合に 使用する芳香族ポリエステルは、一つ又は一つ以上の式 のジフェノールに基づくものであることが有利であるが、ここでRは二価の、少 な(とも一つの芳香族又は脂環式の環を含有する炭化水素基である。Such a problem arises when measuring by DSC at a temperature in the range of 220 to 400℃. one or more glass transition points and higher than 4ON/mm”, preferably 6O Consisting of a sintered body with a tensile strength according to DIN 53455 higher than "N/mm" This problem can be solved by the molded article according to the present invention, which is characterized by the following. In this case The aromatic polyester used may have one or more formulas is advantageously based on a diphenol of (Both are hydrocarbon groups containing one aromatic or alicyclic ring.
同一の種類及び品買の出発材料を用いて、本発明による焼結体は、注型フィルム と比較して、四塩化炭素のようなある種の溶剤に対する高い耐性を有しているこ とが認められている。このような事実及び本明細書中でさらに詳細に記述するそ の他の事実から、焼結体を形成するポリエステルは、ある程度の架橋を有してい るものと結論することができる。Using starting materials of the same type and quality, the sintered body according to the invention can be made into a cast film. It has a high resistance to certain solvents such as carbon tetrachloride compared to It is recognized that These facts and those described in further detail herein Other facts indicate that the polyester forming the sintered body has some degree of crosslinking. It can be concluded that
本発明の一好適実施形態においては、本発明による焼結体は本質的に9.9−ビ ス(4−ヒドロキシフェニル)フルオレンに基づ(芳香族ポリエステルから成っ ている。In one preferred embodiment of the invention, the sintered body according to the invention is essentially 9.9-bi Based on (4-hydroxyphenyl)fluorene (composed of aromatic polyester) ing.
本発明による焼結体のもう一つの好適実施形態は、本質的に1.1−ポリエステ ルから成るものである。Another preferred embodiment of the sintered body according to the invention consists essentially of 1.1-polyester. It consists of
本発明はさらに本発明の成形体の製造のための有利な方法に関する。The invention furthermore relates to an advantageous method for producing the moldings according to the invention.
この方法は、粉体状の芳香族ポリエステルを圧力下に圧縮すること、圧縮した粉 体を、その圧力を保持しながら、使用したポリエステルのガラス転移点よりも高 い温度まで徐々に加熱すること、このようにして圧縮し且つ圧力下にある粉体を 焼結体が形成されるまで所定の保持時間にわたって三の温度に保つこと、及びこ のようにして得た焼結体をゆっくりと冷却することを特徴としている。この場合 に粉体状にあるポリエステルは3000 N/c+a2よりも高い圧力、好まし くは、500ON/am”よりも高い圧力、たとえば約10,0OON/cm” の圧力下に圧縮することが有利である。This method involves compressing powdered aromatic polyester under pressure, compressed powder The body is heated to a temperature higher than the glass transition temperature of the polyester used while maintaining its pressure. gradually heating the powder to a new temperature, thus compressing the powder and under pressure. holding at three temperatures for a predetermined holding time until a sintered body is formed; It is characterized by slowly cooling the sintered body obtained as described above. in this case Polyester in powder form is exposed to pressure higher than 3000 N/c+a2, preferably or a pressure higher than 500 ON/am", for example about 10,0 OON/cm" It is advantageous to compress under a pressure of .
本発明の方法の好適実施形態によれば、圧縮したポリエステルのゆっくりした加 熱を1.5〜4.0℃/分の範囲の加熱速度で行ない且つ/又は焼結体のゆっく りした冷却を0.5〜2.5℃/分の範囲の速度で行なう。According to a preferred embodiment of the method of the invention, the compressed polyester is slowly The heating is carried out at a heating rate in the range of 1.5 to 4.0°C/min and/or the sintered body is heated slowly. The cooling is carried out at a rate ranging from 0.5 to 2.5°C/min.
本発明の方法のもう一つの好適実施形態においては、製造すべき焼結体の加圧の 方向において測定した平均厚さ1mm当り5〜20分の範囲の保持時間を用いる 。In another preferred embodiment of the method of the invention, the sintered body to be produced is pressurized. Using holding times ranging from 5 to 20 minutes per mm of average thickness measured in the direction .
本発明の方法のさらに他の好適実施形態においては、少なくとも部分的に、加え た最高圧力に対して著るしく低下させた圧力の負荷において、焼結体の冷却を行 う。In yet another preferred embodiment of the method of the invention, at least in part The sintered body is cooled under a pressure load that is significantly lower than the maximum pressure applied. cormorant.
発明の実施のための一方法 次いで本発明を実施例に従って詳細に説明する。A method for carrying out the invention Next, the present invention will be explained in detail according to examples.
これらの実施例によって製造する焼結体は、ヨーロッパ特許第64972及び6 4971号に記載するもののような、次の二種の芳香族ポリエステルである: 1、DSCによって測定した250℃のガラス転移点を有する、1゜1−ビス( 4−ヒドロキシフェニル)−1−フェニルエタンとフタル酸クロリド(イソ/テ レ:50150)に基づく芳香族ポリエステル(以下ではCPEと記す) 2、 9. 9−ビス(4−ヒドロキシフェニル)フルオレンとフタル酸クロリ ド(イソ/テレ:50150)に基づいた、DSCによる測定で325℃のガラ ス転移点を示す、芳香族ポリエステル(以下ではFPEと記す)。The sintered bodies produced by these examples are described in European Patent Nos. 64972 and 6. Two aromatic polyesters, such as those described in No. 4971: 1. 1° 1-bis( 4-Hydroxyphenyl)-1-phenylethane and phthalic acid chloride (iso/te Aromatic polyester (hereinafter referred to as CPE) based on 2, 9. 9-bis(4-hydroxyphenyl)fluorene and chlorine phthalate Glass temperature of 325°C as measured by DSC based on An aromatic polyester (hereinafter referred to as FPE) that exhibits a transition temperature.
焼結体の製造のための出発材料としては、0.5〜3.8dl/gの固有粘度( 前記のヨーロッパ特許中に記載のようにして測定)に相当する、500.000 〜1,200,000の平均分子量MWを有する、合成の際に粉末状として生成 したポリエステルを使用する。合成において生成したポリエステル粉体の中の6 00μmよりも小さい粒度、好ましくは50〜400μmの粒度を有するふるい 画分を使用する。Starting materials for the production of sintered bodies have an intrinsic viscosity of 0.5 to 3.8 dl/g ( 500,000 (measured as described in the aforementioned European patent) Produced as a powder during synthesis with an average molecular weight MW of ~1,200,000 Use recycled polyester. 6 in the polyester powder produced during synthesis A sieve with a particle size of less than 00 μm, preferably between 50 and 400 μm Use fractions.
このような粉体画分は、その小さい粒子の大きさによって良好な焼結性を示す。Such a powder fraction exhibits good sinterability due to its small particle size.
しかしながら、もつとも微細な画分の排除によって、圧搾技術に対して不利とな るおそれがある、充填密度が小さすぎるようになることを防ぐことができる。However, the exclusion of even the finest fractions poses a disadvantage to the pressing technique. This prevents the packing density from becoming too low, which could result in
次いで、いわゆる加圧焼結法によるCPEからの焼結体の製造を詳細に説明する 。Next, the production of a sintered body from CPE by the so-called pressure sintering method will be explained in detail. .
200X220X4mmの寸法の板状の焼結体の製造のために加熱可能な型を使 用する。型を150℃に予熱したのち、下方の型半分のキャビティー中に先ず0 、35 g/ctm”の充填密度として相応する量の真空乾燥したCPE粉を 入れ、型のキャビティー中に押し込まれる下方の型半分の装着によって、型を閉 じる。次いで型をプレス中に移し、CPE粉を500ON/cm”の圧縮力で圧 縮し、型をゆっくりと、すなわち、約り℃/分の加熱速度で、250℃のCPE のガラス転移点より高い温度である270℃まで加熱し、さらにこの温度を約6 0分間保つ。次いで型を約り℃/分の速度で230℃まで冷却したのち、圧力を 、良好な熱伝導率を確保するためのものであるにすぎない、約20 N/ c m2の低い値まで低下させ、その後に型をさらに50℃まで冷却したのちに、仕 上った焼結体を型から取出す。このようにして取得した焼結体は、ASTM D 3418−82に従って測定して250℃のガラス転移点と1、21g/cm’ の密度を有している。A heatable mold is used to produce a plate-shaped sintered body with dimensions of 200 x 220 x 4 mm. use After preheating the mold to 150℃, first pour zero into the cavity in the lower half of the mold. , a corresponding amount of vacuum-dried CPE powder with a packing density of 35 g/ctm”. The mold is closed by loading the lower mold half, which is pushed into the mold cavity. Jiru. Next, the mold was transferred to a press, and the CPE powder was compressed with a compression force of 500ON/cm. CPE at 250°C with a heating rate of approximately 1°C/min. heating to 270°C, which is higher than the glass transition point of Hold for 0 minutes. The mold was then cooled to 230℃ at a rate of ℃/min, and then the pressure was reduced. , only to ensure good thermal conductivity, about 20 N/c m2 to a low value, after which the mold is further cooled to 50°C before finishing. The rising sintered body is taken out from the mold. The sintered body thus obtained is ASTM D Glass transition temperature of 250 °C and 1,21 g/cm’ as measured according to 3418-82 It has a density of
同様にして、FPE粉体からも焼結体を製造することができる。CPE焼結体の 製造の場合とFPEの場合の相違は、後者では330℃(325℃のガラス転移 点よりも高い温度)の保持温度で加工し、冷却の際の圧力低下を250℃で行な うことである。このようにして製造したFPE焼結体は325℃のガラス転移点 と1.22g/cm”の密度を有している。Similarly, sintered bodies can also be produced from FPE powder. CPE sintered body The difference between manufacturing and FPE is that the latter has a glass transition temperature of 330°C (325°C). Processing is carried out at a holding temperature of That is true. The FPE sintered body produced in this way has a glass transition point of 325°C. and a density of 1.22 g/cm''.
CPE又はFPEからの焼結体は、こはく色の色調を有し、アルコール、油脂、 グリースに対して耐性がある。Sintered bodies from CPE or FPE have an amber color and are free from alcohol, fats and oils, Resistant to grease.
先に述べたようにポリエステルは焼結において網状化する。As mentioned above, polyester becomes reticulated upon sintering.
それぞれ平均分子量MW=約500.000を有するCPE及びFPEから注型 フィルム及び焼結体を製造した。フィルム又は焼結体材料の再溶解後に、フィル ム材料はやはり分子量MW=500.000を示したのに対して、焼結体材料の 分子量はMW=50,000の値に低下した。焼結体の低下した分子量からみて 、溶剤に対するその耐性もまた同様に低下するものと考えられるにもかかわらず 、それとは異なって、焼結体は特定の溶剤に対してフィルム材料よりも高い耐性 を示す。たとえば、四塩化炭素中の90時間の浸せきにおいて、CPEはフィル ムの場合は焼結体の場合の約2倍の溶剤を吸収し、FPEではそれは実に9倍と なる。Casting from CPE and FPE each having an average molecular weight MW=about 500.000 A film and a sintered body were manufactured. After remelting the film or sintered material, the film The sintered material also showed a molecular weight MW of 500.000, whereas the sintered material showed a molecular weight MW of 500.000. The molecular weight decreased to a value of MW=50,000. In terms of the reduced molecular weight of the sintered body , even though its resistance to solvents would also be expected to decrease as well. , unlike that, sintered bodies are more resistant to certain solvents than film materials. shows. For example, in a 90 hour immersion in carbon tetrachloride, the CPE In the case of aluminum, it absorbs about twice as much solvent as in the case of sintered material, and in FPE it is nine times as much. Become.
次いで、焼結体製造のための改良方法を以下に記述する。この方法においては、 それ自体を加熱することはできないが、その代りに圧力下に閉鎖子ることができ る型を使用する。ポリエステル粉体(CPE又はFPE)による充填後に型をプ レス中に移し、そこで型の内容物を約10゜00ON/cm”まで圧縮し且つプ レスからの型の取出しののちにも両方の型半分が内容物になお高い圧力を及ぼす ことができるように型を圧力下に閉鎖する。次いで型を加熱オーブン中で、ゆっ くりと、すなわち、2℃/分の加熱速度で、270℃(CPEの場合)又は33 0℃(FPEの場合)まで加熱し、4mmの厚さの焼結板の製造のために60分 にわたってこの温度を保つ。その後にオーブンの加熱を中止して型を冷やす。そ れぞれのガラス転移点よりも20℃低い温度に達したのち、型をオーブンの外で 50℃までさらに冷却し、その後に仕上った焼結体を取出す。Next, an improved method for producing a sintered body will be described below. In this method, It cannot heat itself, but instead the obturator can be under pressure. Use the type shown below. Pour the mold after filling with polyester powder (CPE or FPE) The contents of the mold were then compressed to approximately 10°00 ON/cm” and pressed. After removing the mold from the mold, both mold halves still exert high pressure on the contents. The mold is closed under pressure so that it can be closed. The mold is then slowly placed in a heated oven. i.e. 270°C (for CPE) or 33°C at a heating rate of 2°C/min. Heating to 0 °C (for FPE) and 60 minutes for production of 4 mm thick sintered plates. Maintain this temperature for a long time. After that, stop heating the oven and let the mold cool. So After reaching a temperature 20°C lower than the respective glass transition points, the molds were removed from the oven. The sintered body is further cooled to 50° C., and then the finished sintered body is taken out.
焼結体の製造においては、型をゆっくりと加熱し且つ冷却することが重要である 。許容される加熱及び冷却速度は、製造すべき焼結体の厚さが大であるほど低い 。最高の型温度に対して必要な保持時間についても同様なことがあてはまる。お およその規準として、焼結体の厚さ1mm当りに約15分の保持時間を用いるべ きである。In the production of sintered bodies, it is important to slowly heat and cool the mold. . The permissible heating and cooling rates are lower the greater the thickness of the sintered body to be produced. . The same applies to the holding time required for the highest mold temperature. oh As a rough standard, a holding time of approximately 15 minutes should be used for each mm of thickness of the sintered body. It is possible.
下表においては、CPE又はFPEから上記のようにして製造した焼結体のい( つかの重要な性質を示す。In the table below, the sintered body produced from CPE or FPE as described above ( Indicates some important quality.
1、機械的性質(室温、DIN規格による)性質 単位 CPE FPE 引張強さ N/mm287 72 切断伸び % 9.4 4.2 弾性率(引張り) N/i++a22500 2800曲げ強さ N/mm21 25 123 弾性率(曲げ) N/關22550 2780硬度ロックウェルM 104 1 17 シヨアD 88 91 DIN31680によりビン−円盤測定機により測定。表面粗さRy=2μmを 有するローラーベアリング鋼からの円盤を使用単位 CPE FPE 摩擦数 0.8 0.8 摩耗係数 Ql13/Nl 3.5・10−’ 19.0・10−6単位 CP E FPE 方法 ガラス転移点 ’C25032S DSC熱による形状安定性 ℃217.5 307 TMA(方法A) 線膨張係数 K−’ 75.10−’ 70.10−’ Tel^熱伝導率 1 /mK O,190,254、電気的性質 (Illm) (關) 誘電率 (IMHzにおいて) −室温貯蔵 3.68 4.55C48h/23℃15 0% 一水中貯蔵 3.03 4.13 D24h/23℃ 誘電損失 (IMHzにおいて) −室温貯蔵 18.7−10−’ 16.4−10−’ C48h/23℃150% 一水中貯蔵 23.2・10−317.5・1O−3D24h/23℃ 電気抵抗 オーム −室温貯蔵 3.252.10′43.971.10I5C 48/23℃150% 性質 単位 CPE FPE 吸水率 (水中貯蔵、23℃、24時間) % 0.20 0.25酸素指数: CPE 33.5% FPE 40.0% 工業的利用可能性 上記の焼結体は一般に半製品すなわち成形した部品素材として用いることができ 、次いでそれから通常の機械的切削加工により所望の製品を製造することができ る。1. Mechanical properties (room temperature, according to DIN standards) Properties Unit: CPE FPE Tensile strength N/mm287 72 Cutting elongation % 9.4 4.2 Elastic modulus (tensile) N/i++a22500 2800 Bending strength N/mm21 25 123 Elastic modulus (bending) N/Gate 22550 2780 Hardness Rockwell M 104 1 17 Shore D 88 91 Measured with a bottle-disk measuring machine according to DIN 31680. Surface roughness Ry=2μm Units using discs made from roller bearing steel: CPE, FPE Friction number 0.8 0.8 Wear coefficient Ql13/Nl 3.5・10-' 19.0・10-6 unit CP E FPE method Glass transition point ’C25032S Shape stability by DSC heat ℃217.5 307 TMA (Method A) Linear expansion coefficient K-' 75.10-' 70.10-' Tel^ Thermal conductivity 1 /mK O,190,254, electrical properties (Illm) (關) dielectric constant (at IMHz) - Room temperature storage 3.68 4.55C48h/23℃15 0% Storage in water 3.03 4.13 D24h/23℃ dielectric loss (at IMHz) - Room temperature storage 18.7-10-' 16.4-10-' C48h/23℃150% Storage in water 23.2・10-317.5・1O-3D24h/23℃ Electrical resistance ohm - room temperature storage 3.252.10'43.971.10I5C 48/23℃150% Properties Unit CPE FPE Water absorption rate (Stored in water, 23℃, 24 hours) % 0.20 0.25 Oxygen index: CPE 33.5% FPE 40.0% Industrial applicability The above sintered body can generally be used as a semi-finished product, that is, a material for molded parts. , then the desired product can be manufactured from it by normal mechanical cutting. Ru.
要 約 書 ジブエノール、たとえば1.1−ビス(4−ヒドロキシフエニノリーl−フェニ ルエタン又は9.9−ビス(4−ヒドロキシフェニル)フルオレン、及びフタル 酸ハロゲニドに基いて製造した芳香族ポリエステルから成る焼結体は、220〜 400℃の範囲で一つ又はそれ以上のガラス転移点および4ON/mm”よりも 大きい、好ましくは6ON/mm’よりも太き(弓1張強さを示す。Summary book Dibuenols, such as 1,1-bis(4-hydroxyphenynolyl-phenylene) ruethane or 9,9-bis(4-hydroxyphenyl)fluorene, and phthal Sintered bodies made of aromatic polyesters produced on the basis of acid halides are one or more glass transition points in the range of 400°C and greater than 4ON/mm” Large, preferably thicker than 6ON/mm' (indicating bow 1 tensile strength).
上記の焼結体の製造のために、閉じた型の中でポリエステル粉末に300ON/ cm”よりも大きな圧力を適珀し、その際型はゆっくりと加熱し、長時間ガラス 転移点以上の温度に保持し、その後ゆっくりと冷却する。冷却の間に圧力を低下 しつる。焼結プロセスにおいてポリエステル物質の架橋が生じ、溶媒に対する耐 性が増大する。これらの焼結体は一般に半製品又は予備成形した半完成部品とし て有用であり、これらの部品から次いで所望の製品を機械加工により製造するこ とができる。For the production of the above sintered body, 300ON/L was added to the polyester powder in a closed mold. cm", the mold is heated slowly and the glass is heated for a long time. The temperature is maintained above the transition point and then slowly cooled. Reduce pressure during cooling Shitsuru. Crosslinking of the polyester material occurs during the sintering process, increasing its resistance to solvents. sex increases. These sintered bodies are generally semi-finished products or preformed semi-finished parts. These parts can then be machined into desired products. I can do it.
国際調査報告 一一−−−−−−−k PCT/AT 9110OCN7国際調査報告international search report 11------k PCT/AT 9110OCN7 International Search Report
Claims (11)
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT221/90 | 1990-02-02 | ||
| AT0022190A AT395431B (en) | 1990-02-02 | 1990-02-02 | SHAPED BODY MADE OF AROMATIC POLYESTERS |
| US07/539,082 US5102974A (en) | 1990-02-02 | 1990-06-15 | Formed, sintered body comprising one or more aromatic polyesters |
| US539,082 | 1990-06-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04504546A true JPH04504546A (en) | 1992-08-13 |
Family
ID=25591924
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3503625A Pending JPH04504546A (en) | 1990-02-02 | 1991-02-04 | Molded objects from aromatic polyester |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0471803A1 (en) |
| JP (1) | JPH04504546A (en) |
| CA (1) | CA2050310A1 (en) |
| WO (1) | WO1991011312A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT395431B (en) * | 1990-02-02 | 1992-12-28 | Isonova Tech Innovat Gmbh | SHAPED BODY MADE OF AROMATIC POLYESTERS |
| CA2071477A1 (en) * | 1990-08-28 | 1992-03-01 | Peter Fialla | High purity aromatic polyester, a film and other products and devices containing such polyester as well as a process for preparing such film |
| ATE112710T1 (en) * | 1991-02-04 | 1994-10-15 | Isonova Tech Innovat Gmbh | MOLDED BODY IN AROMATIC POLYESTER. |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3558550A (en) * | 1967-02-07 | 1971-01-26 | Montedison Spa | Sinterings of polytetrafluoroethylene loaded with titanium and the preparation thereof |
| BE789542A (en) * | 1971-10-01 | 1973-03-29 | Carborundum Co | PRODUCTION OF INFUSIBLE AND FORMABLE PARA-OXYBENZOYL POLYESTER |
| US4011293A (en) * | 1973-08-21 | 1977-03-08 | E. I. Du Pont De Nemours And Company | Toughened linear aromatic polymers |
| US3980749A (en) * | 1973-08-31 | 1976-09-14 | The Carborundum Company | Partially crosslinked linear aromatic polyesters |
| ATE31936T1 (en) * | 1981-05-07 | 1988-01-15 | Isovolta | HIGH MOLECULAR MOLECULAR AROMATIC POLYESTER, PROCESS FOR MANUFACTURING FILMS FROM SUCH POLYESTERS AND FOIL FROM SUCH POLYESTERS, ELECTRIC CONDUCTOR WITH INSULATION FROM SUCH POLYESTERS, AND METHOD FOR MANUFACTURING SUCH INSULATION. |
-
1991
- 1991-02-04 JP JP3503625A patent/JPH04504546A/en active Pending
- 1991-02-04 EP EP91903442A patent/EP0471803A1/en not_active Withdrawn
- 1991-02-04 WO PCT/AT1991/000017 patent/WO1991011312A1/en not_active Ceased
- 1991-02-04 CA CA002050310A patent/CA2050310A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EP0471803A1 (en) | 1992-02-26 |
| WO1991011312A1 (en) | 1991-08-08 |
| CA2050310A1 (en) | 1991-08-03 |
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