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Method of producing thermotropic liquid crystalline copolyester, thermotropic liquid crystalline copolyester composition obtained by the same method, and molding made of the same composition

a technology of thermotropic liquid crystalline copolyesters and compositions, which is applied in the direction of group 5/15 element organic compounds, synthetic resin layered products, building components, etc., can solve the problems of corrosive film, serious problem of corrosive out-gases of such corrosive out-gases, etc., and achieve the effect of suppressing the generation of out-gases

Inactive Publication Date: 2001-08-16
NIPPON PETROCHEMICAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0015] One object of the present invention is to provide a method of producing a thermotropic liquid crystalline copolyester which the amount of corrosive out-gases (such as acetic acid and phenol) in a high temperature environment is extremely small, a resin composition containing a thermotropic liquid crystalline copolyester obtained by the method, and electric / electronic components formed by molding the resin composition. Another object of the present invention is to reliably suppress generation of out-gases at a practically acceptable level in the resin compositions in which fillers are blended.

Problems solved by technology

It has been recognized that thermotropic liquid crystalline copolyesters made by known methods tend to emit corrosive out-gases which corrode metal-made conductive portions (e.g. an electronic circuit) of an electric / electronic component in a high temperature environment (such as soldering and mounting-to-surface processes).
Corrosiveness of such corrosive out-gases has been recognized as a serious problem in such cases.
Specifically, in electric / electronic components having metal-made conductive portions which is vulnerable to the gases emitted from a thermotropic liquid crystalline copolyester resin (such as a relay, a switch, a connector, a socket, a resistor, a condenser, a motor, an oscillator, a print circuit board, and a power module), the metal-made conductive portions are oxidized and a corrosive film is formed thereon by the corrosive out-gases and the like due to heat history during the mounting-to-surfaces process.
As a result, failure in the conductive portions may occur.
In addition, in a case in which the electrical / electronic component has an electric contact which is operated in a mechanical manner, a failure in contact may occur due to formation of layers of carbonized materials in the contact portion (the layers are formed mainly in the contact portion by discharge during the contact operation).
The corrosion of this type has particularly been a serious problem in components such as a relay and a switch in which good contact properties must be maintained for a long period.
Accordingly, formation of corrosive film and generation of layers of carbonized materials as described above could cause much worse, more often initial failures or malfunction in these electric / electronic components than now.
Note that the layers of carbonized materials are formed in these components probably because the corrosive out-gases are carbonized by arc discharge and deposited, causing abnormality in conductance.
However, these methods are not necessarily satisfactory.
However, it has not been determined what actually are the corrosive out-gases which cause corrosive damages to metal-made conductive portions of electric / electronic components.
Therefore, although emission of acetic acid is prevented, it does not necessarily mean that a thermotropic liquid crystalline copolyester which is satisfactory in terms of its corrosive out-gas effect on an electric / electronic component can be obtained.
Especially, if the technique pays too much attention to suppression of acetic acid emission and rather increases emission of other corrosive out-gases, such technique or methods inevitably have to face a serious limitation.

Method used

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  • Method of producing thermotropic liquid crystalline copolyester, thermotropic liquid crystalline copolyester composition obtained by the same method, and molding made of the same composition
  • Method of producing thermotropic liquid crystalline copolyester, thermotropic liquid crystalline copolyester composition obtained by the same method, and molding made of the same composition
  • Method of producing thermotropic liquid crystalline copolyester, thermotropic liquid crystalline copolyester composition obtained by the same method, and molding made of the same composition

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0100] A polymerization reactor made of SUS316 as a material and having a double-helical stirring wing (manufactured by Nitto Koatsu Co.) was used. Nitrogen-substitution was carried out by repeating the process of "pressure reduction of the polymerization reactor and nitrogen injection into the reactor" five times. Then, 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA) manufactured by Ueno Seiyaku Co., 79.99 g (0.4815 moles) of isophthalic acid (IPA) manufactured by A.G. International Co., 453.29 g (2.7285 moles) of terephthalic acid (TPA) maufactured by Mitsui Sekiyu Kagaku Kogyo Co., 597.73 g (3.21 moles) of p,p'-biphenol (BP) manufactured by Honshu Kagaku Kogyo Co. and 0.35 g of magnesium acetate as a catalyst manufactured by Tokyo Kasei Co. were charged in the polymerization reactor and the monomers in the polymerization reactor were mixed by stirring at the rotation rate of the stirring wing of 50 rpm. 2 g of the monomer mixture in the polymerization reactor was taken out ...

example 2

[0107] A device which was similar to that used in Example 1 was employed. 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA), 79.99 g (0.4815 moles) of isophthalic acid (IPA), 453.29 g (2.7285 moles) of terephthalic acid (TPA), 597.73 g (3.21 moles) of p,p'-biphenol (BP) and 0.35 g of magnesium acetate as a catalyst were charged in the polymerization reactor. The temperature in the polymerization reactor was raised to 70.degree. C. and the process of "pressure reduction ad nitrogen injection" was repeated five times with rotating the stirring wing at 50 rpm, effecting the nitrogen substitution and the drying of the monomers in 2 hours. After the drying of the monomers was completed, 2 g of the monomer mixture in the polymerization reactor was taken out of the reactor and the water content therein was measured. 0.015 weight % of water content was detected in the monomer mixture. In other words, 0.37 g (0.02 moles) of H.sub.2O was present in the polymerization reactor.

[0108] The mo...

example 3

[0114] A device which was similar to that used in Example 1 was employed. Nitrogen substitution was carried out by repeating the process of "pressure reduction and nitrogen injection" of the polymerization reactor five times. 1,330.10 g (9.63 moles) of p-hydroxybezoic acid (HBA), 132.90 g (0.80 moles) of isophthalic acid (IPA), 400.37 g (2.41 moles) of terephthalic acid (TPA), 597.73 g (3.21 moles) of p,p'-biphenol (BP) and 0.35 g of magnesium acetate as a catalyst were charged in the polymerization reactor. The monomers in the polymerization reactor were mixed by stirring at the rotating rate of the stirring wing of 50 rpm. 2 g of the monomer mixture in the polymerization reactor was taken out of the reactor and the water content therein was measured. 0.200 weight % of water content was detected in the monomer mixture. In other words, 4.92 g (0.27 moles) of H.sub.2O was present in the polymerization reactor.

[0115] The monomer which had been taken out of the reactor for the measurem...

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Abstract

A method of producing a thermotropic liquid crystalline copolyester having an extremely small amount of out-gases comprising the steps of: (1) charging in a reactor 5-100 mol % of aromatic hydroxycarboxylic acid, 0-47.5 mol % of aromatic dicarboxylic acid and 0-47.5 mol % of aromatic diol, so that the sum of mol % of each material is 100 mol % and the mol % of aromatic dicarboxylic acid and that of aromatic diol are substantially equal; (2) adding acetic anhydride of an amount which satisfies the formula, (B-C) / A>=1.04, "A" representing the total molar number of the hydroxy group in a reaction system, "B" representing the molar number of acetic anhydride to be added, and "C" representing the molar number of water present in the reaction system prior to addition of acetic anhydride; (3) acetylation; (4) melt polymerization; and (5) solid-phase polymerization.

Description

[0001] 1. Field of the Invention[0002] The present invention relates to a method of producing a thermotropic liquid crystalline copolyester which the amount of corrosive out-gases emitted in a high temperature environment is extremely small, a thermotropic liquid crystalline copolyester resin composition obtained by the method, and a resin molded article made of the same resin composition for use in electrical / electronic components. More specifically, the present invention relates to a method of producing a thermotropic liquid crystalline copolyester which the amount of corrosive out-gases (such as acetic acid and phenol) emitted in a high temperature environment is extremely small due to the setting of the amount of acetic anhydride in the reaction system in which acetylation is carried out before polymerization to a specific range, a thermotropic liquid crystalline copolyester resin composition which the amount of corrosive out-gases (such as acetic acid and phenol) emitted in a h...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C08G63/60C08G63/80C08K5/524
CPCC08G63/605C08G63/80C08K5/524C08L67/00Y10T428/12007Y10T428/12528Y10T428/12569Y10T428/31681Y10T428/31786Y10T428/31989
Inventor MUROUCHI, SATOSHIYAMADA, YOSHIKUNIKOBAYASHI, TOSHITAKA
Owner NIPPON PETROCHEMICAL CO LTD
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