JP2010111843A - Polyamide and method for producing polyamide - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a polyamide excellent in heat resistance, flowability, toughness, low water-absorbing capacity, and rigidity, and having a high melting point. <P>SOLUTION: The polyamide is obtained by polymerizing (a) a dicarboxylic acid including at least 50 mol% of an alicyclic dicarboxylic acid and (b) a diamine including at least 50 mol% of a diamine with a substituent branched from a main chain. In addition to this, the polyamide is obtained by additionally copolymerizing with a lactam and/or an aminocarboxylic acid. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

  The present invention relates to a polyamide and a method for producing the polyamide.

  Polyamides represented by polyamide 6 and polyamide 66 (hereinafter sometimes abbreviated as “PA6” and “PA66”, respectively) and the like are excellent in molding processability, mechanical properties or chemical resistance. Polyamides are widely used as various parts materials for automobiles, electric and electronic, industrial materials, industrial materials, daily use and household goods.

In the automobile industry, as an environmental measure, there is a demand for reducing the weight of the vehicle body by replacing metal in order to reduce exhaust gas. In order to meet these requirements, polyamides are increasingly used for exterior materials and interior materials, and the level of required properties such as heat resistance, strength, and appearance for polyamide materials is further improved. Above all, since the temperature in the engine room is also increasing, there is an increasing demand for higher heat resistance for the polyamide material.
Further, in the electrical and electronic industries such as home appliances, in order to cope with the lead-free surface mount (SMT) solder, it is required to increase the heat resistance of the polyamide material that can withstand the rise in melting point of the solder.
Polyamides such as PA6 and PA66 have a low melting point and cannot satisfy these requirements in terms of heat resistance.

In order to solve the above problems of conventional polyamides such as PA6 and PA66, high melting point polyamides have been proposed. Specifically, a polyamide composed of terephthalic acid and hexamethylenediamine (hereinafter sometimes abbreviated as “PA6T”) has been proposed.
However, since PA6T is a high-melting-point polyamide having a melting point of about 370 ° C., even if an attempt is made to obtain a molded product by melt molding, the polyamide undergoes severe thermal decomposition, making it difficult to obtain a molded product having sufficient characteristics.

  In order to solve the above-mentioned problems of PA6T, PA6T may be abbreviated as aliphatic polyamide such as PA6 and PA66 or amorphous aromatic polyamide (hereinafter referred to as “PA6I”) composed of isophthalic acid and hexamethylenediamine. ) And the like, and a high melting point semi-aromatic polyamide mainly composed of terephthalic acid and hexamethylenediamine (hereinafter referred to as “6T copolymer polyamide”) whose melting point is lowered to about 220 to 340 ° C. Have been proposed).

  As a 6T copolymer polyamide, Patent Document 1 discloses an aromatic polyamide (hereinafter referred to as “a mixture of hexamethylene diamine and 2-methylpentamethylene diamine”), which is composed of an aromatic dicarboxylic acid and an aliphatic diamine. May be abbreviated as “PA6T / 2MPDT”).

  Further, in contrast to an aromatic polyamide composed of an aromatic dicarboxylic acid and an aliphatic diamine, a high melting point aliphatic polyamide composed of adipic acid and tetramethylene diamine (hereinafter sometimes abbreviated as “PA46”) or a fat. An alicyclic polyamide composed of a cyclic dicarboxylic acid and an aliphatic diamine has been proposed.

Patent Documents 2 and 3 disclose semialicyclic polyamides of alicyclic polyamides (hereinafter sometimes referred to as “PA6C”) composed of 1,4-cyclohexanedicarboxylic acid and hexamethylenediamine and other polyamides. (Hereinafter, it may be abbreviated as “PA6C copolymer polyamide”).
Patent Document 2 discloses that the heat and heat resistance of semi-alicyclic polyamide blended with 1 to 40% of 1,4-cyclohexanedicarboxylic acid as a dicarboxylic acid unit is improved in solder heat resistance. Is disclosed that the automobile parts are excellent in fluidity and toughness.

Furthermore, Patent Document 4 discloses that a polyamide comprising a dicarboxylic acid unit containing 1,4-cyclohexanedicarboxylic acid and a diamine unit containing 2-methyl-1,8-octanediamine is light resistance, toughness, moldability, lightness, And excellent heat resistance and the like. In addition, as a method for producing the polyamide, 1,4-cyclohexanedicarboxylic acid and 1,9-nonanediamine are reacted at 230 ° C. or less to form a prepolymer, and the prepolymer is solid-phase polymerized at 230 ° C. to have a melting point of 311 ° C. The production of polyamides is disclosed.
In Patent Document 5, a polyamide using 1,4-cyclohexanedicarboxylic acid having a trans / cis ratio of 50/50 to 97/3 as a raw material is excellent in heat resistance, low water absorption, light resistance, and the like. It is disclosed.

JP-T 6-503590 Japanese National Patent Publication No. 11-512476 Special table 2001-514695 gazette Japanese Patent Laid-Open No. 9-12868 International Publication No. 2002/048239 Pamphlet

  Although the 6T copolymer polyamide certainly has the characteristics of low water absorption, high heat resistance, and high chemical resistance, it has low flowability and insufficient moldability and molded product surface appearance. Inferior in light resistance. Therefore, the appearance of a molded product such as an exterior part is required, or improvement is desired in applications where it is exposed to sunlight or the like. In addition, the specific gravity is large, and improvement in lightness is also desired.

  The PA6T / 2MPDT disclosed in Patent Document 1 can partially improve the problems of the conventional PA6T copolymer polyamide, but in terms of fluidity, moldability, toughness, molded product surface appearance, and light resistance. The level of improvement is insufficient.

  PA46 has good heat resistance and moldability, but has a high water absorption rate, and has a problem that dimensional change due to water absorption and deterioration of mechanical properties are remarkably large. Dimensional change required for automotive applications, etc. There are cases where the demand cannot be met.

The PA6C copolymer polyamides disclosed in Patent Documents 2 and 3 also have problems such as high water absorption and insufficient fluidity. The polyamides disclosed in Patent Documents 4 and 5 also have toughness, rigidity, and fluidity. In terms of sex, the improvement is insufficient.

  The problem to be solved by the present invention is to provide a polyamide having excellent heat resistance, fluidity, toughness, low water absorption and rigidity and having a high melting point.

  As a result of intensive studies to solve the above problems, the inventors of the present invention obtained a polyamide obtained by polymerizing alicyclic dicarboxylic acid and a diamine having a substituent branched from the main chain as main components. The present inventors have found that the problem can be solved and have completed the present invention.

That is, the present invention is as follows.
(1) (a) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid;
(B) A polyamide obtained by polymerizing at least 50 mol% of a diamine containing a diamine having a substituent branched from the main chain.
(2) The polyamide according to (1), wherein the diamine having a substituent branched from the main chain is 2-methylpentamethylenediamine.
(3) The polyamide according to (1) or (2), wherein the alicyclic dicarboxylic acid is 1,4-cyclohexanedicarboxylic acid.
(4) The polyamide according to any one of (1) to (3), wherein the dicarboxylic acid further contains an aliphatic dicarboxylic acid having 10 or more carbon atoms.
(5) The polyamide according to any one of (1) to (4), wherein (c) lactam and / or aminocarboxylic acid is further copolymerized.
(6) The polyamide according to any one of (1) to (5), which has a melting point of 270 to 350 ° C.
(7) The polyamide according to any one of (1) to (6), wherein the trans isomer ratio is 50 to 85%.
(8) The polyamide according to any one of (1) to (7), wherein the b value is 0 or less.
(9) (a) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid;
(B) polymerizing at least 50 mol% of a diamine containing an aliphatic diamine having a substituent branched from the main chain,
A method for producing polyamide.
(10) The method for producing a polyamide according to (9), wherein polymerization is carried out while maintaining a trans isomer ratio at 50 to 80%.
(11) A polyamide obtained by the production method according to (9) or (10).

  According to the present invention, it is possible to provide a polyamide having excellent heat resistance, fluidity, toughness, low water absorption and rigidity, and having a high melting point.

  Hereinafter, a mode for carrying out the present invention (hereinafter referred to as “the present embodiment”) will be described in detail. In addition, this invention is not limited to the following embodiment, It can implement by changing variously within the range of the summary.

[polyamide]
The polyamide of the present embodiment is a polyamide obtained by polymerizing the following (a) and (b):
(A) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid,
(B) A diamine containing at least 50 mol% of a diamine having a substituent branched from the main chain.
In the present embodiment, the polyamide means a polymer having an amide (—NHCO—) bond in the main chain.

(A) Dicarboxylic acid (a) The dicarboxylic acid used in the present embodiment contains at least 50 mol% of an alicyclic dicarboxylic acid.
(A) By containing at least 50 mol% of the alicyclic dicarboxylic acid as the dicarboxylic acid, it is possible to obtain a polyamide that simultaneously satisfies heat resistance, fluidity, toughness, low water absorption, rigidity, and the like.

(A-1) Examples of alicyclic dicarboxylic acids (also referred to as alicyclic dicarboxylic acids) include 1,4-cyclohexanedicarboxylic acid, 1,3-cyclohexanedicarboxylic acid, and 1,3-cyclopentane. Examples thereof include alicyclic dicarboxylic acids having 3 to 10 carbon atoms, preferably 5 to 10 carbon atoms, such as dicarboxylic acid.
The alicyclic dicarboxylic acid may be unsubstituted or may have a substituent.

  In this embodiment, examples of the substituent include an alkyl group having 1 to 4 carbon atoms such as a methyl group, an ethyl group, an n-propyl group, an isopropyl group, an n-butyl group, an isobutyl group, and a tert-butyl group. Etc.

The alicyclic dicarboxylic acid is preferably 1,4-cyclohexanedicarboxylic acid from the viewpoints of heat resistance, fluidity, rigidity, and the like.
As the alicyclic dicarboxylic acid, one kind may be used, or two or more kinds may be used in combination.

An alicyclic dicarboxylic acid has a trans isomer and a cis geometric isomer.
As the alicyclic dicarboxylic acid as a raw material monomer, either a trans isomer or a cis isomer may be used, or a mixture of various ratios of a trans isomer and a cis isomer may be used.
Since alicyclic dicarboxylic acids are isomerized at a high temperature to a certain ratio, and the cis isomer has higher water solubility in the equivalent salt with the diamine than the trans isomer, the trans isomer / cis cis is used as a raw material monomer. The body ratio in terms of molar ratio is preferably 50/50 to 0/100, more preferably 40/60 to 10/90, and still more preferably 35/65 to 15/85.
The trans isomer / cis isomer ratio (molar ratio) of the alicyclic dicarboxylic acid can be determined by liquid chromatography (HPLC) or NMR.

  Examples of dicarboxylic acids other than (a-2) alicyclic dicarboxylic acids of (a) dicarboxylic acids used in the present embodiment include aliphatic dicarboxylic acids and aromatic dicarboxylic acids.

  Examples of the aliphatic dicarboxylic acid include malonic acid, dimethyl malonic acid, succinic acid, 2,2-dimethyl succinic acid, 2,3-dimethyl glutaric acid, 2,2-diethyl succinic acid, and 2,3-diethyl glutaric acid. , Glutaric acid, 2,2-dimethylglutaric acid, adipic acid, 2-methyladipic acid, trimethyladipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, dodecanedioic acid, tetradecanedioic acid, hexadecanedioic acid, octadecane Examples thereof include linear or branched saturated aliphatic dicarboxylic acids having 3 to 20 carbon atoms such as diacid, eicosane diacid, and diglycolic acid.

Examples of the aromatic dicarboxylic acid include unsubstituted or various terephthalic acid, isophthalic acid, naphthalenedicarboxylic acid, 2-chloroterephthalic acid, 2-methylterephthalic acid, 5-methylisophthalic acid, and 5-sodium sulfoisophthalic acid. And aromatic dicarboxylic acids having 8 to 20 carbon atoms substituted with the above substituent.
Examples of the various substituents include halogen groups such as an alkyl group having 1 to 6 carbon atoms, an aryl group having 6 to 12 carbon atoms, an arylalkyl group having 7 to 20 carbon atoms, a chloro group and a bromo group, and 3 carbon atoms. Groups of 10 to 10 alkylsilyl groups and sulfonic acid groups and salts thereof such as sodium salts.

The dicarboxylic acid other than the alicyclic dicarboxylic acid is preferably an aliphatic dicarboxylic acid in terms of heat resistance, fluidity, toughness, low water absorption, and rigidity, and more preferably has 6 or more carbon atoms. It is an aliphatic dicarboxylic acid.
Among these, aliphatic dicarboxylic acids having 10 or more carbon atoms are preferable from the viewpoints of heat resistance and low water absorption.
Examples of the aliphatic dicarboxylic acid having 10 or more carbon atoms include sebacic acid, dodecanedioic acid, tetradecanedioic acid, hexadecanedioic acid, octadecanedioic acid, and eicosanedioic acid.
Of these, sebacic acid and dodecanedioic acid are preferable from the viewpoint of heat resistance and the like.
As dicarboxylic acid other than alicyclic dicarboxylic acid, you may use by 1 type and may be used in combination of 2 or more types.

(A) As the dicarboxylic acid, a trivalent or higher polyvalent carboxylic acid such as trimellitic acid, trimesic acid, and pyromellitic acid may be further included within the range not impairing the object of the present embodiment.
As the polyvalent carboxylic acid, one kind may be used, or two or more kinds may be used in combination.

The proportion of (a-1) alicyclic dicarboxylic acid in (a) dicarboxylic acid is at least 50 mol%. The ratio of alicyclic dicarboxylic acid is 50-100 mol%, and it is preferable that it is 60-100 mol%. When the ratio of the alicyclic dicarboxylic acid is at least 50 mol%, a polyamide that simultaneously satisfies heat resistance, fluidity, toughness, low water absorption, rigidity, and the like can be obtained.
(A) The ratio of dicarboxylic acid other than (a-2) alicyclic dicarboxylic acid in dicarboxylic acid is 0 to 50 mol%, and preferably 0 to 40 mol%.

  (A-1) The alicyclic dicarboxylic acid is preferably 50.0 to 99.9 mol% and (a-2) the aliphatic dicarboxylic acid having 10 or more carbon atoms is preferably 0.1 to 50.0 mol%, More preferably, (a-1) the alicyclic dicarboxylic acid is 60.0 to 90.0 mol% and (a-2) the aliphatic dicarboxylic acid having 10 or more carbon atoms is 10.0 to 40.0 mol%. The (a-1) alicyclic dicarboxylic acid is 70.0 to 85.0 mol% and (a-2) the aliphatic dicarboxylic acid having 10 or more carbon atoms is 15.0 to 30.0 mol%. preferable.

In the present embodiment, the (a) dicarboxylic acid is not limited to the compounds described as the dicarboxylic acid, and may be a compound equivalent to the dicarboxylic acid.
The compound equivalent to the dicarboxylic acid is not particularly limited as long as it can be a dicarboxylic acid structure similar to the dicarboxylic acid structure derived from the dicarboxylic acid, and examples thereof include anhydrides and halides of dicarboxylic acids. Can be mentioned.

(B) Diamine (b) The diamine used in the present embodiment contains at least 50 mol% of a diamine having a substituent branched from the main chain.
(B) By containing at least 50 mol% of a diamine having a substituent branched from the main chain as the diamine, a polyamide that simultaneously satisfies fluidity, toughness, rigidity, and the like can be obtained.

  Examples of the substituent branched from the main chain include alkyl groups having 1 to 4 carbon atoms such as methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, and tert-butyl group. Is mentioned.

(B-1) Examples of the diamine having a substituent branched from the main chain include 2-methylpentamethylenediamine (also referred to as 2-methyl-1,5-diaminopentane) and 2,2,4-. Examples include branched saturated aliphatic diamines having 3 to 20 carbon atoms such as trimethylhexamethylenediamine, 2,4,4-trimethylhexamethylenediamine, 2-methyloctamethylenediamine, and 2,4-dimethyloctamethylenediamine. .
The diamine having a substituent branched from the main chain is preferably 2-methylpentamethylenediamine from the viewpoint of rigidity and the like.
As the diamine having a substituent branched from the main chain, one kind may be used, or two or more kinds may be used in combination.

  Examples of the diamine other than the diamine having a substituent branched from the (b-2) main chain of the (b) diamine used in the present embodiment include an aliphatic diamine, an alicyclic diamine, and an aromatic diamine. Can be mentioned.

  Examples of the aliphatic diamine include ethylene diamine, propylene diamine, tetramethylene diamine, pentamethylene diamine, hexamethylene diamine, heptamethylene diamine, octamethylene diamine, nonamethylene diamine, decamethylene diamine, undecamethylene diamine, dodecamethylene diamine, And straight-chain saturated aliphatic diamines having 2 to 20 carbon atoms such as tridecamethylenediamine.

  Examples of the alicyclic diamine (also referred to as alicyclic diamine) include 1,4-cyclohexanediamine, 1,3-cyclohexanediamine, 1,3-cyclopentanediamine, and the like.

  Examples of the aromatic diamine include metaxylylenediamine.

The diamine other than the diamine having a substituent branched from the main chain is preferably an aliphatic diamine and an alicyclic diamine, more preferably in terms of heat resistance, fluidity, toughness, low water absorption, rigidity, and the like. Is a linear saturated aliphatic diamine having 4 to 13 carbon atoms, more preferably a linear saturated aliphatic diamine having 6 to 10 carbon atoms, and still more preferably hexamethylene diamine.
As the diamine other than the diamine having a substituent branched from the main chain, one kind may be used, or two or more kinds may be used in combination.

(B) As the diamine, a trivalent or higher polyvalent aliphatic amine such as bishexamethylenetriamine may be further included within a range not impairing the object of the present embodiment.
As the polyvalent aliphatic amine, one kind may be used, or two or more kinds may be used in combination.

  (B) The ratio of the diamine having a substituent branched from the (b-1) main chain in the diamine is at least 50 mol%. The ratio of the diamine having a substituent branched from the main chain is 50 to 100 mol%, and preferably 60 to 100 mol%. When the ratio of the diamine having a substituent branched from the main chain is at least 50 mol%, a polyamide having excellent fluidity, toughness, rigidity, and the like can be obtained.

  (B) The ratio of diamine other than the diamine having a substituent branched from the (b-2) main chain in the diamine is 0 to 50 mol%, and preferably 0 to 40 mol%.

  The amount of (a) dicarboxylic acid added is preferably about the same molar amount as the amount of (b) diamine added. Considering the escape of (b) diamine out of the reaction system during the polymerization reaction, the molar amount of (b) diamine as a whole is preferably 0. It is 90-1.20, More preferably, it is 0.95-1.10, More preferably, it is 0.98-1.05.

(C) Lactam and / or aminocarboxylic acid From the viewpoint of toughness, the polyamide of the present embodiment is preferably further copolymerized with (c) lactam and / or aminocarboxylic acid.
The (c) lactam and / or aminocarboxylic acid used in the present embodiment means a lactam and / or aminocarboxylic acid capable of polycondensation.
The lactam and / or aminocarboxylic acid is preferably a lactam and / or aminocarboxylic acid having 4 to 14 carbon atoms, and more preferably a lactam and / or aminocarboxylic acid having 6 to 12 carbon atoms.

Examples of the lactam include butyrolactam, pivalolactam, ε-caprolactam, caprilactam, enantolactam, undecanolactam, laurolactam (dodecanolactam), and the like.
Among these, from the viewpoint of toughness, ε-caprolactam and laurolactam are preferable, and ε-caprolactam is more preferable.

Examples of the aminocarboxylic acid include ω-aminocarboxylic acid and α, ω-amino acid that are compounds in which the lactam is ring-opened.
The aminocarboxylic acid is preferably a linear or branched saturated aliphatic carboxylic acid having 4 to 14 carbon atoms substituted with an amino group at the ω position, such as 6-aminocaproic acid, 11-aminoundecanoic acid, And 12-aminododecanoic acid and the like, and examples of the aminocarboxylic acid include paraaminomethylbenzoic acid.

  As the lactam and / or aminocarboxylic acid, one kind may be used, or two or more kinds may be used in combination.

  (C) It is preferable that the addition amount of a lactam and / or aminocarboxylic acid is 0-20 mol% with respect to the molar amount of the whole monomer of (a), (b) and (c).

When the polyamide is polymerized from (a) dicarboxylic acid and (b) diamine, a known end-capping agent can be further added to adjust the molecular weight.
Examples of the end-capping agent include monocarboxylic acids, monoamines, acid anhydrides such as phthalic anhydride, monoisocyanates, monoacid halides, monoesters, and monoalcohols. In view of the above, monocarboxylic acid and monoamine are preferable.
As the terminal blocking agent, one kind may be used, or two or more kinds may be used in combination.

The monocarboxylic acid that can be used as the end-capping agent is not particularly limited as long as it has reactivity with an amino group. For example, formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproic acid , Caprylic acid, lauric acid, tridecylic acid, myristic acid, palmitic acid, stearic acid, pivalic acid, and isobutyric acid; alicyclic monocarboxylic acids such as cyclohexanecarboxylic acid; and benzoic acid, toluyl And aromatic monocarboxylic acids such as acid, α-naphthalenecarboxylic acid, β-naphthalenecarboxylic acid, methylnaphthalenecarboxylic acid, and phenylacetic acid.
As monocarboxylic acid, you may use by 1 type and may be used in combination of 2 or more types.

The monoamine that can be used as the end-capping agent is not particularly limited as long as it has reactivity with a carboxyl group. For example, methylamine, ethylamine, propylamine, butylamine, hexylamine, octylamine, Aliphatic monoamines such as decylamine, stearylamine, dimethylamine, diethylamine, dipropylamine, and dibutylamine; alicyclic monoamines such as cyclohexylamine and dicyclohexylamine; and aromatic monoamines such as aniline, toluidine, diphenylamine, and naphthylamine; Etc.
Monoamines may be used alone or in combination of two or more.

The combination of (a) dicarboxylic acid and (b) diamine is not limited to the following: (a-1) at least 50 mol% or more of alicyclic dicarboxylic acid and (b-1) at least 50 mol% or more. The combination of 2-methylpentamethylenediamine of (a-1) at least 50 mol% or more of 1,4-cyclohexanedicarboxylic acid and (b-1) at least 50 mol% or more of 2-methylpentamethylenediamine is more preferable. preferable.
By polymerizing these combinations as polyamide components, it is possible to obtain a high-melting-point polyamide that simultaneously satisfies heat resistance, fluidity, toughness, low water absorption, and excellent rigidity.

In the polyamide of the present embodiment, the alicyclic dicarboxylic acid structure exists as a geometric isomer of a trans isomer and a cis isomer.
The trans isomer ratio of the alicyclic dicarboxylic acid structure in the polyamide is
The ratio which is a trans isomer in the whole alicyclic dicarboxylic acid in polyamide is represented, and the trans isomer ratio is preferably 50 to 85 mol%, more preferably 50 to 80 mol%, still more preferably. 60 to 80 mol%.
(A-1) As the alicyclic dicarboxylic acid, it is preferable to use an alicyclic dicarboxylic acid having a trans isomer / cis isomer ratio (molar ratio) of 50/50 to 0/100. And (b) the polyamide obtained by polymerization of the diamine preferably has a trans isomer ratio of 50 to 85 mol%.
When the trans isomer ratio is within the above range, in addition to the characteristics of high melting point, toughness, and rigidity, polyamide has properties that are contrary to thermal rigidity due to high glass transition temperature and usually heat resistance. It has the property of simultaneously satisfying fluidity, high crystallinity and low water absorption.
These characteristics of the polyamide consist of a combination of (a) at least 50 mol% 1,4-cyclohexanedicarboxylic acid, (b) at least 50 mol% 2-methylpentamethylenediamine, and the trans isomer ratio is from 50 to This is particularly noticeable with polyamides of 85 mol%.
In the present embodiment, the trans isomer ratio can be measured by the method described in the Examples below.

The polyamide production method of the present embodiment includes (a) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid and (b) at least 50 mol% of a fatty acid having a substituent branched from the main chain. If it is a manufacturing method of polyamide including the process of polymerizing the diamine containing a group diamine, it will not be limited in particular.
The method for producing the polyamide preferably further includes a step of increasing the degree of polymerization of the polyamide.

Examples of the method for producing the polyamide include various methods as exemplified below:
1) Suspension of aqueous solution or water of dicarboxylic acid and diamine or suspension of water or water of a mixture of dicarboxylic acid and diamine salt and other components (hereinafter abbreviated as “the mixture” in this paragraph). A method of polymerizing a suspended liquid while heating and maintaining a molten state (hereinafter sometimes abbreviated as “hot melt polymerization method”),
2) A method of increasing the degree of polymerization while maintaining the solid state of the polyamide obtained by the hot melt polymerization method at a temperature below the melting point (hereinafter, sometimes abbreviated as “hot melt polymerization / solid phase polymerization method”). ,
3) A method in which an aqueous solution or a suspension of water of dicarboxylic acid and diamine or a mixture thereof is heated, and the precipitated prepolymer is further melted again by an extruder such as a kneader to increase the degree of polymerization (hereinafter referred to as “prepolymer · Sometimes abbreviated as "extrusion polymerization method").
4) A method in which an aqueous solution or a suspension of water of dicarboxylic acid and diamine or a mixture thereof is heated, and the degree of polymerization is increased while maintaining the solid state of the precipitated prepolymer at a temperature below the melting point of the polyamide (hereinafter referred to as “ Abbreviated as “prepolymer / solid phase polymerization method”),
5) A method of polymerizing a dicarboxylic acid and a diamine or a mixture thereof while maintaining a solid state (hereinafter sometimes abbreviated as “solid phase polymerization method”),
6) A “solution method” in which a dicarboxylic acid halide and a diamine equivalent to dicarboxylic acid are used for polymerization.

In the polyamide production method, it is preferable to carry out the polymerization while maintaining the trans isomer ratio of the alicyclic dicarboxylic acid at 50 to 85%, and from the viewpoint of the fluidity of the polyamide, the polymerization should be carried out at 50 to 80%. Is more preferable.
By maintaining the trans isomer ratio within the above range, particularly 80% or less, it is possible to obtain a polyamide having an excellent color tone and tensile elongation and a high melting point.
In the production method of polyamide, in order to increase the degree of polymerization and increase the melting point of the polyamide, it is necessary to increase the heating temperature and / or lengthen the heating time. The tensile elongation may decrease due to coloring or thermal deterioration. In addition, the rate at which the molecular weight increases may decrease significantly.
Since it is possible to prevent a decrease in tensile elongation due to polyamide coloring or thermal deterioration, it is preferable to perform polymerization while maintaining the trans isomer ratio at 80% or less.

  As a method for producing polyamide, since it is easy to maintain the trans isomer ratio at 80% or less and the obtained polyamide is excellent in color tone, 1) hot melt polymerization method and 2) hot melt polymerization Polyamide is preferably produced by a solid phase polymerization method.

In the method for producing polyamide, the polymerization form may be a batch type or a continuous type.
The polymerization apparatus is not particularly limited, and examples thereof include known apparatuses such as an autoclave type reactor, a tumbler type reactor, and an extruder type reactor such as a kneader.

The method for producing the polyamide is not particularly limited, and the polyamide can be produced by a batch-type hot melt polymerization method described below.
Examples of the batch-type hot melt polymerization method include, for example, a polyamide component ((a) dicarboxylic acid, (b) diamine, and, if necessary, (c) lactam and / or aminocarboxylic acid) using water as a solvent. About 40 to 60% by mass of the contained solution is concentrated to about 65 to 90% by mass in a concentration tank operated at a temperature of 110 to 180 ° C. and a pressure of about 0.035 to 0.6 MPa (gauge pressure). To obtain a concentrated solution. The concentrated solution is then transferred to an autoclave and heating is continued until the pressure in the container is about 1.5-5.0 MPa (gauge pressure). Thereafter, the pressure is maintained at about 1.5 to 5.0 MPa (gauge pressure) while draining water and / or gas components, and when the temperature reaches about 250 to 350 ° C., the pressure is reduced to atmospheric pressure (gauge pressure is , 0 MPa). By reducing the pressure to atmospheric pressure and then reducing the pressure as necessary, by-product water can be effectively removed. Thereafter, pressurization is performed with an inert gas such as nitrogen to extrude the polyamide melt as a strand. The strand is cooled and cut to obtain pellets.

The method for producing the polyamide is not particularly limited, and the polyamide can be produced by a continuous hot melt polymerization method described below.
As a continuous hot melt polymerization method, for example, a solution of about 40 to 60% by mass containing water and a polyamide component as a solvent is preheated to about 40 to 100 ° C. in a container of a preliminary apparatus, and then a concentrated layer / Concentrated to about 70-90% at a pressure of about 0.1-0.5 MPa (gauge pressure) and a temperature of about 200-270 ° C. to obtain a concentrated solution. The concentrated solution is discharged into a flasher maintained at a temperature of about 200 to 350 ° C., and then the pressure is reduced to atmospheric pressure (gauge pressure is 0 MPa). After reducing the pressure to atmospheric pressure, reduce the pressure as necessary. The polyamide melt is then extruded into strands, cooled and cut into pellets.

As the molecular weight of the polyamide in the present embodiment, a relative viscosity ηr at 25 ° C. was used as an index.
The molecular weight of the polyamide in the present embodiment is preferably a 98% sulfuric acid concentration of 1% and a relative viscosity ηr at 25 ° C. measured according to JIS-K6810 from the viewpoint of mechanical properties such as toughness and rigidity, and moldability. Is 1.5 to 7.0, more preferably 1.7 to 6.0, and even more preferably 1.9 to 5.5.
The relative viscosity at 25 ° C. can be measured according to JIS-K6810 as described in the following examples.

The melting point of the polyamide in the present embodiment is preferably 270 to 350 ° C. as Tm2 from the viewpoint of heat resistance. Melting | fusing point Tm2 becomes like this. Preferably it is 270 degreeC or more, More preferably, it is 275 degreeC or more, More preferably, it is 280 degreeC or more. The melting point Tm2 is preferably 350 ° C. or lower, more preferably 340 ° C. or lower, further preferably 335 ° C. or lower, and still more preferably 330 ° C. or lower.
By setting the melting point Tm2 of the polyamide to 270 ° C. or higher, a polyamide having excellent heat resistance can be obtained. By setting the melting point Tm2 of the polyamide to 350 ° C. or lower, the thermal decomposition of the polyamide in the melt processing such as extrusion and molding can be suppressed.

  The heat of fusion ΔH of the polyamide in the present embodiment is preferably 10 J / g or more, more preferably 14 J / g or more, still more preferably 18 J / g or more, and still more preferably, from the viewpoint of heat resistance. Is 20 J / g or more.

The measurement of the melting point (Tm1 or Tm2) and the heat of fusion ΔH of the polyamide in the present embodiment can be performed according to JIS-K7121 as described in the following examples.
Examples of the measuring device for the melting point and the heat of fusion include Diamond-DSC manufactured by PERKIN-ELMER.

The glass transition temperature Tg of the polyamide in the present embodiment is preferably 90 to 170 ° C. The glass transition temperature is preferably 90 ° C. or higher, more preferably 100 ° C. or higher, and further preferably 110 ° C. or higher. The glass transition temperature is preferably 170 ° C. or lower, more preferably 165 ° C. or lower, and further preferably 160 ° C. or lower.
By setting the glass transition temperature to 90 ° C. or higher, a polyamide having excellent heat resistance and chemical resistance can be obtained. Further, by setting the glass transition temperature to 170 ° C. or less, a molded product having a good appearance can be obtained.
The glass transition temperature can be measured according to JIS-K7121 as described in the following examples.
Examples of the glass transition temperature measuring device include Diamond-DSC manufactured by PERKIN-ELMER.

The melt shear viscosity ηs of the polyamide in the present embodiment is preferably 20 to 140 Pa · s, more preferably 25 to 115 Pa · s, and further preferably 30 to 90 Pa · s.
The melt shear viscosity can be measured by the method described in the following examples.
When the melt shear viscosity is within the above range, a polyamide having excellent fluidity can be obtained.

The tensile strength of the polyamide in the present embodiment is preferably 70 MPa or more, more preferably 80 MPa or more, and further preferably 85 MPa or more.
The tensile strength can be measured according to ASTM D638 as described in the following examples.
When the tensile strength is 70 MPa or more, a polyamide having excellent rigidity can be obtained.

The tensile elongation of the polyamide in the present embodiment is preferably 3.0% or more, more preferably 5.0% or more, and further preferably 7.0% or more.
The tensile elongation can be measured according to ASTM D638 as described in the following examples.
When the tensile elongation is 3.0% or more, a polyamide having excellent toughness can be obtained.

The water absorption rate of the polyamide in the present embodiment is preferably 5.0% or less, more preferably 4.0% or less, and even more preferably 3.0% or less.
The water absorption rate can be measured by the method described in the following examples.
When the water absorption is 5.0% or less, a polyamide composition excellent in low water absorption can be obtained.

The color tone b value of the polyamide in the present embodiment is preferably 0 or less, more preferably -2 or less.
The color tone b value can be measured by the method described in Examples below.
When the color tone b value is 0 or less, a polyamide composition excellent in heat discoloration can be obtained.

  The polyamide of the present embodiment uses a known molding method such as press molding, injection molding, gas assist injection molding, welding molding, extrusion molding, blow molding, film molding, hollow molding, multilayer molding, and melt spinning. Various molded products can be obtained.

  The molded product obtained from the polyamide in the present embodiment is excellent in heat resistance, toughness, low water absorption, rigidity, and moldability. Therefore, the polyamide of the present embodiment can be suitably used as various parts materials for automobiles, electrical and electronic products, industrial materials, daily products and household products, and for extrusion applications.

Hereinafter, the present embodiment will be described more specifically with reference to examples and comparative examples, but the present embodiment is not limited to only these examples.
The raw materials and measurement methods used in Examples and Comparative Examples are shown below. In the present embodiment, 1Kg / cm ² means 0.098 MPa.

[raw materials]
The following compounds were used in this example.
(A) Dicarboxylic acid (1) 1,4-cyclohexanedicarboxylic acid (CHDA) manufactured by Eastman Chemical Co., Ltd. Product name 1,4-CHDA HP grade (trans isomer / cis isomer (molar ratio) = 25/75)
(2) Terephthalic acid (TPA) Wako Pure Chemical Industries product name Terephthalic acid (3) Adipic acid (ADA) Wako Pure Chemical Industries product name Adipic acid (4) Suberic acid (C8DA) Wako Pure Chemical Industries product name Suberin Acid (5) Azelaic acid (C9DA) Wako Pure Chemical Industries product name Azelaic acid (6) Sebacic acid (C10DA) Wako Pure Chemical Industries product name Sebacic acid (7) Dodecanedioic acid (C12DA) Wako Pure Chemical Industries product Name Dodecanedioic acid (8) Tetradecanedioic acid (C14DA) manufactured by Tokyo Chemical Industry Product name Tetradecanedioic acid (9) Hexadecanedioic acid (C16DA) Product name manufactured by Tokyo Chemical Industry Hexadecanedioic acid

(B) Diamine (10) 2-Methylpentamethylenediamine (2MPD) Product name 2-methyl-1,5-diaminopentane (11) Hexamethylenediamine (HMD) Product name Hexamethylene Diamine (12) 1,9-nonamethylenediamine (NMD) Aldrich product name 1,9-nonanediamine (13) 2-methyloctamethylenediamine (2MOD) Refer to the production method described in JP-A No. 05-17413 Manufactured.
(14) Mixture of 2,2,4-trimethyl-1,6-hexanediamine and 2,4,4-trimethyl-1,6-hexanediamine (TMHD) Aldrich product name C, C, C-1, 6 -Hexamethylenediamine

[Calculation of polyamide content]
(A-1) The mol% of the alicyclic dicarboxylic acid is (the number of moles of (a-1) alicyclic dicarboxylic acid added as a raw material monomer / the number of moles of all (a) dicarboxylic acids added as raw material monomers. ) × 100.
(B-1) The mol% of the diamine having a substituent branched from the main chain was added as the raw material monomer (b-1) The number of moles of the diamine having the substituent branched from the main chain / the raw material monomer. All (b) moles of diamine) × 100 were obtained by calculation.
Further, (c) mol% of lactam and / or aminocarboxylic acid is ((c) moles of lactam and / or aminocarboxylic acid added as raw material monomer / all (a) dicarboxylic acid added as raw material monomer. (B) mole number of all diamines + (c) mole number of lactam and / or aminocarboxylic acid) × 100.
In addition, when calculating by the above formula, the denominator and the numerator do not include the number of moles of diamine having a substituent branched from the main chain (b-1) added as an additional component.

[Measuring method]
(1) Melting points Tm1, Tm2 (° C.)
According to JIS-K7121, it measured using Diamond-DSC by PERKIN-ELMER. The measurement condition is that the temperature of an endothermic peak (melting peak) that appears when about 10 mg of a sample is heated to 300 to 350 ° C. according to the melting point of the sample at a heating rate of 20 ° C./min in a nitrogen atmosphere is Tm1 (° C.) After maintaining the temperature in the molten state at the highest temperature rise for 2 minutes, the temperature was lowered to 30 ° C. at a temperature drop rate of 20 ° C./min, held at 30 ° C. for 2 minutes, and the same at the temperature rise rate of 20 ° C./min. The maximum peak temperature of the endothermic peak (melting peak) that appears when the temperature was raised to the melting point was Tm2 (° C.), and the total peak area was the heat of fusion ΔH (J / g). When there were a plurality of peaks, those having ΔH of 1 J / g or more were regarded as peaks. For example, when two peaks of melting point 295 ° C., ΔH = 20 J / g and melting point 325 ° C., ΔH = 5 J / g are present, the melting point is 325 ° C.

(2) Glass transition temperature Tg (° C)
According to JIS-K7121, it measured using Diamond-DSC by PERKIN-ELMER. Measurement conditions were such that a sample in a molten state obtained by melting a sample on a hot stage (EP80 manufactured by Mettler) was rapidly cooled using liquid nitrogen and solidified to obtain a measurement sample. Using 10 mg of the sample, the glass transition temperature was measured by raising the temperature in the range of 30 to 350 ° C. under a temperature raising speed of 20 ° C./min.

(3) Relative viscosity ηr at 25 ° C
It implemented according to JIS-K6810. Specifically, a 1% concentration solution ((polyamide 1 g) / (98% sulfuric acid 100 mL)) was prepared using 98% sulfuric acid and measured under a temperature condition of 25 ° C.

(4) Melt shear viscosity ηs (Pa · s)
At a temperature of melting point + 20 ° C. obtained above (1) to evaluate the fluidity in a molten shear viscosity ηs at a shear rate of 1,000 sec ^-1. The specific measurement method uses a twin capillary rheometer RH7-2 manufactured by ROSAND, UK. The orifice has a die diameter of 1.0 mm and a die entrance angle of 180 degrees, and the L / D is 16 and 0.25. Two orifices were used.

(5) Tensile strength (MPa) and tensile elongation (%)
Using a dumbbell injection molding test piece (3 mm thickness) for the ASTM tensile test, it was performed according to ASTM D638. The molding test piece is a cylinder with a dumbbell test piece (3 mm thickness) for ASTM tensile test (ASTM D638) (mold temperature = Tg + 20 ° C.) attached to an injection molding machine (PS40E manufactured by Nissei Resin Co., Ltd.). Molding was performed at a temperature = (Tm2 + 10) ° C. to (Tm2 + 30) ° C.

(6) Water absorption rate (%)
A pre-test mass (mass before water absorption) was measured in a dry as mold of a dumbbell injection molded test piece (3 mm thick) for ASTM tensile test. It was immersed in pure water at 80 ° C. for 24 hours. Then, the test piece was taken out from the water, the surface adhering moisture was wiped off, and after standing in a constant temperature and humidity (23 ° C., 50 RH%) atmosphere for 30 minutes, the mass after test (mass after water absorption) was measured. The increment of the mass after water absorption with respect to the mass before water absorption was taken as the water absorption amount, the ratio of the water absorption amount with respect to the mass before water absorption was determined by the number of trials n = 3, and the average value was taken as the water absorption rate (%).

(7) Color tone b value Polymer pellets are injection molding machines, injection molding conditions are cylinder temperature Tm2 + 30 ° C., mold temperature Tg + 20 ° C., molding cycle 60 seconds, dumbbell injection molding specimen for ASTM tensile test (ASTM dumbbell, 3 mm thick) was obtained. The color tone b value of the initial molded product was determined using a color difference meter ND-300A manufactured by Nippon Denshoku. The measurement was performed by using three dumbbell injection molding test pieces, measuring three times one by one at the center position of the wide portion on the side opposite to the gate, and obtaining from the average value.

(8) Trans isomer ratio 30-40 mg of polyamide was dissolved in 1.2 g of hexafluoroisopropanol deuteride and measured by ¹ H-NMR. In the case of 1,4-cyclohexanedicarboxylic acid, the trans isomer ratio was determined from the ratio of the peak area of 1.98 ppm derived from the trans isomer and the peak areas of 1.77 ppm and 1.86 ppm derived from the cis isomer.

[Example 1]
Polymerization reaction of polyamide was carried out by “hot melt polymerization method”.
(A) CHDA 896 g (5.20 mol) and (b) 2MPD 604 g (5.20 mol) were dissolved in 1500 g of distilled water to prepare an equimolar 50 mass% homogeneous aqueous solution of raw material monomers. To this homogeneous aqueous solution, 15 g (0.13 mol) of 2MPD was added.
The obtained aqueous solution was charged into an autoclave (made by Nitto High Pressure Co., Ltd.) having an internal volume of 5.4 L, kept warm until the liquid temperature (internal temperature) reached 50 ° C., and the autoclave was purged with nitrogen. The pressure in the vessel of the autoclave, as gauge pressure (hereinafter, all the pressure in the tank is expressed as gauge pressure.) To approximately 2.5 Kg / cm ^2, heating was continued at a liquid temperature of about 50 ° C. (The liquid temperature in this system was about 145 ° C.). In order to keep the pressure in the tank at about 2.5 Kg / cm ² , water was removed from the system while heating was continued, and concentrated until the concentration of the aqueous solution reached about 75% (the liquid temperature in this system was about It was 160 ° C.). The removal of water was stopped and heating was continued until the pressure in the tank reached about 30 Kg / cm ² (the liquid temperature in this system was about 245 ° C.). Heating was continued until the final temperature reached −50 ° C. while removing water out of the system to keep the pressure in the tank at about 30 Kg / cm ² . After the liquid temperature rose to a final temperature of −50 ° C. (300 ° C. in this case), the pressure was lowered while heating was continued, taking about 120 minutes until the pressure in the tank reached atmospheric pressure (gauge pressure was 0 kg / cm ² ). .
Thereafter, the heater temperature was adjusted so that the final temperature of the resin temperature (liquid temperature) was about 350 ° C. With the resin temperature kept in this state, the inside of the tank was maintained for 30 minutes under a reduced pressure of 400 torr with a vacuum apparatus. Thereafter, it was pressurized with nitrogen to form a strand from the lower nozzle (nozzle), water-cooled, cut, and discharged in a pellet form to obtain a polyamide. Table 4 shows the measurement results of the obtained polyamide based on the above measurement method.

[Examples 2 to 21]
In Example 1, as the (a) dicarboxylic acid, (b) diamine, and (c) lactam and / or aminocarboxylic acid, the compounds and amounts shown in Table 1 or 2 were used, and the final temperature of the resin temperature. The polyamide was polymerized by the method described in Example 1 except that the temperature was set to the temperature described in Table 4 or 5 ("hot melt polymerization method"). Tables 4 and 5 show the measurement results of the obtained polyamide based on the above measurement method.

[Comparative Example 1]
In Example 1, as the (a) dicarboxylic acid, (b) diamine, and (c) lactam and / or aminocarboxylic acid, the compounds and amounts shown in Table 3 were used, and the final temperature of the resin temperature was expressed. Polymerization of polyamide was carried out by the method described in Example 1 except that the temperature described in 6 was used (“hot melt polymerization method”).
In Comparative Example 1, since it was solidified in the autoclave during the polymerization, it could not be taken out as a strand. Therefore, after cooling, it was taken out as a lump and pulverized with a pulverizer to a size about pellets. Since the foaming was severe, the molded product could not be obtained.

[Comparative Examples 2 to 7]
In Example 1, as the (a) dicarboxylic acid, (b) diamine, and (c) lactam and / or aminocarboxylic acid, the compounds and amounts shown in Table 3 were used, and the final temperature of the resin temperature was expressed. Polymerization of polyamide was carried out by the method described in Example 1 except that the temperature described in 6 was used (“hot melt polymerization method”). Table 6 shows the measurement results of the obtained polyamide based on the above measurement method.

As is clear from the results in Table 4-6, the polyamides of Examples 1 to 21 obtained by polymerizing specific (a) and (b) are all of heat resistance, fluidity, toughness, low water absorption, and rigidity. In this respect, it has particularly excellent characteristics.
On the other hand, in Comparative Example 1, which is a polyamide containing less than 50 mol% of 2-methylpentamethylenediamine, it solidifies during copolymerization and cannot be taken out as a strand, and a molded product is obtained. I couldn't.
Furthermore, the polyamide of Comparative Example 4 produced by the method disclosed in Patent Document 1 has too low fluidity and is not sufficient in terms of moldability. Moreover, the toughness was not sufficient.

[Example 22]
Polymerization reaction of polyamide was carried out by “hot melt polymerization / solid phase polymerization method”.
About hot melt polymerization, the same operation as Example 1 was carried out in the same amount and procedure to obtain polyamide (polyamide (I)). Table 7 shows the measurement results of the obtained polyamide based on the above measurement method. Of this, 1300 g was charged into a ribbon stirring type heating device (ribocorn, manufactured by Okawara Seisakusho) for solid phase polymerization, and nitrogen substitution was performed at room temperature. Heating was performed for 12 hours so that the resin temperature was 200 ° C. while nitrogen was being circulated. Thereafter, the temperature was decreased while flowing nitrogen, and when the temperature reached about 50 ° C., the pellets were taken out from the apparatus to obtain polyamide (polyamide (II)). Table 7 shows the measurement results of the obtained polyamide based on the above measurement method.
In contrast to polyamide (I), in polyamide (II) after solid phase polymerization, the relative viscosity at 25 ° C. is increased and the tensile elongation is increased. The trans isomer ratio did not change before and after solid state polymerization. Also, the degree of coloring did not change.

Table 7 also shows the measurement results obtained based on the above-described measurement method for the polyamide of Example 1 obtained by hot melt polymerization.

[Example 23]
Polymerization reaction of polyamide was carried out by “prepolymer / solid phase polymerization method”.
Distilled water (500 g) was added to (a) CHDA 896 g (5.20 mol) and (b) 2MPD 604 g (5.20 mol) to prepare an equimolar 33% by mass slurry solution of raw material monomers. 15 g (0.13 mol) of 2MPD was added to the slurry.
The obtained slurry was charged into an autoclave (made by Nitto High Pressure Co., Ltd.) having an internal volume of 5.4 L, and the inside of the autoclave was purged with nitrogen. After stirring for 30 minutes at a liquid temperature of 100 ° C., the temperature was raised to 200 ° C. over 2 hours. At this time, the pressure in the autoclave tank was 22 kg / cm ² . The temperature was raised to 220 ° C., and the pressure in the tank was maintained at 22 kg / cm ² and maintained for 2 hours while removing water from the system. The pressure was reduced over 60 minutes until the pressure in the tank reached atmospheric pressure (gauge pressure was 0 kg / cm ² ). Thereafter, the resin temperature (liquid temperature) was lowered to room temperature, and then the lower flange of the autoclave was removed to obtain a solid polyamide prepolymer (polyamide (I)). Table 7 shows the measurement results of the obtained prepolymer based on the above measurement method. The trans isomer ratio of 1,4-cyclohexanedicarboxylic acid in the prepolymer was 85%. Moreover, coloring was seen with polyamide (I).
Using 1300 g of the obtained prepolymer, solid phase polymerization was carried out in the same manner as in Example 22 to obtain polyamide (polyamide (II)). Table 7 shows the measurement results of the obtained polyamide based on the above measurement method. Polyamide (II) was improved in relative viscosity as compared with the prepolymer, but colored.

[Example 24]
A polyamide polymerization reaction was carried out by the “prepolymer / extrusion polymerization method”.
For the production of the prepolymer, the same operation as in Example 23 was carried out in the same amount and procedure, and a polyamide prepolymer was obtained (polyamide (I)). 1300 g of the obtained prepolymer was used for post-polymerization in an extrusion polymerization apparatus (KRC kneader manufactured by Kurimoto Iron Works Co., Ltd.). The prepolymer was introduced so that the jacket temperature was 350 ° C., the degree of vacuum was −0.5 MPa (gauge pressure), and the residence time was 30 minutes. The strand was cooled and cut to obtain polyamide as a pellet (polyamide (II)). Table 7 shows the measurement results of the obtained polyamide based on the above measurement method. Polyamide (II) was improved in relative viscosity at 25 ° C. as compared with the prepolymer, but was colored.

  The present invention can provide a high-melting-point polyamide having excellent heat resistance, fluidity, toughness, low water absorption, and rigidity. The polyamide of the present invention can be suitably used as a molding material for various parts such as automobiles, electric and electronic, industrial materials, industrial materials, daily products and household products. Have potential.

Claims (11)

(A) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid;
(B) A polyamide obtained by polymerizing at least 50 mol% of a diamine containing a diamine having a substituent branched from the main chain.   The polyamide according to claim 1, wherein the diamine having a substituent branched from the main chain is 2-methylpentamethylenediamine.   The polyamide according to claim 1 or 2, wherein the alicyclic dicarboxylic acid is 1,4-cyclohexanedicarboxylic acid.   The polyamide in any one of Claims 1-3 in which the said dicarboxylic acid further contains C10 or more aliphatic dicarboxylic acid.   (C) The polyamide according to any one of claims 1 to 4, wherein lactam and / or aminocarboxylic acid are further copolymerized.   The polyamide according to any one of claims 1 to 5, which has a melting point of 270 to 350 ° C.   The polyamide according to any one of claims 1 to 6, wherein the trans isomer ratio is 50 to 85%.   The polyamide in any one of Claims 1-7 whose b value is 0 or less. (A) a dicarboxylic acid containing at least 50 mol% of an alicyclic dicarboxylic acid;
(B) polymerizing at least 50 mol% of a diamine containing an aliphatic diamine having a substituent branched from the main chain,
A method for producing polyamide.   The method for producing a polyamide according to claim 9, wherein polymerization is carried out while maintaining a trans isomer ratio at 50 to 80%.   A polyamide obtained by the production method according to claim 9 or 10.