Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/68—Polyesters containing atoms other than carbon, hydrogen and oxygen
  • C08G63/688—Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur
  • C08G63/6884—Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/6886—Dicarboxylic acids and dihydroxy compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/68—Polyesters containing atoms other than carbon, hydrogen and oxygen
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
  • C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
  • C08G63/12—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from polycarboxylic acids and polyhydroxy compounds
  • C08G63/16—Dicarboxylic acids and dihydroxy compounds
  • C08G63/18—Dicarboxylic acids and dihydroxy compounds the acids or hydroxy compounds containing carbocyclic rings
  • C08G63/19—Hydroxy compounds containing aromatic rings
  • C08G63/193—Hydroxy compounds containing aromatic rings containing two or more aromatic rings

Definitions

• the present invention relates to an aromatic polyester having excellent heat resistance and excellent molding characteristics.
• the present invention relates to an aromatic polyester having excellent heat resistance and excellent moldability.
• the scented or re-ester that is produced by the induction method is characterized by its tensile strength, bending strength, thermal properties such as thermal properties, thermal conversion temperature, thermal decomposition temperature, and other electrical properties. It is known that it is a resin with excellent properties and properties. However, in comparison with aromatic and aliphatic polyolefins such as polyethylene terephthalates, the thermal properties have been improved, but in recent years, However, considering the heat resistance required for high-performance towns, the thermal properties of the above-mentioned aromatic ⁇ concluderate are not necessarily satisfactory.
• Specific force between the number of structural units A and the number of structural units C: 1: 0.04 to 0.66, the number of structural units A and the number of barrel units B plus C The ratio of the total and is: I:
• Aromatic polyesters having a ratio of 0.99 to 1.10] 3 and the logarithm of the polymerization ⁇ ; 0.2 to 2.0 are provided:
• the carnyl groups are meta or c.
• the hydrogen atom is in the meta or ha in the S02 group.
• the hydrogen atom is in the meta.
• La e. X in the formula C is a divalent ⁇ -hydrogen group having 1 to 10 carbon atoms, 0, CO,
• ⁇ R 4 each represents hydrogen, a hydrocarbon Motoma other 1 to 8 carbon atoms shows the C b gain down atom, it may also different connexion in each other the same bur, X is-out bets S 0 2 R ⁇ ] all ⁇ R 4 are not simultaneously hydrogen], corresponding to ⁇ units by lever type a to 5 the invention - corresponding to structural units of the click Cal Bonn acid component and the formula B and C 2 two bi scan By the copolycondensation with the phenol component], a polyester which can improve the drawbacks of the conventional aromatic polyester and maintain good heat resistance can be obtained. These balls are compressed and extruded.
• molded products having a transparent color can be obtained, which have sufficient mechanical properties and excellent heat resistance as recommended.
• the dicarboxylic acid component used in the polyester of the present invention which corresponds to the structural unit is of the formula A, isisophthalic acid and terephthalic acid or Derivatives thereof may be mentioned. These may be used alone or in mixtures of two or more.
• Examples of the above-mentioned derivatives of cucalpo and acid include dichloride and -quester.
• a raw material constituting a vestibule using a polyester a lower aliphatic alcohol having 1 to 10 carbon atoms and a phenol having 6 to 18 carbon atoms are used.
• bis (hydroxyphenyl) sulfones * are used as the bisphenol component corresponding to the structural unit of the formula B of the present invention.
• Bis (hydroxifenil) sulfones include bis (4-hydroxifene), sulfone and bis (31 hydro).
• Bis (hydroxyphenyl) snorefone can be used either as a single structure or as a mixture of isomers.
• the bis (hydroxyphenyl) sulfones mentioned above have a hydroxyl group, or have an alkali metal or an alkaline earth metal. In some cases, it may be subjected to the reaction as various derivatives such as a salt thereof, an ester with an aliphatic or aromatic carboxylic acid. Depending on the polymerization reaction method and conditions]
• the bisphenol component corresponding to the structural unit of the formula C includes the following formula I
• a specific example of the bisphenols represented by the formula I is 2,2-bis (4'-hydroxyphenyl). , Bis (4-hydroxy 3)-bis (4'-hydroxy 3 '-methyl fu) .
• Emissions 2, 2 - bi scan (- click b Honoré 4 - arsenide mud key sheet full d two Honoré) flop D c 0 emissions, 1, 1 - bi scan (4, - heat de port key sheet full et two Honoré ) Cyclohexane, 1,1-bis (4 '-Hydroxifene) Isobutane, 1, 1-bis-Hydroxifene Le) Uz off Engineering two Honoré meta emissions, 2, 2 - bi scan (3, 5 '- di main switch Honoré 4, one heat mud key sheet full d two Honoré) flop b c 0 emissions, bi scan (3 , 5-, 4-hydroxy * hydroxy * 2) methane, vis (4-hydroxy fen nin).
• the amount of bis (hydroxifene) used for the dicanolenic acid component in the snorephon territory is based on the amount of dicalonate per mole.
• 0.36 06 mol preferably 0.40 to: L 0 mol, particularly preferably 0.45 0.96 mol.
• the amount of the bisphenols of the formula I with respect to the -zocalbonic acid component is 0.040.66 with respect to 1 mol of quincalum. Mol, preferably in the range of 0.08 0.62 mol
• the resulting polymer will be obtained.
• the nature of is reduced.
• the value of dicarboxylic acid residue in the liquor is equivalent to the value of bisulfonate. If there are less than 0.36 rufone residues, the-property tends to be inferior 9, whereas if it exceeds 1.06, the moldability of the polymer will be reduced. It is easy to cause problems due to the transparency and toughness of molded products.
• the bisphenol residue in the dicarboxylic acid in the borane is equivalent to 0 ′′ .04. If the value is not clean, the poly-forming property, the toughness of the molded product, the transparency, etc. are insufficient.] Easy, and conversely, if the value exceeds 0.66, the property of exposing to heat? ⁇ 5 o
• the ballistell of the present invention is obtained by the following method.
• Logarithmic viscosity i nh. Force 0.2 to 2.0, preferably 0.3 to 0.8.
• the method for producing the polymer of the present invention is not particularly limited, and any known methods can be applied. Examples of typical polymerization methods include the following methods.
• bis (hydroxyphenyl) sulfones and bisphenols of the formula I are dissolved in the aqueous phase together with the aluminum hydroxide metal hydroxide. Dissolves isophthaloyl chloride or terephthalate port in a water-insoluble organic solvent and mixes the two phases.
• the polymer of the present invention may contain one or more of the following reaction components or mixed components in addition to the components already described.
• phenols and alcohols each having a size of 1 tongue form a tongue for controlling the molecular weight and a stable group for the purpose of further improving the stability of the polymer. Is also used. concrete
• Examples of compounds include phenol, 0-phenyl phenol, ⁇ -phenyl phenol, and naphtho phenol.
• Examples of specific compounds include phosphorous acid, phosphite diethyl, phosphite diphenyl, phosphite triethyl, Recyclyl, trioctyl phosphite, tri-silicone tridecyl, 2 (
• the polymer of the present invention has high heat resistance, the viscosity at the time of melting does not become tight, the processing quality is good, and the polymer can be melted as necessary.
• the polymer of the present invention can be molded into a desired product by molding under ordinary molding methods and conditions.
• compression molding, extrusion molding, and injection molding can be sufficiently performed with the capacity range S of each of the 10 molding machines that have been used in the past.)) It can be obtained in a desirable condition such as cracks.
• the molding temperature is between 250 and 400 ° is, preferably 280 The range is up to 380.
• the addition of a compound that lowers the melt viscosity and / or a stabilizer may cause a significant reduction in the molding temperature.
• a compound that lowers the melt viscosity and / or a stabilizer may cause a significant reduction in the molding temperature.
• various types of products such as ordinary molded products such as tiers, films, sheet-like products, and parts with precision fine microstructures are available. It can be easily formed.
• t 1 is the flow time of the polymer solution
• t 2 is the flow time of the solvent alone.
• C is the polymer-solution concentration ( ⁇ Z ").
• the logarithmic viscosity of the obtained polymer is 0.78] 9, which is an NMR spectrum] 9, and the amount of bis (4-hydroxyphenyl) in the polymer ) Sulfone residues and 2,2-bis (4, -hydroxyphenyl) pro.
• the abundance ratio of the residue was about 3: 2.
• the gel was analyzed by gel chromatography and the polymer was analyzed, and the resulting D-gram was obtained by Fuichi Hi. (Column Shodex A — 804, 80 ⁇ 5 OO im, developing solvent tetrahydrofuran flow rate 1.0 ?? min, pressure 10 cm G temperature 9) It was confirmed that a uniform co-woven assembly was generated.
• the solution dissolved in methane 2 was added to the solution in the reactor kept at 10 and being agitated by 1 S, and the mixture was stirred at 10 for 1 hour while stirring. No unreacted monomer was observed when the reaction was sampled and analyzed by gel permeation chromatography for S molecules. Then, 1N salt water solution 40 was added, and then the water of 2 was added. The mixture was allowed to stand, the mixture was allowed to stand, the lower layer was separated, and the mixture was further washed twice with 2 of water. After cleaning, the -chloromethane layer was added to the methanol (5), which was rapidly stirred with a homomixer, to deposit lima c. The paste was separated, washed with methanol and dried to obtain a polymer powder of 187 ⁇ .
• the logarithmic viscosity of the obtained polymer is 0.72]?-NMR spectrum!?, The viscosity of the polymer (4-hydroxyphenylene) A) The abundance ratio of sulfone residues to 2,2-bis (4-hydroxyphenyl) prophane residues was 4: 1.
• the product was dissolved in a 1-port orifice-containing film, and dropped into a vigorously stirred methanol of 5 using a homomixer. Precipitated. The precipitated rimer was separated, enriched with methanol, and dried to obtain a 170 ⁇ volume.
• the resulting polymer has a logarithmic viscosity of 0.58, which is the NMR spectrum.]
• the bis (4-hydroxyphenyl) s in the polymer Lemon residues and 2,2-bis (4'-hydroxyphenyl) probes.
• the abundance ratio of the amino acid residues was about 9: 1. Jeongjeong 4
• the logarithmic viscosity of the obtained polymer is 0.46], which is an NMR spectrum.] 5 bis (4-hydroxypheno 2) snorehon residue And 2, 2-vis (4'-hydroxifeneil). The abundance ratio of the amino acid residues was about 1: 1.
• Example 7 - 2 of the actual example 1 2 - bi scan (4 '- cash arsenide mud key sheet full d d le) flop B C 0 emissions, 3, 3', 5, 5 '- Te DOO ra Reaction and post-treatment as in Example 1 except that chill 4, 4'- and hydroxybiphenyl 48.2 ⁇ (0.20 mol) were used.
• chill 4, 4'- and hydroxybiphenyl 48.2 ⁇ (0.20 mol) were used.
• the teaching viscosity of the obtained Lima was 0.55.
• the logarithmic viscosity of the obtained boron was 0.52.
• the bis (4-hydroxy phenyl) is 87.6 ⁇ (0.35 mol) and the bis (4-hydroxy phenyl) air
• the reaction and post-treatment were carried out in the same manner as in Example 2, except that Ter. 30.39 (0.15 mol) was used.
• Ter. 30.39 (0.15 mol) was used.
• the logarithmic viscosity of the obtained polymer was 0.75.
• the logarithmic viscosity of the obtained boron was 0.68.
• the logarithmic viscosity of the obtained polymer is 0.63. ?????????????? In addition, the main beak] ?????????????????
• the logarithmic viscosity of the obtained polymer was 0.76, and it was confirmed from the J? And NMR spectra that the polymer was the target polymer.
• polyester of the present invention obtained in Example 4468 was obtained by comparing the bisphenol component obtained in Comparative Example 2 with 22-vis (4'-hydroxy). (Shi Fen 2) Proc. Only!) Polyester! ), It has a very high softening temperature and can be used at high S.
• the bisphenol component component and the bis (4-hydroxyphenyl) sulfone alone are the only ones that were obtained in Comparative Example 1.
• the tertiary softening temperature is high, but the heating pressure is high.] 3
• the obtained sheet was white soaked and opaque, and it was not ft., And a sheet having practical strength was not obtained.
• the sheet of Comparative Example 3 is as large as that of Comparative Example 1, but the softening degree is clearly lower than that of the actual one.
• Example 2 The polymer scepter powder obtained in Example 2 and Comparative Example 3 was pressed at 300 mm, 100 cm 2 G, and the sheet thickness was 0.5 Sir. It was created. The sheet was left for a predetermined period of time in a 1-year-old gear (manufactured by Toyo Seiki Co., Ltd.) held at 1803 ⁇ 4, and the change in logarithmic viscosity was measured to obtain the result shown in Table 12.
• Example 468 and Comparative Example 12 were manufactured in two squares, and was extracted and pelletized in the same manner as above. Furthermore, molding was performed by injection molding in the same manner as described above under the conditions shown in Table 13 to obtain the hardness measurement values shown in Table 13.
• Comparative Example 1 ' The polymer to be applied is the one that was extruded under the above conditions, and the strand became cloudy, and was extremely dangerous. It was not possible to obtain a pellet that could be used.
• the aromatic ⁇ ester of the present invention is obtained by a molding method such as pressure box, extrusion, injection, etc.]
• a colorless transparent molded article is obtained, and these are good mechanical properties. Properties and features: Have an extraordinarier £ ⁇ heat ⁇ .

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• Chemical & Material Sciences (AREA)
• Health & Medical Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Medicinal Chemistry (AREA)
• Polymers & Plastics (AREA)
• Organic Chemistry (AREA)
• Polyesters Or Polycarbonates (AREA)

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• 1981
  • 1981-04-30 JP JP56064255A patent/JPS57180631A/ja active Granted
• 1982
  • 1982-04-28 DE DE8282901303T patent/DE3267992D1/de not_active Expired
  • 1982-04-28 WO PCT/JP1982/000142 patent/WO1982003867A1/ja not_active Ceased
  • 1982-04-28 US US06/453,893 patent/US4440920A/en not_active Expired - Fee Related
  • 1982-04-28 EP EP82901303A patent/EP0077834B1/en not_active Expired
  • 1982-04-28 BR BR8207674A patent/BR8207674A/pt unknown
  • 1982-04-29 KR KR8201873A patent/KR850001921B1/ko not_active Expired
  • 1982-04-29 CA CA000401913A patent/CA1169192A/en not_active Expired
  • 1982-04-30 IT IT8221017A patent/IT8221017A0/it unknown

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